Claims Analysis
Total Claims: 10
Claim 1
Independent Claim
195 words
A process for converting natural gas to methanol or products derivative of methanol, comprising the steps of: partially oxidizing natural gas with an oxidant stream to form a synthesis gas containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) less than 1.0; combining the synthesis gas with a hydrogen rich recycle gas stream secured as a permeate gas stream from diffusion of a tail gas stream remaining after completion of methanol recovery through a semipermeable membrane preferential for permeation of H 2 in preference to N 2 , said hydrogen rich recycle gas stream being used in an amount that provides a combined synthesis-recycle gas stream containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) which is greater than that of the synthesis gas; passing said combined synthesis-recycle gas stream into a plurality of contacts with a methanol conversion catalyst with recovery of methanol from said gas stream between contacts with a methanol conversion catalyst to form after the last methanol recovery step a tail gas stream from which the hydrogen rich recycle gas stream is secured by diffusion.
Claim 2
Dependent Claim
195 words
A process for converting natural gas to methanol or products derivative of methanol, comprising the steps of: partially oxidizing natural gas with an oxidant stream to form a synthesis gas containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) less than 1.0; combining the synthesis gas with a hydrogen rich recycle gas stream secured as a permeate gas stream from diffusion of a tail gas stream remaining after completion of methanol recovery through a semipermeable membrane preferential for permeation of H 2 in preference to N 2 , said hydrogen rich recycle gas stream being used in an amount that provides a combined synthesis-recycle gas stream containing H 2 , CO and CO 2 in a ratio of (H 2 )/(2CO+3CO 2 ) which is greater than that of the synthesis gas; passing said combined synthesis-recycle gas stream into a plurality of contacts with a methanol conversion catalyst with recovery of methanol from said gas stream between contacts with a methanol conversion catalyst to form after the last methanol recovery step a tail gas stream from which the hydrogen rich recycle gas stream is secured by diffusion.
Claim 3
Dependent Claim
22 words
The process of claim 1, wherein said synthesis gas has a ratio of (H 2 )/(2CO+3CO 2 ) of 0.85 or less.
Claim 4
Dependent Claim
26 words
The process of claim 2, wherein the combined synthesis-recycle gas stream has a ratio of (H 2 )/(2 CO+3 CO 2 ) of 0.95 or greater.
Claim 5
Dependent Claim
23 words
The process of claim 3, wherein the combined synthesis-recycle gas stream is passed into at least three contacts with a methanol conversion catalyst.
Claim 6
Dependent Claim
44 words
The process of claim 4, wherein the oxidant stream is secured from compressed air taken from a gas turbine and the non-permeate portion of the tail gas following recovery of the hydrogen rich recycle gas stream is utilized as fuel for the gas turbine.
Claim 7
Dependent Claim
22 words
The process of claim 5, wherein the non-permeate portion of the tail gas has a heating value of 100 BTU/scf or greater.
Claim 8
Dependent Claim
22 words
The process of claim 6, wherein the non-permeate portion of the tail gas is used in its entirety as gas turbine fuel.
Claim 9
Dependent Claim
26 words
The process of claim 6, wherein the non-permeate portion of the tail gas has at least 30% of its heat of combustion content supplied by hydrogen.
Claim 10
Dependent Claim
29 words
The process of claim 8, wherein no more than 30% of the heat of combustion content of the non-permeate portion of the tail gas is supplied by a hydrocarbon.