公开(公告)号：US20190144768A1

公开(公告)日：2019-05-16

申请号：US15812340

申请日：2017-11-14

申请人： ExxonMobil Research and Engineering Company

发明人： Mohsen N. Harandi ,  Suriyanarayanan Rajagopalan

IPC分类号： C10J3/46 ,  C10J3/82 ,  C10J3/48 ,  B01J8/26 ,  C07C29/151 ,  C07C273/10 ,  C01C1/04

CPC分类号： C10J3/466 ,  B01J8/26 ,  B01J2208/00752 ,  B01J2208/00982 ,  C01C1/0405 ,  C07C29/1518 ,  C07C273/10 ,  C10J3/48 ,  C10J3/485 ,  C10J3/82 ,  C10J3/84 ,  C10J2300/0903 ,  C10J2300/0943 ,  C10J2300/0959 ,  C10J2300/1665 ,  C10J2300/1668 ,  C07C31/04

摘要： Systems and methods are provided for producing high quality synthesis gas from a fluidized coking system that includes an integrated gasifier. Additionally or alternately, systems and methods are provided for integrating a fluidized coking process, a coke gasification process, and processes for production of compounds from the synthesis gas generated during the coke gasification. The integrated process can also allow for reduced or minimized production of inorganic nitrogen compounds by using oxygen from an air separation unit as the oxygen source for gasification. Although the amount of nitrogen introduced as a diluent into the gasification will be reduced, minimized, or eliminated, the integrated process can also allow for gasification of coke while reducing, minimizing, or eliminating production of slag or other glass-like substances in the gasifier. Examples of compounds that can be produced from the synthesis gas include, but are not limited to, methanol, ammonia, and urea.

公开(公告)号：US20170267539A1

公开(公告)日：2017-09-21

申请号：US15476494

申请日：2017-03-31

申请人： Ethan Novek

发明人： Ethan Novek

IPC分类号： C01C1/26 ,  C07C273/10 ,  C07C269/06 ,  C07C269/00 ,  H02K7/18 ,  C07C273/04

CPC分类号： C01C1/26 ,  B01D53/343 ,  B01D53/58 ,  B01D53/62 ,  B01D61/06 ,  B01D2251/206 ,  B01D2251/60 ,  B01D2251/606 ,  B01D2252/10 ,  B01D2252/202 ,  B01D2252/205 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2258/0283 ,  C01B32/50 ,  C07C269/00 ,  C07C269/06 ,  C07C273/04 ,  C07C273/10 ,  H02K7/1823 ,  Y02C10/04 ,  Y02E50/346 ,  Y02P20/125 ,  Y02P20/129 ,  Y02P20/152

摘要： The present invention pertains to new methods for generating energy and useful nitrogen compounds from captured carbon dioxide. It involves employing an osmotic engine, draw solution, and feed solution. An osmotic gradient between the solutions assists in generating energy and a solution of ammonium carbonate, ammonium bicarbonate or mixture thereof. This solution may be decomposed to form ammonia, carbon dioxide, a precipitate, or a mixture thereof.

公开(公告)号：US20160251228A1

公开(公告)日：2016-09-01

申请号：US14992204

申请日：2016-01-11

申请人： Khalid T. Alkusayer

发明人： Khalid T. Alkusayer

IPC分类号： C01C1/04 ,  B01J19/00 ,  B01J19/24

CPC分类号： C01C1/0488 ,  B01J19/0006 ,  B01J19/24 ,  B01J19/2475 ,  B01J2219/00058 ,  B01J2219/24 ,  C01B3/025 ,  C01B3/06 ,  C01B3/16 ,  C01B3/505 ,  C01B3/58 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/0435 ,  C01B2203/066 ,  C01B2203/068 ,  C01B2203/1205 ,  C01C1/0405 ,  C01C1/0411 ,  C01C1/0417 ,  C01C1/0452 ,  C01C1/0458 ,  C07C273/10 ,  C25B5/00 ,  Y02E60/36 ,  Y02E60/566 ,  Y02P20/52

摘要： A method for synthesizing ammonia for agricultural fertilizers employs water (H2O) as the source of hydrogen (H2) in ammonia (NH3) synthesis, and gathers carbon monoxide (CO) as a limiting reagent for combining in a WGS (Water-Gas-Shift) reaction for producing hydrogen. The WGS reaction employs CO with the water to produce Carbon Dioxide (CO2) and H2, consuming undesirable CO from other industrial applications. A by-product of the process includes generating 1.5 mole of CO2 for each mole of ammonia synthesized. An intermediate step consumes 3 moles of hydrogen for each mole of Nitrogen (N2). The use of methane gas is avoided as the process employs CO and the WGS reaction as an exclusive source of H2 without introducing methane (CH4). A downstream synthesis of ammonia can be done through a fuel cell to produce electricity for the ammonia synthesis for further sustainability.

公开(公告)号：US20160167974A1

公开(公告)日：2016-06-16

申请号：US14826771

申请日：2015-08-14

申请人： Ethan Novek

发明人： Ethan Novek

IPC分类号： C01C1/26 ,  C01B31/20 ,  H02K7/18 ,  C07C273/10 ,  C07C269/00 ,  C01C1/02 ,  C07C269/06

CPC分类号： C01C1/26 ,  B01D53/343 ,  B01D53/58 ,  B01D53/62 ,  B01D61/06 ,  B01D2251/206 ,  B01D2251/60 ,  B01D2251/606 ,  B01D2252/10 ,  B01D2252/202 ,  B01D2252/205 ,  B01D2257/406 ,  B01D2257/504 ,  B01D2258/0283 ,  C01B32/50 ,  C07C269/00 ,  C07C269/06 ,  C07C273/04 ,  C07C273/10 ,  H02K7/1823 ,  Y02P20/125 ,  Y02P20/129

摘要： The present invention pertains to new methods for generating energy and useful nitrogen compounds from captured carbon dioxide. It involves employing an osmotic engine, draw solution, and feed solution. An osmotic gradient between the solutions assists in generating energy and a solution of ammonium carbonate, ammonium bicarbonate or mixture thereof. This solution may be decomposed to form ammonia, carbon dioxide, a precipitate, or a mixture thereof.

摘要翻译： 本发明涉及从捕获的二氧化碳产生能量和有用的氮化合物的新方法。 它涉及采用渗透引擎，拉伸溶液和进料溶液。 溶液之间的渗透梯度有助于产生能量和碳酸铵，碳酸氢铵或其混合物的溶液。 该溶液可以分解形成氨，二氧化碳，沉淀物或其混合物。

公开(公告)号：US20150368191A1

公开(公告)日：2015-12-24

申请号：US14311477

申请日：2014-06-23

申请人： ALSTOM Technology Ltd

发明人： Frank ENNENBACH ,  Ulrich KOSS

IPC分类号： C07C273/10 ,  C01C1/12 ,  C01C1/04 ,  C07C273/04

CPC分类号： C07C273/10 ,  C01C1/04 ,  C01C1/0488 ,  C01C1/12 ,  C07C273/04 ,  Y02P20/52

摘要： A method of forming urea by integration of an ammonia production process with that of a urea production process, as well as a system for the method is disclosed. Also, an alternative method of forming urea by integration of a part of an ammonia production process with that of a urea production process, as well as a system for the alternative method.

摘要翻译： 公开了通过氨生产过程与尿素生产过程的整合形成尿素的方法以及该方法的系统。 此外，通过将氨生产过程的一部分与尿素生产过程的一部分相结合形成尿素的替代方法以及用于替代方法的系统。

公开(公告)号：US20140217206A1

公开(公告)日：2014-08-07

申请号：US14143890

申请日：2013-12-30

申请人： 4A TECHNOLOGIES, LLC

发明人： Terry R. Collins ,  James L. Simonton ,  Mario G. Beruvides ,  Jessie Lozada ,  Ernesto Iznaga

IPC分类号： B02C19/00 ,  B02C21/00 ,  C10L5/44

CPC分类号： C07C273/10 ,  B02C19/0056 ,  B02C21/00 ,  B03B9/061 ,  C10J3/72 ,  C10J3/82 ,  C10J2300/0906 ,  C10J2300/0916 ,  C10J2300/1668 ,  C10L5/363 ,  C10L5/44 ,  Y02E50/10 ,  Y02E50/30

摘要： A modular system and method for producing urea from bio-mass includes means and steps for “homogenizing” a biomass feedstock stream having components with different bulk density BTU content into a stream having a consistent bulk density BTU content. The steps include cleaning the incoming bio-mass feedstock stream to remove non-organic matter, blending the cleaned bio-mass feedstock stream to obtain a homogeneous blend having a consistent bulk density BTU content, and milling the homogeneous blend bio-mass feedstock stream to a predetermined size no greater than 12 mm.

摘要翻译： 用于从生物质量生产尿素的模块化系统和方法包括将具有不同体积密度BTU含量的组分的生物质原料料“均质化”为具有一致体积密度BTU含量的流的手段和步骤。 这些步骤包括清洁进入的生物质原料流以除去非有机物质，混合清洁的生物质原料流以获得具有一致堆积密度BTU含量的均匀共混物，以及将均匀混合生物质原料流研磨至 预定尺寸不大于12mm。

公开(公告)号：US20100205856A1

公开(公告)日：2010-08-19

申请号：US12682442

申请日：2008-08-13

申请人： William Louis Kubic ,  F. Jeffrey Martin

发明人： William Louis Kubic ,  F. Jeffrey Martin

IPC分类号： C10L1/182 ,  C07C1/04 ,  C07C273/04 ,  C07C1/20 ,  C10G31/00

CPC分类号： C10G2/50 ,  B01D53/62 ,  B01D2251/30 ,  B01D2251/40 ,  B01D2251/604 ,  B01D2251/606 ,  B01D2257/504 ,  C01B3/02 ,  C01B2203/061 ,  C01B2203/062 ,  C07C273/10 ,  C10G2/30 ,  C10G3/00 ,  C10G2300/1022 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10G2400/30 ,  C25B1/02 ,  G21D9/00 ,  Y02C10/04 ,  Y02C10/06 ,  Y02P20/133 ,  Y02P20/134 ,  Y02P20/152 ,  Y02P30/40 ,  Y02P30/42

摘要： The present invention is directed to providing a method of producing synthetic fuels and organic chemicals from atmospheric carbon dioxide. Carbon dioxide gas is extracted from the atmosphere, hydrogen gas is obtained by splitting water, a mixture of the carbon dioxide gas and the hydrogen gas (synthesis gas) is generated, and the synthesis gas is converted into synthetic fuels and/or organic products. The present invention is also directed to utilizing a nuclear power reactor to provide power for the method of the present invention.

摘要翻译： 本发明旨在提供从大气二氧化碳生产合成燃料和有机化学物质的方法。 从大气中抽取二氧化碳气体，通过分解水分获得氢气，生成二氧化碳气体与氢气（合成气体）的混合物，将合成气转化成合成燃料和/或有机物。 本发明还涉及利用核动力反应堆为本发明的方法提供动力。

公开(公告)号：US06340451B1

公开(公告)日：2002-01-22

申请号：US09538971

申请日：2000-03-31

申请人： Giorgio Pagani ,  Federico Zardi

发明人： Giorgio Pagani ,  Federico Zardi

IPC分类号： C01C104

CPC分类号： C01C1/0488 ,  C07C273/10 ,  Y02P20/52

摘要： A method for the simultaneous modernization of a plant for ammonia synthesis and a plant for urea synthesis, provides—inter alia—the arrangement of a carbamate synthesis section and a carbamate decomposition section, in order to obtain a predetermined amount of carbamate in aqueous solution and of hydrogen and nitrogen in gaseous phase which are fed to the existing sections for urea synthesis, respectively ammonia synthesis. Thanks to this method of modernization it is possible to remarkably increase the production capacity and at the same time to reduce the energy consumption of the urea and ammonia plants without being forced to replace or anyway overload the existing sections of decarbonation, methanation and compression, in general.

摘要翻译： 用于氨合成设备的同时现代化的方法和用于尿素合成的设备的方法尤其提供氨基甲酸酯合成段和氨基甲酸酯分解段的排列，以便在水溶液中获得预定量的氨基甲酸酯， 的氢气和氮气，分别送入现有的尿素合成段，分别为氨合成。 由于这种现代化方法，可以显着提高生产能力，同时可以降低尿素和氨厂的能源消耗，而不会被迫更换或反过来现有的脱碳，甲烷化和压缩部分， 一般。

公开(公告)号：US4690812A

公开(公告)日：1987-09-01

申请号：US692563

申请日：1985-01-18

申请人： Gerhard Ranke ,  Ulrich Schrader

发明人： Gerhard Ranke ,  Ulrich Schrader

IPC分类号： C01B3/34 ,  C01C1/04 ,  C07C67/00 ,  C07C239/00 ,  C07C273/10

CPC分类号： C07C273/10

摘要： The combined production of ammonia and urea by the reaction of gases containing hydrocarbons with steam is conducted by using a steam reformer, downstream secondary reformer, and shift converter. The ammonia synthesis gas (hydrogen, nitrogen and carbon dioxide) is subjected to a high pressure scrubbing step with a physical solvent, to remove the acid impurities, especially CO.sub.2. The pressure on the loaded solvent is reduced to a first intermediate pressure for degasing of the coabsorbed inerts and then to a second intermediate pressure for removal of the bulk of the absorbed CO.sub.2, which is then used for urea synthesis. To remove residual CO.sub.2, the solvent is stripped with air and the resultant air stream containing the stripped residual CO.sub.2 is fed to the secondary reformer.

摘要翻译： 通过使用蒸汽重整器，下游次级重整器和换档转换器，通过含有烃与气体的气体的反应将氨和尿素合并生产。 将氨合成气（氢气，氮气和二氧化碳）用物理溶剂进行高压洗涤，除去酸性杂质，特别是二氧化碳。 负载溶剂上的压力降低到第一中间压力，用于对吸附的惰性气体进行脱气，然后降低到第二中间压力，以除去大部分吸收的CO 2，然后将其用于尿素合成。 为了除去残留的CO 2，用空气汽提溶剂，将含有汽提残余CO 2的所得空气流送入二次重整器。

公开(公告)号：US4320103A

公开(公告)日：1982-03-16

申请号：US184175

申请日：1980-09-04

申请人： Giorgio Pagani

发明人： Giorgio Pagani

IPC分类号： C01C1/04 ,  C07C67/00 ,  C07C239/00 ,  C07C273/04 ,  C07C273/10 ,  C07C126/00

CPC分类号： C07C273/10 ,  C01C1/0458 ,  C01C1/0488 ,  Y02P20/125 ,  Y02P20/52

摘要： In an integrated flexible installation for producing ammonia and urea, the improved method which consists in that a portion of the gaseous stream comprising carbon dioxide, hydrogen and nitrogen is fed to a complementary decarbonation area and then admixed with a portion of a similar, but non-decarbonated stream of gas prior to entering the carbon-dioxide-absorption unit. Liquid ammonia is recovered from a portion of the ammoniated aqueous solution used for abating the ammonia and sent to a distillation column to recover liquid ammonia therefrom.

摘要翻译： 在用于生产氨和尿素的集成柔性装置中，改进的方法包括将包含二氧化碳，氢气和氮气的气流的一部分进料到互补脱碳区域，然后与一部分类似但非非 - 在进入二氧化碳 - 吸收单元之前的气体流。 从用于减轻氨的氨化水溶液的一部分回收液氨，并送入蒸馏塔以从其中回收液态氨。