SG/B269-421-LE-T-9805/1019 - Hydrogen Production Plant on Job Work basis at Panipat Refinery, Panipat, Haryana

Amount

Fixed Monthly Job Work charge for Hydrogen Production Plant

MJoH The base monthly JOB WORK charge (Rs./month)

WConstant A constant relating to WPI and CPI adjustment and shall not be less than 65% Note-1: [ Wconstant + Wmp + WCPI + We =100]. WConstant shall not be less than 65% and We shall not be more than 20%. Values to be quoted in percentage. 1.1 The We component shall not be more than 20%. In case it is more than 20% the balance excess shall be adjusted against Wconstant. .(Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.2 Wconstant should not be less than 65%. If in case it is less than 65%, the Wconstant shall be increased to 65% & balance shall be adjusted against Wmp and WCPI proportionately. (Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.3 The figures shall be rounded off to two decimal point

Wmp Component fraction related to wholesale price index for manufactured products Note-1: [ Wconstant + Wmp + WCPI + We =100]. WConstant shall not be less than 65% and We shall not be more than 20%. Values to be quoted in percentage. 1.1 The We component shall not be more than 20%. In case it is more than 20% the balance excess shall be adjusted against Wconstant. .(Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.2 Wconstant should not be less than 65%. If in case it is less than 65%, the Wconstant shall be increased to 65% & balance shall be adjusted against Wmp and WCPI proportionately. (Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.3 The figures shall be rounded off to two decimal point.

WCPI component fraction related to All India Consumer price index for Industrial worker Note-1: [ Wconstant + Wmp + WCPI + We =100]. WConstant shall not be less than 65% and We shall not be more than 20%. Values to be quoted in percentage. 1.1 The We component shall not be more than 20%. In case it is more than 20% the balance excess shall be adjusted against Wconstant. .(Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.2 Wconstant should not be less than 65%. If in case it is less than 65%, the Wconstant shall be increased to 65% & balance shall be adjusted against Wmp and WCPI proportionately. (Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.3 The figures shall be rounded off to two decimal point.

We component percentage related to Foreign Exchange and shall not be more than 20% Note-1: [ Wconstant + Wmp + WCPI + We =100]. WConstant shall not be less than 65% and We shall not be more than 20%. Values to be quoted in percentage. 1.1 The We component shall not be more than 20%. In case it is more than 20% the balance excess shall be adjusted against Wconstant. .(Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.2 Wconstant should not be less than 65%. If in case it is less than 65%, the Wconstant shall be increased to 65% & balance shall be adjusted against Wmp and WCPI proportionately. (Bidder to ensure the same while quoting the figures in BoQ.In case of deviation the relevant BoQ will not get Validated and the bidder will not be able to upload the BoQ) 1.3 The figures shall be rounded off to two decimal point. Note-2: For evaluation following shall be considered in the NPV, • WPI-MPn/ WPI-MPo =1.042, • CPIn/ CPIo= 1.056 • FEcomputed / FEo= 1 i.e. both the elements shall be considered equal / identical. Note-3: By the time, payment of JOB WORK Charge starts, FEcomputed / FE0 shall be a constant fig.

Variable Job work charges for Hydrogen Production Plant

AH (Tonne of Hydrogen gas) (In Rs)

Description of Work / Item(s)

Amount

Guarantee Figures per Tonne of H2 at Capacity Points for design case-1 (RLNG as Feed+fuel) at 10.125 TPH of Net H2 Export (100 % HGU capacity)

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-1 (RLNG as Feed+fuel) at 8.60625 TPH of Net H2 Export (85 % HGU capacity)

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-1 (RLNG as Feed+fuel) at 6.58125 TPH of Net H2 Export (65 % HGU capacity)

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-1 (RLNG as Feed+fuel) at 3.0375 TPH of Net H2 Export (30 % HGU capacity)

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-2 (SR sour Naphtha as Feed+fuel) at 10.125 TPH of Net H2 Export (100 % HGU capacity)

SR high Sulphur Naphtha Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Refinery Fuel gas

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-2 (SR sour Naphtha as Feed+fuel) at 8.60625 TPH of Net H2 Export (85 % HGU capacity)

SR high Sulphur Naphtha Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Refinery Fuel gas

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-2 (SR sour Naphtha as Feed+fuel) at 6.58125 TPH of Net H2 Export (65 % HGU capacity)

SR high Sulphur Naphtha Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Refinery Fuel gas

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-2 (SR sour Naphtha as Feed+fuel) at 3.0375 TPH of Net H2 Export (30 % HGU capacity)

SR high Sulphur Naphtha Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Refinery Fuel gas

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-3 (HROG+RLNG as Feed+fuel) at 10.125 TPH of Net H2 Export (100 % HGU capacity) Note-2

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-3 (HROG+RLNG as Feed+fuel) at 8.60625 TPH of Net H2 Export (85 % HGU capacity) Note-2

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-3 (HROG+RLNG as Feed+fuel) at 6.58125 TPH of Net H2 Export (65 % HGU capacity) Note-2

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export

Re-circulating Cooling Water Supply

Guarantee Figures per Tonne of H2 at Capacity Points for design case-3 (HROG+RLNG as Feed+fuel) at 3.0375 TPH of Net H2 Export (30 % HGU capacity) Note-2.

RLNG Consumption

Power Consumption

DM Water Consumption

HP Steam Export,

Re-circulating Cooling Water Supply

Matheson Tri-Gas Inc.

Prodair Air Products India Private Limited

Prodair Air Products India Private Limited

Matheson Tri-Gas Inc.