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A refrigeration method reduces compressor energy usage in a hydrocarbon refrigeration system by incorporating a distillation/adsorption cycle. The method and related systems can use waste or other heat sources to replace a portion of the mechanical energy of the compression cycle in a novel process

A refrigeration method reduces compressor energy usage in a hydrocarbon refrigeration system by incorporating a distillation/adsorption cycle. The method and related systems can use waste or other heat sources to replace a portion of the mechanical energy of the compression cycle in a novel process scheme easily adapted to either new or existing refrigeration systems. The present hybrid vapor compression-adsorption cycle combines both the refrigerant and adsorption medium in the compression cycle and separates these components using conventional multi-stage distillation to then separate them for the refrigeration and adsorption cycles.

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1. A mixed refrigerant process, comprising: supplying a hydrocarbon refrigerant with a molecular weight of between 28 and 72 to a pressure reducer, the hydrocarbon refrigerant being a liquid when supplied;reducing the pressure of the liquid hydrocarbon refrigerant to produce a two phase refrigerant;

1. A mixed refrigerant process, comprising: supplying a hydrocarbon refrigerant with a molecular weight of between 28 and 72 to a pressure reducer, the hydrocarbon refrigerant being a liquid when supplied;reducing the pressure of the liquid hydrocarbon refrigerant to produce a two phase refrigerant;delivering the two phase hydrocarbon refrigerant to at least one heat exchanger to cool to at least one process stream, wherein the two phase hydrocarbon refrigerant is vaporized in the at least one heat exchanger;increasing a pressure of the vaporized two phase hydrocarbon refrigerant to a pressure less than a baseline refrigerant pressure, the baseline refrigerant pressure being a pressure required to condense a vapor fraction of the two phase hydrocarbon refrigerant at an ambient condition surrounding the hydrocarbon refrigerant;mixing a sorbent hydrocarbon of a molecular weight at least 14 greater than the hydrocarbon refrigerant with the two phase hydrocarbon refrigerant to form a hydrocarbon mixture;cooling the hydrocarbon mixture until the hydrocarbon mixture is substantially condensed;increasing a pressure of the hydrocarbon mixture to a pressure greater than the baseline refrigerant pressure;fractionally distilling the hydrocarbon mixture into a lighter overhead hydrocarbon stream and a heavier hydrocarbon liquid in a distillation tower, the lighter overhead hydrocarbon stream being the liquid hydrocarbon refrigerant and the heavier hydrocarbon liquid being the sorbent hydrocarbon, andcooling the sorbent hydrocarbon. 2. The process of claim 1, further comprising: flashing the supplied liquid hydrocarbon refrigerant to remove a vapor portion; andmixing the removed vapor portion with the vaporized hydrocarbon refrigerant from the heat exchanger. 3. The process of claim 2, wherein the vapor portion is mixed with the vaporized hydrocarbon refrigerant after the sorbent hydrocarbon is mixed with the hydrocarbon refrigerant stream. 4. The process of claim 1, wherein the hydrocarbon mixture is heated with the sorbent hydrocarbon from the distillation tower. 5. The process of claim 1, wherein the hydrocarbon refrigerant includes at least one of: (i) ethane, (ii) propane, (iii) butane, (iv) ethylene, (v) propylene, and (vi) butylenes. 6. The process of claim 1, wherein the sorbent hydrocarbon includes one of: (i) propylene, (ii) propane, (iii) butane, and (iv) a hydrocarbon having a molecular weight between that of proplyene and decane. 7. A mixed refrigerant process, comprising: supplying a hydrocarbon refrigerant with a molecular weight of between 28 and 72 to a pressure reducer, the hydrocarbon refrigerant being a liquid when supplied;flashing the supplied liquid hydrocarbon refrigerant to a pressure less than a supplied pressure and greater than a refrigeration pressure to remove a vapor portion;reducing the pressure of the liquid hydrocarbon refrigerant to produce a two phase refrigerant;delivering the two phase hydrocarbon refrigerant to at least one heat exchanger to cool to at least one process stream, wherein the two phase hydrocarbon refrigerant is vaporized in the at least one heat exchanger;increasing a pressure of the vaporized two phase hydrocarbon refrigerant to a pressure less than a baseline refrigerant pressure, the baseline refrigerant pressure being a pressure required to condense a vapor fraction of the two phase hydrocarbon refrigerant at an ambient condition surrounding the hydrocarbon refrigerant;mixing a sorbent hydrocarbon of a molecular weight at least 14 greater than the hydrocarbon refrigerant with the two phase hydrocarbon refrigerant to form a hydrocarbon mixture;cooling the hydrocarbon mixture until the hydrocarbon mixture is substantially condensed;increasing a pressure of the hydrocarbon mixture to a pressure greater than the baseline refrigerant pressure;fractionally distilling the hydrocarbon mixture into a lighter overhead hydrocarbon stream and a less volatile hydrocarbon liquid in a distillation tower, the lighter overhead hydrocarbon stream being the liquid hydrocarbon refrigerant and the less volatile bottom product hydrocarbon liquid being the sorbent hydrocarbon, andcooling the sorbent hydrocarbon.