# US 6,066,192 A · Method of treating or recovering gaseous hydrocarbon contained in waste gas > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 6,066,192 A - Document ID: US6066192A - Status: Granted - Kind: A - Application number: 09/077,874 - Filed: 1998-06-08 - Granted: 2000-05-23 - Earliest claimed: 1995-12-06 - Assignees: Cosmo Engineering Co., Ltd.; Idemitsu Engineering Co., Ltd. - Inventors: Kawai Toshinaga; Tahara Hiroshi; Suzuki Kenithirou - Web page: https://patentgrep.com/patent/US6066192A ## CPC - B01D 53/0438: {Cooling or heating systems} - B01D 53/0431: {Beds with radial gas flow} - B01D 53/0423: {Beds in columns} - B01D 53/047: Pressure swing adsorption - B01D 2253/102: Carbon - B01D 2253/106: Silica or silicates - B01D 2253/108: Zeolites - B01D 2253/308: Pore size - B01D 2256/24: Hydrocarbons - B01D 2259/40052: Recycled product or process gas - B01D 2259/401: using a single bed - B01D 2259/402: using two beds - B01D 2259/4146: Contiguous multilayered adsorbents - B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28) ## Abstract A method of treating a gaseous hydrocarbon contained in waste gas by using adsorbent layers of single-tower or multi-tower configuration is characterized in that (1) double-cylinder type or multi-cylinder type adsorption apparatus, in which each adsorbent layer is indirectly cooled by cooling water, are employed as adsorption apparatus; (2) each adsorbent layer is a packed layer of one or more kinds of materials selected from activated carbon, synthetic zeolites and hydrophobic silica gel; (3) swing time required for switching between adsorption and desorption processes is set to 1 to 15 minutes; (4) each adsorbent layer is evacuated under vacuum while being purged by using part of clean gas evacuated from each adsorbent layer and/or air in the desorption process; and (5) the gaseous hydrocarbon is recovered from outflow purge gas. This method makes it possible to prevent abnormal temperature increase within each adsorbent layer and enhance the safety of the apparatus. It also makes it possible to decrease the residual gaseous hydrocarbon content of the waste gas released into the atmosphere down to 1 vol % or less. ## Claims ### Claim 1 A method of treating or recovering a gaseous hydrocarbon contained in waste gas employing a pair of adsorption apparatus which alternately performs adsorption and desorption processes, in which the waste gas containing the gaseous hydrocarbon is passed through one of the adsorption apparatus so that the gaseous hydrocarbon is adsorbed by adsorbent layers, enabling the adsorption apparatus to release the treated waste gas containing substantially no gaseous hydrocarbon, while at the same time the other adsorption apparatus is switched to the desorption process, the gaseous hydrocarbon adsorbed by the adsorbent is drawn by a vacuum pump to separate the gaseous hydrocarbon from said adsorbent layers, and the gaseous hydrocarbon is recovered from separated outflow purge gas, said method being characterized in that: (1) double-cylinder or multi-cylinder adsorption apparatus, in which each adsorbent layer is indirectly cooled by cooling water, are employed as said adsorption apparatus; (2) adsorbent layers include a first layer employing the hydrophobic silica gel placed on an upstream side and a second layer employing the activated carbon placed on a downstream side as said adsorbent layers; (3) swing time required for switching between the adsorption and desorption processes is set to 1 to 15 minutes; (4) each adsorbent layer is evacuated under vacuum while being purged by using part of clean gas evacuated from each adsorbent layer and/or air in the desorption process; and (5) the gaseous hydrocarbon is recovered from the outflow purge gas. ### Claim 2 (depends on 1) A method of treating or recovering the gaseous hydrocarbon contained in the waste gas as defined in claim 1, which is characterized in that the density of the gaseous hydrocarbon contained in the waste gas released from said adsorbent layers into the atmosphere is lowered to 1 vol % or less. ### Claim 3 A method of treating or recovering a gaseous hydrocarbon contained in waste gas employing a pair of adsorption apparatus which alternately performs adsorption and desorption processes, in which the waste gas containing the gaseous hydrocarbon is passed through one of the adsorption apparatus so that the gaseous hydrocarbon is adsorbed by adsorbent layers, enabling the adsorption apparatus to release the treated waste gas containing substantially no gaseous hydrocarbon, while at the same time the other adsorption apparatus is switched to the desorption process, the gaseous hydrocarbon adsorbed by the adsorbent is drawn by a vacuum pump to separate the gaseous hydrocarbon from said adsorbent layers, and the gaseous hydrocarbon is recovered from separated outflow purge gas, said method being characterized in that: (1) double-cylinder or multi-cylinder adsorption apparatus, in which each adsorbent layer is indirectly cooled by cooling water, are employed as said adsorption apparatus; (2) each adsorbent layer is a packed layer of one or more kinds of materials selected from activated carbon, synthetic zeolites and hydrophobic silica gel; (3) swing time required for switching between the adsorption and desorption processes is set to 1 to 15 minutes, and (4) each adsorbent layer is evacuated under vacuum while being purged by using part of clean gas evacuated from each adsorbent layer and/or air in the desorption process; and (5) the gaseous hydrocarbon is recovered from the outflow purge gas, and as means for recovering the gaseous hydrocarbon from the waste gas which is used in the desorption process employing a combination of evacuation under vacuum and purging operation, the steps of: 1) causing the outflow purge gas of a completely dry vacuum pump which is employed as said vacuum pump to be discharged upon increasing its gas pressure to 10 atmospheres, exceeding the normal atmospheric pressure; and 2) increasing the density of the gaseous hydrocarbon contained in the outflow purge gas by using as a cooling medium of the vacuum pump a liquid hydrocarbon of the same properties as the gaseous hydrocarbon contained in the waste gas and returning resultant gaseous hydrocarbon to an outlet pipe of a desorption apparatus, or by injecting the liquid or gaseous hydrocarbon of the same properties into the adsorption apparatus upon completion of the adsorption process to purge the apparatus and evacuating it under vacuum; and then accelerating liquefaction of the gaseous hydrocarbon by cooling it, or accelerating recovery of the gaseous hydrocarbon by an absorption method. ### Claim 4 (depends on 3) A method of treating or recovering the gaseous hydrocarbon contained in the waste gas as defined in claim 3 which is characterized in that a portion of the waste gas which has not been condensed in the step of liquefaction by condensation of the outflow purge gas is returned to an intake port of the absorption apparatus. ### Claim 5 (depends on 4) A method of treating or recovering the gaseous hydrocarbon contained in the waste gas as defined in claim 4, wherein the density of the gaseous hydrocarbon contained in the waste gas released from said adsorbent layers into the atmosphere is lowered to 1 vol % or less. ### Claim 6 (depends on 3) A method of treating or recovering the gaseous hydrocarbon contained in the waste gas as defined in claim 3, wherein the density of the gaseous hydrocarbon contained in the waste gas released from said adsorbent layers into the atmosphere is lowered to 1 vol % or less. ### Claim 7 A method of treating or recovering a gaseous hydrocarbon contained in waste gas employing a pair of adsorption apparatus which alternately performs adsorption and desorption processes, in which the waste gas containing the gaseous hydrocarbon is passed through one of the adsorption apparatus so that the gaseous hydrocarbon is adsorbed by adsorbent layers, enabling the adsorption apparatus to release the treated waste gas containing substantially no gaseous hydrocarbon, while at the same time the other adsorption apparatus is switched to the desorption process, the gaseous hydrocarbon adsorbed by the adsorbent is drawn by a vacuum pump to separate the gaseous hydrocarbon from said adsorbent layers, and the gaseous hydrocarbon is recovered from separated outflow purge gas, said method being characterized in that: (1) double-cylinder or multi-cylinder adsorption apparatus, in which each adsorbent layer is indirectly cooled by cooling water, are employed as said adsorption apparatus; (2) each adsorbent layer is a packed layer of one or more kinds of materials selected from activated carbon, synthetic zeolites and hydrophobic silica gel; (3) swing time required for switching between the adsorption and desorption processes is set to 1 to 15 minutes, and at least a specified amount of air is used when the state of reduced pressure created in the desorption process is returned to the normal atmospheric pressure when switching between the adsorption and desorption processes, and (4) each adsorbent layer is evacuated under vacuum while being purged by using part of clean gas evacuated from each adsorbent layer and/or air in the desorption process; and (5) the gaseous hydrocarbon is recovered from the outflow purge gas. ### Claim 8 (depends on 7) A method of treating or recovering the gaseous hydrocarbon contained in the waste gas as defined in claim 7, wherein the density of the gaseous hydrocarbon contained in the waste gas released from said adsorbent layers into the atmosphere is lowered to 1 vol % or less.