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公开(公告)号:US09927178B1
公开(公告)日:2018-03-27
申请号:US15149152
申请日:2016-05-08
申请人: TDA Research, Inc.
CPC分类号: F28C1/04 , F01K9/003 , F02C6/18 , F05D2220/31 , F05D2220/32 , F05D2260/213
摘要: A seasonal process that captures stores and uses water in an ambient temperature-dependent manner to improve the efficiency of a natural gas power plant, comprising: (a) providing a natural gas power plant, the natural gas power plant having a flue gas stream, a cooling tower, and a gas turbine; (b) providing a water collection system; (c) providing a water storage facility; wherein the flue gas stream comprises uncondensed water vapor; wherein the water collection system is operably connected to the flue gas stream and the flue gas stream is directed to flow, at least in part, into the water collection system; wherein the water collection system is operably connected to the water storage facility; wherein the water storage facility is operably connected to the cooling tower and the water storage facility is operably connected to the gas turbine; wherein the process comprises the following steps of condensing flue gas water or using water that has been condensed from the flue gas stream based on outdoor ambient dry bulb temperature: (I) Only condensing water from the flue gas stream to produce a condensed water stream if outdoor ambient dry bulb temperature is less than 85° F.; (II) Only using condensed water to spray cool the cooling tower if outdoor ambient dry bulb temperature is at least 85° F.; (III) Only using condensed water to fog cool the gas turbine if outdoor ambient dry bulb temperature is at least 55° F.; wherein condensed water that is not immediately used to cool the cooling tower or to fog cool the gas turbine is stored in the water storage facility; and wherein the process uses a total amount of water on an annual basis to cool the cooling tower and to fog cool the gas turbine that does not exceed the annual amount of water condensed from the flue gas stream. Optionally, the process has a cooling tower that is a dry cooling tower and condensed water is used to spray cool the dry cooling tower, or the cooling tower is a wet cooling tower, or the cooling tower is a hybrid wet-dry cooling tower. The process may further comprise a water collection system having a three stage desiccant cycle and a calcium chloride desiccant that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condensing column that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure or comprises plastic piping or plastic vessels. Or the process may further comprise using a water collection system having at least one direct contact condenser and a rotating wheel heat exchanger that recovers at least about 60 wt % of the water from the flue gas, operates at or above ambient pressure, or further comprises plastic piping or plastic vessels. The coefficient of performance for the cooling process is optionally at least 2.0.
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2.
公开(公告)号:US20150010452A1
公开(公告)日:2015-01-08
申请号:US14325519
申请日:2014-07-08
申请人: TDA Research, Inc.
CPC分类号: B01D53/06 , B01D2253/104 , B01D2257/504 , B01D2258/0283 , B01D2259/4009 , B01D2259/402 , B01D2259/4065 , Y02C10/04 , Y02C10/06 , Y02C10/08
摘要: A circulating moving bed and process for separating a carbon dioxide from a gas stream is disclosed. The circulating moving bed can include an adsorption reactor and a desorption reactor, and a sorbent that moves through the two reactors. The sorbent can enter the adsorptive reactor and one end and move to an exit point distal to its entry point, while a CO2 feed stream can enter near the distal point and move countercurrently through the sorbent to exit at a position near the entry point of the sorbent. The sorbent can adsorb the CO2 by concentration swing adsorption and adsorptive displacement. The sorbent can then transfer to a regeneration reactor and can move countercurrently against a flow of steam through the regeneration reactor. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing desorption and desorptive displacement with steam.
摘要翻译: 公开了一种循环移动床和用于从气流中分离二氧化碳的方法。 循环移动床可以包括吸附反应器和解吸反应器,以及移动通过两个反应器的吸附剂。 吸附剂可以进入吸附反应器并且一端移动到远离其入口点的出口点,而CO 2进料流可以进入远端附近并且逆流地通过吸附剂,以在接近入口处的入口附近的位置离开 吸附剂 吸附剂可通过浓度变化吸附和吸附位移吸附CO2。 然后,吸附剂可以转移到再生反应器,并且可以逆流逆向通过再生反应器的蒸汽流。 吸附剂可以再生,并且通过使用浓缩挥发解吸和用蒸汽解吸取代从吸附剂中解吸二氧化碳来重新捕获二氧化碳。
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公开(公告)号:US20150007725A1
公开(公告)日:2015-01-08
申请号:US14325579
申请日:2014-07-08
IPC分类号: B01D53/06
CPC分类号: B01D53/83 , B01D53/06 , B01D53/08 , B01D53/62 , B01D2251/304 , B01D2251/306 , B01D2253/104 , B01D2258/0283 , B01D2259/4009 , Y02C10/04 , Y02C10/08
摘要: A rotary moving bed and process for separating a carbon dioxide from a gas stream is disclosed. The rotary moving bed can have a rotational assembly rotating on a vertical axis, and a plurality of sorbent cells positioned horizontally to the axis of rotation that fills a vertical space in the moving bed, where the sorbent cells adsorb the carbon dioxide by concentration swing adsorption and adsorptive displacement. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing adsorption and desorptive displacement with steam. The gas flows in the system flow in a direction horizontal to the axis of rotation and in a direction opposite the rotational movement of the sorbent cells.
摘要翻译: 公开了一种用于从气流中分离二氧化碳的旋转移动床和方法。 旋转移动床可以具有在垂直轴线上旋转的旋转组件和水平地定位在旋转轴线上的多个吸附单元,其填充移动床中的垂直空间,其中吸附单元通过浓度变化吸附吸附二氧化碳 和吸附位移。 吸附剂可以再生,并且通过使用浓度变化吸附和蒸汽的解吸位移从吸附剂中解吸二氧化碳来重新捕获二氧化碳。 气体在系统流动中沿着与旋转轴线水平的方向和与吸附剂单元的旋转运动相反的方向流动。
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公开(公告)号:US20210016220A1
公开(公告)日:2021-01-21
申请号:US17034283
申请日:2020-09-28
发明人: Jeannine Elizabeth Elliott , Robert James Copeland , Jeff Lind , Daniel P. Leta , Patrick P. McCall
摘要: A system and method for separating and/or purification of CO2 gas from a CO2 feed stream is described. The system and method include a plurality of fixed sorbent beds, adsorption zones and desorption zones, where the sorbent beds are connected via valve and lines to create a simulated moving bed system, where the sorbent beds move from one adsorption position to another adsorption position, and then into one regeneration position to another regeneration position, and optionally back to an adsorption position. The system and method operate by concentration swing adsorption/desorption and by adsorptive/desorptive displacement.
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公开(公告)号:US20150007727A1
公开(公告)日:2015-01-08
申请号:US14325637
申请日:2014-07-08
发明人: Jeannine Elizabeth Elliott , Robert James Copeland , Daniel P. Leta , Patrick P. McCall , Chuansheng Bai , Bruce A. DeRites
CPC分类号: B01D53/06 , B01D53/08 , B01D2251/30 , B01D2251/40 , B01D2253/104 , B01D2253/1122 , B01D2257/504 , B01D2258/0283 , B01D2259/40086 , B01D2259/4009 , B01D2259/402 , B01D2259/4065 , Y02C10/04 , Y02C10/08
摘要: A process for separating a carbon dioxide from a gas stream is disclosed. The process can include passing the gas stream over a sorbent that adsorbs the carbon dioxide by concentration swing adsorption and adsorptive displacement. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing adsorption and desorptive displacement. A carbon dioxide separation system is also disclosed. Neither the system nor the process rely on temperature swing or pressure swing adsorption.
摘要翻译: 公开了一种从气流中分离二氧化碳的方法。 该方法可以包括使气流通过吸附剂吸附二氧化碳,通过浓缩变化吸附和吸附位移。 吸附剂可以再生,二氧化碳通过使用浓度变化吸附和解吸位移从吸附剂中解吸二氧化碳而重新捕获。 还公开了二氧化碳分离系统。 系统和过程都不依赖于温度摆动或变压吸附。
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6.
公开(公告)号:US20150007726A1
公开(公告)日:2015-01-08
申请号:US14325552
申请日:2014-07-08
发明人: Jeannine Elizabeth Elliott , Robert James Copeland , Jeff Lind , Daniel P. Leta , Patrick P. McCall
IPC分类号: B01D53/04
CPC分类号: B01D53/0446 , B01D53/06 , B01D53/10 , B01D2253/104 , B01D2257/504 , B01D2258/0283 , B01D2259/40003 , B01D2259/40086 , B01D2259/4009 , B01D2259/402 , B01D2259/4065 , B01D2259/4067 , Y02C10/08
摘要: A system and method for separating and/or purification of CO2 gas from a CO2 feed stream is described. The system and method include a plurality of fixed sorbent beds, adsorption zones and desorption zones, where the sorbent beds are connected via valve and lines to create a simulated moving bed system, where the sorbent beds move from one adsorption position to another adsorption position, and then into one regeneration position to another regeneration position, and optionally back to an adsorption position. The system and method operate by concentration swing adsorption/desorption and by adsorptive/desorptive displacement.
摘要翻译: 描述了从CO 2进料流中分离和/或纯化CO 2气体的系统和方法。 该系统和方法包括多个固定吸附剂床,吸附区和解吸区,其中吸附剂床通过阀和管线连接以产生模拟移动床系统,其中吸附剂床从一个吸附位置移动到另一个吸附位置, 然后进入一个再生位置到另一个再生位置,并且任选地返回到吸附位置。 该系统和方法通过浓度变化吸附/解吸和吸附/解吸位移操作。
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公开(公告)号:US12121846B2
公开(公告)日:2024-10-22
申请号:US17034283
申请日:2020-09-28
发明人: Jeannine Elizabeth Elliott , Robert James Copeland , Jeff Lind , Daniel P. Leta , Patrick P. McCall
CPC分类号: B01D53/0446 , B01D53/06 , B01D53/10 , B01D2253/104 , B01D2257/504 , B01D2258/0283 , B01D2259/40003 , B01D2259/40086 , B01D2259/4009 , B01D2259/402 , B01D2259/4065 , B01D2259/4067 , Y02C20/40
摘要: A system and method for separating and/or purification of CO2 gas from a CO2 feed stream is described. The system and method include a plurality of fixed sorbent beds, adsorption zones and desorption zones, where the sorbent beds are connected via valve and lines to create a simulated moving bed system, where the sorbent beds move from one adsorption position to another adsorption position, and then into one regeneration position to another regeneration position, and optionally back to an adsorption position. The system and method operate by concentration swing adsorption/desorption and by adsorptive/desorptive displacement.
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公开(公告)号:US20240238118A1
公开(公告)日:2024-07-18
申请号:US18413629
申请日:2024-01-16
申请人: TDA Research, Inc
IPC分类号: A61F7/02 , A41D13/002 , A41D13/005 , A61F7/00
CPC分类号: A61F7/02 , A41D13/0025 , A41D13/0053 , A61F2007/0018 , A61F2007/006 , A61F2007/0067 , A61F2007/0234 , A61F2007/026
摘要: A cooling garment for use by workers in hot, humid climates comprising: a moisture-wicking under layer; an outer layer with an air permeability less than 200 L/m2/s when subjected to 125 Pascals of air pressure; at least one air channel formed between the layers and supported in at least some locations by a porous filler material; and an above ambient pressure gas supply attached operably to the inlet of the channel. Also a cooling garment comprising: a moisture-wicking under layer; an outer layer; one large air channel formed between the layers; tacks connecting the outer layer to the moisture-wicking under layer to prevent ballooning; and an above ambient pressure gas supply operably attached to the inlet of the channel.
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公开(公告)号:US09539540B2
公开(公告)日:2017-01-10
申请号:US14325579
申请日:2014-07-08
CPC分类号: B01D53/83 , B01D53/06 , B01D53/08 , B01D53/62 , B01D2251/304 , B01D2251/306 , B01D2253/104 , B01D2258/0283 , B01D2259/4009 , Y02C10/04 , Y02C10/08
摘要: A rotary moving bed and process for separating a carbon dioxide from a gas stream is disclosed. The rotary moving bed can have a rotational assembly rotating on a vertical axis, and a plurality of sorbent cells positioned horizontally to the axis of rotation that fills a vertical space in the moving bed, where the sorbent cells adsorb the carbon dioxide by concentration swing adsorption and adsorptive displacement. The sorbent can be regenerated and the carbon dioxide recaptured by desorbing the carbon dioxide from the sorbent using concentration swing adsorption and desorptive displacement with steam. The gas flows in the system flow in a direction horizontal to the axis of rotation and in a direction opposite the rotational movement of the sorbent cells.
摘要翻译: 公开了一种用于从气流中分离二氧化碳的旋转移动床和方法。 旋转移动床可以具有在垂直轴线上旋转的旋转组件和水平地定位在旋转轴线上的多个吸附单元,其填充移动床中的垂直空间,其中吸附单元通过浓度变化吸附吸附二氧化碳 和吸附位移。 吸附剂可以再生,并且通过使用浓度变化吸附和蒸汽的解吸位移从吸附剂中解吸二氧化碳来重新捕获二氧化碳。 气体在系统流动中沿着与旋转轴线水平的方向和与吸附剂单元的旋转运动相反的方向流动。
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10.
公开(公告)号:US10899973B1
公开(公告)日:2021-01-26
申请号:US16292096
申请日:2019-03-04
申请人: TDA Research, Inc.
摘要: The present invention provides a steam reforming process for heavy oil or hydrocarbons using a circulating fluidized bed reactor, the process having a reforming step and a regeneration step, wherein the reforming step and the regeneration step comprise a fluidized reactor containing a fluidizable nickel-containing reforming catalyst and produce hydrogen as a product of the reforming bed. The invention produces high purity hydrogen in the synthesis gas product stream and avoids irreversible fouling on the catalyst.
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