Application of Terms of Amendment. This Amendment shall be binding on the Parties on the date of execution by the last Party to sign below, subject to the above amended provisions of Section 3.B and new Section 3.C with regard to the effective date of the High Pressure Gathering Fee as to any particular Delivery Point. All provisions of the Agreement not expressly amended above shall remain in full force and effect.
Application of Terms of Amendment. This Amendment to Special Addendum shall be binding on the Parties on the date of the last to occur of the following: (i) execution of an unaltered copy of this Amendment by the last Party to sign below and exchange between the Parties of fully executed original copies of this Amendment; and (ii) likewise, execution of an unaltered copy of the Agreement Amendment by the last Party to sign same and exchange between the Parties of fully executed original copies of the Agreement Amendment. All provisions of the Special Addendum not expressly amended above shall remain in full force and effect. Dynegy Contract No. 014904 — Ref. No. 095 Accepted and Agreed to: Burlington Resources Oil & Gas Company LP Accepted and Agreed to: By: BXXX XX Inc., its sole General Partner Dynegy Midstream Services, Limited Partnership By: By: Printed Name: Printed Name: Cxxxx Xxxxx Title: Title: Vice President Date: Date: Accepted and Agreed to: Burlington Resources Trading Inc. By: Printed Name Title: Date: Amendment to Special Addendum to Gas Gathering and Purchase Agreement Page 3 Dynegy Contract No. 014904 — Ref. No. 095 Amended Attachment 2 – Phase V Expansion Basis of Design To Special Addendum to Gas Gathering and Purchase Agreement A. Inlet Flow Rate to Plant Design Design Cyro Plant II Cyro Plant I Gas, MMcfd 150 100 Hydrocarbon liquid, bpd none none Produced water, bpd none none B. Inlet Pressure and Temperature To Plant Pressure, psig Temperature, °F Pressure, psig Temperature, °F Cyro II Cryo II Cyro I Cyro I Design operating 765 75 to 105 765 75 to 105 Minimum operating 765 75 765 75 Maximum operating 800 105 800 105 Mechanical design 1,100 — 900 — C. Inlet Composition to Plant Component Mol Percent Mol Percent Cyro II Cyro I Nitrogen 2.142 2.640 Carbon dioxide 0.023 0.380 Methane 78.729 76.200 Ethane 10.461 10.290 Propane 5.432 6.360 Isobutane 0.734 0.700 Normal butane 1.442 1.730 Isopentane 0.320 0.680 Normal pentane 0.288 0.680 Hexanes plus 0.429 0.340 Total 100.000 100.00 Trace components: * Total CO2 <1.000 <1.000 Water 10 lbs per MMcf Saturated Propylene Nil Nil Butylenes Nil Nil BTEX Nil Nil Hydrogen sulfide Nil Nil Mercaptans Nil Nil Other sulfur species Nil Nil Oxygen 5 ppmv 5 ppmv * NOTE – Total CO2 before treater. Amended Attachment 2 — Phase V Expansion Basis of Design Page 1
