公开(公告)号：US20160152905A1

公开(公告)日：2016-06-02

申请号：US14952060

申请日：2015-11-25

Applicant: Sundrop Fuels, Inc.

Inventor： Renus C. Kelfkens ,  Wayne W. Simmons ,  Douglas S. Jack ,  Jerrod Wayne Hohman ,  Sidney P. White

IPC: C10J3/46 ,  C10J3/50 ,  C01B3/38 ,  C10K3/00 ,  C10G2/00 ,  C10L1/04 ,  C10J3/48 ,  C10J3/84

CPC classification number: 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

Abstract: 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.

Abstract translation: 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料合成气从第一阶段进一步重整成化学级合成气，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。

公开(公告)号：US09771531B2

公开(公告)日：2017-09-26

申请号：US14952060

申请日：2015-11-25

Applicant: Sundrop Fuels, Inc.

Inventor： Renus C. Kelfkens ,  Wayne W. Simmons ,  Douglas S. Jack ,  Jerrod Wayne Hohman ,  Sidney P. White

IPC: C10G3/00 ,  C10G2/00 ,  C10J3/46 ,  C10G45/44 ,  C10K1/08 ,  C10K1/32 ,  C10K3/02 ,  C10G45/00 ,  C10L1/04 ,  C10K3/00 ,  C10J3/84 ,  C10J3/50 ,  C01B3/38 ,  C10J3/48

CPC classification number: 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

Abstract: 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.

公开(公告)号：US20170137284A1

公开(公告)日：2017-05-18

申请号：US15419826

申请日：2017-01-30

Applicant: Sundrop Fuels, Inc.

Inventor： Wayne W. Simmons ,  Sidney P. White ,  Christopher Perkins

IPC: C01B3/38 ,  B01J19/00 ,  C10J3/84 ,  B01J19/24 ,  C10J3/48 ,  C10J3/62

CPC classification number: C01B3/384 ,  B01J19/0013 ,  B01J19/0033 ,  B01J19/2445 ,  B01J19/245 ,  B01J2219/00117 ,  B01J2219/00186 ,  C01B3/22 ,  C01B3/34 ,  C01B2203/0216 ,  C01B2203/0233 ,  C01B2203/061 ,  C01B2203/0811 ,  C01B2203/1241 ,  C01B2203/1685 ,  C01B2203/84 ,  C07C29/15 ,  C07C29/1518 ,  C10G2/30 ,  C10G2/32 ,  C10G3/00 ,  C10G2300/1014 ,  C10G2300/1025 ,  C10G2300/807 ,  C10J3/00 ,  C10J3/466 ,  C10J3/482 ,  C10J3/485 ,  C10J3/506 ,  C10J3/54 ,  C10J3/56 ,  C10J3/58 ,  C10J3/60 ,  C10J3/62 ,  C10J3/721 ,  C10J3/723 ,  C10J3/82 ,  C10J3/84 ,  C10J2200/09 ,  C10J2200/15 ,  C10J2200/158 ,  C10J2300/0906 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/094 ,  C10J2300/0973 ,  C10J2300/0976 ,  C10J2300/0989 ,  C10J2300/0993 ,  C10J2300/1223 ,  C10J2300/123 ,  C10J2300/1284 ,  C10J2300/1292 ,  C10J2300/1621 ,  C10J2300/1659 ,  C10J2300/1665 ,  C10J2300/1693 ,  C10J2300/1853 ,  C10J2300/1861 ,  C10K1/024 ,  C10L1/04 ,  C10L2200/0492 ,  C10L2290/02 ,  C10L2290/04 ,  C10L2290/06 ,  C10L2290/08 ,  C10L2290/28 ,  C10L2290/42 ,  C10L2290/50 ,  C10L2290/52 ,  C10L2290/547 ,  F24S20/20 ,  Y02B40/18 ,  Y02E10/41 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/129 ,  Y02P20/134 ,  Y02P20/136 ,  Y02P20/145 ,  Y02P30/20 ,  Y02T50/678 ,  C07C31/04

Abstract: A multiple stage synthesis gas generation system is disclosed including a high radiant heat flux reactor, a gasifier reactor control system, and a Steam Methane Reformer (SMR) reactor. The SMR reactor is in parallel and cooperates with the high radiant heat flux reactor to produce a high quality syngas mixture for MeOH synthesis. The resultant products from the two reactors may be used for the MeOH synthesis. The SMR provides hydrogen rich syngas to be mixed with the potentially carbon monoxide rich syngas from the high radiant heat flux reactor. The combination of syngas component streams from the two reactors can provide the required hydrogen to carbon monoxide ratio for methanol synthesis. The SMR reactor control system and a gasifier reactor control system interact to produce a high quality syngas mixture for the MeOH synthesis.