| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 81 | 요구되는 공급량을 최적화하기 위한 에너지 저장 기술 | KR1020147008587 | 2012-09-18 | KR1020140060332A | 2014-05-19 | 쿠친스키콘라트예지; 스폴딩더글라스존 |
| 화력발전소의 연소 보일러/터빈용 조연성 가스 공급 시스템, 연소 보일러/터빈 시스템, 및 이들을 포함하는 화력발전소가 개시된다. 상기 가스 공급 시스템은 공급되는 공기로부터 산소 부화 가스를 분리 및 생산하는 공기 분리 모듈; 상기 공기 분리 모듈의 출구와 유동적으로 연결되며, 분리된 산소 부화 가스를 액체 상태로 저장하는 조연성 가스 저장 모듈; 상기 공기 분리 시스템 및/또는 상기 조연성 가스 저장 시스템으로부터 선택적으로 산소 부화 가스를 연소 보일러로 공급하는 조연성 가스 공급 모듈;을 포함한다. 상기 공기 분리 모듈의 산소 부화 가스 생산 능력은, 사전에 미리 결정된 작동 기간에 걸친 부하 계수를 기준으로 조절된 연소 보일러/터빈용 수요율, 및/또는 부하 계수를 기초로 한 종전의 용량보다 장기간 에너지 저장 능력을 제공하도록 용량이 증가된 ASU 용량에 따라 결정되는 것을 특징으로 한다.
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| 82 | 액체 공기 생산, 동력 저장 및 동력 방출 시스템 및 장치 | KR1020117022618 | 2010-03-12 | KR1020110120974A | 2011-11-04 | 데이비드밴더 |
| 본 발명은 유입 공기를 수직방향의 냉각관 조립체 안으로 유입되도록 유도하는 단계와, 공기를 냉각하고 수분 부분을 제거하는 단계를 포함하는 에너지 저장 및 방출 시스템 및 장치에 관한 것이다. 상기 공기는 상기 냉각관 조립체로부터 밖으로 향하여 압축된다. 남아있는 수분은 실질적으로 제거된다. 상기 공기는 냉매 루프 공기를 사용하여 실질적으로 액화되도록 주 열교환기에서 냉각된다. 상기 실질적으로 액화된 공기는 저장 장치로 향한다. 에너지 방출 모드에서, 작동 루프 공기는 상기 방출된 액체 공기가 실질적으로 증발되도록 방출된 액체 공기를 가온시키고, 상기 방출된 액체 공기는 상기 작동 루프 공기가 실질적으로 액화되도록 상기 작동 루프 공기를 냉각시킨다. 상기 실질적으로 증발된 공기는 연소실로 향하여 연소 흐름에 의하여 연소된다. 팽창된 연소가스의 일부는 상기 방출된 액체 공기를 가열하여 실질적으로 증발시키는데 사용될 수 있다.
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| 83 | 보일-오프 기체의 처리 방법 및 시스템 | KR1020107002936 | 2008-07-09 | KR1020100058470A | 2010-06-03 | 브리지우드폴 |
| A flowline system for transferring cryogenic liquids between a cryogenic liquid storage tank and a cryogenic liquid receiving/loading facility, and a method of maintaining the system at or marginally above cryogenic temperature during periods between transfer of cryogenic liquids between the cryogenic liquid storage tank and the cryogenic liquid receiving/loading facility are provided. The flowline system has a main transfer conduit and a vapour return line in fluid communication with the cryogenic liquid storage tank and the cryogenic liquid receiving/loading facility. A cooling medium line is provided that is in fluid communication with the main transfer conduit, the vapour return line, and a source of cooled boil-off gas, wherein the cooled boil-off gas is at or marginally above cryogenic temperature. The cooled boil-off gas is circulated between said tank and said facility through the main transfer conduit and the vapour return line during periods between transfer of cryogenic liquids to maintain the main transfer conduit and the vapour return line at or marginally above cryogenic temperature. | ||||||
| 84 | 액화 천연 가스의 제조 방법 및 장치 | KR1020107002935 | 2008-07-07 | KR1020100047256A | 2010-05-07 | 브리지우드폴 |
| A process and system for liquefying a hydrocarbon gas is provided. The hydrocarbon feed gas is pre-treated to remove sour species and water therefrom. The pre-treated feed gas is then passed to a refrigeration zone where it is cooled and expanded to produce a hydrocarbon liquid. A closed loop single mixed refrigerant provides most of the refrigeration to the refrigeration zone together with an auxiliary refrigeration system. The auxiliary refrigeration system and closed loop single mixed refrigerant are coupled in such a manner that waste heat generated by a gas turbine drive of the compressor in the closed loop single mixed refrigerant drives the auxiliary refrigeration system and the auxiliary refrigeration system cools the inlet air of the gas turbine. In this way, substantial improvements are made in the production capacity of the system. | ||||||
| 85 | PROCESS FOR EXTRACTING ETHANE AND HEAVIER HYDROCARBONS FROM LNG | EP05794337.5 | 2005-08-26 | EP1797383B1 | 2018-12-12 | WINNINGHAM, Horace, G. |
| A process for the extraction and recovery of ethane and heavier hydrocarbons (C2+) from LNG. The process covered by this patent maximizes the utilization of the beneficial cryogenic thermal properties of the LNG to extract and recover C2+ form the LNG using a unique arrangement of heat exchange equipment, a cryogenic fractionation column and processing parameters that essentially eliminates (or greatly reduces) the need for gas compression equipment minimizing capital cost, fuel consumption and electrical power requirements. This invention may be used for one or more of the following purposes: to condition LNG so that send-out gas delivered from an LNG receiving and regasification terminal meets commercial natural gas quality specifications; to condition LNG to make Lean LNG that meets fuel quality specifications and standards required by LNG powered vehicles and other LNG fueled equipment; to condition LNG to make Lean LNG so that it can be used to make CNG meeting specifications and standards for commercial CNG fuel; to recover ethane, propane and/or other hydrocarbons heavier then methane from LNG for revenue enhancement, profit or other commercial reasons. | ||||||
| 86 | METHOD FOR PROVIDING AN AIR FRACTION TO, AND PROCESSING THE AIR FRACTION IN, A PROCESSING UNIT AND CORRESPONDING SYSTEM | EP17020115.6 | 2017-03-28 | EP3382308A1 | 2018-10-03 | Guzmann, Marcus; Schrader, Dierk |
The invention relates to a method for providing an air fraction to, and processing the air fraction in, a processing unit (2), wherein the air fraction is provided by a process involving the steps of submitting an amount of air to a compression step comprising the use of a compressor (111) in a compression section (11) of an air separation unit (1), and of separating at least a part of the compressed air in a separation section (12) of the air separation unit (1), wherein the compressor (111) is at least in part driven by a steam turbine (112) in which steam generated by a steam generation unit (3) is expanded from a first pressure level to a second pressure level. The expanded steam is at least in part supplied to a steam consumer (21) of the processing unit (2) and/or is at least in part used at a temperature level not exceeding a temperature level at which the steam is withdrawn from the steam turbine (112) in order to heat a regeneration gas stream used in a purification section (13) of the air separation unit (1). A corresponding system (100) is also provided according to the present invention.
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| 87 | BOIL-OFF GAS TREATMENT PROCESS AND SYSTEM | EP08772638 | 2008-07-09 | EP2171341A4 | 2017-12-13 | BRIDGWOOD PAUL |
| A process and system for liquefying a hydrocarbon gas is provided. The hydrocarbon feed gas is pre-treated to remove sour species and water therefrom. The pre-treated feed gas is then passed to a refrigeration zone where it is cooled and expanded to produce a hydrocarbon liquid. A closed loop single mixed refrigerant provides most of the refrigeration to the refrigeration zone together with an auxiliary refrigeration system. The auxiliary refrigeration system and closed loop single mixed refrigerant are coupled in such a manner that waste heat generated by a gas turbine drive of the compressor in the closed loop single mixed refrigerant drives the auxiliary refrigeration system and the auxiliary refrigeration system cools the inlet air of the gas turbine. In this way, substantial improvements are made in the production capacity of the system. | ||||||
| 88 | PROCESS FOR EXTRACTING ETHANE AND HEAVIER HYDROCARBONS FROM LNG | EP05794337 | 2005-08-26 | EP1797383A4 | 2017-07-26 | WINNINGHAM HORACE G |
| A process for the extraction and recovery of ethane and heavier hydrocarbons (C2+) from LNG. The process covered by this patent maximizes the utilization of the beneficial cryogenic thermal properties of the LNG to extract and recover C2+ form the LNG using a unique arrangement of heat exchange equipment, a cryogenic fractionation column and processing parameters that essentially eliminates (or greatly reduces) the need for gas compression equipment minimizing capital cost, fuel consumption and electrical power requirements. This invention may be used for one or more of the following purposes: to condition LNG so that send-out gas delivered from an LNG receiving and regasification terminal meets commercial natural gas quality specifications; to condition LNG to make Lean LNG that meets fuel quality specifications and standards required by LNG powered vehicles and other LNG fueled equipment; to condition LNG to make Lean LNG so that it can be used to make CNG meeting specifications and standards for commercial CNG fuel; to recover ethane, propane and/or other hydrocarbons heavier then methane from LNG for revenue enhancement, profit or other commercial reasons. | ||||||
| 89 | A METHOD AND SYSTEM FOR PRODUCTION OF LIQUID NATURAL GAS | EP08772637 | 2008-07-07 | EP2179234A4 | 2015-10-14 | BRIDGWOOD PAUL |
| A process and system for liquefying a hydrocarbon gas is provided. The hydrocarbon feed gas is pre-treated to remove sour species and water therefrom. The pre-treated feed gas is then passed to a refrigeration zone where it is cooled and expanded to produce a hydrocarbon liquid. A closed loop single mixed refrigerant provides most of the refrigeration to the refrigeration zone together with an auxiliary refrigeration system. The auxiliary refrigeration system and closed loop single mixed refrigerant are coupled in such a manner that waste heat generated by a gas turbine drive of the compressor in the closed loop single mixed refrigerant drives the auxiliary refrigeration system and the auxiliary refrigeration system cools the inlet air of the gas turbine. In this way, substantial improvements are made in the production capacity of the system. | ||||||
| 90 | GRÜNE VERBUNDANLAGE ZUR HERSTELLUNG VON CHEMISCHEN UND PETROCHEMISCHEN PRODUKTEN | EP13756082.7 | 2013-08-26 | EP2869910A1 | 2015-05-13 | BUSSKAMP, Konrad; DÖRICHT, Volkmar; KIENER, Christoph; ROHRMUS, Dominik; STELZIG, Philipp Emanuel |
| The invention relates to an environmentally-friendly integrated installation which comprises a combined air separation and carbon dioxide capture installation, and an electrolysis unit. In certain embodiments, the integrated installation additionally comprises a unit for producing renewable energy. Moreover, the invention also relates to a control unit and a computer program product for said integrated installation, a method for producing chemical products in the integrated installation, and the use of the integrated installation to produce chemical products and as a chemical store for fluctuating renewable energies. | ||||||
| 91 | VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG ELEKTRISCHER ENERGIE | EP13732098.2 | 2013-06-25 | EP2867599A2 | 2015-05-06 | ALEKSEEV, Alexander |
| The process and the apparatus serve to generate electric energy in a combined system comprising a power station and air treatment plant. The power station has a first gas expansion unit (300) which is connected to a generator for generating electric energy. The air treatment plant has an air compression unit (2), a heat exchanger system (21) and a tank (200) for liquid. In a first operating mode, feed air is, in the air treatment plant, compressed in the air compression unit (2) and cooled in the heat exchanger system (21), a storage fluid containing less than 40 mol% of oxygen is produced from the compressed and cooled feed air and the storage fluid is stored as low-temperature liquid (101) in the tank (200) for liquid. In a second operating mode, low-temperature liquid (103) is taken from the tank (200) for liquid and vaporized or pseudovaporized under superatmospheric pressure and the gaseous high-pressure storage fluid (104) produced in this way is expanded in the gas expansion unit (300). In the second operating mode, the (pseudo)vaporization of the low-temperature liquid is carried out in the heat exchanger system (21) of the air treatment plant. | ||||||
| 92 | Method and apparatus for the removal of a sorbate component from a process stream with subsequent regeneration of the sorbent using solar energy | EP09177657.5 | 2009-12-01 | EP2335813A1 | 2011-06-22 | The designation of the inventor has not yet been filed |
A rich stream (212) comprising one or more sorbate components is treated with a sorbent to capture one or more of the one or more sorbate components and to provide a lean stream (214) that is diminished in sorbate component content and a loaded sorbent (200, 206, 228) comprising the sorbent and one or more sorbate components. Solar energy from the sun is collected in a concentrated solar power system (10) to provide a pressurized steam stream (42) with the captured solar thermal energy. The pressurized steam stream (42) is converted into electric power (45) and an exhaust steam stream (43). Heat from the exhaust steam stream (43) is used to regenerate the loaded sorbent (200, 206, 228).
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| 93 | Procédé de liquéfaction et de déazotation de gaz naturel, installation de mise en oeuvre | EP02291595.3 | 2002-06-26 | EP1273860A3 | 2003-01-15 | Paradowski, Henri |
Procédé de liquéfaction et de déazotation de gaz naturel, installation de mise en oeuvre, et gaz obtenus par cette séparation. L'invention concerne un procédé de liquéfaction et de déazotation de gaz naturel (1) contenant de l'azote, dans lequel ledit gaz naturel (1) est refroidi, liquéfié et séparé en une première fraction de tête (9) relativement plus volatile enrichie en azote, et en une première fraction de pied (15). Le procédé est caractérisé en ce que la première fraction de tête (9) est refroidie et liquéfiée, séparée en une deuxième fraction de tête (11) relativement plus volatile qui fournit de l'azote gazeux (29), et en une deuxième fraction de pied (12) qui est retraitée, et en ce que la première fraction de pied (15) est refroidie pour fournir du gaz naturel liquéfié essentiellement exempt d'azote (24). D'autres modes de réalisation sont décrits. |
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| 94 | Procédé de liquéfaction et de déazotation de gaz naturel, installation de mise en oeuvre | EP02291595.3 | 2002-06-26 | EP1273860A2 | 2003-01-08 | Paradowski, Henri |
Procédé de liquéfaction et de déazotation de gaz naturel, installation de mise en oeuvre, et gaz obtenus par cette séparation. L'invention concerne un procédé de liquéfaction et de déazotation de gaz naturel (1) contenant de l'azote, dans lequel ledit gaz naturel (1) est refroidi, liquéfié et séparé en une première fraction de tête (9) relativement plus volatile enrichie en azote, et en une première fraction de pied (15). Le procédé est caractérisé en ce que la première fraction de tête (9) est refroidie et liquéfiée, séparée en une deuxième fraction de tête (11) relativement plus volatile qui fournit de l'azote gazeux (29), et en une deuxième fraction de pied (12) qui est retraitée, et en ce que la première fraction de pied (15) est refroidie pour fournir du gaz naturel liquéfié essentiellement exempt d'azote (24). D'autres modes de réalisation sont décrits. |
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| 95 | 전기 에너지를 생성하기 위한 프로세스 및 장치 | KR1020157002452 | 2013-06-25 | KR1020150028332A | 2015-03-13 | 아렉시이프,알렉산더 |
| 프로세스 및 장치는, 전력 스테이션 및 에어 처리 플랜트를 포함하는 결합된 시스템에서 전기 에너지를 생성하도록 기능한다. 전력 스테이션은, 전기 에너지를 생성하기 위해 발전기에 접속되는 제 1 가스 팽창 유닛(300)을 갖는다. 에어 처리 플랜트는, 에어 압축 유닛(2), 열 교환기 시스템(21), 및 액체를 위한 탱크(200)를 갖는다. 제 1 동작 모드에서, 공급 에어는, 에어 처리 플랜트에서, 에어 압축 유닛(2)에서 압축되고 열 교환기 시스템(21)에서 냉각되고, 40 mol%보다 적은 산소를 함유하는 저장 유체는 압축되고 냉각된 공급 에어로부터 생성되며, 저장 유체는 낮은-온도 액체(101)로서 액체를 위한 탱크(200)에 저장된다. 제 2 동작 모드에서, 낮은-온도 액체(103)는, 액체를 위한 탱크(200)로부터 취해지고 초대기의(superatmospheric) 압력 하에서 기화되거나 의사기화되며, 이러한 방식으로 생성된 가스형 높은-압력 저장 유체(104)는 가스 팽창 유닛(300)에서 팽창된다. 제 2 동작 모드에서, 낮은-온도 액체의 (의사)기화는 에어 처리 플랜트의 열 교환기 시스템(21)에서 수행된다.
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| 96 | 액체 공기 생산, 동력 저장 및 동력 방출 시스템 및 장치 | KR1020117022618 | 2010-03-12 | KR101334068B1 | 2013-11-28 | 데이비드밴더 |
| 본 발명은 유입 공기를 수직방향의 냉각관 조립체 안으로 유입되도록 유도하는 단계와, 공기를 냉각하고 수분 부분을 제거하는 단계를 포함하는 에너지 저장 및 방출 시스템 및 장치에 관한 것이다. 상기 공기는 상기 냉각관 조립체로부터 밖으로 향하여 압축된다. 남아있는 수분은 실질적으로 제거된다. 상기 공기는 냉매 루프 공기를 사용하여 실질적으로 액화되도록 주 열교환기에서 냉각된다. 상기 실질적으로 액화된 공기는 저장 장치로 향한다. 에너지 방출 모드에서, 작동 루프 공기는 상기 방출된 액체 공기가 실질적으로 증발되도록 방출된 액체 공기를 가온시키고, 상기 방출된 액체 공기는 상기 작동 루프 공기가 실질적으로 액화되도록 상기 작동 루프 공기를 냉각시킨다. 상기 실질적으로 증발된 공기는 연소실로 향하여 연소 흐름에 의하여 연소된다. 팽창된 연소가스의 일부는 상기 방출된 액체 공기를 가열하여 실질적으로 증발시키는데 사용될 수 있다.
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| 97 | Wind power generation using nitrogen gas | KR20100093840 | 2010-09-28 | KR20120032276A | 2012-04-05 | KIM SUNG CHUL |
| PURPOSE: Wind power generation using nitrogen gas is provided to enhance the entire efficiency of a hybrid electricity producing device since generation is done in conjunction of nitrogen separated from an air separator with a wind generator. CONSTITUTION: Wind power generation using nitrogen gas comprises an air separator(102) and a wind generator(123). The air separator separates nitrogen and oxygen from air. The wind generator is driven by nitrogen emitting from the air separator. The air separator separates nitrogen and oxygen using a boiling point. The pressure of the nitrogen created by the air generator is within 1.0 ~ 5.0 Bar. At the air separator, flow speed is within 0.5 ~ 2 m/s. At the air separator, flow rate is within 1000 ~ 5000 m^3/min. | ||||||
| 98 | 액화 천연 가스의 냉각 공정 및 생산방법 | KR1020057013373 | 2003-12-04 | KR1020050092770A | 2005-09-22 | 브릿즈우드,폴,윌리암 |
| Process and apparatus for the production of liquefied natural gas utilising a refrigeration cycle, characterised by the steps of: i) Pre-treatment of a natural gas stream; ii) Chilling of either or both of the resulting pre-treated gas stream or a refrigerant gas stream within the refrigeration cycle; and iii) Liquefaction of the natural gas. | ||||||
| 99 | CARBON DIOXIDE CAPTURE FROM FLUE GAS | PCT/US2008085075 | 2008-11-28 | WO2009070785A3 | 2009-08-20 | BAXTER LARRY L |
| A method for capturing carbon dioxide from a flue gas includes (i) removing moisture from a flue gas to yield a dried flue gas; (ii) compressing the dried flue gas to yield a compressed gas stream; (iii) reducing the temperature of the compressed gas stream to a temperature T1 using a first heat exchanger; (iv) reducing the temperature of the compressed gas stream to a second temperature T2 using a second heat exchanger stream, where T2 1 and at least a portion of the carbon dioxide from the compressed gas stream condenses, thereby yielding a solid or liquid condensed-phase carbon dioxide component and a light-gas component; (v) separating the condensed-phase component from the light-gas component to produce a condensed-phase stream and a light-gas stream; and (vi) using at least a portion of the condensed-phase stream and/or the light- gas stream in the second heat exchanger. | ||||||
| 100 | PROCESS FOR EXTRACTING ETHANE AND HEAVIER HYDROCARBONS FROM LNG | PCT/US2005030591 | 2005-08-26 | WO2006026525A3 | 2007-04-05 | WINNINGHAM HORACE G |
| A process for the extraction and recovery of ethane and heavier hydrocarbons (C2+) from LNG. The process covered by this patent maximizes the utilization of the beneficial cryogenic thermal properties of the LNG to extract and recover C2+ form the LNG using a unique arrangement of heat exchange equipment, a cryogenic fractionation column and processing parameters that essentially eliminates (or greatly reduces) the need for gas compression equipment minimizing capital cost, fuel consumption and electrical power requirements. This invention may be used for one or more of the following purposes: to condition LNG so that send-out gas delivered from an LNG receiving and regasification terminal meets commercial natural gas quality specifications; to condition LNG to make Lean LNG that meets fuel quality specifications and standards required by LNG powered vehicles and other LNG fueled equipment; to condition LNG to make Lean LNG so that it can be used to make CNG meeting specifications and standards for commercial CNG fuel; to recover ethane, propane and/or other hydrocarbons heavier then methane from LNG for revenue enhancement, profit or other commercial reasons. | ||||||
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