Schedule -I |
Format for Declaring capacity of pipeline |
| HVJ-GREP-DVPL |
|
Name of entity |
GAIL (India) Limited |
Name of Pipeline |
HVJ-GREP-DVPL Pipeline |
Sectionwise capacity on the pipeline (to be furnished for each section separately) |
Total capacity is 52 MMSCMD. |
a. Number of sections |
b. name of section with start and end point |
c. capacity -(i) Volume terms (ii) energy terms) |
Number of AHA's |
Nine |
Number of entry points on the pipeline route |
Three |
Location of entry points |
Hazira, Dahej and Ankot |
| Number of Exit Points |
All Consumers are Exit points |
| Location of Exit Points |
All Consumers are Exit points |
| Entry point wise Capacity of Pipeline (to be furnished separately for each pipeline) |
Total capacity is 52 MMSCMD. |
| Exit point wise Capacity of Pipeline (to be furnished separately for each pipeline) |
Total capacity is 52 MMSCMD. |
| Technical parameters |
|
| a)Inlet pressure at entry point |
Hazira-Min 40.0 KG/CM2g |
| |
Dahej--89 bar(a) or less. |
| |
Ankot-- 87-92 barg |
| b)Calorific Value band at entry point |
Hazira- Min 8500 Kcal/SCM GCV |
| |
Dahej-- Min 8500 Kcal/SCM GCV |
| |
Ankot-- Min 8500 Kcal/SCM GCV |
| c)Temperature |
Not more than 55 Degree Centigrade |
| d)Other elements as per Schedule II |
As per GSPA with various Suppliers and PNGRB Guidelines |
| i) Hydrocarbons dew pt (Degree Celsius, max.)* |
Plus 5 |
| ii)Water dew pt (Degree Celsius, max.)* |
0 |
| iii)Hydrogen sulphide (ppm by wt. max.) |
5 |
| (ix)Total Sulphur (ppm by wt. max.) |
10 |
| (x)Carbon Dioxide (mole % max.) |
6 |
| (xi)Total inerts (mole %) |
8 |
| (xii)Temperature(Degree Celsius, max) |
55 |
| (xiii)Oxygen (% mole vol. max.) |
0.5 |
| Status of extra capacity available in the pipeline system for common carrier: |
Nil |
| Details of common carrier capacity being used by transporter itself or on contract carrier basis. |
Nil |
| Any demand pending with the transporter for common carrier usage of the pipeline alongwith duration of such pendency |
Nil |
| Preference on entry and exit points |
Entry points are near Gas Sources and Exit points are various Consumers. |
DUPL-DPPL |
|
Name of entity |
GAIL (India) Limited |
Name of Pipeline |
DUPL-DPPL |
Sectionwise capacity on the pipeline (to be furnished for each section separately) |
Two |
a. Number of sections |
Total Capacity 19.2 MMSCMD |
b. name of section with start and end point |
c. capacity -(i) Volume terms (ii) energy terms) |
Calorific Value band at entry point |
8500 Kcal/SCM GCV to 10420 Kcal/SCM GCV |
Number AHA's |
Two |
| Number of entry points on the pipeline route |
Two |
| Location of entry points |
Dahej and Mashkal |
| Number of Exit Points |
All Consumers are Exit points |
| Location of Exit Points |
All Consumers are Exit points |
| Entry point wise Capacity of Pipeline (to be furnished separately for each pipeline) |
19.2 MMSCMD |
| Exit point wise Capacity of Pipeline (to be furnished separately for each pipeline) |
19.2 MMSCMD |
| Technical parameters |
|
| a)Inlet pressure at entry point |
Dahej--89 bar(a) or less. |
| |
Mashkal--60-92 barg |
| b)Calorific Value band at entry point |
Dahej- Min 8500 Kcal/SCM GCV |
| |
Mashkal-- Min 8500 Kcal/SCM GCV |
| c)Temperature |
Not more than 55 Degree Centigrade |
| d)Other elements as per Schedule II |
As per GSPA with various Suppliers and PNGRB Guidelines |
| i)Hydrocarbons dew pt (Degree Celsius, max.)* |
Plus 5 |
| ii)Water dew pt (Degree Celsius, max.)* |
0 |
| iii)Hydrogen sulphide (ppm by wt. max.) |
5 |
| (ix)Total Sulphur (ppm by wt. max.) |
10 |
| (x)Carbon Dioxide (mole % max.) |
6 |
| (xi)Total inerts (mole %) |
8 |
| (xii)Temperature(Degree Celsius, max) |
55 |
| (xiii)Oxygen (% mole vol. max.) |
0.5 |
| Status of extra capacity available in the pipeline system for common carrier: |
4.8 |
| Details of common carrier capacity being used by transporter itself or on contract carrier basis. |
Nil |
| Any demand pending with the transporter for common carrier usage of the pipeline alongwith duration of such pendency |
NIL |
| Prefernec on entry and exit points |
Entry points are near Gas Sources and Exit points are various Consumers. |