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公开(公告)号：US09995530B2
公开(公告)日：2018-06-12
申请号：US15052076
申请日：2016-02-24
CPC分类号： F25J3/04412 , F25J3/0266 , F25J3/04018 , F25J3/04084 , F25J3/04157 , F25J3/04193 , F25J3/04296 , F25J3/04303 , F25J3/04309 , F25J3/04393 , F25J3/04533 , F25J3/04563 , F25J3/04612 , F25J3/04618 , F25J3/066 , F25J3/067 , F25J2205/20 , F25J2210/04 , F25J2210/42 , F25J2210/70 , F25J2230/02 , F25J2230/04 , F25J2235/80 , F25J2240/40 , F25J2245/02 , F25J2245/42 , F25J2250/42 , F25J2260/44 , F25J2260/80 , F25J2270/904 , Y02C10/04 , Y02C10/12 , Y02E20/344
摘要： A cryogenic method for capturing carbon dioxide in the gaseous emissions produced from the fossil-energy combustion of solid, liquid, or gaseous fossil fuels in a power generation installation employing an OxyFuel mode of combustion. The method includes: producing essentially pure carbon dioxide under elevated pressure and at near ambient temperatures in a Carbon-Dioxide Capture Component from the carbon-dioxide content of at least a part of the gaseous emissions produced from fossil-energy fueled combustion in the Oxyfuel mode of combustion; separating atmospheric air in an Air Separation Component into a stream of liquid nitrogen and a stream of high-purity oxygen; supplying low temperature, compressed purified air to a cryogenic air separation unit (cold box) within the Air Separation Component; collecting low temperature thermal energy from coolers employed within the Carbon-Dioxide Capture Component and the Air Separation Component; and converting the collected thermal energy to electricity within a Thermal-Energy Conversion Component.
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2.发明申请METHOD TO OPTIMIZE THE UTILIZATION OF CAPTURED CARBON DIOXIDE THROUGH THE CULTIVATION AND PROCESSING OF MICROALGAE 审中-公开通过微生物加工和加工优化捕获的二氧化碳的方法公开(公告)号：US20150307830A1
公开(公告)日：2015-10-29
申请号：US14261854
申请日：2014-04-25
CPC分类号： C12M29/24 , C12M21/02 , C12M43/08 , C12P1/00 , C12P3/00 , C12P5/023 , C12P7/6463 , Y02E50/343
摘要： A method for cultivating and processing microalgae includes directing a continuous supply of carbon dioxide into an enclosed photobioreactor containing microalgae. The enclosed photobioreactor is exposed to insolation for the cultivation of the microalgae by means of controlled photosynthesis chemical reactions. The microalgae are cultivated and the microalgae are processed to create an algae biomass and a gaseous mixture. The algae biomass is extracted to produce an essentially pure algae oil and oil free algae biomass. The gaseous mixture is separated into unreacted carbon dioxide and oxygen. The separated unreacted carbon dioxide is recycled to the photobioreactor and the oxygen in excess of export quantity is stored.
摘要翻译： 微藻的培养和加工方法包括将二氧化碳的连续供应引导到包含微藻的封闭的光生物反应器中。 封闭的光生物反应器通过受控的光合作用化学反应暴露于日晒以培养微藻。 培养微藻，并处理微藻以产生藻类生物质和气体混合物。 提取藻类生物质以产生基本上纯的藻类油和无油藻类生物质。 将气体混合物分离成未反应的二氧化碳和氧气。 将分离的未反应的二氧化碳再循环到光生物反应器中，并且存储超过出口量的氧气。
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3.发明授权公开(公告)号：US09187724B1
公开(公告)日：2015-11-17
申请号：US14261854
申请日：2014-04-25
CPC分类号： C12M29/24 , C12M21/02 , C12M43/08 , C12P1/00 , C12P3/00 , C12P5/023 , C12P7/6463 , Y02E50/343
摘要： A method for cultivating and processing microalgae includes directing a continuous supply of carbon dioxide into an enclosed photobioreactor containing microalgae. The enclosed photobioreactor is exposed to insolation for the cultivation of the microalgae by means of controlled photosynthesis chemical reactions. The microalgae are cultivated and the microalgae are processed to create an algae biomass and a gaseous mixture. The algae biomass is extracted to produce an essentially pure algae oil and oil free algae biomass. The gaseous mixture is separated into unreacted carbon dioxide and oxygen. The separated unreacted carbon dioxide is recycled to the photobioreactor and the oxygen in excess of export quantity is stored.
摘要翻译： 微藻的培养和加工方法包括将二氧化碳的连续供应引导到包含微藻的封闭的光生物反应器中。 封闭的光生物反应器通过受控的光合作用化学反应暴露于日晒以培养微藻。 培养微藻，并处理微藻以产生藻类生物质和气体混合物。 提取藻类生物质以产生基本上纯的藻类油和无油藻类生物质。 将气体混合物分离成未反应的二氧化碳和氧气。 将分离的未反应的二氧化碳再循环到光生物反应器中，并且存储超过出口量的氧气。
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4.发明申请公开(公告)号：US20170241707A1
公开(公告)日：2017-08-24
申请号：US15052076
申请日：2016-02-24
CPC分类号： F25J3/04412 , F25J3/0266 , F25J3/04018 , F25J3/04084 , F25J3/04157 , F25J3/04193 , F25J3/04296 , F25J3/04303 , F25J3/04309 , F25J3/04393 , F25J3/04533 , F25J3/04563 , F25J3/04612 , F25J3/04618 , F25J3/066 , F25J3/067 , F25J2205/20 , F25J2210/04 , F25J2210/42 , F25J2210/70 , F25J2230/02 , F25J2230/04 , F25J2235/80 , F25J2240/40 , F25J2245/02 , F25J2245/42 , F25J2250/42 , F25J2260/44 , F25J2260/80 , F25J2270/904 , Y02C10/04 , Y02C10/12 , Y02E20/344
摘要： A cryogenic method for capturing carbon dioxide in the gaseous emissions produced from the fossil-energy combustion of solid, liquid, or gaseous fossil fuels in a power generation installation employing an OxyFuel mode of combustion. The method includes: producing essentially pure carbon dioxide under elevated pressure and at near ambient temperatures in a Carbon-Dioxide Capture Component from the carbon-dioxide content of at least a part of the gaseous emissions produced from fossil-energy fueled combustion in the Oxyfuel mode of combustion; separating atmospheric air in an Air Separation Component into a stream of liquid nitrogen and a stream of high-purity oxygen; supplying low temperature, compressed purified air to a cryogenic air separation unit (cold box) within the Air Separation Component; collecting low temperature thermal energy from coolers employed within the Carbon-Dioxide Capture Component and the Air Separation Component; and converting the collected thermal energy to electricity within a Thermal-Energy Conversion Component.
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