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1. 发明申请

US20180163571A1 OXYFUEL POWER PLANT PROCESS 审中-公开
公开(公告)号：US20180163571A1
公开(公告)日：2018-06-14
申请号：US15833227
申请日：2017-12-06
申请人： Sebastian Obermeier , Alexander Alekseev
发明人： Sebastian Obermeier , Alexander Alekseev
IPC分类号： F01K11/02 , F01K9/02 , F01K9/00 , F01K7/16
CPC分类号： F01K11/02 , F01K7/16 , F01K9/003 , F01K9/02 , F23J2219/70 , F27D2009/0013
摘要： An oxyfuel power plant having improved efficiency of operation by the provision of at least two condensation units, the first being a warmer operating direct contact cooler and the second being a colder operating direct contact cooler. Each apparatus is loaded with a different quantity of water, with the warmer direct contact cooler having two to three times the amount of water that is in the colder direct contact cooler.

2. 发明申请

US20120240620A1 METHOD AND DEVICE FOR GENERATING AN OXYGEN PRODUCT BY LOW-TEMPERATURE SEPARATION OF AIR 审中-公开
标题翻译：用于通过空气低温分离产生氧气产品的方法和装置
公开(公告)号：US20120240620A1
公开(公告)日：2012-09-27
申请号：US13425569
申请日：2012-03-21
申请人： Gerhard POMPL , Georg Demski , Alexander Alekseev
发明人： Gerhard POMPL , Georg Demski , Alexander Alekseev
IPC分类号： F25J3/04
CPC分类号： F25J3/04896 , F25J3/042 , F25J3/04303 , F25J3/04412 , F25J3/0449 , F25J3/04927 , F25J2235/50 , F25J2245/50 , F25J2250/02 , F25J2250/10
摘要： The method and device serve for generating an oxygen product by low-temperature separation of air having a distillation column system for nitrogen-oxygen separation that comprises a high-pressure column (6) and a low-pressure column (7) which contain mass-transfer sections. Liquid that drains off from the lowest mass-transfer section (32) of the low-pressure column (7) is introduced into a main condenser (8) constructed as a bath evaporator and condenser-evaporator. Between the bottom end of the lowest mass-transfer section (32) of the low-pressure column (7) and the main condenser (8) there is arranged a liquid buffer (33). In the event of a reduction in load, liquid is introduced into the liquid buffer (33) and is stored there. In the event of an increase in load, liquid stored in the liquid buffer (33) is introduced (34) into the main condenser (8).
摘要翻译：该方法和装置用于通过低温分离具有用于氮 - 氧分离的蒸馏塔系统的空气来产生氧气产物，该系统包括高压塔（6）和低压塔（7）转移部分。从低压塔（7）的最低质量转移段（32）排出的液体被引入构成浴蒸发器和冷凝器 - 蒸发器的主冷凝器（8）中。在低压塔（7）的最低质量传递部分（32）的底端与主冷凝器（8）之间布置有液体缓冲器（33）。在负载减少的情况下，液体被引入液体缓冲器（33）并存储在那里。在负载增加的情况下，储存在液体缓冲器（33）中的液体被引入（34）到主冷凝器（8）中。

3. 发明申请

US20170211880A1 METHOD FOR OBTAINING AN AIR PRODUCT, AND AIR SEPARATION PLANT 审中-公开
公开(公告)号：US20170211880A1
公开(公告)日：2017-07-27
申请号：US15399804
申请日：2017-01-06
申请人： Alexander Alekseev
发明人： Alexander Alekseev
IPC分类号： F25J3/04 , F01K23/06
CPC分类号： F25J3/04078 , F01K23/068 , F25J3/04084 , F25J3/0409 , F25J3/04109 , F25J3/04175 , F25J3/04224 , F25J3/04296 , F25J3/04381 , F25J3/04387 , F25J3/04393 , F25J3/04412 , F25J3/04496 , F25J3/04787 , F25J3/04836 , F25J2205/24 , F25J2230/42 , F25J2240/04 , F25J2240/10 , F25J2245/40 , F25J2245/42 , Y02E20/18
摘要： An air product is produced in an air separation plant having a heat exchanger, an expansion/compression unit, a rectification unit, liquid storage, cold storage and an air compressor. The air supplied to the rectification unit is conducted through the main air compressor at a pressure level at least 3 bar above the highest operation pressure for the rectification unit. Cryogenic liquids are produced in a first production amount by a first operating mode, a lower second production amount by a second operating mode and a higher third production amount by a third operating mode. Cryogenic liquid is stored in the liquid storage in the third operating mode and removed from storage in the second operating mode. Cryogenic liquid is evaporated in different amounts in each operating mode, which amounts differ by no more than 10%.

4. 发明申请

US20110214453A1 PROCESS AND DEVICE FOR CRYOGENIC AIR FRACTIONATION 审中-公开
标题翻译：低温空气分离的方法和装置
公开(公告)号：US20110214453A1
公开(公告)日：2011-09-08
申请号：US13058723
申请日：2009-08-11
申请人： Alexander Alekseev
发明人： Alexander Alekseev
IPC分类号： F25J3/04
CPC分类号： F25J3/04181 , C01B13/0248 , C01B13/0259 , C01B2210/0046 , F25J3/0409 , F25J3/04157 , F25J3/04206 , F25J3/04218 , F25J3/04309 , F25J3/04412 , F25J3/04533 , F25J3/04581 , F25J3/04618 , F25J3/0486 , F25J3/04878 , F25J3/04957 , F25J2205/32 , F25J2205/34 , F25J2205/70 , F25J2210/06 , F25J2240/44 , F25J2245/42 , F25J2250/40 , F25J2250/50
摘要： The process and the device serve for cryogenic air fractionation, in particular for supplying an oxygen-enriched (product stream to an oxyfuel power plant. The distillation column system for nitrogen/oxygen separation has a high-pressure column (26) and a low-pressure column (32). The high-pressure column (26) and the low-pressure column (32) are thermally coupled via a condenser-evaporator (37). Feed air (1) is compressed in an air compressor (3), cooled at least in a first post-cooler (6) and purified in a purification device (22), cooled in a main heat exchanger (23a, 23b, 23c) and introduced at least in part (25, 29) into the high-pressure column (26). At least one liquid stream (33, 35) is introduced from the high-pressure column (26) into the low-pressure column (32). An oxygen-enriched product stream (41, 45, 46,47, 48) is taken off from the low-pressure column (32). A first nitrogen stream (63, 64, 65, 66) is withdrawn from the high-pressure column (26) and warmed to a temperature of at least 280 K (6). The warmed first nitrogen stream (67) is work-expanded (72) in a first warm expansion engine (68). The first nitrogen stream (70, 71) which is expanded in the first warm expansion engine (68) is work-expanded in a second warm expansion engine (72).
摘要翻译：该方法和装置用于低温空气分馏，特别是用于向富氧燃料发电厂供应富氧（产物流），用于氮气/氧气分离的蒸馏塔系统具有高压塔（26）和低压塔高压塔（26）和低压塔（32）通过冷凝器 - 蒸发器（37）热耦合，进料空气（1）在空气压缩机（3）中被压缩，至少在第一后冷却器（6）中冷却并在纯化装置（22）中净化，在主热交换器（23a，23b，23c）中冷却，并将至少部分（25,29）引入高压釜至少一个液体流（33,35）从高压塔（26）引入低压塔（32）中，富氧产物流（41,45,46，从高压塔（32）中取出第一氮气流（63,64,65,66）从高压塔（26）中取出并加热到温度至少280 K（6）。加热的第一氮气流（67）在第一暖膨胀发动机（68）中工作膨胀（72）。在第一暖膨胀发动机（68）中膨胀的第一氮气流（70,71）在第二暖膨胀发动机（72）中工作膨胀。

5. 发明申请

US20110067444A1 Processes and Device for Low Temperature Separation of Air 审中-公开
标题翻译：低温分离空气的方法和装置
公开(公告)号：US20110067444A1
公开(公告)日：2011-03-24
申请号：US12885603
申请日：2010-09-20
申请人： Alexander Alekseev
发明人： Alexander Alekseev
IPC分类号： F25J3/04
CPC分类号： F25J3/04175 , F25J3/04054 , F25J3/04084 , F25J3/0409 , F25J3/04096 , F25J3/04296 , F25J3/04303 , F25J3/04309 , F25J3/04315 , F25J3/04375 , F25J3/04393 , F25J3/04412 , F25J3/04648 , F25J3/04781 , F25J2205/04 , F25J2215/54 , F25J2240/04 , F25J2240/10 , F25J2240/42 , F25J2240/44 , F25J2240/46 , F25J2270/02
摘要： The process and device serve for the low-temperature separation of air in a distillation-column system includes at least one separation column. A main air stream is compressed in an air compressor at a first pressure and is then purified. A first air stream, which is formed from at least one part of the purified main air stream, is further compressed at a second pressure that is higher than the first pressure. From the further compressed first air stream, a throttling stream and a turbine stream are branched off. The throttling stream is cooled down and liquefied or pseudo-liquefied in a main heat exchanger and is then passed on to expansion equipment. The expanded throttling stream is conducted into the distillation-column system. The turbine stream is cooled down in the main heat exchanger and under an intermediate temperature of the main heat exchanger is conducted into an expansion machine.
摘要翻译：用于蒸馏塔系统中的空气的低温分离的方法和装置包括至少一个分离塔。主空气流在空气压缩机中以第一压力被压缩，然后被净化。由净化的主空气流的至少一部分形成的第一气流在高于第一压力的第二压力下被进一步压缩。从进一步压缩的第一空气流中，分流流和涡轮流分支。节流流在主热交换器中被冷却并液化或伪液化，然后传递到膨胀设备。膨胀的节流流进入蒸馏塔系统。涡轮流在主热交换器中被冷却，在主热交换器的中间温度下进入膨胀机。

6. 发明申请

US20090188280A1 PROCESS AND DEVICE FOR LOW-TEMPERATURE SEPARATION OF AIR 审中-公开
公开(公告)号：US20090188280A1
公开(公告)日：2009-07-30
申请号：US12282606
申请日：2007-03-06
申请人： Alexander Alekseev , Dietrich Rottmann , Florian Schliebitz , Dirk Schwenk
发明人： Alexander Alekseev , Dietrich Rottmann , Florian Schliebitz , Dirk Schwenk
IPC分类号： F25J3/08
CPC分类号： F25J3/04454 , F25J3/04054 , F25J3/0409 , F25J3/04175 , F25J3/04193 , F25J3/04296 , F25J3/04303 , F25J3/04393 , F25J3/04412 , F25J2240/04
摘要： The process and the device are used for low-temperature separation of air with a distilling-column system for nitrogen-oxygen separation (20), which has at least one separation column (21, 22). A main air stream (1, 5) is compressed in an air compressor (2) and purified in a purification device (4). A first air stream (7) and a second air stream (8) are diverted from the main air stream (5). The first air stream (7) is further compressed in two secondary compressors (10, 13) that are connected in series. The further compressed first air stream (15) is cooled by indirect heat exchange (16), and at least partially liquefied or pseudo-liquefied, and then introduced into the distilling-column system for nitrogen-oxygen separation (20). The second air stream (8) is cooled by indirect heat exchange (16) and then, divided into two partial streams (24, 27), is actively depressurized in two expanders (25, 28), whereby the two expanders have essentially the same inlet pressure. The actively depressurized partial streams (26, 29) of the second air stream are introduced (30, 129) at least in part into the distilling-column system for nitrogen-oxygen separation (20). The mechanical energy that is produced in the active depressurization (25, 28) of the second air stream is used at least partially in the driving of the two secondary compressors (10, 13) that are connected in series. A liquid product stream (31) is removed from the distilling-column system for nitrogen-oxygen separation (20), brought to an elevated pressure in the liquid state (32), and evaporated or pseudo-evaporated under this elevated pressure by indirect heat exchange (16) with the first air stream (15), and finally removed as a gaseous product stream (34). Both secondary compressors (10, 13) are operated with an inlet temperature that is higher than 250 K, in particular higher than 270 K.

7. 发明申请

US20160160694A1 PROCESS AND COMBINED PLANT FOR STORAGE AND RECOVERY OF ENERGY 审中-公开
标题翻译：过程和组合工厂储存和恢复能源
公开(公告)号：US20160160694A1
公开(公告)日：2016-06-09
申请号：US14961341
申请日：2015-12-07
申请人： Alexander Alekseev , Christoph Stiller , Brian Stöver
发明人： Alexander Alekseev , Christoph Stiller , Brian Stöver
IPC分类号： F01K25/08
CPC分类号： F01K25/08 , F25J1/0012 , F25J1/0015 , F25J1/0017 , F25J1/002 , F25J1/0037 , F25J1/004 , F25J1/0042 , F25J1/0045 , F25J1/0202 , F25J1/0228 , F25J1/0251 , F25J1/0264 , F25J2205/24 , F25J2205/66 , F25J2210/06 , F25J2235/02 , F25J2240/10 , F25J2240/90
摘要： The present invention relates to a process and plant for storage and recovery of energy using a combined plant that comprises a gas treatment unit and an energy generation unit, wherein in a first operating mode, a low-temperature gas liquefaction product is generated from compressed feed gas that is cooled in a heat-exchange system, and using the gas liquefaction product, a storage liquid is provided, and in a second operating mode, using the stored liquid, a low-temperature process liquid is provided that is warmed in the heat-exchange system, obtaining a pressurized fluid that is work-producingly expanded in the energy generation unit.
摘要翻译：本发明涉及一种使用包括气体处理单元和能量产生单元的组合设备来储存和回收能量的方法和设备，其中在第一操作模式中，从压缩进料产生低温气体液化产物在热交换系统中冷却的气体，并且使用气体液化产物，提供储存液体，并且在第二操作模式中，使用所储存的液体，提供在热量中加热的低温处理液体 - 交换系统，获得在能量产生单元中工作扩展的加压流体。

8. 发明申请

US20130152595A1 PROCESS FOR THE ENHANCEMENT OF POWER PLANT WITH CO2 CAPTURE AND SYSTEM FOR REALIZATION OF THE PROCESS 审中-公开
标题翻译：用CO2捕获和发电工艺实现发电厂的过程
公开(公告)号：US20130152595A1
公开(公告)日：2013-06-20
申请号：US13710951
申请日：2012-12-11
申请人： Alexander Alekseev , Rob Smith , Ramachandran Krishnamurthy
发明人： Alexander Alekseev , Rob Smith , Ramachandran Krishnamurthy
IPC分类号： F01N3/00
CPC分类号： F01N3/00 , B01D53/265 , B01D53/62 , B01D2252/204 , B01D2256/12 , B01D2257/102 , B01D2257/504 , B01D2258/0283 , F23C9/00 , F23J2215/50 , F23L7/007 , F23L2900/07001 , Y02A50/2342 , Y02C10/04 , Y02E20/322 , Y02E20/344
摘要： Improved methods and systems for power plants with CO2 capture and especially power plants with CO2 capture for enhanced oil recovery (EOR) purposes.
摘要翻译：改进的CO2捕集发电厂的方法和系统，特别是具有二氧化碳捕集功能的发电厂，以提高采收率（EOR）的目的。

9. 发明申请

US20130025276A1 METHOD AND DEVICE FOR PRODUCING A CARBON DIOXIDE-RICH GAS MIXTURE, METHOD AND DEVICE FOR IMPROVED OIL RECOVERY AND CORRESPONDING USE OF A GAS ENGINE 审中-公开
标题翻译：用于生产二氧化碳气体混合物的方法和装置，用于改进油回收和相应使用气体发动机的方法和装置
公开(公告)号：US20130025276A1
公开(公告)日：2013-01-31
申请号：US13560281
申请日：2012-07-27
申请人： Robert ADLER , Alexander Alekseev , Andreas Opfermann
发明人： Robert ADLER , Alexander Alekseev , Andreas Opfermann
IPC分类号： F01N3/00 , F02B37/00 , F02M25/07
CPC分类号： F23L7/007 , C01B32/50 , F23J2215/50 , F23L2900/07001 , F23L2900/07007 , Y02E20/322 , Y02E20/344
摘要： The invention relates to a method for producing a carbon dioxide-rich gas mixture (44) wherein a hydrocarbon-containing fuel (21) is burned in a combustion chamber of a gas engine (10) in a gas atmosphere, and the exhaust gas (14) of the gas engine (10) is processed into the carbon dioxide-rich gas mixture (44). The gas atmosphere in the combustion chamber has an oxygen content (33) that corresponds to 0.9 to 1.1 times the amount of oxygen required for complete combustion of the hydrocarbon-containing fuel (21), and the gas atmosphere has a volumetric ratio of nitrogen to oxygen (33) in that is less than 3.5 to 1. The invention also relates to an apparatus for producing the carbon dioxide-rich gas mixture (44), and a method and apparatus for enhanced oil recovery using the method and apparatus for producing the carbon dioxide-rich gas mixture (44).
摘要翻译：本发明涉及一种生产富含二氧化碳的气体混合物（44）的方法，其中含烃燃料（21）在气体气氛中在燃气发动机（10）的燃烧室中燃烧，并且废气（燃气发动机（10）的气体（14）被处理成富含二氧化碳的气体混合物（44）。燃烧室中的气体气氛具有相当于含烃燃料（21）完全燃烧所需氧量的0.9〜1.1倍的氧含量（33），气体气体的氮与氧气（33）的含量小于3.5比1.本发明还涉及一种用于生产富含二氧化碳的气体混合物（44）的装置，以及一种用于生产二氧化碳气体混合物（44）的方法和装置，富含二氧化碳的气体混合物（44）。

10. 发明申请

US20180155202A1 METHODS FOR CARBON DIOXIDE PRODUCTION AND POWER GENERATION 审中-公开
公开(公告)号：US20180155202A1
公开(公告)日：2018-06-07
申请号：US15819013
申请日：2017-11-21
申请人： Alexander Alekseev , Stevan Jovanovic , Ramachandran Krishnamurthy
发明人： Alexander Alekseev , Stevan Jovanovic , Ramachandran Krishnamurthy
IPC分类号： C01B32/50 , B01D53/60 , B01D53/34 , B01D53/26 , H02K7/18
CPC分类号： C01B32/50 , B01D53/265 , B01D53/343 , B01D53/60 , B01D2256/22 , B01D2257/104 , B01D2257/302 , B01D2257/404 , B01D2257/80 , B01D2258/0283 , F01K13/00 , F22B1/003 , H02K7/1823 , Y02A50/2344 , Y02E20/344 , Y02P20/124 , Y02P20/152
摘要： A method of integrating energy into a power cycle during production of carbon dioxide using the steps of a) combusting a fuel and oxygen in a reactor to produce a mixture of carbon dioxide and water, and form a heat of reaction; b) capturing the heat of reaction; c) converting the heat of reaction into electrical energy; d) feeding the electrical energy into the power cycle; and e) purifying and recovering carbon dioxide. Alternatively, a method for the production of carbon dioxide and power is disclosed by a) combusting a fuel and oxygen in a reactor to produce a flue gas comprising carbon dioxide and contaminants and a heat of reaction; b) recovering heat from the reactor and producing electricity from the heat; c) integrating the electricity into a power cycle; and d) removing contaminants from the carbon dioxide and recovering purified carbon dioxide.

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