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A process for recovery of ethylene from a polymerization product stream of a polyethylene production system, comprising separating a light gas stream from the polymerization product stream, wherein the light gas stream comprises ethane and unreacted ethylene, contacting the light gas stream with an

A process for recovery of ethylene from a polymerization product stream of a polyethylene production system, comprising separating a light gas stream from the polymerization product stream, wherein the light gas stream comprises ethane and unreacted ethylene, contacting the light gas stream with an absorption solvent system, wherein the contacting the light gas stream with the absorption solvent system occurs at a temperature in a range of from about 40° F. to about 110° F., wherein at least a portion of the unreacted ethylene from the light gas stream is absorbed by the absorption solvent system, and recovering unreacted ethylene from the absorption solvent system to yield recovered ethylene.

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1. A process comprising contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loo

1. A process comprising contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer,separating a as stream from the polymerization product stream, wherein the gas stream comprises unreacted ethylene and ethane;separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least one gaseous component from the gas stream to form a recycle stream comprising unreacted ethylene and a waste stream comprising ethane, wherein absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone; andrecycling the unreacted ethylene of the recycle stream to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor. 2. The process of claim 1, wherein the bimodal polymer comprises a high molecular weight polymer and a low molecular weight polymer. 3. The process of claim 2, wherein the high molecular weight polymer has a low density, and wherein the low molecular weight polymer has a high density. 4. The process of claim 1, wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 5. The process of claim 1, wherein the at least one gaseous component comprises the unreacted ethylene, optionally isobutane, and optionally unreacted comonomer. 6. The process of claim 1, wherein separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least one gaseous component from the gas stream comprises: contacting the gas stream with the absorption solvent system, wherein at least a portion of the unreacted ethylene from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane is unabsorbed by the absorption solvent system;recovering the unreacted ethylene from the absorption solvent system in the recycle stream; andrecovering the unabsorbed ethane in the waste stream. 7. The process of claim 1, further comprising: removing at least a portion of elemental oxygen or oxygen-containing compounds from the gas stream prior to separating the at least one gaseous component from the gas stream. 8. The process of claim 1, wherein separating a gas stream from the polymerization product stream comprises: routing the polymerization product stream to a separator selected from a distillation column, a flash tank, a filter, a membrane, a reactor, an absorbent, an adsorbent, a molecular sieve, or combinations thereof. 9. The process of claim 1, further comprising: combusting ethane of the waste stream. 10. A process comprising: contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;separating a gas stream from the polymerization product stream, wherein the gas stream comprises unreacted ethylene and ethane;separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least gaseous component from the gas stream to form a recycle stream comprising unreacted ethylene and a waste stream comprising ethane; andrecycling the unreacted ethylene of the recycle stream to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor, wherein separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least one gaseous component from the gas stream comprises:contacting the gas stream with the absorption solvent system, wherein at least a portion of the unreacted ethylene from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane is unabsorbed by the absorption solvent system;recovering the unreacted ethylene from the absorption solvent system in the recycle stream; andrecovering the unabsorbed ethane in the waste stream; and wherein contacting the gas stream with the absorption solvent system occurs at a pressure in a range of frown about 40 psig to about 60 psig, and wherein recovering the unreacted ethylene from the absorption solvent system in the recycle stream comprises depressurizing the absorption solvent system utilizing pressure swing absorption. 11. The process of claim 10, wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 12. The process of claim 10, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 13. A process comprising: contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;separating a gas stream from the polymerization product stream, wherein the gas stream comprises unreacted ethylene and ethane;separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least on gaseous component horn the gas stream to form a recycle stream comprising unreacted ethylene and a waste stream comprising ethane; andrecycling the unreacted ethylene of the recycle stream to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor, wherein separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least one gaseous component from the gas stream comprises: contacting the gas stream with the absorption solvent system at a pressure in a range of from about 40 psig to about 60 psig, wherein at least a portion of the unreacted ethylene from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane is unabsorbed by the absorption solvent system;introducing a complexed stream comprising a complex of the absorption solvent system and unreacted ethylene into a solvent regenerator;depressurizing the solvent regenerator to a pressure in a range of from about 0 psig to about 10 psig; andrecovering the recycle stream from the solvent regenerator. 14. The process of claim 13, wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 15. The process of claim 13, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 16. A process comprising: contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;separating a as stream from the polymerization product stream, wherein the gas stream comprises unreacted ethylene and ethane;separating, using an absorption solvent system at a temperature in a range of from about 40° F. to about 110° F., at least one gaseous component from the gas stream to form a recycle stream comprising unreacted ethylene and a waste stream comprising ethane; andrecycling the unreacted ethylene of the recycle stream to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor, and further comprising:converting ethane of the waste stream into ethylene; andrecycling the ethylene obtained by converting ethane to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor. 17. The process of claim 16, wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 18. The process of claim 16, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 19. A polyethylene production system, comprising: a first loop slurry reactor;a second loop slurry reactor connected in series with the first loop slurry reactor, wherein the first loop slurry reactor and the second loop slurry reactor are configured to contact ethylene with a polymerization catalyst under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;a first separator configured to receive the polymerization product stream, to recover the bimodal polymer in a polymer stream, and to recover unreacted ethylene and ethane in a gas stream; andone or more absorption reactors configured to receive the gas stream, wherein the one or more absorption reactors contains an absorption solvent system which is at a temperature in a range of from about 40° F. to about 110° F., wherein at least a portion of the unreacted ethylene received from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane received from the gas stream is unabsorbed by the absorption solvent system, and wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 20. The system of claim 19, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 21. A polyethylene production system, comprising: a first loop slurry reactor;a second loop slurry reactor connected in series with the first loop slurry reactor, wherein the first loop slurry reactor and the second loop slurry reactor are configured to contact ethylene with a polymerization catalyst under suitable reaction condition to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;a first separator configured to receive the polymerization product stream, to recover the bimodal polymer in a polymer stream, and to recover unreacted ethylene and ethane in a gas stream; andone or more absorption reactors configured to receive the gas stream, wherein the one or more absorption reactors contains an absorption solvent system which is at a temperature in a range of from about 40° F. to about 110° F., wherein at least a portion of the unreacted ethylene received from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane received from the gas stream is unabsorbed by the absorption solvent system, wherein the one or more absorption reactors operate with pressure swing absorption to recover the unreacted ethylene, the system further comprising: a recycle stream comprising unreacted ethylene recovered from the one or more absorption reactors, wherein the recycle stream flows unreacted ethylene to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor, anda waste stream comprising the unabsorbed ethane recovered from the one or more absorption reactors. 22. The system of claim 21, wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 23. The system of claim 21, further comprising: a processing device configured to combust ethane received from the waste stream or configured to convert ethane received from the waste stream to ethylene. 24. The system of claim 21, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 25. A polyethylene production system, comprising: a first loop slurry reactor;a second loop slurry reactor connected in series with the first loop slurry reactor, wherein the first loop slurry reactor and the second loop slurry reactor are configured to contact ethylene with a polymerization catalyst under suitable reaction condition to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer;a first separator configured to receive the polymerization product stream, to recover the bimodal polymer in a polymer stream, and to recover unreacted ethylene and ethane in a gas stream; andone or more absorption reactors configured to receive the gas stream, wherein the one or more absorption reactors contains an absorption solvent system which is at a temperature in a range of from about 40° F. to about 110° F., wherein at least a portion of the unreacted ethylene received from the gas stream is absorbed by the absorption solvent system, wherein at least a portion of the ethane received from the gas stream is unabsorbed by the absorption solvent system, and further comprising:a complexed stream flowing from the one or more absorption reactors, wherein the complexed stream comprises a complex of the absorption solvent system and unreacted ethylene; a solvent regenerator configured to receive the complexed stream and to recover the unreacted ethylene from the complex; and a recycle stream comprising the unreacted ethylene recovered from the complex,wherein the unreacted ethylene recovered from the complex is recycled to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor via the recycle stream. 26. The system of claim 25, wherein the complexed stream further comprises ethane, the system further comprising: a waste gas stream comprising the unabsorbed ethane recovered by the solvent regenerator from the complexed stream. 27. The system of claim 26, further comprising a processing device configured to combust ethane received from the waste stream or configured to convert ethane received from the waste stream to ethylene. 28. The system of claim 25, wherein the absorption solvent system comprises copper chloride, aniline, and N-methylpyrrolidone. 29. The system of claim 25, wherein the bimodal polymer comprises a high molecular weight polymer having a low density and a low molecular weight polymer having a high density and wherein the polymerization catalyst is selected from a Ziegler Natta catalyst, a Ziegler catalyst, a chromium catalyst, a chromium oxide catalyst, a chromocene catalyst, a metallocene catalyst, a nickel catalyst, or combinations thereof. 30. A process comprising: contacting ethylene and a polymerization catalyst in a first loop slurry reactor and in a second loop slurry reactor connected in series with the first loop slurry reactor, under suitable reaction conditions to yield a polymerization product stream flowing from the second loop slurry reactor, wherein the polymerization product stream comprises a bimodal polymer,separating a gas stream from the polymerization product stream, wherein the gas stream comprises unreacted ethylene and ethane;separating, using an absorption solvent system comprising copper chloride, aniline, and N-methylpyrrolidone, at least one gaseous component from the gas stream to form a recycle stream comprising unreacted ethylene and a waste stream comprising ethane; andrecycling the unreacted ethylene of the recycle stream to the first loop slurry reactor, the second loop slurry reactor, or both the first loop slurry reactor and the second loop slurry reactor.