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公开(公告)号:US12123617B2
公开(公告)日:2024-10-22
申请号:US18231069
申请日:2023-08-07
申请人: FFI IONIX IP, INC.
发明人: Bamdad Bahar , William Parmelee , Omar Abdelaziz , Qu Ming
CPC分类号: F24F3/1417 , B01D1/14 , B01D5/0003 , B01D5/0027 , B01D5/0039 , B01D5/0087 , B01D5/009 , B01D53/263 , B01D53/268 , C07D233/58 , C08L27/12 , F25B17/02 , B01D2252/30 , F24F3/001 , F24F2003/1458
摘要: A cooling system utilizes an organic ionic salt composition for dehumidification of an airflow. The organic ionic salt composition absorbs moisture from an inlet airflow to produce an outlet airflow with a reduce moisture from that of the inlet airflow. The organic ionic salt composition may be regenerated, wherein the absorbed moisture is expelled by heating with a heating device. The heating device may be an electrochemical heating device, such as a fuel cell, an electrochemical metal hydride heating device, an electrochemical heat pump or compressor, or a condenser of a refrigerant cycle, which may utilize an electrochemical pump or compressor. The efficiency of the cooling system may be increased by utilization of the waste heat the cooling system. The organic ionic salt composition may circulate back and forth or in a loop between a conditioner, where it absorbs moisture, to a regenerator, where moisture is desorbed by heating.
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公开(公告)号:US11658314B2
公开(公告)日:2023-05-23
申请号:US17793546
申请日:2021-01-12
发明人: Mads Bang , Deni Maric , Peter Leander Jensen , Fan Zhou
IPC分类号: H01M8/04007 , H01M8/04119 , B01D5/00 , F01N3/022
CPC分类号: H01M8/04007 , B01D5/0027 , F01N3/022 , H01M8/04164 , B01D2258/0208 , H01M2250/20
摘要: In order to prevent injury from hot exhaust gas, water is condensed by a metal net in the exhaust pipe.
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公开(公告)号:US20190210874A1
公开(公告)日:2019-07-11
申请号:US16354602
申请日:2019-03-15
发明人: Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC分类号: C01B3/52 , B01D53/26 , B01D5/00 , C01B3/58 , C01B3/38 , B01D61/36 , B01D53/76 , B01D53/48 , B01D53/14 , B01D53/047 , B01D53/04 , B01D50/00 , B01D46/00 , B01D29/66 , B01D29/27 , B01D17/02 , B01D47/10 , B01D53/12 , B01D53/18 , B01D53/32 , C01B3/56 , C01B3/24
CPC分类号: C01B3/52 , B01D5/0027 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D5/009 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/006 , B01D53/0423 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , C01B2203/0227 , C01B2203/0233 , C01B2203/025 , C01B2203/0261 , C01B2203/04 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0435 , C01B2203/045 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , H05K999/99 , Y02P20/13 , Y02P30/30
摘要: A system and method for processing unconditioned syngas first removes solids and semi -volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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公开(公告)号:US20190054392A1
公开(公告)日:2019-02-21
申请号:US16069367
申请日:2017-01-09
发明人: Markus LEHMANN
CPC分类号: B01D3/065 , B01D1/16 , B01D1/26 , B01D1/289 , B01D3/007 , B01D5/0027 , B01D5/0036 , B01D5/0039 , B01D5/006 , C02F1/041 , C02F1/12 , C02F2303/10
摘要: A low-temperature distillation facility for distilling a mixed fluid into a pure fluid. An aggregation device has an inlet connected to the vapour space of a supercooling chamber, wherein captured mixed fluid from an evaporator enters the supercooling chamber. The aggregation device's outlet is connected to the vapour space of a superheating chamber, wherein captured pure fluid from a condenser can be sprayed into the superheating chamber. An energy source cools the temperature in the supercooling chamber and heats the temperature in the superheating chamber. A heat exchanger is arranged between the exits of the supercooling chamber and of the superheating chamber. During the process, vapour flows from the supercooling chamber via the aggregation device to the superheating chamber.
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公开(公告)号:US20180200668A1
公开(公告)日:2018-07-19
申请号:US15410106
申请日:2017-01-19
申请人: Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
发明人: Larry Baxter , Aaron Sayre , Stephanie Burt , Nathan Davis
CPC分类号: B01D53/263 , B01D5/0027 , B01D5/003 , B01D5/0054 , B01D5/0087 , B01D53/265 , B01D2252/103 , B01D2252/30 , B01D2252/504 , B01D2258/0283 , C10L3/106 , C10L2290/12 , C10L2290/541
摘要: A method for continuously removing water vapor from a carrier gas is disclosed. This method includes, first, causing direct contact of the carrier gas with a liquid mixture in a separation chamber, the carrier gas condensing at a lower temperature than the water vapor. A combination of chemical effects cause the water vapor to condense, complex, or both condense and complex with the liquid mixture. The liquid mixture is chosen from the group consisting of: first, a combination of components that can be maintained in a liquid phase at a temperature below the water vapor's condensation point, whereby the water vapor condenses into the liquid mixture; second, a combination of components where at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas; and third, a combination of components that can both be maintained in a liquid phase at a temperature below the water vapor's condensation point, and wherein at least one component forms a chemical complex with the water vapor and thereby extracts at least a portion of the water vapor from the carrier gas. The liquid mixture is then reconstituted after passing through the separation chamber by a chemical separation process chosen to remove an equivalent amount of the water vapor from the liquid mixture as was removed from the carrier gas. The reconstituted liquid mixture is restored to temperature and pressure through heat exchange, compression, and expansion, as necessary, in preparation for recycling back to the separation chamber. The liquid mixture is then returned to the separation chamber. In this manner, the carrier gas leaving the exchanger has between 1% and 100% of the water vapor removed.
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6.
公开(公告)号:US10011483B2
公开(公告)日:2018-07-03
申请号:US15430654
申请日:2017-02-13
发明人: Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC分类号: C01B3/38 , C01B3/58 , C01B3/52 , C01B3/56 , B01D53/26 , B01D53/14 , B01D5/00 , B01D17/02 , B01D29/27 , B01D29/66 , B01D47/10 , B01D53/18 , B01D53/04 , B01D46/00 , B01D53/32 , B01D53/047 , B01D50/00 , B01D61/36 , B01D53/48 , B01D53/76 , B01D53/12
CPC分类号: C01B3/52 , B01D5/0027 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D5/009 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/006 , B01D53/0423 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , C01B2203/0227 , C01B2203/0233 , C01B2203/025 , C01B2203/0261 , C01B2203/04 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0435 , C01B2203/045 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , H05K999/99 , Y02P20/13 , Y02P30/30
摘要: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
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公开(公告)号:US20180036649A1
公开(公告)日:2018-02-08
申请号:US15732136
申请日:2017-09-22
申请人: Kai Jiang
发明人: Kai Jiang
CPC分类号: B01D5/0048 , B01D5/0027 , B01D5/0054 , B01D5/009 , C02F1/10 , C02F9/00 , C02F2303/04 , E03B3/11 , E03B3/28 , E03B3/40 , Y02A20/109
摘要: Applicant discloses a new viewpoint and its application for the freshwater generation here: Air temperature exchanges between the inside and outside of the deserts always play an important role in the generation of freshwater in desert environment. Because this procedure is continually happening in days and nights, and the desert area is large in the world, so, the amount of the water production by this way is extent to which one could be imagined. According the viewpoint disclosed here, it will bring big benefits to take over the shortage water plight and for the development of the desert. According this doctrine, the easiest way to collect the water from the desert is just setting an impermeable layer under the dune: the fresh water should flow out. By use of artificial stacked large amount sands can also obtain the freshwater in anywhere which the changes of the temperature are big.
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8.
公开(公告)号:US09816400B1
公开(公告)日:2017-11-14
申请号:US15053802
申请日:2016-02-25
IPC分类号: F01K23/04 , F01K17/04 , F01K11/02 , F24J3/08 , F03G6/00 , C02F1/04 , C02F1/16 , C02F103/08 , F01K7/32 , F03G7/05 , F01K25/10 , F01K7/22 , F28B9/10
CPC分类号: F01K17/04 , B01D5/0027 , B01D5/006 , C02F1/16 , C02F2103/08 , C02F2303/10 , F01K7/22 , F01K7/32 , F01K11/02 , F01K23/04 , F01K25/103 , F03G6/003 , F03G7/05 , F28B9/10 , Y02E10/10 , Y02E10/34 , Y02E10/40 , Y02E10/46
摘要: A unique method and ternary cycle process that captures heat from low temperature sources currently considered not commercially usable to produce electricity and desalinate water. In one cycle a novel flash tower operating at vacuum pressure causes a fraction of low temperature water to flash into steam. The steam passes to an indirect heat exchanger with a circulating refrigerating agent such as CO2, which condenses the steam on its outside surfaces to produce desalinated water product. The steam heat of condensation vaporizes the refrigerating agent, which is part of a binary refrigerate cycle that uniquely conditions it for turbine expansion to produce electricity in a connected electric generator.
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9.
公开(公告)号:US09504935B2
公开(公告)日:2016-11-29
申请号:US14379386
申请日:2012-11-02
发明人: Yi-Cheng Lin
CPC分类号: B01D5/0051 , B01D5/0027 , B01D5/0087 , B01D5/009 , B01D53/002 , B01D53/346 , B01D53/78 , B01D2252/103 , B01D2257/708 , B01D2258/02 , B05D3/0486
摘要: A process and apparatus for treatment of volatile organic compounds and the process comprises an untreated airflow dew point temperature sensing step of sensing a dew point temperature of the untreated airflow as a reference temperature, a humidification and condensation processing step of spraying water mist all over the exhaust gas flow and condensing the exhaust gas flow into condensate contained the volatile organic compounds, a treated exhaust gas flow dew point temperature sensing step of sensing a dew point temperature of the treated exhaust gas flow after the humidification and condensation processing step, a collection step of collecting dropped condensate from the humidification and condensation processing step and then transporting the dropped condensate back to the humidification and condensation processing step for circulation spray, and a control step of controlling the dew point temperature of the treated exhaust gas flow to be close to the reference temperature.
摘要翻译: 一种用于处理挥发性有机化合物的方法和装置,该方法包括:未处理气流露点温度检测步骤,用于检测未处理气流的露点温度作为参考温度;加湿和冷凝处理步骤, 排气流并将废气流冷凝成含有挥发性有机化合物的处理废气流露点温度检测步骤,其在加湿冷凝处理步骤之后检测经处理的废气流的露点温度;收集步骤 从加湿冷凝处理步骤收集掉的冷凝物,然后将滴下的冷凝物输送到用于循环喷雾的加湿冷凝处理步骤,以及控制处理废气流的露点温度接近于 参考温度。
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公开(公告)号:US09499404B2
公开(公告)日:2016-11-22
申请号:US14347431
申请日:2012-09-27
发明人: Ravi Chandran , Daniel Michael Leo , Shawn Robert Freitas , Dave G. Newport , Hamilton Sean Michael Whitney , Daniel A. Burciaga
IPC分类号: C01B3/52 , C01B3/56 , B01D53/047 , B01D53/12 , B01D53/14 , B01D53/18 , B01D53/32 , C01B3/24 , B01D5/00 , B01D47/10 , B01D17/02 , B01D29/27 , B01D29/66
CPC分类号: C01B3/52 , B01D5/0027 , B01D5/006 , B01D5/0072 , B01D5/0075 , B01D5/009 , B01D17/0208 , B01D29/27 , B01D29/66 , B01D46/0036 , B01D47/10 , B01D50/006 , B01D53/0423 , B01D53/0462 , B01D53/047 , B01D53/0476 , B01D53/12 , B01D53/1406 , B01D53/1412 , B01D53/1431 , B01D53/1462 , B01D53/1468 , B01D53/1487 , B01D53/18 , B01D53/265 , B01D53/326 , B01D53/48 , B01D53/76 , B01D61/362 , B01D2252/102 , B01D2252/103 , B01D2252/20436 , B01D2252/504 , B01D2252/602 , B01D2256/16 , B01D2256/20 , B01D2257/304 , B01D2257/306 , B01D2257/406 , B01D2257/504 , B01D2257/60 , B01D2257/708 , B01D2259/402 , C01B3/24 , C01B3/38 , C01B3/382 , C01B3/386 , C01B3/56 , C01B3/58 , C01B2203/0227 , C01B2203/0233 , C01B2203/025 , C01B2203/0261 , C01B2203/04 , C01B2203/0415 , C01B2203/042 , C01B2203/043 , C01B2203/0435 , C01B2203/045 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/061 , C01B2203/062 , C01B2203/068 , C01B2203/0877 , C01B2203/1235 , C01B2203/1241 , C01B2203/142 , C01B2203/147 , C01B2203/84 , H05K999/99 , Y02P20/13 , Y02P30/30
摘要: A system and method for processing unconditioned syngas first removes solids and semi-volatile organic compounds (SVOC), then removes volatile organic compounds (VOC), and then removes at least one sulfur containing compound from the syngas. Additional processing may be performed depending on such factors as the source of syngas being processed, the products, byproducts and intermediate products desired to be formed, captured or recycled and environmental considerations.
摘要翻译: 用于处理未条件合成气的系统和方法首先除去固体和半挥发性有机化合物(SVOC),然后除去挥发性有机化合物(VOC),然后从合成气中除去至少一种含硫化合物。 可以根据诸如待处理的合成气的来源,期望形成,捕获或再循环的产物,副产物和中间产物等因素进行附加处理和环境考虑。
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