专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明申请

WO2016086141A1 BIOMASS TO TRANSPORTATION FUELS USING A FISCHER-TROPSCH PROCESS 审中-公开
标题翻译：使用FISCHER-TROPSCH过程的运输燃料的生物量
公开(公告)号：WO2016086141A1
公开(公告)日：2016-06-02
申请号：PCT/US2015/062697
申请日：2015-11-25
申请人： SUNDROP FUELS, INC.
发明人： KELFKENS, Renus, C. , SIMMONS, Wayne, W. , JACK, Douglas, S. , HOHMAN, Jerrod, Wayne , WHITE, Sidney, P.
IPC分类号： C07C1/04
CPC分类号： C10J3/466 , C01B3/38 , C01B2203/0233 , C01B2203/062 , C01B2203/1241 , C10G2/32 , C10G2/34 , C10G3/00 , C10G45/00 , C10G45/44 , C10G2300/1011 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10J3/485 , C10J3/506 , C10J3/84 , C10J2300/0916 , C10J2300/0976 , C10J2300/1659 , C10J2300/1807 , C10J2300/1853 , C10K1/08 , C10K1/32 , C10K3/008 , C10K3/023 , C10L1/04 , C10L2200/0492 , C10L2270/023 , C10L2270/026 , C10L2270/04 , C10L2290/04 , C10L2290/06 , C10L2290/10 , C10L2290/42 , C10L2290/541 , C10L2290/542 , C10L2290/543 , C10L2290/548 , Y02E50/32 , Y02P20/145 , Y02P20/582 , Y02P30/20
摘要： An integrated plant to generate chemical grade syngas from a steam biomass reforming in a multiple stage bio reforming reactor for use with either a high temperature or low temperature Fischer-Tropsch synthesis process to produce fuel from biomass is discussed. The first stage has a reactor to cause a chemical devolatilization of a biomass feedstock from the biomass feedstock supply lines into its constituent gases of CO, H2, CO2, CH4, tars, chars, and other components into a raw syngas mixture. A second stage performs further reforming of the raw syngas from the first stage into the chemical grade syngas by further applying heat and pressure to chemically crack at least the tars, reform the CH4, or a combination of both, into their corresponding syngas molecules. The second stage feeds the chemical grade syngas derived from the biomass feedstock to the downstream Fischer-Tropsch train to produce the fuel from the biomass. One or more recycle loops supply tail gas or FT product back into the plant.
摘要翻译：讨论了一种用于在多级生物重整反应器中从蒸汽生物质重整产生化学级合成气的综合工厂，用于与高温或低温费 - 托合成方法一起使用以从生物质产生燃料。第一阶段具有反应器，以使生物质原料从生物质原料供应管线进入其CO，H 2，CO 2，CH 4，焦油，焦炭和其它组分的组成气体中的化学脱挥发分成原始合成气混合物。第二阶段通过进一步施加热和压力来将原始合成气从第一阶段进一步转化为化学级合成气，至少化学裂化焦油，将CH 4或两者的组合重整成相应的合成气分子。第二阶段将来自生物质原料的化学级合成气进料到下游费 - 托列车，以从生物质产生燃料。一个或多个回收循环将尾气或FT产物回送到工厂。

2. 发明申请

WO2018187716A1 INTEGRATED BIOFUELS PROCESS CONFIGURATIONS, EMPLOYING A 2-STAGE BIO-REFORMING REACTOR SYSTEM, IN WHICH RENEWABLE CARBON CONTENT OF GASOLINE AND DIESEL ARE OPTIMIZED FOR VALUE 审中-公开
公开(公告)号：WO2018187716A1
公开(公告)日：2018-10-11
申请号：PCT/US2018/026504
申请日：2018-04-06
申请人： SUNDROP FUELS, INC.
发明人： JACK, Douglas, S. , KELFKENS, Renus, C. , LYTHGOE, Steven, C. , SIMMONS, Wayne, W.
IPC分类号： C10J3/46 , C01B3/38 , C10G2/00
摘要： A bio-reforming reactor receives biomass to generate chemical grade syngas for a coupled downstream train of any of 1) a methanol-synthesis-reactor train, 2) a ethanol-to-gasoline reactor train, and 3) a high-temperature Fischer-Tropsch reactor train, that use this syngas derived from the biomass in the bio-reforming reactor. A renewable carbon content of the produced gasoline, jet fuel, and/or diesel derived from the coupled downstream trains of any of 1) the methanol-synthesis-reactor train, 2) the methanol-to-gasoline reactor train, or 3) the high-temperature Fischer-Tropsch reactor train are optimized for recovery of renewable carbon content to produce fuel products with 100% biogenic carbon content and/or fuel products with 50 - 100% biogenic carbon content. A carbon-dioxide gas feedback loop cooperates with a CO2 separation unit to supply a fraction of the CO2 gas that is removed from the chemical grade syngas produced from the reactor output of the BRR to supply extracted CO2 gas to the biomass feed system.

3. 发明申请

WO2017044748A1 AN INTEGRATED PROCESS PLANT HAVING A BIOMASS REFORMING REACTOR USING A FLUIDIZED BED 审中-公开
标题翻译：使用流化床的生物质改性反应器的综合工艺设备
公开(公告)号：WO2017044748A1
公开(公告)日：2017-03-16
申请号：PCT/US2016/050950
申请日：2016-09-09
申请人： SUNDROP FUELS, INC.
发明人： JACK, Douglas, S. , KELFKENS, Renus, C. , SIMMONS, Wayne, W. , ARGO, Andrew , BROERMAN, Andrew, W.
IPC分类号： C01B3/02 , C01B3/38 , C01B3/44 , C10G11/18
CPC分类号： C10J3/84 , B01J8/24 , C01B3/02 , C01B3/24 , C01B3/26 , C01B3/56 , C01B2203/0233 , C01B2203/0272 , C01B2203/0277 , C01B2203/04 , C01B2203/0465 , C01B2203/0475 , C01B2203/048 , C01B2203/0485 , C01B2203/0495 , C01B2203/061 , C01B2203/062 , C01B2203/063 , C01B2203/0816 , C01B2203/1041 , C01B2203/1058 , C01B2203/1241 , C01B2203/1247 , C01B2203/1252 , C01B2203/1258 , C01B2203/1676 , C10J3/466 , C10J3/485 , C10J2200/15 , C10J2300/0916 , C10J2300/0976 , C10J2300/0993 , C10J2300/1659 , C10J2300/1665 , C10J2300/1853 , Y02P20/125 , Y02P20/145
摘要： An interconnected set of two or more stages of reactors to form a bio-reforming reactor that generates syngas for a number of different liquid fuel or chemical processes is discussed. A first stage includes a circulating fluidized bed reactor that is configured to cause a chemical devolatilization of the biomass into its reaction products of constituent gases, tars, chars, and other components, which exit through a reactor output from the first stage. A second stage of the bio-reforming reactor has an input configured to receive a stream of some of the reaction products that includes the constituent gases and at least some of the tars as raw syngas, and then chemically reacts the raw syngas within a vessel of the second stage to make the raw syngas from the first stage into a chemical grade syngas by further cracking the tars, excess methane, or both.
摘要翻译：讨论了两个或更多阶段的反应器的互连的组合，以形成生成用于多种不同液体燃料或化学过程的合成气的生物重整反应器。第一阶段包括循环流化床反应器，其被配置为使生物质进入其组成气体，焦油，焦炭和其它组分的反应产物的化学脱挥发分，所述组分气体，焦油，焦炭和其它组分通过来自第一级的反应器输出而排出。生物重整反应器的第二阶段具有被配置为接收包括构成气体的一些反应产物的流和至少一些焦油作为原始合成气的输入，然后使原料合成气在容器内的化学反应第二阶段是通过进一步开裂焦油，多余的甲烷或两者将第一阶段的原始合成气进入化学级合成气。

4. 发明申请

WO2014043552A1 IMPROVING RENEWABLE CARBON CONTENT IN METHANOL AND OTHER PRODUCTS FROM GASIFICATION OF BIOMASS 审中-公开
标题翻译：改善甲醇和其他产品中可再生碳含量的生物量
公开(公告)号：WO2014043552A1
公开(公告)日：2014-03-20
申请号：PCT/US2013/059782
申请日：2013-09-13
申请人： SUNDROP FUELS, INC.
发明人： KELFKENS, Renus, C. , KOSSTRIN, Herbert, M.
IPC分类号： C01B3/38 , F01N3/20 , C09K3/00 , G05B1/00
CPC分类号： C07C29/1518 , Y02E50/18 , C07C31/04
摘要： An integrated plant is provided to improve carbon utilization of carbon molecules from gasified woody biomass to be converted into methanol. Detectors ensure a minimized sulfur content of less than 0.05% by dry weight of the woody biomass. A biomass gasifier reacts woody biomass in a rapid gasification reaction to produce a syngas composition having a ratio of hydrogen to carbon dioxide that is higher than needed for methanol synthesis. Parallel to the gasifier, a hydrocarbon reforming reactor provides a syngas composition having a ratio of hydrogen to carbon monoxide that is higher than needed for methanol synthesis. The combined syngas mixture from the biomass gasifier and the hydrocarbon reforming reactor comprises feed to a methanol synthesis plant, such that a majority of the carbon dioxide produced by the biomass gasification reaction and the hydrogen produced by the hydrocarbon reforming reactor are synthesized into methanol.
摘要翻译：提供了一个综合设备，以提高碳化合物的碳分子从气化的木质生物质转化成甲醇。检测器确保木质生物质的干重减少硫含量小于0.05％。生物质气化器在快速气化反应中使木质生物质反应以产生具有高于甲醇合成所需的氢气与二氧化碳的比例的合成气组合物。平行于气化器，烃重整反应器提供了比甲醇合成所需的氢气与一氧化碳的比例高的合成气组合物。来自生物质气化器和烃重整反应器的合成合成气混合物包括进料到甲醇合成装置，使得通过生物质气化反应产生的大部分二氧化碳和由烃重整反应器产生的氢气合成为甲醇。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式