20130906INTG to Staff 1-5.pdf

EXECUTIVE OFFiCES
INTERMOUNTAIN GAS COMPANY prn
555 SOUTH COLE ROAD •P.O.BOX 7608 •BOISE,IDAHO 83707 •[phone] •FAX:[phone]
SFF—5 PM :3
September 6 2013 1,)f:rL-,
——,,--•r’’
Jean Jewel!
Idaho Public Utilities Commission
472 West Washington St.
P.0.Box 83720
Boise,ID 83720-0074
RE:first Production Request of the Commission Staff to Intermountain Gas Company
Case No.INT-G-13-05
Dear Jean:
Enclosed for filing with this Commission are an original and seven (7)copies of Intermountain Gas
Company’s responses to the First Production Request of the Commission Staff,in the above
referenced Case.
If you have any questions or require additional information regarding the attached,please contact me
at 377-6168.
Sincerely,
Michael P.McGrath
Director -Regulatory Affairs
Intermountain Gas Company
Enclosure
cc Scott Madison
Morgan W.Richards
REQUEST NO.1:
Question -Please describe in detail hrnt’the Company determines f existing customers are on the
correct rate.Please explain how billing audits are conthtcted and how frequently those audits are
peiforined.
Answer —Intermountain Gas Co’s CIS system (Customer Watch)will not allow an account to bill if the
premise category and the rate class do not match.ie;commercial premise on a residential rate.If a miss-
match is found between the premise and rate category,the account appears on the daily report called
“Billing Exceptions by Status”(C16380).This report identifies all active meters within a given cycle that
did not charge because of the disctepancy.Billing Audit personnel then work the report and make the
necessary corrections to ensure correct billing which in turn allows the system to generate the correct
charges and statement/bill.In addition,Report Cl7580 “Audit Account Package and Premise”generates
every Monday and reveals any discrepancies between premise category and the assigned rate class that
were changed the week prior.This report is “worked”and corrections are made.
On a daily basis,there are regular reports that might reveal a discrepancy in the customers’rate class
based on current usage.The two reports that would reveal this are the Fail/Low Meter reads compared to
last year’s report and the Zero Usage Atidit (C1697OA).Both reports are worked daily and used to
determine why usage declined.e.g.:usage in the summer declined substantially or usage goes to zero.In
addition to checking the functionality of the meter,the work order also requests an inventory check.If the
customer rate is RS2,and the usage declines substantially from the previotis summer month,it is possible
the customer has converted natural gas water heat to another source of energy.Verification of this would
initiate a change in rate from RS2 to RS I.
In addition to these audits,whenever the Billing Audit group initiates an order for a service trip,a request
is made for an inventory check while the technician is at the premise.If access is unavailable,a door tag
is left requesting the customer call in to the CSC.A note is made on the accotmt so the CSR can make the
inquiry if the customer does call in.A customer’s rate is never changed from RS2-RSI without field
verification or verbal verification from the customer that the equipment has been changed out,thus
meriting the change in rate class.
In addition to the above audits,the customer and/or plumbing contractor should notify IGC regarding the
addition of any natural gas water heating appliance.
Person Preparing Answer:Cheryl A.Imlach,Manager Revenue Accounting,Ph 377-6179
Record Holder:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6168
REQUEST NO.2:
Question -for CY2012,please provide the number of customers imioved to a different rate schedule.
listing both the previous and new rate schedule assigned.
Answer -During CY2012,736 customer accounts were moved to a different rate schedule.To illustrate
the effectiveness of the audit tools mentioned in Request No.1,22$or 31%of those were changed to the
current rate within I day of starting service.
GS1O 2 T4
GS1I
GS11 26 GSIO 3
RSI 13
RS2 8
14 2
GS2O 3 GSI1 3
ISR 1 RS2 I
RS1 245 GSII 16
ISR
RS2 228
RS2 456 GSII 16
ISR 3
RSI 437
T4 3 GSIO I
GS1I
GS2O I
Person Preparing Answer:Cheryl A.Imlach,Manager Revenue Accounting,Ph 377-6179
Record Holder:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6168
REQUEST NO.3:
Question -Please describe in detail the process used to determine whether a new customer who places a
connect order should be assigned the rate schedule assigned to the previous customer.If there are
scripts followed by call center customer service representatives,please provide a copy ofthose scripts.
Answer —Please reference the Answer to Request No.4.
Person Preparing Answer:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6168
Record Holder:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6168
REQUEST NO.4:
Question -Please describe in detail the procedures in place to ensure that a customer reqitesting service
at a previously unserved location,e.g.,new construction,is assigned to the correct rate schedule.
Answer -Consumer Sales Representatives work with home owners,local HVAC companies,architects
and engineers to determine the required load,appliances to be used and determine the appropriate rate on
new residential and small commercial sales,single and multiple meter manifolds.This information is
entered onto the Service Line Agreement,Form 512,and the data is entered into our Customer
Information System.
Single meter or multiple meter manifold sales from new construction may be handled by our GIS Field
Technicians or an Operation Aide as a part of the Joint Trench Service program.In this case,the rate
selected has been based on historical uses by the builder on new homes with a minimum of gas being
tised for space and water heating needs.Contact with the builder is made and we ask that they sign a
Service Installation Agreement,form 5 19,to speed up the processing of new starts.At this time we ask
which appliances they intend to add on all of his homes.The load and appliances on these homes may be
estimated on initial paperwork to be verified later by the Consumer Sales Representative,GIS Field
Technician,Operations Aide or Customer Service Representative,CSR,when the meter set is requested.
When the customer calls our Customer Service Center to initiate and/or start service on newly constructed
homes they are asked several questions to determine what appliances are in the home.The CSR is
looking for the combination of space and water heat which qualifies the customer for the RS-2 rate.When
another customer establishes service at the same location IGC assumes the appliances from the original
request for service hasn’t changed which could affect the rate class (furnace &water heater)and they are
then billed under the established rate class.
For customers setting up a commercial account at a residential premise,a CSR may ask if the customer is
also living there.If the customer indicates they are living there,the customer would still be billed as
residential.
If a current customer with an established RS-1 rate indicates they have installed a water heater and want
the better rate we take their word for it.The billing department monitors two reports which could indicate
the customer may need their rate adjusted.The Meter Read Compared to Last Year and the Zero Usage
Audit will catch any discrepancies in usage on RS-2 accounts that have zero consumption during the
summer months.
When these reports show a potential error a phone call is made to the ctistomer and/or a service order is
created for a service technician to check the meter and verify appliances in the home.If the technician
speaks with the ctistomer and they indicate they have removed their water heater,the technician
completes his order and directs it to the billing department to make the rate adjustment.IGC will not
adjust the rate without speaking with the customer or verifying the equipment first.
Person Preparing Answer:Randy Morgan,District Manager,Ph 377-6829
Record Holder:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6162
REQUEST NO.5:
Question -Please provide copies of or links to information made available to customers to enable them
to choose the most appropriate rate schethilefor their customer class and type of use.
Answer —
•RSI and RS2 rate explanations are part of the “Rates and Tariffs”page on the website.
http://www.intgas.com/rates-services/rates
This page includes a statement advising the customer to contact us if they feel they are on the
incorrect rate.It also has bulleted items explaining each rate and a link to the tariff:
“If you think you should be in a different category,please call our Customer Service Center
at
•The FAQ page of the website also has a question of “What rate do I pay?”In the FAQ
explanation it indicates the rate is based on the type of service used and links to the “Rates and
Tariffs”page referenced above.
•The back of the billing statement includes a breakdown of each type of rate.This information is
also available online for those that receive their bills electronically.
http://www.intas.com/customer-service/biIlunderstanding
Person Preparing Answer:Mike Kingery,Manager of Programs and Support Services,Ph 898-
7169
Record Holder:Michael P.McGrath,Director —Regulatory Affairs,Ph 377-6168
Original:Gas Measurement
Ist Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Division Ot htt Date 12 tL/L,.Report No.____________
Project No._________________Service No.O1D35I7 Pipe Size “4 Leak Order No.
Gas Pressure at Time of Break:Normal PuN Down Time of Break I 0:‘j
Outage:Yes No U How Long No.of Customers Time Under Control 1 LIb
Location 52O &1’t 0&l 4 VP L I dtkf1 I Total Time of Blow i-irs
tc d b (tL --
1Ahhu’14k Y”&itL
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I MJRGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 56 A
Percent Open A Gauge Pressure B CD.2 (IN 2)O.1%5 B
Rated Capacity B ID.2 C Time of Blow (ht)/A.’)C
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (TH/MCF)D
Constant D Constant .004041 E Total Therms I *
Total Therms Total Therms 0 Per Therm (),‘4 I 7—
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $7.q
feet or more.
Regulator Station No.
Customer Name -
Is customer billed for lost volume?
Yes j No *AxBxCxD=Therms
Ax B x C x D Therms (A +B)x C x Dx E =Therms If more than 500 therms send to Engineering
Remarks:
t/e/k-ok C2O 4pfl-’-Z1 10’
Pi ‘-‘-i g -/t
Submitted By:
DivisIon Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report No.77
Leak Order No.7)5’77
Time of Break_____________
Time Under Control_______________
Total Time of Blow i Hrs
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2 (IN 2)B
Rated Capacity B l.D.2 C Time of Blow (hr),C
Time of Blow C PIpe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/7)’.L2 D
Constant D Constant .004041 E Total Therms *
Total Therms Total Therms 0 Pet Therm .
Report blowing relief 2”and larger only Report 4’pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD....Therms
AxBxCxD=Therms (A+B)xCxDxETherms lfmorethan 500thermssendtoEngineering
Remarks:/4i %1/tl///.Z 47i?%?’%i(‘291?(}4’/A7/2
I
7i4i
Original:Gas Measurement
1st Copy DMsion Numerical File
2nd Copy:Attach to corresponding
documents in division
Town ((LIflO E;Je<)Division Date
Project No._______________Service No9941/74//Pipe Size
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No LI How Long
____________
No.of Customers
Locafion /3V AJ 46Y g
/
Submitted By:
Division Operations Manager
Form No.IGC 308 (1/06)
Town RD-1M £-
Project No.57i -ô57
Gas Pressure at Time of Break:
Outage:Yes []No ]
Location jE(.41r <74
Intermountain Gas Company
DIVISION GAS LOSS REPORT
__________
Date I —13—13
Service No.
____________
Pipe Size____________________
Normal 3 ‘/)Pull Down
__________________
How Long
_______________
No.of Customers
s2 3J ck’
Report No.(‘jI’J /443
Leak Order No.7)/(d’/
Time of Break (,;3t
Time Under Control
Total Time of Blow /Hrs
/
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure .3 S)A
Percent Open A Gauge Pressure B l.D.2 2)•B
Rated Capacity B I.D.2 C Time of Blow (hr)/j t’9 c
Time of Blow C Pipe Length fIn 1,000 ft.)D Avg.BTU (TH/MCF))f),D
Constant D Constant .004041 E Total Therms q 2..7 *
Total Therms Total Therms 0 Per Therm •..14 I ‘d(i;_.
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $3 7 ‘5
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoD *AxBxCxD=Therms
Ax B x Cx D =Therms (A ÷ B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:R4 5fIik)4i)4 +i41 74l4(/
t4%ct y
1\rf
i .1 I
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:411 LJL7
Division Operations Manager ---,/
Form No.ICC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town (fte,dAJ’Division [,J.Qt2 j-.tcy Date /(/1 3 Report No.(t50
-/7c?
Project No.__________________Service No.(i 3 Pipe Size 3iS,‘S Leak Order No.
_________________
Gas Pressure at lime of Break:Normal 5’Pull Down
______________________
Time of Break 9,cp c1.,
Outage:Yes Q No How Long 7 No.of Customers lime Under Control ij:j—
Location I LD -/YY\.D.LA-A.tLt.C4.A-l Total lime of Blow o?.L/I Hrs
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure_______________________Avg.Atmospheric Pressure A Guage Pressure 35 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)0 .(p B
Rated Capacity B l.D.2 C Time of Blow (hr)2 .
3h
c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)1 Q.73 D
Constant D Constant .004041 E Total Therms (*
Total Therms Total Therms 0 Per Therm &.q i 3 Ii
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $ci(,%z H.
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNo *AxBxCxD=Therms
AxBxCxD=Therms (A÷B)xCxDxE=Therms lfmorethan500thermssendtoEngineehng
Remarks:(1’O L)s (LL +0 5 -c [r h.cL.6 -
r2
Original:Gas Measurement Submitted By:7
1st Copy:Division Numerical File
2nd Copy Attach to corresponding
documents in division Division Operations Manager_______________________
Form No.ICC 308 (1/06)
ntermountain Gas Company
DIVISION GAS LOSS REPORT
Town /3 0 I DMsion
__________
Date /-/6 -/3
Project No._______________Service No./!/95 /2 Pipe Size Vi “
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes E No How Long 3 )tc 7 ‘1l.No.of Customers
______________
Location &X’IJF,d Ip h /9’.
Report No.t/.i ‘737
Leak Order No.
__________________
Time of Break //5t ,ri
Time Under Control 3
Total Time of Blow 3./2 Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2 fIN 2)6 7 ‘1
Rated Capacity B 1.0.2 C Time of Blow (hr)3 “c
lime of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU fTH/MCF)10.73 D
Constant D Constant .004041 E Total Therms 1 (,pL.*
Total Therms Total Therms Per Therm i//f /
Report blowing relief 2”and larger only Report 4 pipe &larger for 2,000 linear Total Cost $L_4 ).f 0
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesDNoU *AXBXCXD=ThermS
Ax B x C x D =Therms (A +B)x C x D x E Therms If more than 500 therms send to Engineering
Remarks:“i/o k
C-13%,4DTE-s2,339 ht/t é’tv-
—r/7
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:j’%l ‘1?
Division Operations Manager \
Form No.ICC 308 (1/06)
Intermountan Gas Company
DIVISION GAS LOSS REPORT
ReportNo.L/50_,i7qo
Leak Order No.
__________________
Time of Break £4 O
Time Under Control L’.3 j.m.
Total Time of Blow I.7Z H
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 (IN 2)‘s”B
Rated Capacity B l.D.2 C Time of Blow (hr)I’‘7 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)1O 3 D
Constant D Constant .004041 E Total Therms 1.(j *
Total Therms Total Therms 0 Per Therm ‘I “/L—
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $\j 7 t
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNofl *AxBxCxD=Therms
AxBxCxD=Therms (A+B)xCxDxE=Therms If more than 500thermssendto Engineering
Remarks:/-1 11 ü I C
,C L.f/f 9
Original:Gas Measurement
1st Copy:DMslon Numerical File
2nd Copy:Attach to corresponding
documents in division DMsion
Town 0 t S Division
___________
Date -
Project No!/25 ?T5 Service No.
___________
Pipe Size “xi /Y
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes EEl No How Long I Ht.‘I3 i t)9.No.of Customers
Location L/fI Whi snrujirjd teJtttf
,
Submitted By:
Form No.IGC 308 (1/06)
lntermountan Gas Company
DIVISION GAS LOSS REPORT
Report NoL4d /Y7
Leak Order No.—
Time of Break 6,i9 /,ifl_?
Time Under Control 7,’2 A’/t.
Total Time of Blow uk.
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:-
DMsion Operations Manager
Town B/’ib’ó’tvision J4///,Q Date
Project No.__________________Service No.&t4 pipe Size —
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes JJ No How Long
______________
No.of Customers
Location 6’9/N 5e%//,,7-
j
REUEF BLOW GAS LOSS LINE PACK UNE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure L2L5 A
Percent Open A Gauge Pressure B 1.0.2 (IN 2)‘é2.5 B
Rated CapacIty B 1.0.2 C Time of Blow (hr)/‘9 c
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (TH/MCF)/61 .5 D
Constant D Constant .004041 E Total Therms 51’’9,C2LfJ *
Total Therms Total Therms Per Therm “‘/i i ‘2.
Report blowing relief 2”and larger only Report 4”pipe &larger for 2000 linear Total Cost $/f,7,29
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCxDTherms (A÷ B)xCxDxETherms Ifmorethan500thermssendtoEnglneering
Remarks:
Form No.IGC 308 (1/06)
•Town
_______________
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes []No
Location
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division O1ZL /_Date :;?t:•2oi
Service No.
___________
Pipe Size 4 lt
Normal
_____________
Pull Down
_____________________
How Long
______________
No.of Customers
ôg -.M.%-
Report No.6O45i
Leak Order No.
_________________
Time of Break 1 (f W7
Time Under Control f
Total Time of Blow Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure %55 A
Percent Open A Gauge Pressure B l.D.2 (IN 2)é’7c f B
Rated Capacity B l.D.2 C Time of Blow (hr)/7L c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)iô 13 D
Constant D Constant .004041 E Total Therms 2-*
Total Therms Total Therms Pet Therm 7 L/f I Z
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $7 7 4
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD.Therms
Ax B x Cx D =Therms (A +B)x C x Dx E =Therms If mote than 500 therms send to Engineering
Remarks:
%ppj C’-732-
,L -t’
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
________________________________
Division Operations Manager (12_
Form No.ICC 308 (1106)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Division Operations Manaó?7’—
Town (4U441ICk Division Date c”7”/3 Report No.5(9”1/77
Project No.________________Service No.%%t29 Pipe Size Leak Order No.?€7•s5Y?/
Gas Pressure at Time of Break:Normal .%:3-Pull Down lime of Break
Outage:Yes 121 No How Long No.of Customers Time Under Control t2.f..3 /2i_2
Location j4’7gIJ Total Time of Blow______________
(4’9/2ileü ?kQy7
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Bulid Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2(IN 2)//9J B
Rated Capacity B LD.2 C Time of Blow fhr)2/7 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/‘c5 D
Constant D Constant .004041 E Total Therms c2
Total Therms Total Therms 0 Per Them,Vt ‘/_...,
Report blowing relief 2 and larger oniy Report 4”pipe &larger for 2,000 linear Total Cost $4 ‘g
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesUNoU *AxBxCxD.Them,s
Ax B x C x D =Therms (A +B)x Cx D x E =Therms If more than 500 therms send to Engineering
Remarks:
Form No.IGC 308 (1/06)
Town QWS DMsIon
_______
Project No7L//i1)t,L6
____________
Gas Pressure at lime of Break:
Outage:Yes No []
____________
Location e Vi t/
Date I /i Report No/Y)Jt 3
_________________
Leak Order NoE72
________________
Tame of Break %‘/5 /V2-7.
_____________
Time Under Confrol p
Total lime of Blow ,Hrs
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
ntermountain Gas Company
DIVISION GAS LOSS REPORT
Service No.
______________
Pipe Size c:::’c
Normal _Y)Pull Down
___________________
How Long h t.i No.of Customers /
hr Ji/ti
(I
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 (IN 2)4/B
f-’C7%Rated Capacity B l.D.2 C lime of Blow fhr)cJ C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU fTH/MCF)/9..6 D
Constant D Constant .004041 E Total Therms 5 .i..7 *
Total Therms Total Therms Per Therm t74”g/z
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $2—’—f 3.9 L4
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes No *AxBxCxD =Therms
Ax B x C x D Therms (A +B)XC X D x E =Therms If more than 500 therms send to Engineering
Remarks:G
/L
t I 51 rIo 1)
Submifted By:
Division Operations Manager_______________________________
Form No.IGC 308 (1/06)
Town
Project No.________________
Gas Pressure at Time of Break:
Outage:Yes No fl
Location JC2 ‘,
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Leak Order No.-
Time of Break
Time Under Control-
Total Time of Blow
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Division
______________
Date______________________
Service No.31 £7 1’Lf 5 Pipe Size 3/’q “A
Normal
___________
Pull Down__________________
HowLong aHr5.II t’Plifl.No.ofCustomers
___________
Report No.q:)•2 L -céL()
7:op,
2.1?Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2 (IN 2).‘7 5 B
Rated Capacity B ID.2 C Time of Blow (hr)2 1 c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/O 73 D
Constant 0 Constant .004041 E Total Therrns j3O.3 *
Total Therms Total Therms 0 Per Therm /“
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $9 9 9 Z_
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesONo *AxBxCxD.Therms
AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngineering
3/,,IRemarks:f’-/‘1-10 1f’
1+DO Z
17t7
Submitted By:__1vli ‘—Lt_4/A,-L.)
Division Operations Manager
Form No.ICC 308 (1106)
Town e4/,bLILI4DIVSlOfl J1/I,
Project No.6 %5”—&/c7 Service No.
____________
Gas Pressure at Time of Break:Normal ....7 ?
Outage:Yes No Q How Long
______________
Location fle,rna’4<,o /h//
Report No.é5o2 1/7F1
Leak Order No.69e2 597
Time of Break /6 ‘J /9 4
Time Under Control //i57),%
Total Time of Blow Hrs
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Date
________________________
Pipe Size ‘:;:2”,4
Pull Down
_____________________
No.of Customers
fr4
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure______________________Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 2)/f &t’t 0 B
Rated Capacity B I.D.2 C Time of Blow fhr)8 c
Time of Blow C Pipe Length fIn 1,000 ft.)D Avg.BTU (TH/MCF)/6’..5
Constant D Constant .004041 E Total Therrns
Total Therms Total Therms Per Therm ‘Ii ‘/
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $I (0.
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCxD=Therms fAi-B)xCxDxE=Therms Ifmorethan500thermssendtoEngineering
Remarks:,j I’/?6k
(-i?Hnp-’--j2i f(L.{:C&r
Original:Gas Measurement
1st Copy:DMsion Numerical Ale
2nd Copy:Attach to corresponding
documents In dIvision
SubmItted By:
Division Operations
/
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town C dt I Division
______
Date Zo 2013
3/7 A/?)
Project No._________________Service No.-“1 v63 Pipe Size
_____________________
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long
______________
No.of Customers
______________
iS0 AUI &4T)k)4 2AJ diIJe/J
0
Report No.________
Leak Order No.
_______________
Time of Break (0 5
Time Under Control J I ‘.I EE
Total]imeofBlofl’lLfl irs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B ID.2 (IN 2)6,B
Rated Capacity B I.D.2 C Time of Blow (hr)1.3 33 .C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU fTH/MCF)D
Constant D Constant .004041 E Total Therms /L//.qq *
Total Therms Total Therms Per Therm O.%/‘
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $,.c.37
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesQNo *AxBxCxD...Therms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:
Original:Gas Measurement
1 st Copy:DMslon Numerical File
2nd Copy:Attach to corresponding
documents In dMslon
Submitted By:
DMslon Operations Manager_____________________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Division Sfr/iii Date 2?c%/3 Report No%f&’//7
Project No.________________Service No.%%.f’6/Pipe Size .44/,V Leak Order No.‘e?7
Gas Pressure at Time of Break:Normal Pull Down Time of Break /1 r$9
,
Outage:Yes []No [=1 How Long No.of Customers Time Under Control
Location V7 Q 5’//72t2 P,1 .-%Total Time of Blow ]%&Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure .5.5 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)B
Rated Capacity B l.D.2 C Time of Blow (hr)I’)&€)c
Time of Blow C Pipe Length (In 1.000 ft.)D Avg.BTU (TH/MCF),‘c2 i,5 D
Constant D Constant .004041 E Total Therms 7’2 a31It *
Total Therms Total Therms 0 Per Therm ‘/6’!
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/%2’,4’
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes El No El *A x B x C x D =Therms
Ax B x Cx D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Division Operations Manage%
e%dJ
42a L2Ih/
Form No.ICC 308 (1/06)
ntermountain Gas Company
DIVISION GAS LOSS REPORT
Town
_____________
DMsion fr7Q Date QI 5 Report No.__________
1Or\Lø)2 27IProjectNo.__________________Service No.tS öL-’’Q’D f/Pipe Size .Leak Order No.
_________________
Gas Pressure at Time of Break:Normal Pull Down Time of Break
Outage:Yes No How Long
_____________
No.of Customers
______________
Time Under Control tO’246’1
Locafion 2 f I I €i(J I fl4 91,‘Yl VQ&.-Total Time of Blow P1iS’)Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure_____________________Avg.Atmospheric Pressure A Guage Pressure ..55 A
Percent Open A Gauge Pressure B l.D.2 (IN 2).I q3C B
Rated Capacity B l.D.2 C Time of Blow (hr),c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU CH/MCF)Jt 13 D
Constant D Constant .004041 E Total Therms 7 O3 *
Total Therms Total Therms Per Therm 4’/f/cQ
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCxDTherms (A+B)xCxDxETherms lfmorethan 500thermssendtoEngineering
Remarks:
Odginal:Gas Measurement Submitred By:
____________________________________
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in dMslon Division Operations Manager________________________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Thuideait
Project No.__________________
Gas Ptessure at Time of Break:
Outage:Yes [El No
Location JQ/’j ?3 IL/lu)
Division
______________
Date
Service No.2o 4 9 I Pipe Size
Normal 15 Pull Down
How Long c IY i,r7 No.of Customers
[c/-f.
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)—B
Rated Capacity B I.D.2 C Time of Blow (hr)r 3 &c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/0 7 3 D
Constant D Constant .004041 E Total Therms /63 6 O *
Total Therms Total Therms 0 Per Therm —Y //
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $(///
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD.Therms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:)4i:,l ‘
Original:Gas Measurement
let Ccpy Division Numerical Ale
2nd Copy Attach to corresponding
documents in division
Submitted By:-4’y]‘-/j
Division Operations Manager
ReportNo.UI5D I775
Leak Order No.
__________________
Time oIBreak aprri.
Time Under Control /95 pin
Total Time of Blow 3 t’Hrs
Form No.IGC 308 (1/06)
Town h1j
Project No.__________________
Gas Pressure at lime of Break;
Outage:Yes []No
Location c?A!
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division /f347)y7 Date______
Service Pipe Size_______
Normal
____________
Pull Down
_______
How Long
______________
No.of Customers
Report NQ)/
Leak Order No4’)-”
Time of Break_____________
lime Under Control______________
Total lime of Blow ,Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)/4’B
Rated Capacity B f.D.2 C Time of Blow fhr),l.33 c
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (TH/MCF)//2.D D
Constant D Constant .004041 E Total Therms /4t gi:93 *
Total Therms Total Therms 0 Per Therm ,
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNo *AxBxCxD.merms
Ax B x Cx D =Therms (A +B)XC X D x E =Therms If more than 500 therms send to Engineering
Remarks:/214 a%a’/‘zz%%‘
L1LtJ%r 2,%
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:/iL4 ,21,1Léd’
Division Operations Manager
Form No.IGC 308 (1)06)
Intermountain Gas Company
DMSION GAS LOSS REPORT
Town Uij)1c2V i (.1 e)
Project No.7/3 —i2:?
Gas Pressure at Time of Break:
Outage:Yes [2]No [2]
Location
Division
_________
Date ?/i 2-I t2’
Service No.
_____________
Pipe Size
_____________________
Normal
____________
Pull Down___________________
How Long
_____________
No.of CustomersJeYg2,,(
Report No.7)(9-
Leak Order No.7Z —2?
Time of Break 42 ,41t1’.
Time Under Control /%V3 A/1’
Total Time of Blow
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B LD.2 (IN 2)
—B
Rated Capacity B l.D.2 C Time of Blow (hr)2,9 C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTh (TH/MCF)—D
Constant D Constant .004041 E Total Therms Cf.1 4.*
Total Themis Total Therms 0 Per Therm ()44 I a
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $L 7,3 i_I
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoU *AxBxCxD=Therms
Ax B x C x D =Therms (A +B)xC x D x E =Therms If more than 500 therms send to Engineering
Remarks:‘-‘‘‘i”
F/D&€2 13 i&r
Submitted By:
Division Operations Manager________________________
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town k’H tLCk61
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes [J No []
Location Iñ2 1).
Division t.fj k-..Q Date 3 ]3 /3
Service No.‘1 ,7 Pipe Size 3/g’i
Normal Pull Down
___________________
How Long a 2.z1 rIi No.of Customers
flL4&’i2A
Report No./SDcI 7?
Leak Order No.
__________________
1]meofBreak 22,.55 flTh
Ti me Under Control 3 .2,iOpiti
Total Time of Blow Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2).7 2 5 B
Rated Capacity B I.D.2 C Time of Blow fhr).(/5 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)tV’73 D
Constant D Constant .004041 E Total Therms I j/.*
Total Therms Total Therms Per Therm 0 c/i I
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $O..‘3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesONoD *AxBxCxDTherms
AxBxCxD=Therms fA+B)xCxDxE=Therms Ifmorethan500thermssendto Engineering
Remarks:(1 ..I O.Ss 4-0 5/ti”(A.i hui k.._tj.
Original:Gas Measurement
1st Copy Division Numerical File
2nd Copy Attach to corresponding
documents in division
Submitted By:(“J.A41 (.ALLS14 J5.,u—t_.
Division Operations Manager______________________
Form No.IGC 308 (1/06)
Town
Project No.—-1 61
Gas Pressure at lime of Break:
Outage:Yes EJ No 121
Locaon
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Division
Service No.
Normal
How Long
I
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Date_____
______________
Pipe Size________
_____________
Pull Down
_______
No.of Customers
Sce..I
LL\mv.
Report No.D-a17-9
Leak Order No.
_________________
lime of Break I
limeUnderControl 3C ivi
Total lime of Blow 7 3 ttrs
REUEF BLOW GAS LOSS LINE PACK UNE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 56 A
Percent Open A Gauge Pressure B l.D.2 fIN 2)q.B
Rated Capacity B l.D.2 C lime of Blow (hr)7 3 C
lime of Blow C Pipe Length (In 1000 ft.)D Avg.BTU (TH/MCF)10.7 D
Constant 0 Constant .004041 E Total Therms 2.>q.*
Total Therms Total Therms Per Therm Ly />/
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $//.3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNo *AxBxCxD...Therms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:-p’o QQe..
/pfr/g J,2CL
Zc k//
--1--
Submitted By:—1Yi ‘1A
‘
DMsIon Operations Manager____________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Division
Project No.tfi3 1 1 3 3 Service No.
Gas Pressure at Time of Break:Normal
Outage:Yes LI No How Long
LocaUon 133 &
-tk -/.3Date
I I I
______________
Pipe Size 7
6 Pull Down______
a [irs IE)PThfl.No.ofCustomers
ReportNo.qQ I75
Leak Order No.
__________________
Time of Break tt in
Time Under Control ///5 .vti
Total Time of Blow 9.5 Hrs
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 ‘A
Percent Open A Gauge Pressure B l.D.2 fIN 2)/•q B
Rated Capacity B I.D.2 C Time of Blow (hr)2.C
Time of Blow C Pipe Length (In 1,000 ft.)0 Avg.BTU (TH/MCF)/0 7 3 D
Constant D Constant .004041 E Total Therms Z 7 (,*
Total Therms Total Therms 0 Per Therm q /‘/
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $9 5 (i’.L.j ‘
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesENoO *AxBxCxD...Therms
Ax B x C x D =Therms (A ÷ B)x Cx D x E =Therms If more than 500 therms send to Engineering
Remarks:2 “I .3”i-/a I -m fp o F
,p-L.gq 9.,g5p /Q/7
—Ti1-7fr
Submitted By:‘42’7 fQu—c--t_’
Division Operations Manager_____________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
_______________________
Division
______________
Date 3 ‘/
Project No.______________Service No.3 tc9i25 Pipe Size 3/LI’
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long 31 rum.No.of Customers
Location /tnt#i rL I-i /Dr
Report No.c/SO /7
Leak Order No.
__________________
TimeofBreak ‘F!/Pr19
Time Under Control f 9 O P 1?
Total Time of Blow &C Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B ID.2 (IN )7 6 B
Rated Capacity B I.D.2 C Time of Blow (hr)It C C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/0.7 3 D
Constant D Constant .004041 E Total Therms 5 .
)3 *
Total Therms Total Therms 0 Per Therm ‘1 //Z
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $I &‘.c 7
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD...Therms
Ax B xC x D =Therms (A +B)XC X Dx E =Therms It more than 500 therms send to Engineering
Remarks:/t “?“H I C.
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding’
documents in division
Submifted By:
_______________________
Division Operations Mana__?ç)
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town J (1(1 tIc)/1/S Division
_________
Date -Report No.-/
Project No.
________________
Service No.
____________
Pipe Size_____________________Leak Order No.’7i —
Gas Pressure at Time of Break:Normal
______________
Pull Down
_______________________
Time of Break /L7 Of2’)
/;3i
Outage:Yes No How Long No.of Customers Time Under Control 3 9 tjr’7’f
Location J 1//A /(%m%1 ?1.Total Time of Blow____________
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2(IN 2)B
Rated Capacity B 1.0.2 C Time of BIow(hr)),c
Time of Blow C Pipe Length fin 1000 ft.)D Avg.BTU (TH/MCF)—0
Constant 0 Constant E Total Therrns 9 j 3,f
Total Therms Total Therms *Per Therm E4
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $‘“feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesONoD *AXBXCXD.Therms
A x B x C x 0 =Therms *(A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:M iO/Z1 Z %‘14 cQ’1/XtL&-AD%/?frJ./y //
11,‘1U?%1C-1
I-9 31 _)rykA —‘o’5Yb
37fi-I51
Original:Gas Measurement Submitted By:
1st Copy:Division Numerical File /
2nd Copy:Attach to corresponding
documents In division DMsion Operations Manager______________________________________________
Form No.IGC 308 f1)06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Date 3O-/3
Service No.
____________
Pipe Size St d
Normal 55 Pull Down
___________________
How Long ii ‘4 91,9.No.of Customers
_______________
1 2kti--‘%7u)7J
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure_____________________Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 fIN 2)1/.3 ‘B
Rated Capacity B 1.0.2 C Time of Blow (hr)/?6’C
lime of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/0.‘73 D
Constant D Constant .004041 E Total Therms It,!z /3 *
Total Therms Total Therms 0 Per Therm 1//>/
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $44 2 3.1
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesLNoU *AxBxCxD.Therms
AxBxCxD=Therms (A+B)xCxDxETherms lfmorethan500thermssendtoEngineehng
Remarks:
fi0D-ILL?—S,ao2 f7o e rv,a =
c_t-7sL
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy Attach to corresponding
documents In division
DivisionTown
Project No.Ii Ii 3
Gas Pressure at lime of Break:
Outage:Yes [J No Li
Location AJ R1
Report No.V6o—217 /
Leak Order No.
_________________
TimeofBreak__________
Time Under Control M.
Total lime of Blow I 0 Hrs
Submitted By:—171.c_f4 j-Pj-j
Division Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
DMsion (2.p4)k..QTownL(1’UA,.4.cAA)iZL
___________
Date 3 h Ii ‘
Project No.__________________Service No.
______________
Pipe Size 5JL
Gas Pressure at Time of Break:Normal 5S Pull Down
Outage:Yes No fl How Long L.tfr’-i No.of Customers
Location Y—oa-fiA
Report No.C15V tlc?1
Leak Order No.
__________________
T,meofBreak ):L?IIp)%...l
Time Under Control Z-/
TotalTimeofBlow Irs
RELIEF BLOW GAS LOSS LINE PACIC LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2(IN 2)0.2-s B
Rated Capacity B 1.0.2 C Time of Blow (hr)0 .3 (o 7 c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)I 0 73 D
Constant D Constant .004041 E Total Therms ).c../(*
Total Therms Total Therms Per Therm g t I
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $4 3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesflNofl *AxBxCxD=Therms
Ax B XC X 0 =Therms (A +B)x Cx Dx E Therms If more than 500 therms send to Engineering
Remarks:Q ,c t D.S.dLJV iJq “,il-..5d-L)lCJ CJ i
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:fj1L kJ4
Division Operations Manager__________________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
—Division i1lU Date_______________
9’nt 1/
Service No.L,ODIU Pipe Size__________________
______________
Pull Down
__________________________________________________________
Leak Order No.
______________________________________________
Time of Break 9 SO Pwi
______________
No.of Customers
_______________
Time Under Control 3 7O
Li (t%F]C2L l)v ,&t2Iotal lime of Blow t’H
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure ,_55 A
Percent Open A Gauge Pressure B LD.2 (IN 2)O.t3I?B
Rated Capacity B I.D.2 C Time of Blow (hr)ô 6 C
lime of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)13 D
Constant D Constant .004041 E Total Therms .5_f /5 *
Total Therms Total Therms 0 Per Therm (
Report blowing relief 2’and larger only Report 4”pipe &larger for 2000 linear Total Cost $?3.
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoO *AxBxCxD=Therms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:
Original:Gas Measurement
1st Cop Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
Division Operations Manager
Town Yi t
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes []No
Location
Normal
How Long
Report No.6o-g7
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town atdn ety
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes No []
Location r
DMsion
__________
Date ,3 mR 5—13
Serce No.—‘1c?1 Pipe Size “A
Normal 5 Pull Down___________________
How Long 2 t).3 No.of Customers
I 3t,th t
Report No.L/.
Leak Order No.
_________________
Timeof Break l1 pjnt
TimeUnderControl 3’&5 p.m.
TotalTimeofBlow Hrs
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2(IN 2)B
Rated Capacity B ID.2 C Time of Blow (hr)•0 c
lime of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU CTH/MCF)/D.7 D
Constant D Constant .004041 E Total Therms If 7 .3 *
Total Therms Total Therms 0 Per Therm 17 /f I
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $4 ¶1
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoü *AxBxCxD_Therms
AxBxCxDmerms (Al-B)xCxDxETherms lfmorethan500thermssendtoEnglneering
/1 Ii ii
Remarks:/.71 ttük
/-ipf2--zz.C--.’t =-ç7 /j
_9I 7a’—
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:—fyj ‘%iJ7q...c1
Division Operations Manager___________________________
Form No.IGC 308 (1/06)
Town
______________________
Project No.__________________
______________
Gas Pressure at Time of Break:Normal
Outage:Yes No How Long
_____________
Location ..3’Z -ia1%I%i (rI’F..
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure ,A
Percent Open A Gauge Pressure B l.D.(IN 2)•B
Rated Capacity B 1.0.2 C Time of Blow (ht)4 5 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/t1,73 D
Constant D Constant .004041 E Total Therms ‘I g *
Total Therms Total Therms Per Therm J,/f /2
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost $3 •D 7
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes D N0E *AxBxCxD=Therms
AxBxCxD=Therms (A÷B)xCxDxETherms If morethan 500 therms sendto Engineering
Remarks:L1T 4P1..F MLL4ET
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in dMsion
Intermountain 6as Company
DIVISION GAS LOSS REPORT
—Division
________
Date 3-%1 3
Ser4ce No.3 R2572 Pipe Size ‘-&‘
‘
______________
Pull Down
______________________
No.of Customers
?O M
Report No.—J 7
Leak Order No.7g74
lime of Break 2 LI ‘7 Pf’-1
Time Under Control 3
Total lime of Blow ,
Submitted By:[J LU1 V VV
Division Operations Manager________________I
Form No.IGC 308 (1/08)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
__________________
Division
___________
Date 19 —13
Project No._______________Service No.LI 3 LI 25 Pipe Size 3/4
“A
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes JJ No fj How Long ‘/7 mii .No.of Customers
Location 5JS tfJAtJo ///I//J}&.’i
Report No.t/5_Z.I iT OO
Leak Order No.
__________________
TimeofBreak J7
TimeUnderControl /L1 p.,,
Total Time of Blow .7 j Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B l.D.2 fIN 2)7 2 B
Rated Capacity B I.D.2 C Time of Blow (hr)7 ‘c
Time of Blow C Pipe Length fin 1,000 ft.)D Avg.BTU (TH/MCF)/0.7 D
Constant D Constant .004041 E Total Therms 33 *
Total Therms Total Therms 0 Per Therm 9 /8 /Z
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/3 ‘.OC..
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesUNoO *AxBxCxD...Therms
Ax B x C x D =Therms (A +B)xC x Dx E =Therms If more than 500 therms send to Engineering
Remarks:4 S//iti /Qf/1j
Original:Gas Measurement
1st Copy Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:-17’7 ‘1,Q.t,tt7Y
Division Operations Manager
Form No.ICC 308 (1/06)
Town ltttnPa
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes Q No Q
Location 4)Lf IA)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division
____________
Date 119LA 2 S
Service No.U q t-he Size Y
Normal
______________
Pull Down
______________________
How Long
______________
No.of Customers
AVL flñn-C
U
Report No.36O-q575
Leak Order No.
_________________
Time of Break jO
Time Under Control IO Lt&Ø.tby)
Total lime of Blow t2)Hrs
‘WI
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheri Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B ID.2 (IN 2)‘7?c5 B
Rated Capacity B I.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/O ‘Z D
Constant D Constant .004041 E Total Therms /3.3b *
Total Therms Total Therms 0 Per Therm L/f /,7
Report blowing relief 2”and larger only Report 4 pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCx DTherms (A+B)xCxDxE=Therms lfmorethan 500thermssendtoEngineering
Remarks:
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:f ¶o
Division Operations Manager 77._L_i
I
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town J’i Division
_______
Date____________
Project No._______________Service NoJ 2’9-%4?Pipe Size 3/4/
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long /ii—1”No.of Customers /
Locaon 4Ii Al
Report No.’2-/%7
Leak Order No’7-
Time of Break /4 ‘4?41(7,
Time Under Control //“i1 A,f/.
Total lime of Blow ,/7 Hr
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B LD.2(IN 2).7?‘3 B
Rated Capacity B ID.2 C Time of Blow (hr)//‘7 C
Time of Blow C Pipe Length (in 1.000 ft.)D Avg.BTU (TH/MCF)//2 D
Constant D Constant .004041 E Total Therms ,%4 74’7/*
Total Therms Total Therms 0 Per Therm
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesDNoU *AxBxCxD_Therms
Ax B x Cx D =Therms (A +B)x Cx D x E =Therms If more than 500 therms send to Engineering
Remarks:/d/’-d%,)///?/q//21&
I,/
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to correspondIng
documents in division
Submitted By:414/
Division Operations
Form No.ICC 308 (1/06)
Intermountan Gas Company
DIVISION GAS LOSS REPORT
mwn fl\.LA.CkA-’G4f Division Ljo-€.fv Date ,3 /I I 13
Project No.______________SeMceNo.9 Pipe Size l/z IL y
Gas Pressure at Time of Break:Normal 5 5 Pull Down
Outage:Yes [El No How Long ,).()No.of Customers
_______________
LoQation U j 0-CO-I.0(1 fliL4CXy
Report No.g5o —?1?9
Leak Order No.
_________________
TimeofBreak__________
Time Under Control 3 00
Total lime of Blow ,DJ’fliHrs
RELIEF BLOW GAS LOSS UNE PACK LINE RUPTURE!PURGE
Build Up Pressure_______________________Avg.Atmospheric Pressure A Guage Pressure 5 5 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)1%3 B
Rated Capacity B ID.2 C Time of Blow (hr)fl.33 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)1 0 75 o
Constant 0 Constant .004041 E Total Therms 3 05 *
Total Therms Total Therms Per Therm O IL r s”I..
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoD *AxBxCxD=Therms
AxBxCxDTherms (A+B)xCxDxETherms Ifmorethan500thermssendtoEngineedng
Remarks:C9(t Jt)Jc dAL 40 /z /Cit I
Originat Gas Measurement
1st Copy:Division Numerical File
2nd Copy.Attach to corresponding
documents In division
Submitted By:-
Division Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town /a 7ofDlvision 5M’/i,Date 2
Project No._______________Service No.t5ioi..7’%ipe Size ,_y
Gas Pressure at TIme of Break:Normal Pull Down
Outage:Yes EJ No How Long
______________
No.of Customers
_______________
Location II/N/dk)ct 37
Report NO4”i/8
Leak Order No.;‘&-c-’5’::9
Time of Break 3/3 S7)4n?
Time Under Control ‘%‘5Q
Total Time of Blow 7Z fl71,11i Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Ja
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 2 ‘2 A
Percent Open A Gauge Pressure B l.D.2 2).?c2 ta_c B
Rated Capacity B l.D.2 C Time of Blow (lit)/‘‘‘C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/D ..D
Constant D Constant .004041 E TotalTherms t%-”
Total Therms Total Therms Per Therm %c9/cs
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 lInear Total Cost $O 7
feet or more.
Regulator Station No.
Customer Name
is customer billed for lost volume?-
YesNoD *AxBxCxD.Ther
Ax B x Cx D =Therms (A +B)x Cx D x E =Therms If more than 500 therms send to Engineering
Remarks:O/d5-7 S&’i//C
-t.
Submitted By:Za47c
Division Operations Manag ‘/
1
Form No.IGC 308 (1/06)
Mor-’.-jcy
Original:Gas Measurement
1st Copy:DivisIon Numerical Ale
2nd Copy Attach to corresponding
documents In division
1’
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes Li No
Location
—Division
_____________
Date 5 Ic_’1 IL 3
Service No.9 0 ?Pipe Size /q 1%
Normal 5.5 Pull Down
____________________
How Long 5 Y’t’J..r,No.of Customers
______________
Report No.-If 03
Leak Order No.
__________________
Time of Break /
Time Under Control I O.J2-i
TotalrimeofBlow .Sbf”-tf)Hrs
RELIEF BLOW GAS LOSS UNE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)Q B
Rated Capacity B I.D.2 C Time of Blow (hr)0 (3,c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)p 2 5 D
Constant D Constant .004041 E Total Therms 355 ,IS *
Total Therms Total Therms Per Therm g
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost $1 g,s I
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesDNoO *AxBxCxD...Therms
Ax B xC x D =Therms (A +B)x C x D x E =Therms If mote than 500 therms send to Engineering
Remarks:3)q”A I
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
DMslon Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIViSION GAS LOSS REPORT
Town 1JaJt?vra
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes []No []
Location Ip/
Report No.35O%577
Leak Order No.
_________________
Time of Break 442o
Time Under Control 5.io
Total Time of Blow I Hrs
th stcd
b/gj /74O4
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In divIsion
Division Ocih.ea Date_______________
Ij1J V
Service No.y.7C !9 I Pipe Size U f
Normal
_____________
Pull Down
_____________________
How Long
______________
No.of Customers
S.‘twii Snr-i,to
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 65 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)t5.I’?3%’B
Rated Capacity B l.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (TH/MCF)/O 13 D
Constant D Constant .004041 E Total Therrns /1 *
Total Therms Total Therms 0 Per Therm 1./f
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $1*7 77
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes No *AxBxCxD..Therms
AxBxCxDTherms (A+B)xCxDxE=Therms Ifmorethan500thermssendtoEngineenng
Remarks:
Submitted By:fl
Division Operations Manager /__1y_(
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
__________________
DMsion
___________
Date t ‘
Project No._______________Service No.fj/-_(,/3 Pipe Size___________________
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long l37i’14’No.of Customers_____________
Locaon
Report No.-t 4L’44
Leak Order No.ff 7%‘J
Time of Break 1’//-1p
Time Under Control
Total Time of Blow •._,?
ML:k/
..d
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D,2 (IN 2)B
Rated Capacity B I.D.2 C Time of Blow (hr),5’C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU(TH/MCF)](2 7i D
Constant D Constant .004041 E Total Therms t *
Total Therms Total Therms 0 Per Therm t 41 ‘
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $,
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNo *AxBxCxD..merms
Ax B x Cx D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:J 41çAt 1l </O,i#/4 5”*i6 C1/X/
“T’k
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy Attach to corresponding
documents In division Division Operations Manager
Submitted By:
7
Form No.ICC 308 (1/06)
Original:Gas Measurement
1st Copy:DMslon Numerical File
2nd Copy:Attach to corresponding
documents in division
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Service No.
______________
Pipe Size
______________________
Normal
____________
Pull Down
___________________
How Long j “2-Hts No.of Customers_____________
rsi 5 +‘+S Cv0 S
DivisionTown
Project No.2 5-3514
Gas Pressure at Time of Break:
Outage:Yes Q No fl
Location tflCU_N\Un
Date
U-
ReportNo.’t50 I8’I(Q
Leak Order No.
_________________
Time of Break 0 p IT)
Time Under Control 3
Total Time of Blow L 5 0 Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure______________________Avg.Atmospheric Pressure A Guage Pressure ‘5 A
Percent Open A Gauge Pressure B l.D.2f1N 2)3,Ii 7 Y 8 B
Rated Capacity B 1.0.2 C Time of Blow (lw)I’C
Time of Blow C Pipe Length (in 1.000 ft.)D Avg.BTU (TH/MCF)/p.D
Constant D Constant .00404 1 E Total Therms 7 ‘7.L..*
Total Therms Total Therms 0 Per Them,/_/,ft
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $P .)0 ‘
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoE *AxBxCxD=Therms
AxBxCxDTherms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngineering
Remarks:R tr
7)D 95 Q I]?Z.VL
(&/7 -ct<.
Q
Submled By:
_________________________
DMon Operations Manager
Form No.IGC 30B (1/06)
Town (IL14’j
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes E]No t]
Location
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division 9tLJII h.&t?Date_______________
Service No.g4o—’ipe Size
Normal
_____________
Pull Down
_____________________
How Long
_____________
No.of Customers
(QgI M dvk3tivii.
Report No.______________
Leak Order No.
__________________
Time of Break IOtrJ ,4y
Time Under Control j2’ü hi
Total Time of Blow Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)O.T25 B
Rated Capacity B l.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (THIMCF)D
Constant 0 Constant .004041 E Total Therms *
Total Therms Total Therms 0 Per Therm 0.,)Z_‘
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $Ii .]
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNo *AxBxCxD..merms
Ax B x Cx D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:
(W-‘C1 ‘O €)=/37.S
—r1---7 -7 /
Original:Gas Measurement
let Copr Division Numerical Ffle
2nd Copy:Attach to corresponding
documents In division
Submitted By:
DIvision Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
Project No._______________
Gas Pressure at Time of Break:
Outage:Yes No
Location i
—DMsion 5o.J..4D4o-htt._Date
Service No.‘s-525 Pipe Size
Normal 55 Pull Down
_______
How Long No.of Customers
1_.t’I i ReportNo.tLUOtLN5
LeakOrderNo.LtZ-L-j7 4
Time of Break 3 .OO Q’f”
lime Under Control bc ?t.qt
Total Time of Blow ]Hrs
RELIEF BLOW GAS LOSS UNE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 A
Percent Open A Gauge Pressure B l.D.Z (IN 2)().7 5 B
Rated Capacity B I.D.C Time of Blow (hr)C
lime of Blow C Pipe Length (In 1000 ft.)D Avg.BTU (TH/MCF)—D
Constant D Constant .004041 E Total Therms 2(..p.j *
Total Therms Total Therms Per Therm O.-I I f Z.
Report blowing relief 2 and larger only Report 4”pipe &larger for 2000 linear Total Cost $5pLf 2_9
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
Yes jJ No “Ax B x C x D =Therms
Ax B x Cx D =Therms (A +B)x C x Dx E =Therms If more than 500 therms send to Engineering
Remarks:
\JQwLcvta q_/c tpO /rafev)
TL-77-
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
Division Operations Manager
Form No.IGC 308 (1/06)
Report No._________
Leak Order No.
_________________
)0 ?%,4#i
IIb1 A1
Total Time of Blow 5 ill (k I-irs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 (IN 2).2 B
Rated Capacity B I.D.2 C Time of Blow (hr)t S 3 c
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (TH/MCF)It’‘ff5 D
Constant D Constant .004041 E Total Therms *
Total Therms Total Therms 0 Per Therm a t/iI/2
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/.g,t
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesJNoU *AxBxCxD.merms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
Division Operations Manager
&w_/-jj---
Town t ct-I (4r
Project No.________________
Gas Pressure at Time of Break:
Outage:Yes []No
Location
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division
__________
Date %Lol3
AI”7>,A0?7/
Service No.UI t’IU—Pipe Size •t
Normal Pull Down
How Long
______________
No.of Customers
I22 A)t,o sf -i-r
Form No.IGC 308 (7/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town q(4j h g
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes No Li
Location i..4 1 jij,()
Division
___________
Date__________________
Service No.(Pipe Size__________________
Normal ,5’S Pull Down
____________________
How Long 1 No.of Customers I /
11 AfI47
Report No.(/)()i’’/d
Leak Order No./J 71/73
Time of Break
Time Under Control/i,4tl 1
Total Time of Blow .3,çL Hrs
‘J4A )A lv
‘/
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure ,,,5 J A
Percent Open A Gauge Pressure B I.D.2 (IN 2)B
Rated Capacity B l.D.2 C Time of Blow (hr)3 /4 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/0,1 4 D
Constant D Constant .004041 E Total Therms *
Total Therms Total Therms 0 Per Therm 4 t.j 2_
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesLNoU *AxBxCxD.The
Ax B x C x D =Therms (A +B)x C x D x E =Thorns If more than 500 therms send to Engineering
Remarks:3 £t1,L_c4tf Ii v jk c
Ot
Onginat:Gas Measurement
let Copr Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
Division Operations Manager
Form No.IGC 308 (1/06)
Town Jt4Jj,t1f%tL
Project No.S3 J.s ‘13
Gas Pressure at Time of Break:
Outage:Yes []No [J
Location (4-AJ V(AJ
Intermountain Gas Company
DIVISION GAS LOSS REPORT
_______________
Division
_________
Date t.3 Report No./O)iVlK
________________
Service No.
____________
Pipe Size Leak Order No.—Z1Z
Normal
____________
Pull Down____________________Time of Break “itJ j -*1
How Long
______________
No.of Customers Time Under Control
4 Rt %#Pt1 IL..LiA1A/Total ]]me of Blow
-r,jcAtts,ZcI’
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B LD.2 fIN 2)/B
Rated Capacity B CD.2 C Time of Blow (hr)I c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF))i 7 S D
Constant D Constant .004041 E Total Therms I
Total Therms Total Therms 0 Per Therm s q )
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $j’3 3 /I
feet or more.
Regulator Station No.
Customer Name
Is customer biiled for lost volume?
Yes [J No []*Ax B XC X D =Therms
AxBxCxDTherms (A+B)xCxDxETherms lfmorethan500thermssendtoEngineering
Remarks;i3d f +Ad%’M%C
)L
Original:Gas Measurement
1st Copy:DMslon Numerical File
2nd Copy:Attach to corresponding
documents in division
Submlfted By:
________________________________
Division Operations Manager
/
Form No.IGC 308 f1/06)
Inter-mountain Gas Company
DIVISION GAS LOSS REPORT
Report No4s5 —//2/
Leak Order No.?&—577/
Time of Break J,5t9f&4’?
Time Under Control%5 /54 p177,
Total Time of Blow fc1/tL.rs
Remarks:
A
B
C
D
9l9 B
/,v’,.
lO.6 D
3’*
Original:Gas Measurement
fat Copy:Division Numerical File
2nd Copy.Attach to corresponding
documents in division
Submitted By:ZQd
Division Operations
Town i%7/&i&!t?/sion c5ifY//Date
______
Project No.________________Service No.J&3 Pipe Size
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long
______________
No.of Customers
Location %6o rPJ’%P
&/J€a/7 ///,2 4’.
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure
Percent Open
_______________________
Rated Capacity
_______________________
TIme of Blow
___________________
Constant
Total Therms
__________________
Report blowing relief 2 and larger only
A
B
C
AGuagePressure
l.D.2 (IN 2)
Time of Blow (hr)
Avg.BTU (TH/MCF)
Total Therms
0 PerTherm
Total Cost $
Regulator Station No.
Customer Name
Avg.Atmospheric Pressure
Gauge Pressure
l.D.2
______
Pipe Length (in 1,000 ft.)D
Constant .004041 E
Tçtal Therms
________________________
Report 4”pipe &larger for 2,000 linear
feet or more.
(A+B)xCxDxE=Therms
•4//6/
Ff5,9t
Is customer billed for lost volume?
Yes No
Ax B x C x D =Therms
*A x B x C x D =Therms
If more than 500 therms send to Engineering
Form No.IGC 308 f 1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town /1 t’Division
___________
Date -)—y
Project No.________________Service No./c1 7’7 L//Pipe Size ‘i A
Gas Pressure at Time of Break:Normal 56 Pull Down
Outage:Yes No J How Long /t 0 Th ui,No.of Customers
Location C L)
Report No.]&D—1 P2 O
Leak Order No.
__________________
TimeofBreak 7;3,),yi_.
lime Under Control /D’5D sQ i
Total Time of Blow_______________
Original:Gas Measurement
fat Copy:Division Numerical File
2nd Cop Attach to corresponding
documents In dMslon
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 6 6 A
Percent Open A Gauge Pressure B ID.2 (IN 2)7 B
Rated Capacity B LD.2 C lime of Blow fhr)I 3 c
Time of Blow C Pipe Length fIn 1,000 ft.)D Avg.BTU (TH1MCF)I O,7 3 D
Constant D Constant .004041 E Total Therms 3 U 5•7 *
Total Therms Total Therms Per Therm .‘7’)‘I c%
ji.20
Report blowing relief 2’and larger only Report 4 pipe &larger for 2000 linear Total Cost $1 ‘1
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoLl *AxBxCxD=Therms
Ax B xC x D =Therms (A +B)x C x D x E =Therms If mote than 500 therms send to Engineering
Remarks:s/t Cttt in P
)r 19,C $7t1 :t2.
(Z../ç 772 -dc
7(t—
Submiffed By:p
DIvision Operations Manager .\
Form Na.ICC 308 (1/06)
Town -
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes 121 No 121
Location
Intermountain Gas Company
DIVISION GAS LOSS REPORT
_____
Date________
9/7 Pipe Size____________________
Pull Down
________________________
No.of Custome
_______________
?&eS?J/D ,c/__
Report No.5-;f%1/‘G2.
Leak Order No._c5l%:/
Time of Break c&5 7 /3,97,
Time Under Control
_________________
Total Time of Blow Hrs
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy Attach to corresponding
documents In division
Submitted By:
DMsion Operations
,4f,,i,i/Lvision
_______________
Service No.
Normal
How Long
Ii
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B ID.2 (IN 2)•&/5t c76_5 B
•Rated Capacity B ID.2 C Time of Blow (hr)7’o?5 c
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (TH/MCF)/t2 /
Constant D Constant .004041 E Total Therms //,2
Total Therms Total Therms çt Per Therm 477
Report blowing relief 2”and larger only Report 4”pipe &larger for 2000 linear Total Cost $7
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNofl AxBxCxD=Therms
AxBxCxDTherms (A÷B)xCxDxETherms lfmorethan500thermssendtoEngineering
Remarks:
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
__________
Division OLUhtL Date__________Report No.If5 j
_________
Service No.
V
_______________________________
Pipe Size I Leak Order No.
_________________
Normal
____________
Pull Down___________________Time of Break I e21 Psi
How Long
______________
No.of Customers
_______________
Time Under Control
+M I3k I A VQ Total Time of Blow_________
-
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B ID.2 (IN 2)O•/B
Rated Capacity B I.D.2 C Time of Blow fhr)Q 7 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/t 73 D
Constant D Constant .004041 E Total Therms ‘‘9.*
Total Therms Total Therms 0 Per Therm t5.1’/
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $‘7/‘2
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNofl *AxBxCxDTherms
AxBxCxDTherms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngineering
Remarks:
Original:Gas Measurement
1stCopy Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Town
Project No.
_________________
Gas Pressure at Time of Break:
Outage:Yes No
Locatton )2P)Ls iV
Submitted By:/‘:;&_L-e__——-—
Division OpeUons Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town IA-C)
Project No.___________________
Gas Pressure at Time of Break:
Outage:Yes No
Location 3 flI (P
Division
_____________
Date 4 I —/.3
ServiceNo.
__________
PipeSize 3/
“
Normal
___________
Pull Down
__________________
How Long ().No.of Customers
1)liJDnr]lt2 WY]
Report No.-Jbt--I ?3 (7
Leak Order No.
__________________
Time of Break /“3 Pm
lime Under Control ?65 Prr
Total Time of Blow /3 HIS
Original:Gas Measurement
let Copy:DMslon Numerical File
2nd Copy:Attach to cocrespondlng
documents in dMsiori
Submiffed By:
____________________
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 6 A
Percent Open A Gauge Pressure B ID.2 (IN )B
Rated Capacity B l.D.C Time of Blow (hr)1’3 .C
Time of Blow C Pipe Length (In 1.000 ft.)D Avg.BTU (TH/MCF)/t2 D
Constant D Constant .004041 E Total Therms 3 C I ?*
Total Therms Total Therms Per Therm L//J %
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,ODO linear Total Cost $I 5.i3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesONoO *AxBxCxD.Therms
Ax B XC x D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
j
Remarks:7.4//7,)1
DI-i’-i.ceI,Q;Z7.2/Lr
ri —)
)t /L5
Division OperaHons Manager
V.—
Form No.ICC 308 (1/06)
ntermountain Gas Company
DIVISION GAS LOSS REPORT
ReportNo.350 ,5c1
Leak Order No.
__________________
Time of Break /2 /5
Time Under Control 1 34/p
Total Time of Blow .
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)/?3 B
Rated Capacity B i.D.2 C:Time of Blow (hr)C
Time of Blow C Pipe Length (in 1.000 ft.)D Avg.BTU (TH/MCF)‘3 D
Constant D Constant .004041 E Total Therms ?3.4 *
Total Therms Total Therms 0 Per Therm /a
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost 5 37 ‘/7
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoLJ *AxBxCxD-Therms
AxBxCxD Therms (A+B)xCx DxETherms Ifmorethan 500thermssendto Engineering
Remarks:“/c/,a,’itf,-/•//f
Original:Gas Measurement
1st Copy:DMsIon Numerical File
2nd Copy Attach to corresponding
documents In division
Town N/i 2?Dt..)Division OØL1 AQ_-Date 3 -/3
Project No._______________Service No.31./t 7 /37 1 Pipe Size a -V
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes LI No LI How Long flVfl.No.of Customers
Location I-li /LL11c(.
Submitted By:
Division Operations Manager
Form No.IGC 308 (1/06)
%7
//;
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B ID.2(IN 2)-/9c3 B
Rated Capacity B I.D.2 C Time of Blow fhr)/%7 C
Time of Blow C Pipe Length (in 1.000 ft.)D Avg.BTh fTH/MCF)/1.?‘,5 D
Constant D Constant .004041 E Total Therms c3&’/tó *
Total Therms Total Therms 0 Per Therm f “(9_I
Report blowing relief 2”and larger only Report 4”pipe &larger for 2000 linear Total Cost $024f”6’3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes No El *Ax B xC x D =Therms
Ax B x Cx D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:
Gas Measurement
Division Numerical File
Attach to rrespondlng
documents in dMslon
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town DivIsion Date________________Report No.d513,,/
Project No._______________Service No./6&’67fpipe Size ,?J/Leak Order No.I42 -5?Y
Gas Pressure at Time of Break;Normal Pull Down Time of Break —
Outage:Yes No How Long No.of Customers Time Under Control 1 I%I%’/?,ij,
Location 2%’1 ..L9%’,7__Total Time of Blow____________
Original:
1st Copy:
2nd Copy:
Submitted By:
DMslon Operations Manager
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
Project No._______________
Gas Pressure at Time of Break:
Outage:Yes No U
Location
Division
____________
Date /5I 3
Service No.
___________
Pipe Size ‘?“Y
Normal
____________
Pull Down
___________________
How Long /5 17?in.No.of Customers
fl’7(f),ffl77t,7d
Report ND.3s-75q
Leak Order No.
__________________
TimeofBreak /‘65prt
Time Under Control /0 p ivt
Total Time of Blow 5 HrS
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B l.D.2 fIN 2)/9 3 4r B
Rated Capacity B l.D.2 C Time of Blow (hr)2 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTh (TH/MCF)/0.7 3 D
Constant 0 Constant .004041 E Total Therms F.6 &*
Total Therms Total Therms 0 Per Therm U /?)
Report blowing relIef 2°and larger only Report 40 pipe &larger for 2,000 linear Total Cost $1/
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoU *AxBxCxD...Therms
Ax B x Cx D =Therms (A +B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:/L CWi Ii’?
Original:Gas Measurement
lstCopy Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:fl’J ‘f&ixi—)
Division Operations Manager
Form No.ICC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report No.q30 —2 ygq/
Leak Order No.
__________________
lfmeofBreak3o
lime Under Control 3 c1O A/i
Total Time of Blow p )1A-&-ir
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B .D.2(IN 2)
,B
Rated Capacity B I.D.2 C Time of Blow fhr)c
lime of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)lO 7,.S D
Constant D Constant .004041 E Total Therms 3.5,(cY’*
Total Therms Total Therms Per Therm (),C_fftc-i
Report blowing relief 2”and larger only Report 4”pipe &larger for 2000 linear Total Cost $/(
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoIJ *AxBxCxD_Therms
Ax B x C x D =Therms (A ÷ B)x C x D x E =Therms if more than 500 therms send to Engineering
Remarks:L2a ipSc 2Lu -t /‘4 t—h
Original:Gas Measurement
1st Copy:Division Numerical flle
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Division Operations Manager
Town (hA.,L OUV.DMsion
___________
Date
Project No.__________________Service No.
______________
Pipe Size
______________________
Gas Pressure at Time of Break:Normal 55 Pull Down
Outage:Yes No How Long .5 No.of Customers
_______________
Location j 1
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
_______
Date___________
L9 t9 Pipe Size “a’
__________
Pull Down
________________
)1fl j fl No.of Customers
Report No.____________
Leak Order No.
_________________
TimeofBreak 1O;H
TimeUnderControl 10’//
Total Time of Blow Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 ‘5 A
Percent Open A Gauge Pressure B l.D.2 (IN 9 I B
Rated Capacity B I.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (H/MCF)/0 D
Constant D Constant .004041 E Total Therms .8’6 *
Total Therms Total Therms 0 Per Therm -9 /‘/
qcReportblowingrelief2andlargeronlyReport4pipe&larger for 2,000 linear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-V
YesONo *AxBxCxD...Therms
AxBxCxDTherms (A+B)xCxDxE Therms Ifmorethan500thermssendtoEnglneerlng
Remarks:
II 4;vp
Original:Gas Measurement
lstCopy DIvision Numerical File
2nd Copy:Attach to corresponding
documents In division
Town Division
Project No._________________Service No.
Gas Pressure at Time of Break:Normal
Outage:Yes No How Long
Location AL tndi
Submitted By:
V
4
Division OpeUons Manager________________________
Form No.IGC 308 (1106)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report NoJ -Jtt2
Leak Order No.‘7;
Time of Break -/C 2/%7.
Time Under Control 5iô
Total Time of Blow /
Original:Gas Measurement
1st Copy Division Numerical File
2nd Copy.Attach to corresponding
documents in division
Town
___________
Division
________
Date )-)‘
Project No.
_________________
Service No.
_____________
Pipe Size c’?
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes JJ No fl How Long No.of Customers
Location
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)7,f”)B
Rated Capacity B I.D.C Time of Blow fhr)/%3 c
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (TH/MCF)/?,D
Constant D Constant E TotaiTherms 77d1-61
Total Therms *Total Therms *Per Therm .
Report biowing relief 2 and larger only Report 4 pipe &larger for 2,000 lInear Total Cost $3 Z C
V feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes LINGO *AXBXCXD._Therms
*A x B x C x D =Therms *(A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:(A/LL%’th//Q”14 ,4i74))i L’rJ
fl,IL M7
ii :Ja 1)//7 L72t%)
lJyi&i Jv/
I0
V
L45z 44.s/,
‘.I C
C 1C57
175.z ‘/‘g,-10
Submifted By:
Division Operations
(1
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town mp a—’
Project No.___________________
Gas Pressure at Time of Break:
Outage:Yes [J No El
Location
Division
_____________
Date U —/3
Service No./o/t,?-37 I Pipe Size
/q
“y
Normal Pull Down____________________
How Long
______________
No.of Customers
Lüuct tr
ReportNo.3’Cl95_
Leak Order No.
_________________
lime of Break 3:0
Time Under Control 3 ‘10 Pn’,
Total Time of Blow Q 7 Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B LD.2 (IN )‘B
Rated Capacity B ID.2 C lime of Blow (hr)T c
Time of Blow C Pipe Length fin 1000 ft.)D Avg.BTU (THIMCF)/..73 D
Constant D Constant .004041 E Total Therms ‘/ø /O *
Total Therms Total Therms 0 Per Therm q I /
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $//‘7 I
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesUNo *AxBxCxD.Therms
AxBxCxDTherms fA+B)xCxDxETherms lfmorethan500thermssendtoEngineering
Remarks:
Original:Gas Measurement
lstCopy Division Numerical File
2nd Copy.Attach to corresponding
documents In division
SubmItted By:
DM&on Operations Manager
Form No.IGC 308 (1/06)
Town
__________
Project Service No.
Gas Pressure at Time of Break:Normal
Outage:Yes []No El
Location /?)/-;
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report N1(X)/(
Leak Order No7’)_-
lime of Break ,£2?,/ii’Vl.
Time Under Control //I21.
Total Time of Blow gf5)
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE /PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
PercentOpen A GaugePressure B l.D.2flN 2)B
Rated Capacity B l.D.2 C lime of Blow (hr)i C
lime of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU fTH/MCF)/9 D
Constant D Constant E Total Therms L/Z C I
Total Therms *Total Therms *0 Per Therm
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $1 7 5
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YeSElNOO *AXBXCXD..Therms
*A x B x C x D =Therms *(A +B)XC X Dx E =Therms If more than 500 therms send to Engineering
NtZ,zt/977 114.Z /hr
/s z’io —OK
R/—C 4—-‘/L—L_.
-it,
Submlfted By:t’Z’idi7 A2/11zez2
Division
________
Date If ii
______________
Pipe Size L7
____________
Pull Down
How Long
______________
1 .
No.of Customers
(I
Remarks:4Jjf -iYM
OrigInal:
1 St Copy:
2nd Copy:
Gas Measurement
DMslon Numerical File
Attach to corresponding
documents in division
S
______
Division Operations Manager________________________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town (13/DMsion ().+t,’y’i Date )—/..)Report No.q50
Project No._________________Service No.79 3 L/Pipe Size 3)q ‘/Leak Order No.
Gas Pressure at Time of Break:Normal 55 Pull Down Time of Break 9 ‘5 ‘I&n-i
Outage:Yes No []How Long ,t4L).j’iiJ,Th No.of Customers I Time Under Control 9 .J,cA_-,
Location I 9 P-y3r9/-e_C’,VtQJ-Total Time of Blow ,
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2(IN 2)3 .7 -—.5 B
Rated Capacity B ID.2 C Time Of Blow (hr)0 7 33 c
Time of Blow C Pipe Length fin 1000 ft.)D Avg.BTU (TH/MCF)j (,73 D
Constant D Constant .004041 E Total Therms 5 Cf *
Total Therms Total Therms Per Therm 0 Y /1/
Report blowing relief 2’and larger only Report 4•’pipe &larger for 2,000 linear Total Cost $/,3 .(
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoU *AxBxCxD=Therms
AxBxCxD=Therms (A+B)xCxDxEmerms lfmorethan500thermssendtoEnglneering
Remarks:c I J5 oU-p +n 3 /Q--I’fr
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to correspondIng
documents in division
Submitted By:
I,—.
0M
Division Operations Manager (‘S
Form No.IOC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
5 J3
II ‘I‘a Y
ReportNo.36:—,1,03..
Leak Order No.
__________________
lime of Break to :/pF,
lime Under Control 0
ThtaiTimeofBlow SO Hrs
RELIEF BLOW GAS Loss LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B I.D.2 (IN 2).I 3 6 B
Rated Capacity B I.D.2 C lime of Blow (hr)‘6 C
lime of Blow C Pipe Length fIn 1,000 ft.)D Avg.BTU fTH/MCF)/L 7 3 D
Constant D Constant .004041 E Total Tharms 5 le /3 *
Total Therms Total Therms 0 Per Therm ‘1 /8’/
Report blowing relief 2’and larger only Report 4’pipe &larger for 2,000 lInear Total Cost $3.?7
feet or more.
Regulator Station No.
Customer Name
Is customer bIlled for lost volume?-
YesNo *AxBxCxD=Therms
Ax B x Cx D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:5/t_ei€t-
tI
Originat Gas Measurement
1st Copy:DMsloti Numerical File
2nd Copy:Attach to corresponding
documents In UMsion
Town fli PL4._Division
___________
Date
Project No.________________Service No.3s b 7—3?/Pipe Size
Gas Pressure at Time of Break:Normal 55 Pull Down —
Outage:Yes [21 No How Long 9 m ir.No.of Customers
Location 1/5’]to P iv?D t.
Submitted By:1’Y1 ‘1j1,t-t_-’
Division Operations Manager
Form No.IGC 308 (1/06)
Town
Project No.___________________
Gas Pressure at Time of Break:
Outage:Yes No
Location 3 c 17 i]
Intermountain Gas Company
DIVISION GAS LOSS REPORT
DMslon
____________
Date 5-3 /
Service No.37I1 ‘I 5 Pipe Size 3/[
Normal
____________
Pull Down
___________________
How Long /p /7j No.of Customers
)i )/J 1(i)-vip]Pd
Report No.O-/&‘5 7
Leak Order No.
_________________
Time of Break 1!.?;3/PilL
Time Under Control /U Pin
Total Time of Blow q Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 A
Percent Open A Gauge Pressure B l.D.2 2)7 5 B
Rated Capacity B l.D.2 C Time of Blow (hr)“‘13 c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/0’7 3 D
Constant D Constant .004041 E Total Therms /?3 .‘3 21 *
Total Therms Total Therms 0 Per Therm ‘I I I
Report blowing relief 2 and larger only Report 4”pipe &larger for 2000 linear Total Cost $7
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCxD=Therms fA+B)xCxDxE=Therms If morethan 500thermssend to Engineering
Remarks:S/L (ttt tklttii
Original;Gas Measurement
1st Copy Division Numerical File
2nd Copy Attach to correspondIng
documents In dIvision
Submitted By:1Y)f 7j
Division Operations Manager \\
Form No.IGC 308 (1/06)
Town 14m fl4CIU
Project No.___________________
Gas Pressure at Time of Break:
Outage:Yes No Q
Location
Intermountain Gas Company
DIVISION GAS LOSS REPORT
—Division 74ryi Date /%t //
Service NoL’/29 Pipe Size //
Normal 6 Pull Down
______________
How Long No.of Customers
Report N%9/%2
Leak Order
Time of Break 7/4t6AF1
Time Under Control /c .Oifl
Total J]me of Blow
,
7/
H,s
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B ID.2 fIN 2)B
Rated Capacity B l.D.2 C Time of Blow fhr)i C
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (TH/MCF)Ji).y D
Constant D Constant .004041 E Total Therms c?4’2 *
Total Therms Total Therms 0 Per Therm
Report blowing relief 2”and larger only Report 4”pIpe &larger for 2,000 lInear Total Cost $/I9,
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD...Therms
Ax B x Cx 0 =Therms (A ÷ B)XC X Dx E =Therms If more than 500 therms send to Engineering
Remarks:1S%’a/%/%a/’•7’1 2M1/
/
Original:Gas Measurement
1st Copy.Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submifted By:ik 3,zJL/
DMslon Operations Manager_________________________________________
Form No.IGC 308 f1/06)
Town57±A4
Project No.___________________
Gas Pressure at Time of Break:
Outage:Yes []No []
Location
Intermountan Gas Company
DIVISION GAS LOSS REPORT
DMsion /7)77 Date 3
Service No.‘1Pipe Size_______________
Normal
____________
Pull Down___________________
How Long
______________
No.of Customers
/L)/i-
Report No2//,4/
Leak Order No.Q)‘44
Time of Break //4/2’?
Time Under Control
Total Time of Blow /,b)HIS
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 fIN Z)/9 B
Rated Capacity B I.D.2 C lime of Blow fht)f C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/72 4€9 D
Constant D Constant .004041 E Total Therms /.94 2.-5 *
Total Therms Total Therms 0 Per Therm
Report blowing relief 2”and larger only Report 4”pIpe &larger for 2,000 lInear Total Cost $
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesUNDO *AxBxCxD...Therms
AxBxCxDTherms (A+B)xCxDxETherms lfmorethan500thermssendtoEngineedng
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Remarks:4}JiW%///7 zZZ’7J
/zj9 &rniL
Division Operations Manager____________________________
Form No.IGC 308(1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Q’a-l
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes No Q
Location t tv’
ReportNo.Y ‘C
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B ID.2 (IN 2)1 3 IP B
Rated Capacity B l.D.2 C Time of Blow (hr)‘L”‘3 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)/Oi 7 3 D
Constant D Constant .004041 E Total Therms ‘7?c *
Total Therms Total Therms 0 Per Therm ,‘I I ?I
Report blowing relief 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost $3 .&3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesUNo *AxBxCxDTherms
AxBxCxD=Therms (A+B)xCxDxE=Therms Ifmorethan500thermssendtoEnginéedng
Remarks:s/c..i%E
6’
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:
Division Operations Manager
—Division
______________
Date
Service No.5 Pipe Size____________
Normal
____________
Pull Down
____________
How Long j 1 111 ill.No.of Customers
Leak Order No.
__________________
Time of Break /€39 4 -t,
Time Under Control 1/-’1)c ii-’
Total Time of Blow R’3 Hrs
Form No.ICC 308 (1/06)
Original:Gas Measurement
1st Copy:DMsion Numerical File
2nd Copy:Attach to corresponding
documents In division
Report No.6o’-‘5/’
Leak Order No.______________
Time of Break 7/,FI4i2”
Time Under Control /
Total Time of Blow______________
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town /‘f,7’/%‘Divislon 45/44 Date -
Project No._________________Service No./9,7Y””Pipe Size
Gas Pressure at Time of Break:Normal s.53’Pull Down -
Outage:Yes No [J How Long
_____________
No.of Customers
Location SO hgt2,5 I1/
i’t2”fr’
V
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 2)•‘3 B
Rated Capacity B l.D.2 C Time of Blow (hr)-%.i’‘%3 C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (THIMCF)/-D
Constant D Constant .004041 E Total Therms 5p /c/’*
Total Therms Total Therms 0 Per Therm /‘.9/
Report blowing relief 2”and larger only Report 4’pipe &larger for 2,000 linear Total Cost $1fo?,c5
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesONo *AxBxCxD=Therms
AxBxCxD=Therms (A+B)xCxDxE=Therms Ifmorethan 500thermssendtoEngineering
Remarks:
Submitted By:-<L21Y2 %t
Division Operations Manag ?Qfr_2)1h1ri,v’Y,
C /I,
Form No.ICC 308 (1/06)
Town t DMsion
Intermountain Gas Company
DMSJON GAS LOSS REPORT
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure____________________Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)/‘7 .?t 5
Rated Capacity B ID.2 C Time of Blow (hr)‘
‘‘C
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (TH/MCF)S D
Constant D Constant .004041 E Total Therms -/*
Total Therms Total Therms 0 Per Therm J /r /
Report blowing relief 2 and larger only Report 4”pipe &larger for 2,000 linear Total Cost $3 I.?
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNo *AxBxCxD.Therms
AxBxCxDTherms (A+B)xCxDxE=Therms Ifmorethan 500thermssendtoEngineenng
II I’1/(
Remarks:“8’//,o le..
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in dMsion
Date 5—-—J3
II II
Project No._______________Service No.)6’?b -2 7 I Pipe Size “o?Y
Gas Pressure at Time of Break:Normal 56 Pull Down
Outage:Yes D No Q How Long L/1 IV7Ii1.No.of Customers
Location /,3 NW 2YI-d S1
ReportNo.35O(D5
Leak Order No.,
Time of Break
Time Under Control
Total Time of Blow
/,•5_v Pm
35 Phi
Hrs
Submitted By:1”7
Dision Operations Manager_________________________________
Form No.IGC 308 (1)06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report No.35O-ID D 7
Leak Order No.
_________________
Timeof Break f :7 p,
Time Under Control I 12fr1
Total Time of Blow ,/7 H
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B ID.2 2)/B
Rated Capacity B l.D,2 C Time of Blow (hr)/7 C
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (TH/MCF)10 7 3 D
Constant D Constant .004041 E Total Therms I c7 /*
Total Therms Total Thorms 0 Per Therm L//,
Report blowing relIef 2’and larger only Report 4”pipe &larger for 2,000 linear Total Cost $?
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes No fl Ax B x Cx D =Therms
Ax B xC x D =Therms (A +B)x C x Dx E =Therms If more than 500 therms send to Engineering
Remarks:V /..Th S/L
Original:Gas Measurement
1st Copy:DMsion Numerical File
2nd Copy:Attach to corresponding
documents In division
Town I7/tL r DMslon
___________
Date
Project No.__________________Service No.1117 —.7 /Pipe Size —
Gas Pressure at Time of Break:Normal 5 5 Pull Down
Outage:Yes No How Long /7 m ff7 .No.of Customers
Locatton /u/L NW I1i (ç7L.
1/Ii7;’Y
Submitted By:__-tv1 ‘1 J_’1%”t-’
Division Operations Manager___________
Form No.IGC 308 (1106)
Intermountain Gas Company
DMSION GAS LOSS REPORT
Town 1)1 ce Division
____________
Date 5-13 —1 3
ii,3,
Project No._______________Service No.-]5 Pipe Size /
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No Q How Long 3 Q fl ir.No.of Customers
_____________
Location O I ,-ç .-e 1-
ReportNo.%”S19 ILt
Leak Order No.
__________________
Time of Break /“/5 P17-)
Time Under Control J Y p ni
Total Time of Blow
RELiEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure______________________Avg.Atmospheric Pressure A Guage Pressure ‘5’5 A
Percent Open A Gauge Pressure B ID.2(IN 2)7 ‘5 B
Rated Capacity B l.D.2 C Time of Blow fhr)‘C
Time of Blow C Pipe Lengthfin 1,000 ft.)D Avg.BTU (TH/MCF)/0.‘7 3 D
Constant D Constant .004041 E Total Therms 1 3,/*
Total Therms Total Therms 0 Per Therm 7’1 /
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $‘7’
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesflNoO *AxBxCxD=Therms
AxBxCxDTherms (A+B)xCxDxETherms lfmorethan500thermssendtoEngineering
Remarks:t /1,7 //ti-
Original:Gas Measurement
1st Copy:DivisIon Numerical File
2nd Copy Attach to corresponding
documents in dMsion
Submitted By:—1’)’7 L7
DMslon Operations Manager
S
Form No.IGC 308 (1/06)
Town fJ W Division 4JfTOOT1-t Date 5l Li -
Project No._____________Service No.39-5j7 Pipe Size_________________
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long g Z5 No.of Customers q
Location 3O EA-r 4i c-
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure_____________________Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)Z5 B
Rated Capacity B l.D.2 C Time of Blow (hr)3 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)[O ,7 3 D
Constant D Constant .004041 E Total Therms I •S *
Total Therms Total Therms 0 Per Therm 4 1 ‘I Z
Report blowing relief 2”and larger only Report 4”pipe &larger for 2000 linear Total Cost $L4 .]3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNofl *AxBxCxD=Therms
Ax B x Cx D =Therms (A +B)x C x Dx E =Therms If more than 500 therms send to Engineering
Remarks:L45t \(‘5 (J I I XLJc .J Aô ft PLA.LLb
L)ti ir1YY1 lTtN —l-t-Y
Original:Gas Measurement
1st Copy:DMsion Numerical File
2nd Copy:Attach to corresponding
documents in dMsion
Submitted By:
_______________________
DMsion Operations Manager_____________
______________
ntermoUntain Gas Company
DIVISION GAS LOSS REPORT
Report No.(Ot)-/411
Leak Order No.7L/7
Time of Break ¶A Wi
Time Under Control j 14 M
Total Time of Blow I 3 -irs
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
________________
Division 5As-oun-Date 5-21-2Ot3
Project No.______________Service No.O5Z-57 Pipe Size M STE L
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long
______________
No.of Customers
Location a 20 E Av E,3è iz M
ReportNo.pO—Iz-l5t
Leak Order No.(3Q-75I I
Time of Break Q’?PM
Time Under Control 3 Z PM
Total lime of Blow Hr
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure_____________________Avg.Atmospheric Pressure A Guage Pressure 3Q A
Percent Open A Gauge Pressure B l.D.2 (IN 2)•5 25 B
RatedCapadty B l.D.2 C TimeofBlow(hr)C
lime of Blow C Pipe Length (in 7.000 ft.)D Avg.BTU (TH/MCF)I c.7 3 D
Constant D Constant .004041 E Total Therms 3 L{J..*
Total Therms Total Therms Per Therm •Lj I I 2
Report blowing relief 2’and larger only Report 4’pipe &larger for 2,000 linear Total Cost $I 2...33
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesflNofl *AxBxCxD.Therms
AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngfneering
Remarks:fE 3,1k-i
Original:Gas Measurement
let Copy Division Numerical File
2nd Copy Attach to corresponding
documents In dMsion
Submitted By:VEV1 i T)LARM
Division Operations Manager________________________________
Form No.IGC 308 f1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
,‘5-/,—13
/1 ii‘a Y
Report No.35C ?/‘1
Leak Order No.
__________________
TimeofBreak___________
Time UnderControl /‘‘/‘1 4
Total Time of Blow 7 7 Hrs
RELIEF BLOWGAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 fIN 2)•/‘3 B
Rated Capacity B ID.2 C Time of Blow (hr)7 ‘7 c
lime of Blow C Pipe Length (In 1000 ft.)D Avg.BTU (TH/MCF)/‘‘7 D
Constant D Constant .004041 E Total Therms ?‘7’‘7 *
Total Therms Total Therms 0 Per Therm ‘>/
Report blowing relief 2’and larger only Report 4”pIpe &larger for 2,000 linear Total Cost $J&-7 ‘
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes fl NoO *AxBxCxDTherms
Ax B x Cx D =Therms (A ÷ B)x Cx Dx E =Therms If more than 500 therms send to Engineering
Remarks:/a “ffô/1i S/L
Original:Gas Measurement
1st Copy.Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:72’7 ‘-1
Division Operations Manager___________________________
Town 1Thtt7 Division
___________
Date,
Project No._______________Service No.3t /-3 Pipe Size
Gas Pressure at lime of Break:Normal 56 Pull Down —
Outage:Yes No How Long ‘1/I WI Jfl No.of Customers
Locaon I LU/I 4/d
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town ({/LhL)€LLS Division tbfr)fl Date___________
Project No.
________________
Service No./)’24/’2/_74</Pipe Size_____________________
Gas Pressure at Time of Break:Normal .3 Z Pull Down
Outage:Yes No How Long
______________
No.of Customers
Location J7¼!/.
Report N!’2 i%?5
Leak Order No.’”5’9 —
Time of Break g,1om
/
Time Under Control j3,c’71
Total lime of Blow_______________
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2(IN 2),B
Rated Capacity B l.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)7/2.D
Constant D Constant E Total Therms
Total Therms *Total Therms *C Per Therm
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $%tD.‘/
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNo *AxBxCxD...Therms
*A x B x C x D =Therms *(A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy Attach to corresponding
documents In division
Submitted By:J/%//m
Division Operations Manager /
Remarks:/%2%/4.S4/zJJ 7 4?4f<///p/1
F
Form No.IGC 308 (1/06)
Town
Project No.
___________________
Gas Pressure at Time of Break:
Outage:Yes No [ZJ
Location \Eck{
Division
Service No.
Normal
How Long
(ti
Intermountain Gas Company
DIVISION GAS LOSS REPORT
A
B
C
D
Remarks:I ‘IIiiI?
A
3.(,’7qg’B
.“C
,c1c3 D
I(*
.j/F/2
43 Lfl 22—
DDz 95 31Z7,c ‘I1 -iL
£/-,—?ok
Original.Gas Measurement
1st Copy.Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:‘1Y1
Division Operations Manager________________________
______________
Date
V?I73I7 Pipesize “‘1
____________
Pull Down__________
5 mfl.No.of Customers
ReportNo.3O 9toi7
Leak Order No.
_________________
TimeofBreak 0-fl,
Time Under Control 1 0 0 ‘yij
Total Time of Blow -99 irs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure
Percent Open
_______________________
Rated Capacity
_______________________
Time of Blow
_____________________
Constant
Total Therms
______________________
Report blowing relief 2’and larger only
A
B
5%
C
Guage Pressure
!.D.2(IN 2)
lime of Blow (hr)
Avg.BTh (TH!MCF)
Total Therms
PerTherm
Total Cost $
Regulator Station No.
Customer Name
Avg.Atmospheric Pressure
Gauge Pressure
I.D.2
______
Pipe Length (in 1000 ft.)D
Constant .004041 E
Total Therms
_________________________
Report 4”pipe &larger for 2,000 linear
feet or more.
(A+B)xCxDxETherms
Is customer billed for lost volume?
Yes No
Ax B x C x D =Therms
*A x B x Cx D =Therms
If more than 500 therms send to Engineering
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Division
Project No._________________Service No.
Gas Pressure at Time of Break:Normal
Outage:Yes [J No Li How Long
Location 791 c Vu
Date 6-i-i
_________
Pipe Size
5.5 Pull Down
3’4 (fl y).No.of Customers
1]I’t y
Report No1//L
c7,
Leak Order No.
__________________
TimeofBreak /D’/I
Time UnderControl )//5 p n.
Total Time of Blow •57 Hrs
REUEF BLOW GAS LOSS UNE PACK LINE RUPTURE I PURGE
Build Up Pressure_____________________Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)/3 “B
Rated Capacity B ID.2 C Time of Blow (hr)57 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU CTH/MCF)/0 7 3 D
Constant D Constant .004041 E Total Therms t”5./*
Total Therms Total Therms 0 Per Therm
Report blowing relief?and larger only -Report 4”pipe &larger for 2,000 linear Total Cost $7 3
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoU *AxBxCxDTherms
AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngineedng
Remarks:
Original:Gas Measurement
1st Copy:DMslon Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:1’1 11.-frtt._1
DMsion Operations Manager
Form No.IGC 308 (1/06)
Town
__________
Project No.
___________________
Gas Pressure at lime of Break:
Outage:Yes No
Location /d1’i&t
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division
________
Date__________
Service No.20 Pipe Size____________
Normal
____________
Pull Down______________
How Long No.of Customers
Report No.’%2 7;q4i
Leak Order No.I1
Time of Break 2
Time Under Control //).j3),%4’2.
Total Time of Blow ,
RELIEF BLOW GAS LOSS UNE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)/473x B
Rated Capacity B l.D.2 C Time of Blow (hr)•C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (THIMCF)/D
Constant D Constant E Total Therms
Total Therrns *Total Therms *Pet Therm ,
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $7
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
Yes Noü *AxBxCxDThes
*A x B x C x D =Therms *(A .i-B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:/—%-/%LE 7Z44 4i’
Original:Gas Measurement
1st Copy Division Numerical File
2nd Copy Attach to corresponding
documents in division
T
Submifled By:7/
DMslon Opemtions
Form No.IGC 308 (1/06)
ntermountain Gas Company
DIVISION GAS LOSS REPORT
Town t_!q t &DMsIon
,1_—)1 c:Project No.--)/—LI i Service No.
Gas Pressure at Time of Break:Normal
Outage:Yes [J No How Long
Location
Date_______
______________
Pipe Size V
55 Pull Down_______
1 Hr.l9 mill.No.of Customers
Dr
Report No./)5
Leak Order No.
__________________
TimeofBreak 7.4/7
Time Under Control ‘3 5 /J T’fr)
TotalTimeof Blow I’?O i-irs
Original:Gas Measurement
I at Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In dMslon
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 (IN 2)3.7 /?B
Rated Capacity B I.D.2 C Time of Blow fhr)I’>C
lime of Blow C Pipe Length (In 1.000 ft.)D Avg.BTU (THIMCF)I0 7 3 D
Constant D Constant .004041 V E Total Therms 2..2—.Lj
...
*
Total Therms Total Therms Per Therm J /?I Zi
A•I i i (3Reportblowingrelief2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $‘I I I —
feet or mote.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesUNo *AxBxCxD.Therms
Ax B XC X D =Therms (A +B)xC x Dx E =Therms If mote than 500 therms send to Engineering
Remarks:/lj
V
DD=O5,(‘325,Q I6i k/
V
R/5 ]12%.
/L
U U
Submitted By:‘1Y ‘-1 ,2
DMsion Operations Manager____________________
Form No.IGC 308 (1106)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report No.I )7
Leak Order No.
_______________
Time of Break c 4/jY
Time Under Control /6 .3 Pm
TotalTimeofBlow_____________
.RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B l.D.2 (IN 2)7 B
Rated Capacity B ID.2 C Time of Blow (hr)9 ‘C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)I ‘7 D
Constant D Constant .004041 E Total Therms Z I I *
Total Therms Total Therms 0 Per Therm ‘]I >/—‘
4
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $—
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YeSUNoL *AxBxCxD...Therms
AxBxCxD=Therms fA+5)xCxDxETherms Ifmorethan500thermssendtoEngineerlng
Remarks:‘4t //ot(1ø-j
-i2-,83 rV
Original:Gas Measurement
fat Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:-
Division Operations Manager
Town J3AE.I DMslon
____________
Date
/_riJit1 ,-.4/“Project No._______________Service No.I (1 ‘lIP D Pipe Size_____________
Gas Pressure at Time of Break:Normal 56 Pull Down
Outage:Yes No How Long Ikf ?‘Y /1i1 No.of Customers
Location 315 (TuiL/k&
Form No.ICC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes No LI
Location J 3 i
7-13Division
______________
Date,
Service No.‘19-3)7 Pipe Size
Normal
____________
Pull Down
How Long )Yljn.No.of Customers
Ptid t
Report No.35 ?‘
Leak Order No.
__________________
TimeofBreak
Time Under Control 3 /6 Pi’t-’
Total Time of Blow -(I’Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 (IN 2)7 B
Rated Capacity B I.D.2 C Time of Blow (hr)t r C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTh (TH!MCF)D
Constant D Constant .004041 E Total Therms (2 ‘‘•‘/*
Total Therms Total Therms 0 Per Therm L//?/p2..
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $/a ..
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesflNoO *AXBXCXD.ThermS
AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssend to Engineering
Remarks:5/L-&.t IAI
Original:Gas Measurement
1st Copy:Division Numerical Ffle
2nd Copy:Attach to corresponding
documents in division
Submitted By:1’Y)A-fItJ
Division Operations Manager_________________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town J3oA’,Q_c)
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes [j No
Locaon 38a3 t)
—Division
____________
Date —
/
Service No.2cpipe Size ,j?
Normal 5’5 Pull Down
_______________
How Long (fl//No.of Customers
U?t1
Report No.‘/50-.)/2j
Leak Order No.
__________________
Time of Break______________
Time Under Control /?‘30 pm
Total Time of Blow HYS
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2f1N 2)./?B
Rated Capacity B ID.2 C Time of Blow (hr)t’7 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)1 D
Constant D Constant .004041 E Total Therms 7 ‘7.b *
Total Therms Total Therms 0 Per Therm //1 /
Report blowing relief 2”and larger only Report 4 pipe &larger for 2,000 linear Total Cost $3 .‘1 £
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesDNoU *AxBXCXD=Therms
AxBxCxD =Therms fA+B)xCxDxE=Therms lfmorethan500thermssendtoEnginêering
Remarks:S/t e%ct V7 JLLIJr’
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:‘—IV)L1a4,I,,&J.t_)
Division Operations Manager___________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
Project No.__________________
Gas Pressure at Time of Break:
Outage:Yes []No D
Location c’3 Al
DMsion
___________
Date hit/oIl 3
Selce No./3)Pipe Size____________________
Normal
____________
Pull Down___________________
How Long I fft Iii 11)In.No.of Customers
ReportNo.//(o
Leak Order No.
_______________
Time of Break I-?.-,
Time Under Control ])7 p j-
TotatlfmeofBiow /17 Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B I.D.2 (IN 2)./5 B
Rated Capacity B P.D.2 C Time of Blow (hr)I 7 C
Time of Blow C Pipe Length (in 1000 ft.)D Avg.BTU (THIMCF)/O 7 3 D
Constant D Constant .004041 E Total Therms 9 0.3 )*
Total Therms Total Therms 0 Per Therm t71 >/
.Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $.P lOG’
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
Yes 1=1 NoLJ *AxBxCxD._Therms
Ax B x Cx D =Therms (A +B)x Cx Dx E Therms If more than 500 therms send to Engineering
Remarks:‘/1-1-0 I
—Ii 823,378.
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submifted By:1J’i LuJ
I
Division Operations Manager -—--
Form No.IGC 308 (1/06)
Town
____________
Project No.________________
Gas Pressure at Time of Break:
Outage:Yes No Q
Location ,(3/j’J
Report No.qsl)
Leak Order No.
_________
Time of Break 3 0
Time Under Control 4/.3 j)
Total Time of Blow_________________
RELIEF SLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B I.D.2 2)3.ti ‘7 9 ?B
Rated Capacity B 1.0.2 C Time of Blow (hr)I’3 c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)I ‘7 3 D
Constant D Constant .004041 E Total Therms 7 1 14 J 3,*
Total Therms Total Therms 0 Per Therm L71
-/,
12-
Report blowing relief 2 and larger only Report 4 pipe &larger for 2000 linear Total Cost $“11 6
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YeSUNoU *AxBxCxD...Therms
Ax B x C x D =Therms (A +B)x C x D x E =Therms If more than 500 therms send to Engineering
Remarks:LI,
DD2..-It :S55 o5iTh7 /tr
P_Ic 7LjI->oLç
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:tAA17
Division Operations Manager_________________________
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division Date t7IO/3
Service No.
Normal
How Long
L.11R21..42S Pipe Size______
___________
Pull Down_______
I Ifr S Thin.No.of Customers
/
1r)
Form No.IGC 308 (1106)
rI<)r)i .ce
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town
_______________________
Division
______________
Date -/7 —)
Project No._______________Service No.9 5 Pipe Size
“
Gas Pressure at Time of Break:Normal 6 Pull Down
Outage:Yes No JJ How Long /f}-,.No.of Customers
______________
LocaUon 9’U 7 1 wt
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
ReportNo.+5i9-/1 c
Leak Order No.
__________________
Time of Break /‘
Time Under Control /0 5
Total Time of Blow .3 5 HTS
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 5 A
Percent Open A Gauge Pressure B l.D.2(IN 2)7 B
Rated Capacity B l.D.2 C Time of Blow (hr)c
Time of Blow C Pipe Length (In 1,000 ft.)D Avg.BTU (TH/MCF)/‘7 3 D
Constant D Constant .004041 E Total Therms P1 7 *
Total Therms Total Therms 0 Per Therm
171)/%
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $b Y t’
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesflNoU *AxBxcxDmerms
AxBxCxDTherms (A+B)xCxDxE=Therms If morethan 500thermssend to Engineering
Remarks:5/L 1!ut in h /1
Submitted By:
__________________________
Division Operations Manager___________________________k
___
0FormNo.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town DMslon 5AuSrOM7-I.Date —j7-2ôj3
Project No.________________Service No.57 _K Pipe Size 3/gil
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No [J How Long Y 14 ‘5 No.of Customers 3
Location ,3 1.40 M .i t)1 L4Y’4 i ..j.U
Report No.____________
Leak Order No.75J
TimeofBreak IO;i’7 AM
Time Under Control t 3 AM
Total Time of Blow I.27 Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 3 A
Percent Open A Gauge Pressure B 1.0.‘(IN 2)
.5 2 B
Rated Capacity B I.D.’C Time of Blow (hr)1,27 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)7 D
Constant D Constant .004041 E Total Therms t7,9 *
Total Therms Total Therms 0 Per Therm
Report blowing relief 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $c37,/5
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesNoO *AxBxCxD=Therms
AxBxCxD=Therms CA+B)xCxDxETherms Ifmorethan500thermssendtoEngineedng
Remarks:1T /L)3V1 L..J-jE LjITiC
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Division Operations Manager
kvlk iUM
Form No.IGC 308 (1/06)
intermountain Gas Company
DIVISION GAS LOSS REPORT
Town Ala i?71fla.}DMsion
Project No._______________SeMce No.
Gas Pressure at Time of Break:Normal
Outage:Yes No [J How Long
Location 4L/j
Date_________
I,i3ID-31 I Pipe Size a
5 Pull Down__________________
3I ifl I fl.No.of Customers
ReportNo.30
Leak Order No.
__________________
TimeofBreak 3.5L iY)
Time Under Control t C)p
Total Time of Blow ..7 H
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 6 5 A
Percent Open A Gauge Pressure B ID.2 (IN 2).I 3 B
Rated CapacIty B l.D.2 C Time of Blow fhr)c 7 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU (TH/MCF)“t 7 3 D
Constant D Constant .004041 E Total Therms 5 /L.*
Total Therms Total Therms 0 Per Therm Lj //,
Report blowing relief 2”and larger only Report 4’pipe &larger for 2,000 linear Total Cost $.2 7’&.3
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoU *AxBxCxD=Therms
.AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEnglneering
Remarks:!‘lt s/L.(1 Li’)HtttP
Original:Gas Measurement
let Copy Division Numerical File
2nd Copy:Attach to corresponding
documents In division
Submitted By:‘-IV)L%fl.tYtLt,
Division Operations Manager (E’£_46t
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town The 11 (If t1’fl DMsion
___________
Date______
Project No._______________Service No.31p7363’2 I Pipe Size
_______
Gas Pressure at Time of Break:Normal 56 Pull Down
Outage:Yes fNo fJ How Long 5c7 121/fl-No.of Customers
Location I f.11 F Y I I;.f
Original:Gas Measurement
1st Copy Division Numerical File
2nd Copy Attach to corresponding
documents in division
Report No.62—
Leak Order No.
Time of Break
Time Under Control
Total Time of Blow
/,,7 pm
2ai€Fm
Hr
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure A
Percent Open A Gauge Pressure B 1.0.2 2)7 ??5 B
Rated Capacity B l.D.2 C Time of Blow fhr)‘‘7 c
Time of Blow C Pipe Length fin 1000 ft.)D Avg.BTU (TH/MCF)‘i”0
Constant 0 Constant .004041 E Total Therms //7,-
*
Total Therms Total Therms 0 Per Therm ‘/“2.i
Report blowing relief 2’and larger only Report 4”pipe &larger for 2000 linear Total Cost $/q /
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
Yes NoO *AxBxCxD_Therms
AxBxCxD=Therms (A+B)xCxDxETherms If morethan500thermssend to Engineering
Remarks:Hit 1 P
Submied By:(JJJ
DMsIon Operations Manager .cT.?(
I
Form No.ICC 308(1/06)
Town LLL
Project No._________________
Gas Pressure at Time of Break:
Outage:Yes No []
Location L-11/L/?t..—
Intermountain Gas Company
DMSION GAS LOSS REPORT
REUEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.AtiTlospheric Pressure A Guage Pressure .S A
Percent Open A Gauge Pressure B 1.0.2 (IN 2)0./9 3(5 B
Rated Capacity B I.D.2 C Time of Blow fhr)0333 c
Time of Blow C Pipe Length (in 1,000 ft.)0 Avg.BTU (THIMCF)/0 73 D
Constant D Constant .004041 E Total Therms 3 3 05 *
Total Therms Total Therms 0 Per Therm c.//g’j
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $/5 .9 /feet or more.
Regulator Station No.
Customer Name
Is customer bIlled for lost volume?
YesONoO *AXBXCXD_ThermS
AxBxCxD=Therms (A+B)xCxDxE=Therms lfmorethan500thermssendtoEngineering
Remarks:S 1 OSJ cLc*e 1f fl h
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in division
DMslon
____________
Date ReportNo.1o--2Ack3
p
Service No.Pipe Size 7 Z’Leak Order No.
Normal 55 Pull Down___________________Time of Break L
How Long No.of Customers Time Under Control
3 ‘4.jo U Total Time of Blow____________
Submitted By:cAJ
Division Operations Manager__________________________
Form No.IGC 308 (1/06)
Intermountain Gas Company
DiVISION GAS LOSS REPORT
(YQA&CIJ-’Ovi.
Project No._________________
Gas Pressure at Time of Break:
Outage:Yes No
Location
Division
_____________
Date
.a L5O Pipe Size
55
Leak Order No.
_________________
Time of Break //A..,
Time Under Control 1:3 ,
Total Time of Blow 1 9 ,“ihs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE I PURGE
Build Up Pressure______________________Avg.Atmospheric Pressure A Guage Pressure —5S A
Percent Open A Gauge Pressure B I.D.2 (IN 2).I 3(.t’B
Rated Capacity B ID.2 C Time of Blow (hr)3/7 C
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTh (THIMCF)/(9.3 D
Constant D Constant .004041 E Total Therms 31i’*
Total Therms Total Therms 0 Per Therm 0 /j 7/
Report blowing relIef 2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/..5 /L/
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesNoO *AxBxCxD_Therms
AxBxCxD=Therms (A+B)xCxDxETherms Ifmorethan500thermssendtoEngineering
Remarks:(Ott S I OJJ o4.1-O L/z-1iy t,l CJ ,
Original:Gas Measurement
let Copy:Division Numerical Ale
2nd Copy:Attach to corresponding
documents in division
Submitted By:
Division Operations Manager cQ)
t,-ilt
Service No.
Normal
How Long
Vi”
Report No./5Q —/54/
Pull Down
________
No.of Customers I
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Report No.(415 b j 9
Leak Order No.
__________________
Time of Break It t9 t rvi
Time UnderControl ii ‘3_I
Total Time of Blow His
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 55 A
Percent Open A Gauge Pressure B l.D.2 2)/3 4 B
Rated Capacity B l.D.2 C Time of Blow (hr)i I 5 c
lime of Blow C Pipe Length (in 1,000 ft.)D Avg.BTU fThIMCF)1 0 7 3 D
Constant D Constant .004041 E Total Therms 6///*
Total Therms Total Therms 0 Per Therm i ‘-1/&/2
Report blowing relief 2 and larger only Report 4 pipe &larger for 2,000 linear Total Cost $/0
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?
YesflNoO *AXBXCXD..Therms
AxBxCxD=Therms (A÷ B)xCxDxETherms lfmorethan 500thermssendtoEngineering
Remarks:SI I—Cut (r cA\F
Original:Gas Measurement
1st Copy:Division Numerical File
2nd Copy:Attach to corresponding
documents in dIvisIon
Submitted By:
Division Operations Manager
Town AOjz.)Division
______________
Date
Project No._______________Service No.
___________
Pipe Size
Gas Pressure at Time of Break:Normal 5 Pull Down —
Outage:Yes No U How Long ‘‘l rvi in.No.of Customers
LocaUon 1D
(ç\
ia&-ta
‘a”Y
Form No.IGC 308 (1/06)
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Town -73p Division
______________
Date______________________
.—II 3/1
Project No.________________Service No.—7 C /Pipe Size /9’A
Gas Pressure at Time of Break:Normal Pull Down
Outage:Yes No How Long q 0 fYX fl No.of Customers I
Location U R0 Ht ii s
ReportNo._________
Leak Order No.
_________________
Timeof Break /5 Pni
Time Under Control__L/;5 p -.
Total Time of Blow .Hrs
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 5 A
Percent Open A Gauge Pressure B I.D.2 (IN 2),7 B
Rated Capacity B l.D.2 C Time of Blow (hr)C
Time of Blow C Pipe Length fin 1,000 ft.)D Avg.BTh (TH/MCF)/0’7 3 D
Constant D Constant .004041 E Total Therms 5 *
Total Therms Total Therms 0 Per Therm //-/
Report blowing relief 2’and larger only Report 4’pipe &larger for 2,000 lInear Total Cost $1 /£7,L/5
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesONoU *AXBxCxD=Therms
AxBxCxDTherms (A+B)xCxDxETherms Ifmorethan500thermssendtoEngineering
Remarks:
Original:Gas Measurement
1st Copy:DMsIon Numerical Ale
2nd Copy:Attach to correspondIng
documents In division
Submitted By:-
Division Operations Manager
Form No.ICC 308 (1/06)
Town fl t
Project No.
___________________
Gas Pressure at Time of Break:
Outage:Yes No LI
Locaon
Intermountain Gas Company
DIVISION GAS LOSS REPORT
Division fl Date ‘7t)i 3
/7l’)I A”/OServiceNof/f %,fr//5.9 Pipe Size
Normal
_____________
Pull Down_______________
How Long No.of Customers
/1 AA7
Report No.‘?k2-
Leak Order No!79.S
Time of Break /2,3/AkI.
Time Under Control 7/)4/7 A//.
Total Time of Blow 1./,6)
RELIEF BLOW GAS LOSS LINE PACK LINE RUPTURE!PURGE
/__—Build Up Pressure Avg.Atmospheric Pressure A Guage Pressure 2 A
Percent Open A Gauge Pressure B 1.0.2 fIN 2)B
Rated Capacity B 1.0.2 C Time of Blow (hr)/./t c
Time of Blow C Pipe Length (in 1,000 ft.)D Avg.BTh (TH/MCF)/19.%i2 D
Constant 0 Constant E Total Therms
Total Therms *Total Therms *C Pet Therm
i—7 ‘2Reportblowingrelief2”and larger only Report 4”pipe &larger for 2,000 linear Total Cost $/—,
feet or more.
Regulator Station No.
Customer Name
Is customer billed for lost volume?-
YesENOLI *AxBxCxD=Therms
Ax B x Cx D =Therms *fA ÷ B)x Cx D x E =Therms If more than 500 therms send to Engineering
Remarks:bo ,)M ‘
//A’z2L44S A-&’
Original:Gas Measurement
let Copy:Division Numerical File
2nd Copy Attach to corresponding
documents In division
Submthed By:g t%%—4-’
DMsIon Operations Manager___________________________
V
Form No.IGC 308 (7/06)