Common use of Values of Volume Correction Factor, K2 Clause in Contracts

Values of Volume Correction Factor, K2. (cubic meter/kmol) Molecular Mass of Mixture -150°C -154°C -158°C -160°C -162°C -166°C -170°C 16.0 -0.000039 -0.000031 -0.000024 -0.000021 -0.000017 -0.000012 -0.000009 16.5 0.000315 0.000269 0.000196 0.000178 0.000162 0.000131 0.000101 17.0 0.000669 0.000568 0.000416 0.000377 0.000341 0.000274 0.000210 17.2 0.000745 0.000630 0.000478 0.000436 0.000397 0.000318 0.000246 17.4 0.000821 0.000692 0.000540 0.000495 0.000452 0.000362 0.000282 17.6 0.000897 0.000754 0.000602 0.000554 0.000508 0.000406 0.000318 17.8 0.000973 0.000816 0.000664 0.000613 0.000564 0.000449 0.000354 18.0 0.001049 0.000878 0.000726 0.000672 0.000620 0.000493 0.000390 18.2 0.001116 0.000939 0.000772 0.000714 0.000658 0.000530 0.000425 18.4 0.001184 0.001000 0.000819 0.000756 0.000696 0.000567 0.000460 18.6 0.001252 0.001061 0.000865 0.000799 0.000735 0.000605 0.000496 18.8 0.001320 0.001121 0.000912 0.000841 0.000773 0.000642 0.000531 19.0 0.001388 0.001182 0.000958 0.000883 0.000811 0.000679 0.000566 19.2 0.001434 0.001222 0.000998 0.000920 0.000844 0.000708 0.000594 19.4 0.001480 0.001262 0.001038 0.000956 0.000876 0.000737 0.000623 19.6 0.001526 0.001302 0.001078 0.000992 0.000908 0.000765 0.000652 19.8 0.001573 0.001342 0.001118 0.001029 0.000941 0.000794 0.000681 20.0 0.001619 0.001382 0.001158 0.001065 0.000973 0.000823 0.000709 25.0 0.002734 0.002374 0.002014 0.001893 0.001777 0.001562 0.001383 30.0 0.003723 0.003230 0.002806 0.002631 0.002459 0.002172 0.001934 Source: National Bureau of Standards Interagency Report 77-867. Note 1: Molecular mass of mixture equals S (Xi x Mi).

Appears in 1 contract

Samples: LNG Terminal Use Agreement (Sabine Pass LNG, L.P.)

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Values of Volume Correction Factor, K2. (cubic meter/kmol) Molecular Mass of Mixture -150°C -154°C -158°C -160°C -162°C -166°C -170°C 16.0 -0.000039 -0.000031 -0.000024 -0.000021 -0.000017 -0.000012 -0.000009 16.5 0.000315 0.000269 0.000196 0.000178 0.000162 0.000131 0.000101 17.0 0.000669 0.000568 0.000416 0.000377 0.000341 0.000274 0.000210 17.2 0.000745 0.000630 0.000478 0.000436 0.000397 0.000318 0.000246 17.4 0.000821 0.000692 0.000540 0.000495 0.000452 0.000362 0.000282 17.6 0.000897 0.000754 0.000602 0.000554 0.000508 0.000406 0.000318 17.8 0.000973 0.000816 0.000664 0.000613 0.000564 0.000449 0.000354 18.0 0.001049 0.000878 0.000726 0.000672 0.000620 0.000493 0.000390 18.2 0.001116 0.000939 0.000772 0.000714 0.000658 0.000530 0.000425 18.4 0.001184 0.001000 0.000819 0.000756 0.000696 0.000567 0.000460 18.6 0.001252 0.001061 0.000865 0.000799 0.000735 0.000605 0.000496 18.8 0.001320 0.001121 0.000912 0.000841 0.000773 0.000642 0.000531 19.0 0.001388 0.001182 0.000958 0.000883 0.000811 0.000679 0.000566 19.2 0.001434 0.001222 0.000998 0.000920 0.000844 0.000708 0.000594 19.4 0.001480 0.001262 0.001038 0.000956 0.000876 0.000737 0.000623 19.6 0.001526 0.001302 0.001078 0.000992 0.000908 0.000765 0.000652 19.8 0.001573 0.001342 0.001118 0.001029 0.000941 0.000794 0.000681 20.0 0.001619 0.001382 0.001158 0.001065 0.000973 0.000823 0.000709 25.0 0.002734 0.002374 0.002014 0.001893 0.001777 0.001562 0.001383 30.0 0.003723 0.003230 0.002806 0.002631 0.002459 0.002172 0.001934 Source: National Bureau of Standards Interagency Report 77-867. Note 1: Molecular mass of mixture equals S (Xi x Mi).. Note 2: For intermediate values of temperature and molecular mass a linear interpolation shall be applied. ANNEX II

Appears in 1 contract

Samples: Shareholders Agreement (Cheniere Energy Inc)

Values of Volume Correction Factor, K2. (cubic meter/kmol) Molecular Mass of Mixture -150°C -154°C -158°C -160°C -162°C -166°C -170°C 16.0 -0.000039 -0.000031 -0.000024 -0.000021 -0.000017 -0.000012 -0.000009 16.5 0.000315 0.000269 0.000196 0.000178 0.000162 0.000131 0.000101 17.0 0.000669 0.000568 0.000416 0.000377 0.000341 0.000274 0.000210 17.2 0.000745 0.000630 0.000478 0.000436 0.000397 0.000318 0.000246 17.4 0.000821 0.000692 0.000540 0.000495 0.000452 0.000362 0.000282 17.6 0.000897 0.000754 0.000602 0.000554 0.000508 0.000406 0.000318 17.8 0.000973 0.000816 0.000664 0.000613 0.000564 0.000449 0.000354 18.0 0.001049 0.000878 0.000726 0.000672 0.000620 0.000493 0.000390 18.2 0.001116 0.000939 0.000772 0.000714 0.000658 0.000530 0.000425 18.4 0.001184 0.001000 0.000819 0.000756 0.000696 0.000567 0.000460 18.6 0.001252 0.001061 0.000865 0.000799 0.000735 0.000605 0.000496 18.8 0.001320 0.001121 0.000912 0.000841 0.000773 0.000642 0.000531 19.0 0.001388 0.001182 0.000958 0.000883 0.000811 0.000679 0.000566 19.2 0.001434 0.001222 0.000998 0.000920 0.000844 0.000708 0.000594 19.4 0.001480 0.001262 0.001038 0.000956 0.000876 0.000737 0.000623 19.6 0.001526 0.001302 0.001078 0.000992 0.000908 0.000765 0.000652 19.8 0.001573 0.001342 0.001118 0.001029 0.000941 0.000794 0.000681 20.0 0.001619 0.001382 0.001158 0.001065 0.000973 0.000823 0.000709 25.0 0.002734 0.002374 0.002014 0.001893 0.001777 0.001562 0.001383 30.0 0.003723 0.003230 0.002806 0.002631 0.002459 0.002172 0.001934 Source: National Bureau of Standards Interagency Report 77-867. Note 1: Molecular mass of mixture equals S (Xi x Mi).. Note 2: For intermediate values of temperature and molecular mass a linear interpolation shall be applied. ANNEX II

Appears in 1 contract

Samples: LNG Terminal Use Agreement (Cheniere Energy Inc)

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Values of Volume Correction Factor, K2. (cubic metermetre/kmol) Molecular Mass of Mixture -150°C -154°C -158°C -160°C -162°C -166°C -170°C 16.0 -0.000039 -0.000031 -0.000024 -0.000021 -0.000017 -0.000012 -0.000009 16.5 0.000315 0.000269 0.000196 0.000178 0.000162 0.000131 0.000101 17.0 0.000669 0.000568 0.000416 0.000377 0.000341 0.000274 0.000210 17.2 0.000745 0.000630 0.000478 0.000436 0.000397 0.000318 0.000246 17.4 0.000821 0.000692 0.000540 0.000495 0.000452 0.000362 0.000282 17.6 0.000897 0.000754 0.000602 0.000554 0.000508 0.000406 0.000318 17.8 0.000973 0.000816 0.000664 0.000613 0.000564 0.000449 0.000354 18.0 0.001049 0.000878 0.000726 0.000672 0.000620 0.000493 0.000390 18.2 0.001116 0.000939 0.000772 0.000714 0.000658 0.000530 0.000425 18.4 0.001184 0.001000 0.000819 0.000756 0.000696 0.000567 0.000460 18.6 0.001252 0.001061 0.000865 0.000799 0.000735 0.000605 0.000496 18.8 0.001320 0.001121 0.000912 0.000841 0.000773 0.000642 0.000531 19.0 0.001388 0.001182 0.000958 0.000883 0.000811 0.000679 0.000566 19.2 0.001434 0.001222 0.000998 0.000920 0.000844 0.000708 0.000594 19.4 0.001480 0.001262 0.001038 0.000956 0.000876 0.000737 0.000623 19.6 0.001526 0.001302 0.001078 0.000992 0.000908 0.000765 0.000652 19.8 0.001573 0.001342 0.001118 0.001029 0.000941 0.000794 0.000681 20.0 0.001619 0.001382 0.001158 0.001065 0.000973 0.000823 0.000709 25.0 0.002734 0.002374 0.002014 0.001893 0.001777 0.001562 0.001383 30.0 0.003723 0.003230 0.002806 0.002631 0.002459 0.002172 0.001934 Source: National Bureau of Standards Interagency Report 77-867. Note 1: Molecular mass of mixture equals S (Xi x Mi).

Appears in 1 contract

Samples: LNG Terminal Use Agreement (Cheniere Energy Inc)

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