利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

116 条记录 (耗时 0.024 秒)

    PROCESS FOR THE GASIFICATION OF WET BIOMASS
    6.
    发明申请
    PROCESS FOR THE GASIFICATION OF WET BIOMASS 审中-公开
    湿生物量气化方法

    公开(公告)号：US20140193326A1

    公开(公告)日：2014-07-10

    申请号：US14239617

    申请日：2012-08-20

    申请人： John Harinck ,  Klaas Gerrit Smit

    发明人： John Harinck ,  Klaas Gerrit Smit

    IPC分类号： C07C1/22 ,  C01B3/02

    CPC分类号： C10B49/10 ,  C01B3/02 ,  C07C1/22 ,  C10J3/78 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0979 ,  C10J2300/1884 ,  C10L3/08 ,  C10L9/086 ,  Y02E50/14 ,  Y02P20/145 ,  Y02P20/544

    摘要： A process for the gasification of wet biomass comprises feeding the wet biomass at a temperature of at most 370 C. and a pressure of at least 22.1 MPa (absolute) to a reactor. The reactor comprises a bed of solid particles suspended in a fluid. The temperature of the feed is increased in the presence of the bed of suspended solid particles to a temperature of at least 375° C., forming supercritical water and converting in the presence of the supercritical water at least a portion of the organic materials present in the wet biomass into fluid gasification product.

    摘要翻译： 用于气化湿生物质的方法包括在至多370℃的温度和至少22.1MPa（绝对）的压力下将反应器的湿生物质进料。 反应器包括悬浮在流体中的固体颗粒床。 在悬浮固体颗粒床的存在下，进料的温度升高到至少375℃的温度，形成超临界水并在超临界水存在下转化至少部分有机材料存在于 将湿生物质转化为流化气化产物。

    METHODS FOR SULFATE REMOVAL IN LIQUID-PHASE CATALYTIC HYDROTHERMAL GASIFICATION OF BIOMASS
    7.
    发明申请
    METHODS FOR SULFATE REMOVAL IN LIQUID-PHASE CATALYTIC HYDROTHERMAL GASIFICATION OF BIOMASS 有权
    生物质液相催化氢热气化脱硫方法

    公开(公告)号：US20140054507A1

    公开(公告)日：2014-02-27

    申请号：US14069333

    申请日：2013-10-31

    申请人： Genifuel Corporation ,  Battelle Memorial Institute

    发明人： Douglas C. Elliott ,  James R. Oyler

    IPC分类号： B01J19/14 ,  B01J39/02

    CPC分类号： B01J19/14 ,  B01J21/18 ,  B01J23/462 ,  B01J23/75 ,  B01J23/78 ,  B01J39/02 ,  B09B3/00 ,  B09B3/0083 ,  C10B53/02 ,  C10J3/78 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0979 ,  C10L3/08 ,  C10L5/44 ,  C10L9/086 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/30 ,  Y02P20/145 ,  Y02P20/52

    摘要： Processing of wet biomass feedstock by liquid-phase catalytic hydrothermal gasification must address catalyst fouling and poisoning. One solution can involve heating the wet biomass with a heating unit to a pre-treatment temperature sufficient for organic constituents in the feedstock to decompose, for precipitates of inorganic wastes to form, for preheating the wet feedstock in preparation for subsequent removal of soluble sulfate contaminants, or combinations thereof. Processing further includes reacting the soluble sulfate contaminants with cations present in the feedstock material to yield a sulfate-containing precipitate and separating the inorganic precipitates and/or the sulfate-containing precipitates out of the wet feedstock. Having removed much of the inorganic wastes and the sulfate contaminants that can cause poisoning and fouling, the wet biomass feedstock can be exposed to the heterogeneous catalyst for gasification.

    摘要翻译： 通过液相催化水热气化处理湿生物质原料必须解决催化剂污染和中毒问题。 一种解决方案可以包括用加热单元将湿生物质加热到足以使原料中的有机成分分解的预处理温度，用于沉淀无机废物以形成，用于预热湿原料以备后续除去可溶性硫酸盐污染物 ，或其组合。 处理进一步包括使可溶性硫酸盐污染物与原料中存在的阳离子反应以产生含硫酸盐的沉淀物，并将无机沉淀物和/或硫酸盐沉淀物从湿原料中分离出来。 除去大量无机废物和可能引起中毒和结垢的硫酸盐污染物，湿生物质原料可暴露于非均相催化剂进行气化。

    Methods for sulfate removal in liquid-phase catalytic hydrothermal gasification of biomass
    8.
    发明授权
    Methods for sulfate removal in liquid-phase catalytic hydrothermal gasification of biomass 有权
    生物质液相催化水热气化硫酸盐去除方法

    公开(公告)号：US08608981B2

    公开(公告)日：2013-12-17

    申请号：US13541003

    申请日：2012-07-03

    申请人： Douglas C. Elliott ,  James Oyler

    发明人： Douglas C. Elliott ,  James Oyler

    IPC分类号： C01B3/38 ,  C01B3/24

    CPC分类号： B01J19/14 ,  B01J21/18 ,  B01J23/462 ,  B01J23/75 ,  B01J23/78 ,  B01J39/02 ,  B09B3/00 ,  B09B3/0083 ,  C10B53/02 ,  C10J3/78 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0979 ,  C10L3/08 ,  C10L5/44 ,  C10L9/086 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/30 ,  Y02P20/145 ,  Y02P20/52

    摘要： Processing of wet biomass feedstock by liquid-phase catalytic hydrothermal gasification must address catalyst fouling and poisoning. One solution can involve heating the wet biomass with a heating unit to a pre-treatment temperature sufficient for organic constituents in the feedstock to decompose, for precipitates of inorganic wastes to form, for preheating the wet feedstock in preparation for subsequent removal of soluble sulfate contaminants, or combinations thereof. Processing further includes reacting the soluble sulfate contaminants with cations present in the feedstock material to yield a sulfate-containing precipitate and separating the inorganic precipitates and/or the sulfate-containing precipitates out of the wet feedstock. Having removed much of the inorganic wastes and the sulfate contaminants that can cause poisoning and fouling, the wet biomass feedstock can be exposed to the heterogeneous catalyst for gasification.

    摘要翻译： 通过液相催化水热气化处理湿生物质原料必须解决催化剂污染和中毒问题。 一种解决方案可以包括用加热单元将湿生物质加热到足以使原料中的有机成分分解的预处理温度，用于沉淀无机废物以形成，用于预热湿原料以备后续除去可溶性硫酸盐污染物 ，或其组合。 处理进一步包括使可溶性硫酸盐污染物与原料中存在的阳离子反应以产生含硫酸盐的沉淀物，并将无机沉淀物和/或硫酸盐沉淀物从湿原料中分离出来。 除去大量无机废物和可能引起中毒和结垢的硫酸盐污染物，湿生物质原料可暴露于非均相催化剂进行气化。

    FLUIDIZED BED BIOGASIFIER AND METHOD FOR GASIFYING BIOSOLIDS
    9.
    发明申请
    FLUIDIZED BED BIOGASIFIER AND METHOD FOR GASIFYING BIOSOLIDS 有权
    流化床生物加工器和用于吸收生物体的方法

    公开(公告)号：US20130195727A1

    公开(公告)日：2013-08-01

    申请号：US13361582

    申请日：2012-01-30

    申请人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

    发明人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

    IPC分类号： B01J8/18 ,  B23P17/00 ,  C07C5/02

    CPC分类号： C10J3/466 ,  B01J8/1809 ,  B01J8/1827 ,  B01J2208/00893 ,  B01J2208/00902 ,  C02F11/10 ,  C02F11/12 ,  C02F11/121 ,  C10J3/482 ,  C10J3/84 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0956 ,  C10J2300/1643 ,  C10J2300/1807 ,  C10K1/026 ,  Y02P20/129 ,  Y02W10/40 ,  Y10T29/49

    摘要： A fluidized bed biogasifier is provided for gasifying biosolids. The biogasifier includes a reactor vessel and a feeder for feeding biosolids into the reactor vessel at a desired feed rate during steady-state operation of the biogasifier. A fluidized bed in the base of the reactor vessel has a cross-sectional area that is proportional to at least the fuel feed rate such that the superficial velocity of gas is in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). In a method for gasifying biosolids, biosolids are fed into a fluidized bed reactor. Oxidant gases are applied to the fluidized bed reactor to produce a superficial velocity of producer gas in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). The biosolids are heated inside the fluidized bed reactor to a temperature range between 900° F. (482.2° C.) and 1700° F. (926.7° C.) in an oxygen-starved environment having a sub-stoichiometric oxygen level, whereby the biosolids are gasified.

    摘要翻译： 提供流化床生物气化器用于气化生物固体。 生物气化器包括反应器容器和用于在生物气化器的稳态操作期间以期望的进料速率将生物固体进料到反应器容器中的进料器。 在反应器容器底部的流化床具有与至少燃料供给速率成比例的横截面积，使得气体的表观速度在0.1m / s（0.33ft / s）至3的范围内 m / s（9.84ft / s）。 在气化生物固体的方法中，将生物固体进料到流化床反应器中。 将氧化剂气体施加到流化床反应器以产生0.1m / s（0.33ft / s）至3m / s（9.84ft / s）范围内的发生气体的表观速度。 在具有亚化学计量氧水平的氧缺乏环境中，将生物固体在流化床反应器内加热至900°F（482.2℃）至1700°F（926.7℃）之间的温度范围，由此 生物固体气化。