Sorption cooling process and system
    31.
    发明授权
    Sorption cooling process and system 失效
    吸附冷却过程和系统

    公开(公告)号:US5802870A

    公开(公告)日:1998-09-08

    申请号:US850544

    申请日:1997-05-02

    CPC classification number: F25B49/046 F25B17/083 Y02B30/64

    Abstract: A process and a system are disclosed for sorption heating and cooling which comprise at least 2 sorption zones. Each sorption zone comprises a heat transfer zone and an adsorption zone containing a sorbent such that the heat transfer zone is in intimate thermal contact with the adsorption zone to permit an essentially uniform temperature lengthwise through the sorption zone and thereby employ essentially all of the sorbent in the process at all times. The process comprises passing heat transfer streams such as a hot stream, a cold stream, and a recirculation stream through the heat transfer zone and routing a refrigerant through the adsorption zone of each sorption zone to affect a desorption stroke, an intermediate stroke and an adsorption stroke in the adsorption zone. Rotary and multi-port valves are employed to circulate the refrigerant and the heat transfer streams. The resulting sorption cooling process achieves a significantly higher coefficient of performance than the prior art.

    Abstract translation: 公开了用于吸附加热和冷却的方法和系统,其包括至少2个吸附区。 每个吸附区包括传热区和含有吸附剂的吸附区,使得传热区与吸附区紧密地热接触,以允许纵向通过吸附区基本均匀的温度,从而基本上使用基本上所有的吸附剂 这个过程在任何时候。 该方法包括使热流,例如热流,冷流和再循环流通过传热区,并将制冷剂穿过每个吸附区的吸附区,以影响解吸行程,中间冲程和吸附 吸入区中风。 旋转和多口阀用于循环制冷剂和传热流。 所得到的吸附冷却过程实现了比现有技术显着更高的性能系数。

    Recovery and purification of refrigerants
    32.
    发明授权
    Recovery and purification of refrigerants 失效
    制冷剂的回收和净化

    公开(公告)号:US5620502A

    公开(公告)日:1997-04-15

    申请号:US474818

    申请日:1995-06-07

    Abstract: A process and apparatus for the recovery and purification of a contaminated refrigerant withdrawn from a refrigeration or refrigerant recovery system which employs a compressor and an adsorbent selective for the adsorption of halogenated hydrocarbons. The adsorbent is selected from the group consisting of silicalite, faujasites, steamed and rare earth exchanged zeolite Y, mordenite, ZSM-5 and mixtures thereof, and more particularly the group consisting of a low cerium rare earth exchanged zeolite Y-84, a low cerium rare earth exchanged zeolite LZ-210, Breck Structure Six, ECR-32, and mixtures thereof. A significant increase in the capacity of these adsorbents over conventional adsorbents combined with the use of novel process steps to recover, purify and return a purified refrigerant to the refrigeration system result in significant cost savings at reduced risk of release of halogenated hydrocarbons to the environment.

    Abstract translation: 一种用于回收和净化从制冷或制冷剂回收系统中排出的受污染制冷剂的方法和装置,其使用压缩机和吸附卤代烃的吸附剂。 吸附剂选自硅沸石,八面沸石,蒸汽和稀土交换的沸石Y,丝光沸石,ZSM-5及其混合物,更特别的是低铈稀土交换沸石Y-84,低 铈稀土交换沸石LZ-210,Breck Structure Six,ECR-32及其混合物。 与常规吸附剂相比,这些吸附剂的能力显着增加,并结合使用新的工艺步骤来回收,净化和将纯化的制冷剂返回到制冷系统,导致显着的成本节省,同时降低将卤代烃释放到环境中的风险。

    Combination catalyst/adsorber system for treating an engine exhaust gas
stream
    33.
    发明授权
    Combination catalyst/adsorber system for treating an engine exhaust gas stream 失效
    用于处理发动机废气流的组合催化剂/吸附器系统

    公开(公告)号:US5531068A

    公开(公告)日:1996-07-02

    申请号:US492379

    申请日:1995-06-19

    Abstract: A process for treating an engine exhaust gas stream is disclosed. The process involves arranging a catalyst bed and a molecular sieve bed side by side with a connecting pipe between and parallel to the two beds. When the engine is first started, the cool exhaust is flowed through the catalyst bed, then through the connecting pipe, then through the molecular sieve bed and finally discharged to the atmosphere. When the molecular sieve bed reaches a temperature of about 150.degree. C. to about 200.degree. C. the exhaust stream is diverted such that it is first flowed through the molecular sieve bed, to desorb the adsorbed hydrocarbons, and then through the catalyst bed and finally discharged to the atmosphere. Finally, when all the hydrocarbons are desorbed from the molecular sieve bed, the exhaust stream is diverted such that it is flowed through the catalyst bed and then discharged to the atmosphere.

    Abstract translation: 公开了一种用于处理发动机废气流的方法。 该方法包括在两个床之间并且平行于两个床之间的连接管并排布置催化剂床和分子筛床。 当发动机首次启动时,冷却排气通过催化剂床,然后通过连接管,然后通过分子筛床,最后排放到大气中。 当分子筛床达到约150℃至约200℃的温度时,排气流被转向,使其首先流过分子筛床,以解吸吸附的烃,然后通过催化剂床和 终于排到了大气层。 最后,当所有的烃从分子筛床上解吸时,排气流被转向,使其流过催化剂床,然后排放到大气中。

    Method of coating aluminum substrates with solid adsorbent
    34.
    发明授权
    Method of coating aluminum substrates with solid adsorbent 失效
    用固体吸附剂涂覆铝基材的方法

    公开(公告)号:US5260243A

    公开(公告)日:1993-11-09

    申请号:US895975

    申请日:1992-06-09

    Abstract: Layered adsorbent-substrate tubes are prepared by a method comprising heating the surface of an aluminum substrate, contacting the surface of the substrate with a slurry containing the adsorbent and a binder, and heating the coatings to form hardened surfaces which can have excellent adsorption and mechanical properties in devices for cooling or heating by adsorption of refrigerating fluid on a solid adsorbent.

    Abstract translation: 通过包括加热铝基材的表面,使基材表面与含有吸附剂和粘合剂的浆料接触并且加热涂层以形成硬化表面的方法来制备分层的吸附剂 - 基材管,该表面可以具有优异的吸附和机械 通过在固体吸附剂上吸附冷冻液来冷却或加热的装置中的性质。

    Use of a molecular sieve bed to minimize emissions during cold start of
internal combustion engines
    35.
    发明授权
    Use of a molecular sieve bed to minimize emissions during cold start of internal combustion engines 失效
    使用分子筛床来最大限度地减少内燃机冷起动时的排放

    公开(公告)号:US5051244A

    公开(公告)日:1991-09-24

    申请号:US556149

    申请日:1990-07-20

    Abstract: This invention relates to a process for treating an engine exhaust gas stream. The process involves first flowing the engine exhaust stream, which is relatively cool, over an adsorbent zone which comprises an adsorbent bed, i.e., a molecular sieve bed, capable of preferentially adsorbing pollutants such as hydrocarbons. This provides a first exhaust stream which is flowed over a primary castalyst which converts the pollutants to innocuous compounds and then discharging the resultant treated exhaust stream to the atmosphere. When the adsorbent bed reaches a temperature of about 150.degree. C., the entire engine exhaust stream is completely diverted over the primary catalyst. When the inlet temperature to the primary catalyst has reached about 350.degree. C., a minor portion of the engine exhaust stream is diverted over the adsorbent bed to desorb the pollutants adsorbed on the bed and carry them over the primary catalyst where they are converted to innocuous components. After a certain amount of time, the entire engine exhaust stream is again diverted over the primary catalyst, thereby isolating the adsorbent bed to minimize deterioration. The adsorbent zone may also have a secondary catalyst bed arranged immediately after it.

    Abstract translation: 本发明涉及一种处理发动机废气流的方法。 该方法首先使相对较冷的发动机废气流在包括能够优先吸附诸如烃之类的污染物的吸附床(即分子筛床)的吸附区上。 这提供了第一排气流,其流过主浇铸液,其将污染物转化为无害化合物,然后将得到的经处理的废气流排放到大气中。 当吸附剂床达到约150℃的温度时,整个发动机废气流完全转移到主催化剂上。 当初级催化剂的入口温度达到约350℃时,发动机废气流的一小部分被转移到吸附剂床上以解吸吸附在床上的污染物,并将它们运送到主催化剂上,并将它们转化为 无害组件。 经过一定时间后,整个发动机废气流再次转移到初级催化剂上,从而隔离吸附剂床以使其劣化最小化。 吸附剂区也可以具有紧邻其后布置的第二催化剂床。

    Combined temperature controlled adsorption and heat pump process for fuel ethanol dehydration
    37.
    发明授权
    Combined temperature controlled adsorption and heat pump process for fuel ethanol dehydration 有权
    燃料乙醇脱水联合控温吸附和热泵过程

    公开(公告)号:US08067646B2

    公开(公告)日:2011-11-29

    申请号:US12337154

    申请日:2008-12-17

    CPC classification number: C10L1/02 B01D3/002 C10L1/023

    Abstract: Systems and processes for dehydration of a process stream in the production of motor fuel grade ethanol (MFGE) can include temperature controlled adsorption of water in the process stream, and heat pumping of the associated heat of adsorption. The process can include providing a process stream (110) including ethanol and water to a first temperature controlled adsorber (102) where water is removed by adsorption to produce an MFGE product stream (114) and an associated heat of adsorption. A cooling fluid can be provided to the first temperature controlled adsorber (102) to remove heat of adsorption and produce a heated cooling fluid (120). Heat from the heated cooling fluid can be provided to a heat sink.

    Abstract translation: 在汽油燃料级乙醇(MFGE)生产中脱水工艺流的系统和方法可以包括温度控制的工艺流中的水吸附,以及相关的吸附热的热泵送。 该方法可以包括向第一温度控制的吸附器(102)提供包括乙醇和水的工艺流(110),其中通过吸附除去水以产生MFGE产物流(114)和相关联的吸热。 可以向第一温度控制的吸附器(102)提供冷却流体以除去吸附热并产生加热的冷却流体(120)。 来自加热的冷却流体的热量可以提供给散热器。

    COMBINED TEMPERATURE CONTROLLED ADSORPTION AND HEAT PUMP PROCESS FOR FUEL ETHANOL DEHYDRATION
    38.
    发明申请
    COMBINED TEMPERATURE CONTROLLED ADSORPTION AND HEAT PUMP PROCESS FOR FUEL ETHANOL DEHYDRATION 有权
    用于燃料乙醇脱氢的组合温度控制吸附和热泵过程

    公开(公告)号:US20100132254A1

    公开(公告)日:2010-06-03

    申请号:US12337154

    申请日:2008-12-17

    CPC classification number: C10L1/02 B01D3/002 C10L1/023

    Abstract: Systems and processes for dehydration of a process stream in the production of motor fuel grade ethanol (MFGE) can include temperature controlled adsorption of water in the process stream, and heat pumping of the associated heat of adsorption. The process can include providing a process stream (110) including ethanol and water to a first temperature controlled adsorber (102) where water is removed by adsorption to produce an MFGE product stream (114) and an associated heat of adsorption. A cooling fluid can be provided to the first temperature controlled adsorber (102) to remove heat of adsorption and produce a heated cooling fluid (120). Heat from the heated cooling fluid can be provided to a heat sink.

    Abstract translation: 在汽油燃料级乙醇(MFGE)生产中脱水工艺流的系统和方法可以包括温度控制的工艺流中的水吸附,以及相关的吸附热的热泵送。 该方法可以包括向第一温度控制的吸附器(102)提供包括乙醇和水的工艺流(110),其中通过吸附除去水以产生MFGE产物流(114)和相关联的吸热。 可以向第一温度控制的吸附器(102)提供冷却流体以除去吸附热并产生加热的冷却流体(120)。 来自加热的冷却流体的热量可以提供给散热器。

    Adsorption separation system
    40.
    发明授权
    Adsorption separation system 失效
    吸附分离系统

    公开(公告)号:US07022229B1

    公开(公告)日:2006-04-04

    申请号:US10740875

    申请日:2003-12-19

    CPC classification number: B01D15/1892

    Abstract: An apparatus is presented for separating chemicals using adsorption separation methods. The apparatus uses a plurality of adsorption units holding adsorbent, where the adsorption units are serially connected and are moved to shift the relative position of the feeds and drawoffs to the apparatus.

    Abstract translation: 提出了一种使用吸附分离方法分离化学品的装置。 该装置使用多个吸附单元,其吸附单元串联连接并移动,从而将进料和抽出物的相对位置移动到设备。

Patent Agency Ranking