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1HE GAZETIE OF INDIA : EXTRAORDINARY (PART II-SEC. 3(i)) PETROLEUM AND N~TURAL GAS REGULATORY BOARD NOTIFICATION New Delhi, the 7th June,.2010 . ), •, ' ' . G.S.R. 478 (E}.-ln exercise of the powers conferred by Section 61 of the Pefroleum .and Nat.ural Gas Regulatory Act, 2006 (1~of2006), the Petroleum and Natural Gas Regulatory ' .Board hereby makes the following regulations I namely :-' ' ' ' . 1. · ShOtt tltte and c~ncement.
··. (1 }These regulations may be called the Petroleum and Natural Gas Regulatory Board (Determining Capacity of Petroleum, Petroleum Products and Natural Gas Pipeline) Regulations, 201 O. · ;· · . (2) They· shall come into force on the date of their · publication in the Official ·· ~ ·Gazette. · . 2. Definitions.
· . { 1) ··In these regulations, unless the conte~t otherwise requires,- ( a) "Act" me~ns the Petroleum and Natural Gas Regulatory Board Act, 2006:
• . . . ·~ I , , • , ' .
. . , . . ' . . " . . . . . . ~ (b} "appointed day"· means the date · of October l, 2007 when the . Central Government notified the establishment of the Petroleum and Natural Gas . . . - . . .. Regulatory Board; , ·. (c) "Board" means the Petroleum and Natural Gas 'Regulatory Board ·established· · under sub-section ( 1 ) of section 3 of the Act; · · · fdi .:ctiP'<lCity assess~ent 9roup'; means a group comprising representatives of two .· transporters other than the entity of which the pipeline system capacity is to be certified and a representative of the Board, as decided by the Board on case t9 ~ · . c,ose ·basis or any agency or entity or authorized person or any approved third , party authorized by the Board for determining the capacity of the petroleum~ petroleum products and natural gas pipeline: · . . - . .
' I '• ' I ..
['lllT II-~ 3(i)]
(e) "critical customer" means a customer whose withdrawal . conditions in the pipeline system could affect the capacity of the pipeline;
. '
(f) "extension of pipeline" means increase in length of pipelines .in either direction for transportation of natural gas from an existing transmission. or trunk pipeline or sub-transmission pipeline or spur: iine to another geographical location withe>W inc-rease in authorized capacity of the pipeline: :
(g) "expansion of pipeline" means increase in the capacity of existing pipeline beyond its previously authorized .capacity due to installation of additional · facilities such as compression facilities, addition of compressor stations or loop lines or extension to new sources of gas to tcip additional volomes etc .
. Expansion of pipeline may also incl!)de extension of the_existing pipeline in either.
direction as long as it increases the capacity of the pipeline and in that case it may be treated as expansion of th~ pipeline not extension:
(h) "marginally higher pressure" means an entry point pressure at any intei:mediate · · location in the pipeline system which is higher than the system pressure at_ that.
location so that flow from new source can commence without disturbing .
. existing upstream conditions in the pipeline system: · ·
(i) "Natural Gas Pipeline" means the pipeline as defined under the Petroleum pnd · Natural Gas Regulatory Board (Authorizing Entities .to Lay, Build, Operate or Expand Natural Gas Pipelines) Regulations, 2008;
..
(jJ "p~troleum, petroleum products pipeline" means any. pipeline includ1rig a branch or spur line for transport of petroleum, petroleum products __ and:inciudes ...
- all .connected infrastructure such as pumps, metering units, storage facilities at originating, delivery, tap off points, terminal station and the like connected. to the common carriers or contract carriers including line balancing tar~s o.nd .
tankage required for unabsorbed interface. essential for_ operating o pipertne .
system but excluding pipeline~: · ·.
which are dedicated for supply of petroleum products. to q specific consum~r .
which are not for resale; · · ..
. .
. P_rovided that the transporter may own, hire, outsource or. use on hospitability basis such connected facilities on non discriminatory basis;
. Provided further for the purpose of capacity determination, these regulations .· shall apply to all petroleu'm, petroleum products, pipelines including de~ica_t:ed .
pipelines: · . I "···:
. ' ' .. , - - ----·--·---- ------- --- ----- --------- -- - THE GAZETTE.OF INDIA: EXTRAORDINARY (PART II-SEC. 3(i)J {k) "capacity fcx the pipeline system" means the maximum quantity of petroleum, .
petroleum products or_na_tural gas that can be injected into the system or off taken from the system at Specific points, meeting all the technical and operational parameters fixed in each pipeline section in a steady state conditions : thaf i~, all parameters like flow, pressure, .temperature' are in harmony and vary only along the length of pipeline but not with time; -. . . ' . .
... - - (/) "declared capacity of pipeline" means the volume of natural gas in MMSCMD (million standard cubic meters per -day) that a- pipeline. is capable of .
transporting under the steady state operating conditions. For liquid pipeline the declared capacity of pipeline shall be the quantity of petroleum, petroleum products in MMTPA (million tones per annum), the pipeline is capable of transporting under the operating steady state conditions. Provided that the capacity h6°s been determined based on the appro.ved flow equation and the.
selected software package: -
(m) "section" means a portion of pipeline between any er:itry poir:it to any exit point or any other entry point.in the direction of flO'v\f. Provided the computation of successive section shall start-from second entry point and.so on;
- . .
(n) "selected software package" means the software package used by the entity for determiration of capacity of the pipeline·system or the pipeline section;
- . . .. . . . . . '
(o) "spur-line" means a pipeline necessarily originating or branching out frorri the .
trunk or transmission pipeline or sub-transmission line or another spur line ·or from · a terminal statior) on the existing transmission or trur:ik pipeline with diameter and . ·:
capqcity not greater than the trunk or transmission_ pipeline but having no _ · - - - _, - . / - - compre.ssion facility for supply·- of natl.Jral gas to one or more consumers. Any pipeline having a separate gas source or a C:ompre-ssor shall riot be treated as a spur~line. Jhe lengt_b of spur-line may not. depend upon Jhe length of the trunk pipelirie. A. spur~line'must use·the:capacity of trunk pipeline in order to transport gas:Spur line includes br_anch line also: · - · - (p) "~ection capacity" means the capacity of a particular section of the pipeline .which contains a supply.source or a delivery source or both. In other words, the section capacity is the maximum flow that could be handled by the specific section without disturbing the c;:orinected supply or del[very condition of the_ shippers; - - - · ··
(q) "steady state condition" means calculation carried out based on time-invariant pressure, tempera_ture and flow profiles throughout a pipeline using specified / [ 'WT Il-"lli"l6 3 ( i) ] 21 boundary conditions. In other words, . the steady-state run calculates the hydraulic state of a pipeline system operating at equilibrium with input and output balance; ·
(2) -Words and expressions used and not defined in these regulations, but defined in the Act or in the rules or regulations made thereunder, shall have the meanings respectively assigned to them in the Act or in the rules or regulations, as the case maybe. · ·
3. Applicability.
( 1) These regulations shall apply to an entity:-
(q) which is laying, building, operating or expanding or which proposes to lay, build, operate or expand a petroleum, petroleum products and natural gas pipeline;
(b) which proposes to lay a dedicated pipeline or is directed by the· Board to · convert a dedicated pipeline for supply of petroleum, p~troleum products and natural gas into a common or contract carrier petroleum, petroleum products and natural gas pipeline;·or
(c) which proposes extension or expansion of pipeline resulting into increase in capacity of the petroleum, petroleum products and natural gas pipeline.
(2) These regulations cover the procedure, parameters both constant and variable and frequency of declaration of pipeline capacity in MMSCMD for Natural Gas pipeline or in MMTPA for petroleum .. ar:id petroleum products pipeline.
4. Intent.
( 1) It is intended to apply these regulati~ns to all new and existing petroleum, petroleum products and natural gas pipelines including dedicated pipelines for the purpose of declaration of capacity of the pipeline under steady state conditions.
(2) The capacity of the petroleum, petroleum products and natural gas pipe[ine so determined shall be used for- . .
(a} declaring pipeline as common carrier or contract carrier under the relevant regulation on declaring pipeline as common carrier or contract carrier;
- - --- ---- --- - -------- 22 THE GAZETTE OF INDIA : EXTRAORDINARY (PART 11--S~c. 3(i)), .
(b)determining the ·tariff for petroleum. petroleu'm products and natural gas pipeline as per the . methodolggy or formulae defined under r~levant · regulations .
. (3) The capacity of the petroleum, petroleum products and natural gas pipeline so · / determined shall be used for providing access to available capacity on non · discriminatory basis under the relevant regulations on access code. ·
5. Determining capacity of a Petroleum, Petroleum Products and NaJural Gas Pipeline. - 7' ( 1) The determination of capacity for the pipeline system and for each section of the petroleum. petroleum products and nat.ural gas pipeline shall be based on selected software package and flow equation approved by the Board under this regulation. It is not .necessary for the entities to buy and· install any speeific software package. As long as the · software supports the flow · equation approved by the Board, the entities may continue to use or operate the system .
based on the previously installed software but shall have to determine the capacity of the system based on the flow equation approved by the Board in any of the compatible software package for the purpose of these regulations.
. ~ .
(2) The entity while submitting the capacity of the pipeline system to· the Board shall~.
furnish a declaration that the capacity has been calculated using the approved flow equation. The entity shall also submit the detailed calculations of the capacity and the software used for the purpose within thirty days of the notification of these regulation.s and therea~ter as per the periodicity for· determining capacity of a Petroleum, Petroleum Products and Natural Gas pipeline defined in. regulation 7 of these regulations.
(3) The ·parameters for the steady state simulation for determining the pipeline capacity shall be considered as given below, namely:-
(a)Constant parameters in the unit as specifie_d in the approved flow equation as per sub-clause (v) of this clause.·
(i) Internal diameter - The internal diameter shall be determined based on weighted average of internal diameters based on different pipe thicknesses, used in different sections in the pipeline system. ·· · · ·
(ii) Length - The actual length (for already installed pipeline) or proposed length (for yet to be installed pipeline) of the pipe in the pipeline system. · . I [ 'IWT II-~ 3(i)]
(iii) Roughness - This is :a fixed value for a pipe which determines the unevenness inside a pipe. De~ending on the pipe material the below given value for roughness factor s~,all be used : . · ·. .
TY.De of Material Roughness (micron) Steel - New Pi!De - ·• I - With internal coating 10-15 ' -I Without internal coating 35-40 Steel- old Pipe( more than ten years) ' I - With internal coating 15-20 -I Without internal coating 40-45 For old pipelines alrejdy operating, roughness factor shall. be determined by' • I • duly calibrating. actual field data in the approved flow equation. These factors shall be assessed b~ the capacity assessment group. For new pipelines, roughness factor usep shall be decided . keeping in view the operating conditions and pipeline feature like bends, valves, or any other restrictions present in the system:
Provided that the entity shall declare in advance the roughness factor considered for the pipes with relevant ·operating data to support the value chosen in case it is different from the above values. "' I
(iv) Efficiency· factor -Efficiency factpr within the range of 0.85 to 1.0 shall be used. For old pibelines already operating, efficiency factor ·shall be determined by d01y calibrating actual field data in the approved flow equation. These fattors shall be assessed by the capacity assessment group.
For_new pipeli.nes kfticiency factor used shall be decided keeping in view the. operating co~ditions and pipeline fe.ature like. bends, valves, life of pipeline or any other restrictions present in the system:
Provided that the e~tity shall declare in advance · the efficiency factor considered for the pibes with relevant operating data to support the value chosen in case it is different from the above values. giving complete analysis. The Board may direct the dntity to improve upon such design. .
(v) Formula - For detlrmination of friction factor i~ the pipeline the following flow equation shalljbe used;
TvDe of PIDellne Name of Flow eauation Natural Gas Panhandle Modified ..
, , ~' . ___ ----- - ----- ---"-----~~----,--.:___:_ ___________ _ -.
24 . ' :
TIIE GAZETTE OF INDIA: EXTRAORDINARY [PART II-SEC. 3(i)) ' Panhandle A for Pipe size~ 24" Panhandle B for Pipe size > 24" - Petroleum and Petroleum Products · Colebrook White
Explanation: For the determination of capacity of petroleum and petroleum products pipelines, the roughness factor shall be used. For natural gas pipelines, the efficiency factor shall be used.
(vi)Velocity - The maxirnum allowable velocity of natural gas or petroleum product in the pipeline shall be 20 m/sec in case of natural gas pipeline and 2 m/sec in case of· petroleum product pipelines or as per relevant regulations on Technical Standards and Specifications including Safety Standards w,hichever fs·lower, if specified. · ·
(vii) STP - The pipeline capacity shall be determined at the designed MAOP or de-rated MAOP due to ahy condition, for the petroleum, petroleum products or natural gas pipelines a.nd with the following stantjard Pressure and Temperature:, · Standard pressure Standard temperature ·
(b)Variable parameters- 1 .01325 bar.
1s 0c 'I.. .
\(i) ·Operating temperature - This is the actual temperature that a pipe is exposed to throughout the year. This temperature will be considered, for the purpose of determining capacity, as per the table below:
Country Region Temoerature ( OC) Winter Summer Tropical area such as North .
and North West India 20 30 ' Rest of India 30 .. 30
(ii) Inlet temperature - This is the inlet temperature of th€) petroleum, petroleum products and natural gas from the source into the pipeline.
(iii) Outlet temperature -· This is the outlet temperature. of the . petroleum, petroleum prodlJdS and natural gas at the delivery point.
(iv) Inlet pressure - The ma.xi mum pressure that is available at the entry point to the pipeline system. · ' .
. I ·I · \ I .I I ['IWT 0 II-~ 3(i)) 'l1ffi! '1fi1 ~ I= m:IT"ffi171 2S
(v) Outlet ~ressure - ~he n:inimum pressu~e that is required by the customer at the delivery or exit point as per access arrangement entered into by the shipper and the transporter.
(vi) Source Supply flow - This is the maximum flow that can be available from the source.
(vii) Delivery flow - This is the maximum flow that is required by the customer at the exit point as per access arrangement entered into by the shipper and the transporter. ·
(viii) Elevation difference - Depending on the terrain of the· ground profile, this factor will be considered from the mean sea level of the area.
(ix) Gas composition - The gas composition indicating all components totaling 1003 by volume is to be given with the level of impurities as per Schedule II of the Petroleum and Natural Gas Regulatory Board (Access Code for common or contract carrier Natural Gas Pipelines) Regulations, 2009. From this, necessary input to the flow equation shall be worked out.
In case of more than one source, the weighted average. composition of comingled natural gas beyond the 'second source of entry point shall be considered. Notwithstanding interdependency of various parameters, the gas parameters as described in Schedule II of regulations of Access Code shall be declared before hand with reference to gas properties.
(x) In case of natural gas pipeline, the gas quality at exit point shall be as per the Petroleum and Natural Gas Regulatory Board (Access Code for common or contract carrier Natural Gas Pipelines) Regulations, 2008. In case of petroleum products the entry point parameters shall be such that the deliveries of products at delivery point or tap off point or exit points shall be as per the prevalent BIS specifications applicable.
(4) All entities shall declare to the Board the constant parameters and the variable parameters for the pipeline:-
(i) On first working day of April and first working day of October every year;
or
(ii) Whenever there is any addition or deletion of the supply source of petroleum, petroleum products or natural gas.
26 I THE GAZETTE OF INDIA: EXTRAORDINARY [PART II-SEC. 3(i)] The entities shall also provide on first working day of October and first working day of April every year the hydraulic gradient and system flow diagram for the pipeline.
(SJ The methodology for calculation of pipeline capacity shall be as under:
(a} Natural Gas Pipelines:
(i) The entire pipeline system shall be configured in the selected software package operating offline. The steady state condition of the pipeline hydraulics with contractual flow parameters (pressure, temperature and flow) at entry and exit points shall be simulated in the selected software package.
(ii) At the originating point and at intermediate points in the direction of flow, set the pressure as a fixed parameter corresponding to the maximum allowable operating pressure (MAOP) or available compression facilities and compute the maximum pressure at all exit points with contractual flow.
(iii) Thereafter, assuming gas at the entry point (single source of gas) is unlimited, the selected software will be run till any customer connected to the system reaches limiting condition of pressure required at the respective exit point or . maximum flow capacity is reached at entry or intermediate compressor stations (if installed in the system) or the velocity of natural gas reaches limiting value as defined in these regulations. The capacity at this juncture would be the maximum system capacity achievable in the pipeline system and the customer at the exit point where pressure becomes limiting shall be the critical customer.
(iv) Now simulate the flow from any other source considering the entry should take place at the pressure marginally higher than the available at that section. The exercise carried above shall be repeated. to get threshold pressure limit at any location to calculate the flow exiting from each point in the entire pipeline system an<:! the sum total of these flows shall be the pipeline capacity as determine by the approved flow equation and selected software . .This would be the system capacity for multi source pipeline system.
(v) The section wise capacity of the pipeline system shall be computed between an. entry point and exit points. In case of multi entry, the section .
wise capacity may also be determined taking into account flow from each of the input points. Thus the first section is from first entry point to first exit point and second section shall be from first entry point to second exit point and another section and so on. This exercise shall be repeated for each of '.J "" . .___ __ - . / [ 'tJTIT Il-WJ5 3(i)] the entry point. However, in a real time working, the effect of each source will have to be workout on the pipeline capacity and the flow parameters at · intermediate points shall not be qllowed to reduce the system or· section tapaeity. The procedure mentioned above shall . be applicable for determining the capacity of specific section of the pipeline ..
(vi) In a recii time model of pipeline system,. the flow at specific entry point shall be the actual available flow from that source:' The gas supply from various sources at -entry points .and delivery at. exit points shall be scheduled. to optimize the pipeline system capacity. .
(vii) The obligatory or contractual requirement of pressure at any exit point shall determine the possible capacity within a particular section serving that exit points. Provided further that maintainability of a particular steady state hydraulics condition' at. any exit point shall be mutually determined between capacity determining authority and the transporter within the ·flexibility available in the system. The section wise capacity thus calculated with single or multiple entry and exit points shall be run with the approved flow equation . and selected software package offline in the steady state operation of the system to arrive at capacities of various sections.
(viii) This exercise shall be continued for computing section wise capacity of the pipeline system including the spur lines. In case of spur lines the tap off point shall be designated as the source point or entry point for spur line and computable (to be fed to the flow computing formula) or ·contractual hydraulics Shall· be allowable pressure at that point after accounting for the pressure drop from the tap off point to the consumer point of the spur line or branch line.
(ix) For determining, de-rated MAOP of· an existing pipeline; results based on the Instrumented pig survey shall be considered to calculate de-rating factor.
In dbsence of resuits of the inteillgent pig survey (IPS) in any pipeline, hydro testing shall be carried out to establish MAOP of that pipeline _as per provisions.
in the relevant regulations on Technical Standar~ and Specifications including Safety Standards. Proyided that. in ·absenc;e of hydro testing ·the entity may put up proposal for de-rating based on random thic.kness sur¥ey of the pipeline. Board reserves the right to Check such survey data. ·
(x) The entity shall submit the details of maximum achievable system capacity and section wise capacity of the natural gas pipeline so determined. under the steady state simulation with the details ·of variable or. constant parameters, to the Board in the specified format at Schedule A· along with the hydraulic gradient and system flow diagram fo( the ·pipeline system 2177 G\/10--5 ---·----. ......_,,,..~ . THE GAZETTE OF INDIA : EXTRAORDINARY (PART ll-SEc. 3(i)] including compressor stations, metering and regulating stations as applicable.
(b) Petroleum Product Pipellnt'ts: · · fi) In a multi product pipeline, the m.aximum achievable capacity shall be· determined based on the charactE:lristics of High Speed Diesel (HSD) whereas ~ .for pipelines dedicated fbr transportation of single product like LPG, Naphtha or ATF etc, charact~ristics of that product only shall be consider_ed.
{ii} The entire pipeline ·system shall be ·configured in the s~lected software · package operating offline. The steady state of hydraulics of .the pipeline.
shall be entered into 1the system.
·(iii) At the originating point and at intermediate points in the direction-of flow set the pressure as a fixed parameter corresponding to maximum allowable · operating pressure (MAOPJ or pumping facilities available at these locations, ·.
· as the case may be, ond compute the maximum possible flow in the pipeline system. This shall be the capacity of the pipeline system under prevailing · facilities and conditions. . · · · {iv)Thereafter, assuming products at the entry point~ as unlimited, the Station Discharge Head (SDH) at the pump station equal to Maximum Allowable . ·Operating Pressure (MAOP) of the pipeline, the entire pipeline1system shall pe ·. configured in the.selected software package operating offline. The steady state of hydraulics of the pipeline shall be entered into the system for . computing the maximum achievable flow in the pipeline system using the selected software and approved flow equation · {v) At the first and sut>sequent withdrawal points in the direction of flow getting the required pressure or SDH as a fixed parameter,. the maximum .possible flow within that section shall be computed based on .the methodology specified above. Similarly, t 1 he possible volume flow shall.be calculated from . section to section and tabulated up to· the last exit point taking into account .
the quantity available from btl)er injection points. . . . .
{vi)lf the capacity 6f a pipelin1 have been downgrad~d or decreased due to de~rating of the MA.OP of t~e pipeline due to factors like metal loss, the de rated capacity of. such pip1elines shall be determined considering results of Instrumented pig survey. In the ,absence of results, of IPS in any pip_eline, hydro testing shall be carried o~t to establish . MAOP of that pipeline · as per provi~i?ns. in .. the .releva~t regulation.s on Technical Standard and Spec1f1cahons 1nclud1ng Safety Standards. Provided that in absence of hy9ro testing the entity may put1 up proposal tor_ de~rating based on random -I I - I ' [ 'lfll1 ff-l!f116 3 (i)] - thickness survey of the pipeline. Board reserves the right to check such survey data. ·
(vii) The requirement of a pressure or SDH at any exit point shall determine the - possible capacity within a particular section serving that exit points. Provided further that maintainability of a particular hydraulics condition at any exit point shall be mutually determined between capacity determining authority and the transporter within the flexibility 'available in the system. The section wise capacity thus calculated with single or multiple entry and exit points shall be run with the selected software package dffline in the steady state operation of the system to arrive at capaeities of various sections.
(viii) The entity shall submit the maximum achievable pipeline capacity as welt as section wise capacity of the product pipeline so deterrnined, .under the_ steady state simulation with the-d~tails of variable or constant parameters, to· the Board in the specified format _at Schedule B along with the hydraulic gradient and system flow diagram for the pipeline system. -
(c) In case the contractual pressure at any entry and exit pointis within a band, the arithmetic mean rounded upto first decimal point shall be considered.
(d) The annual capacity of ·pipeline system and sections shall be as per the operation days specified in the Access Code for respective system.
6. ·oeclarlng capacity of Petroleum, Petroleum Products and Natural Gas pfpeiine by the Board. _
(a) The Board, after having satisfied with the data submitted by the entity regarding capacity of the pipeline, shall decide-
(i) to reject the capacity so determined. and direct the entity to revise the capacity calculations based on the revised parameters; or
(ii) to go ahead with the proposal with or without modification:
(b).The capacity so determined shall be declared by the Board as the declared · cqpacity ot' pipeline system- and specific sections and the same shall be - available to the shippers or consumers. The Board shall declare the section wise capacity of the system in the format specified at Schedule C.
(c) The entity, after declaring the pipeline capacity and section wise capacities by the Board, shall publish the same in line with the provisions of the relevant regulations on ·the Access Code for such pipeline as and when notified, on their website.
''-- ---' ---- -- -.... - - - - 30 TIIB GAZETIE OF INDIA : EXTRAORDINARY . . ·- [PART II-SEC. 3(i))
7. Periodicity for determining capacity of a Petroleum, Petroleum Products and Natural Gas pipeline. ·
(i) The capacity .of a pipeline shall be determined on first working d~y of April every year or wheneveri ·
(a)there is a .major change in ttie injected quantity or off taken quantity of petroleum, petroleum products and natura_I gas; · · (b} contract carrier quantity period expires; · (c} there is a change of plus or minus ten percent in gas composition or product quality or in other ()pereiting pdrameters from the operating conditions of the pipeline system within the parameters defined under the relevant regulations on the access code as and when notified; · (d} there is addition or deletion of entry or exit point; or (e} there is addition or deletion of facilities. for example, compressor or pumping station, loop lines or any other facility; · ' · (ii} The entity shall submit the details of the· so re~determined capacity of the pipeline to the Board in line with the provisions of these regulations for the purpose of declaration. of capacity.
8. Provisions relating to· dedicated pipelines for transport of Petroleum, Petroleum . . .
Products and Natural Gas.
- (1) In respect ofexisting dedicated ·pipelines, the following provisions shall appiy, namely:- (a} entity having dedicated pipeline to transport petroleum, petroleum products and natural gas to a specific customer and which is not for resale before the · appointed day· shall submit details of the pipeline capacity as determined based. on the provisions of these regulations to the Board within thirty days of notification of these regulations; · · , .
(b} the Board may, based on the examination of the informi:ition received, declare · the capacity of such pipeline as capacity of dedicated. pipeline. ·. ·· . 9. ·Miscellaneous. · ( 1} · If any dispute arises with regards to the interpretation of any of the provisions of these regulations, the decision of the Board shall be final;
. '
(2) The Board may, either suo moto or on a complaint, ·refer the ·issue of determination of the capacity in a pipeline, to any external consultant or exp.ert. ··I I . I ' I I . . .
"--T·[-j;:::. .... ~- .-,- -~i·~-·f:r--f---,.-~~R~fl'l11~~~.:;:::;;;::r..:., .;;....-;.....r....--r~~rr~.;:;;.,......;.,;,:.;:'1"'1,.,'H-·itrTl',......"1'1Mrl'"li .... ,.,.,.,,....._ .• , ... 1., .. ~ ..... ,,...,.-...,., ... ,.,.,. •. , .. , .. ~,,,.,"::a;...,,..,, .. ,.,1 .. , ..... .,. ~-·'"'""'....,._.,; __ ;....,,;._ ;r'' - ' ( qpr Il-<§'IJ'g 3(i)] 31 Cost in tnis regara shall be borne by the entity or the complainant or as deemed fit by the Board on a case specific basis. However, the recommendation of the consultant or expert shall be advisory in nature to the Board arid shall ndt be binding; ·
(3) rne Board may validate the computed capacity with actual capacity as per the flow regime of the pipeline with actual flow conditions as and when qesired.
1 2 3 4 5 6 7 8 9 10 11 12 13 14 5chedule A [see regulation 5(5)(a)(x)] Format for furnishing information regarding determining capacity of Natural Gas Pipeline - Name of Entity .
Address & Contact details of Entity Name of Natural Gas Pipeline . - Name of Software package used Approved Flow equation . used (mention name of flow equation) Details· of injection/entry point and delivery /exit points and sections on the pipeline Composition of natural gas .
Entity agrees to have considered the Technical Yes/ No standards, specifications and safety standards as - specified by the Board Entity agrees to have considered the relevant provisions Yes/ No of Petroleum .and Natural Gas Regulatory Board Regulations Constant and. variable parameters used under steady state conditions for determining capacity of the pipeline Capacity· of the pipeline under existing operating conditions Maximum achievable Capacity of the pipeline under steady state conditions as determined under section 5 of these regulations Section wise. maximum achievable capacity of the .
pipeline as determined under section 5 of these - regulations .
Expected addition of, entry points and exit points scheduled in near future Note: Submit the system flow diagram & hydraulic gradient ~------· '.
32 1 2 3 4 5 6 7 8 9 10 11 12 13 14 ) THE GAZETTE OF INDIA : EXTRAORDINARY [PART II-SEC. 3(i)] Schedule B . [see regulation S(S)(b)(viii)] / .
Format for furnishing information regarding determining capacity of, Petroleum and Petroleum Products Pipeline Name of Entity ..
Address and Contact aetails of Entity Name of Petroleum and Petroleum Products Pipeline ' Name of Software package used for determining capacity . ~ Approved Flow equation used (mention name of flow - equation) .
.
Details of injection/entry point and delivery/exit points and sections on the pipeline ' . ' Quqlity of various products being transported in the pipeline Constant and variable parameters used under steady state conditions for determining capacity of the pipeline Entity agrees to have considered the Technical standards, Yes/ specifications and safety standards as specified by the Board No Entity agrees to have considered the relevant pr.ovisions o~ Yes/ Petroleum and Natural Gas Regulatory Board Regulations 'No ·Quality specifica.tions considered for the purpose of capacity determination Capacity of the pipeline under existing operating conditions Maximum achievable C_apacity of the pipelir:ie under steady_ state_ conditions as <;:letermined under s~ction 5. of these ' regulations Section wise maximum achievable capacity of the pipeline as determined under sectiori 5 of these regulations ,, Expected addition of entry points and exit points scheduled in near future . - - - Note: Submit the system fiow diagram & hydraulic gradient \ ['llll ll-~ 3(i)) Schedule C [see regulation 6(b)] Format for declaring capacity of Petroleum, Petroleum Products and Natural · Gas Pipeline by the Petroleum and Natural Gas Regulatory Board Date of declaration of capacity by the Board:
1 2 3 4 5 6 7 8 9 Dated:
Name of Entity Address and Contact details of Entity .
Name of Pipeline - Details of injection/entry point and delivery/exit points and sections on the pipeline Name of the software package used by the entity Flow equation used for" the purpose .
Product Quality specifications/gas Parameters considered for the purpose of capacity determination Maximum achievable capacity of the pipeline under steady state conditions Section wise maximum achievable capacity of the pipeline Secretary Petroleum and Natural Gas R_egulatory Board ' [ F. No. S-Admn/11/8/20~0] RATAN P. WATAL, Secy.
Printtd by the Managor, Government of lndie Press, Ring Road, Mayapuri, New Delhi·l 10064 · and Published by the Controller of_l'ublicatkms, Delhi-l lOOS4. .
33 ' ' --- --------~-------..-~-------~---- -- - ---- - -·----- --~