초록 ▼

One exemplary embodiment can be a process for catalytic reforming. The process can include catalytically reforming a hydrocarbon feed in a reaction zone, obtaining an effluent stream having hydrogen and hydrocarbons from the reaction zone, obtaining from at least a portion of the effluent stream a w

One exemplary embodiment can be a process for catalytic reforming. The process can include catalytically reforming a hydrocarbon feed in a reaction zone, obtaining an effluent stream having hydrogen and hydrocarbons from the reaction zone, obtaining from at least a portion of the effluent stream a waste hydrocarbon stream from an adsorption zone, passing at least a portion of the waste hydrocarbon stream as a feed stream across a feed side of a membrane having the feed side and a permeate side, and being selective for hydrogen over one or more C1-C6 hydrocarbons, and withdrawing from the permeate side a permeate stream enriched in hydrogen compared with a residue stream withdrawn from the feed side.

대표청구항 ▼

1. A process for catalytic reforming, comprising: A) catalytically reforming a hydrocarbon feed in a reaction zone;B) obtaining an effluent stream comprising hydrogen and hydrocarbons from the reaction zone;C) separating a reformate liquid stream and a gas stream, comprising hydrogen and at least on

1. A process for catalytic reforming, comprising: A) catalytically reforming a hydrocarbon feed in a reaction zone;B) obtaining an effluent stream comprising hydrogen and hydrocarbons from the reaction zone;C) separating a reformate liquid stream and a gas stream, comprising hydrogen and at least one of nitrogen, one or more carbon oxides, and one or more C1-C6hydrocarbons, from the effluent stream;D) recycling at least a portion of the gas stream to the reaction zone;E) passing at least another portion of the gas stream to said downstream adsorption zone to separate hydrogen;F) withdrawing a hydrogen product stream from the adsorption zone;G) withdrawing a tail gas stream from the adsorption zone;H) compressing and cooling the tail gas stream;I) passing at least a portion of the compressed and cooled tail gas stream as a feed stream across a feed side of said downstream membrane zone comprising a polyimide, cellulose acetate, cellulose triacetate, or polysulfone membrane having the feed side and a permeate side, and being selective for hydrogen over at least one of nitrogen, the one or more carbon oxides, and the one or more C1-C6 hydrocarbons;J) withdrawing from the permeate side a permeate stream enriched in hydrogen compared to a residue stream, sending at least a part of said permeate stream as the hydrogen rich gas recycle stream to the at least another portion of the gas stream; andK) withdrawing from the feed side the residue stream enriched in at least one of nitrogen, the one or more carbon oxides, and the one or more C1-C6 hydrocarbons compared to the permeate stream. 2. The process according to claim 1, wherein the permeate stream comprises no more than about 150 ppm, by mole, of nitrogen and no more than about 250 ppm, by mole, of carbon monoxide. 3. The process according to claim 1, wherein the permeate stream comprises no more than about 100 ppm, by mole, of nitrogen and no more than about 100 ppm, by mole, of carbon monoxide. 4. The process according to claim 1, wherein the permeate stream comprises no more than about 20 ppm, by mole, of nitrogen and no more than about 40 ppm, by mole, of carbon monoxide. 5. The process according to claim 1, wherein an amount of hydrogen by mole percent in the permeate stream is substantially the same as a gas stream obtained from the effluent stream and upstream of the waste hydrocarbon stream. 6. The process according to claim 5, wherein the amount of hydrogen composition in the permeate stream is within about 15%, by mole, of the gas stream. 7. The process according to claim 5, wherein the amount of hydrogen composition in the permeate stream is within about 2%, by mole, of the gas stream. 8. The process according to claim 5, wherein the amount of hydrogen composition in the permeate stream is within about 1%, by mole, of the gas stream. 9. The process according to claim 1, wherein the membrane comprises a hollow fiber membrane. 10. The process according to claim 1, wherein the membrane comprises a spiral wound membrane. 11. The process according to claim 1, wherein the permeate comprises at least about 85%, by mole, hydrogen. 12. The process according to claim 1, wherein the permeate comprises at least about 96%, by mole, hydrogen.