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Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, wh

Methods and apparatuses are provided for isomerizing a hydrocarbon stream. The method includes isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream. The intermediate isomerized stream is fractionated to produce an off gas stream and a heavy isomerized stream, where the off gas stream includes an off gas recycle stream. The off gas recycle stream is dried in an off gas dryer to produce a hydrogen recycle stream, where the off gas drier includes an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream. The off dryer membrane includes a perfluorosulfonated ionomer. The hydrogen recycle stream is then fed into the reactor.

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1. A method of isomerizing hydrocarbons, the method comprising the steps of: isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream;fractionating the intermediate isomerized stream to produce an off gas stream and a heavy isomerized stream, wherein the off gas str

1. A method of isomerizing hydrocarbons, the method comprising the steps of: isomerizing a hydrocarbon stream in a reactor to produce an intermediate isomerized stream;fractionating the intermediate isomerized stream to produce an off gas stream and a heavy isomerized stream, wherein the off gas stream comprises an off gas recycle stream;drying the off gas recycle stream in an off gas dryer to produce a hydrogen recycle stream, wherein the off gas dryer comprises an off gas dryer membrane separating the off gas recycle stream from an off gas purge stream, wherein the off gas dryer membrane comprises a copolymer of tetrafluoroethvlene and perfluoro-3,6-dioxa-4-methyl-7-octene-sulfonic acid, and wherein a molar ratio of tetrafluoroethylene to perfluoro-3,6-dioxa-4-methyl-7-octene-sulfonic acid in the copolymer is from about 6/1 to about 8/1; andfeeding the hydrogen recycle stream into the reactor. 2. The method of claim 1 wherein the off gas dryer membrane is in a sulfonate salt state wherein a counter cation is lithium (Li+), sodium (Na+), or potassium (K+). 3. The method of claim 1 wherein isomerizing the hydrocarbon stream in the reactor further comprises isomerizing the hydrocarbon stream in the reactor wherein the reactor comprises a catalyst, wherein the catalyst comprises a platinum group metal on a porous substrate, the porous substrate comprises alumina, and wherein the catalyst is in a chlorided state. 4. The method of claim 3 wherein isomerizing the hydrocarbon stream further comprises feeding the hydrocarbon stream to the reactor wherein the hydrocarbon stream comprises 80 mass percent or more hydrocarbons having 5 or 6 carbon atoms. 5. The method of claim 3 wherein isomerizing the hydrocarbon stream further comprises feeding the hydrocarbon stream to the reactor wherein the hydrocarbon stream comprises 80 mass percent or more hydrocarbons having 4 carbons atoms. 6. The method of claim 1 wherein the off gas purge stream comprises the heavy isomerized stream. 7. The method of claim 1 wherein the off gas purge stream comprises a dry air stream. 8. The method of claim 1 further comprising: drying a raw make-up hydrogen stream in a make-up hydrogen dryer to produce a feed make-up hydrogen stream, wherein the make-up hydrogen dryer further comprises a feed make-up hydrogen dryer membrane separating the raw make-up hydrogen stream from a make-up hydrogen purge stream, and wherein the feed make-up hydrogen dryer membrane comprises a perfluorosulfonated ionomer; andfeeding the feed make-up hydrogen stream into the reactor. 9. The method of claim 1 further comprising: drying a raw make-up hydrogen stream in the off gas dryer. 10. The method of claim 1 further comprising: splitting the off gas stream into the off gas recycle stream and an off gas discharge stream; andfeeding the off gas discharge stream into a caustic scrubber. 11. The method of claim 1 wherein drying the off gas recycle stream in the off gas dryer further comprises drying the off gas recycle stream in the off gas dryer wherein the off gas dryer comprises a tube. 12. A method of isomerizing hydrocarbons, the method comprising the steps of: contacting a hydrocarbon stream with a catalyst to produce an intermediate isomerized stream;drying a raw make-up hydrogen stream in a make-up hydrogen dryer to produce a feed make-up hydrogen stream, wherein the make-up hydrogen dryer comprises a make-up hydrogen dryer membrane separating the raw make-up hydrogen stream from a make-up hydrogen purge stream, wherein the make-up hydrogen dryer membrane comprises a copolymer of tetrafluoroethylene and perfluoro-3,6-dioxa-4-methvl-7-octene-sulfonic acid, and wherein a molar ratio of tetrafluoroethylene to perfluoro-3,6-dioxa-4-methyl-7-octene-sulfonic acid in the copolymer is from about 6/1 to about 8/1; andcontacting the feed make-up hydrogen stream with the catalyst and the hydrocarbon stream. 13. The method of claim 12 wherein the make-up hydrogen dryer membrane is in a sulfonate salt state wherein a counter cation is lithium (Li+), sodium (Na+), or potassium (K+).