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    CO-PROCESSING FOR CONTROL OF HYDROPYROLYSIS PROCESSES AND PRODUCTS THEREOF
    1.
    发明申请
    CO-PROCESSING FOR CONTROL OF HYDROPYROLYSIS PROCESSES AND PRODUCTS THEREOF 审中-公开
    用于控制水解过程及其制品的CO加工

    公开(公告)号：US20160312125A1

    公开(公告)日：2016-10-27

    申请号：US14696632

    申请日：2015-04-27

    申请人： GAS TECHNOLOGY INSTITUTE

    发明人： Martin B. LINCK ,  Terry L. MARKER ,  Michael J. ROBERTS ,  Larry G. FELIX

    IPC分类号： C10G1/06 ,  C10G3/00

    CPC分类号： C10G1/06 ,  C10G1/002 ,  C10G1/08 ,  C10G3/42 ,  C10G3/50 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/1022 ,  C10G2300/301 ,  C10G2300/305 ,  C10G2300/307 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  Y02P30/20

    摘要： Hydropyrolysis processes are described, in which differing types of feedstocks, including at least one biorenewable feedstock, namely a biomass-containing feedstock, may be co-processed to allow enhancements in operating conditions and/or product properties, depending on changing customer requirements and/or overall market demands. According to specific embodiments, an aliphatic hydrocarbon precursor or an aromatic hydrocarbon precursor is co-processed with the biomass-containing feedstock to enhance an operating condition (e.g., a reactor temperature profile) of the hydropyrolysis process and/or a property (e.g., cetane number) of a liquid product (e.g., a diesel boiling range fraction) obtained from a substantially fully deoxygenated hydrocarbon liquid.

    摘要翻译： 描述了氢解法，其中不同类型的原料，包括至少一种生物可再生原料，即含生物质的原料，可以被共同处理，以允许在操作条件和/或产品性质方面的增强，这取决于不断变化的客户要求和/ 或整体市场需求。 根据具体实施方案，脂族烃前体或芳族烃前体与含生物质的原料共处理以增强加氢热解过程的操作条件（例如，反应器温度分布）和/或性质（例如，十六烷 数量）从基本上完全脱氧的烃液体获得的液体产物（例如柴油沸程级分）。

    BUBBLING BED CATALYTIC HYDROPYROLYSIS PROCESS UTILIZINIG LARGER CATALYST PARTICLES AND SMALL BIOMASS PARTICLES FEATURING AN ANTI-SLUGGING REACTOR
    2.
    发明申请
    BUBBLING BED CATALYTIC HYDROPYROLYSIS PROCESS UTILIZINIG LARGER CATALYST PARTICLES AND SMALL BIOMASS PARTICLES FEATURING AN ANTI-SLUGGING REACTOR 有权
    沸腾床催化水解法过程利用大型催化剂颗粒和小生物颗粒特征抗反应剂

    公开(公告)号：US20150141716A1

    公开(公告)日：2015-05-21

    申请号：US14492840

    申请日：2014-09-22

    申请人： GAS TECHNOLOGY INSTITUTE

    发明人： Terry L. MARKER ,  Larry G. FELIX ,  Martin B. LINCK ,  Michael J. ROBERTS

    IPC分类号： C10G1/06 ,  C10L1/04 ,  C10G1/00

    CPC分类号： C10G1/06 ,  B01J8/1809 ,  B01J8/34 ,  B01J23/755 ,  B01J23/882 ,  B01J2208/00061 ,  B01J2208/00115 ,  B01J2208/00548 ,  B01J2208/0084 ,  B01J2219/00252 ,  C10G1/002 ,  C10G1/086 ,  C10G1/10 ,  C10G3/45 ,  C10G3/46 ,  C10G3/50 ,  C10G3/57 ,  C10G2300/1003 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10L1/04 ,  C10L2200/0469 ,  C10L2290/02 ,  Y02E50/14 ,  Y02E50/32 ,  Y02P30/20

    摘要： This invention relates to a process for thermochemically transforming biomass or other oxygenated feedstocks into high quality liquid hydrocarbon fuels. In particular, a catalytic hydropyrolysis reactor, containing a deep bed of fluidized catalyst particles is utilized to accept particles of biomass or other oxygenated feedstocks that are significantly smaller than the particles of catalyst in the fluidized bed. The reactor features an insert or other structure disposed within the reactor vessel that inhibits slugging of the bed and thereby minimizes attrition of the catalyst. Within the bed, the biomass feedstock is converted into a vapor-phase product, containing hydrocarbon molecules and other process vapors, and an entrained solid char product, which is separated from the vapor stream after the vapor stream has been exhausted from the top of the reactor. When the product vapor stream is cooled to ambient temperatures, a significant proportion of the hydrocarbons in the product vapor stream can be recovered as a liquid stream of hydrophobic hydrocarbons, with properties consistent with those of gasoline, kerosene, and diesel fuel. Separate streams of gasoline, kerosene, and diesel fuel may also be obtained, either via selective condensation of each type of fuel, or via later distillation of the combined hydrocarbon liquid.

    摘要翻译： 本发明涉及将生物质或其它含氧原料热化学变换成高质量液体烃燃料的方法。 特别地，使用含有流化催化剂颗粒的深层的催化加氢热解反应器来接受显着小于流化床中的催化剂颗粒的生物质或其它含氧原料的颗粒。 反应器具有设置在反应器容器内的插入物或其它结构，其抑制床的压块，从而使催化剂的磨损最小化。 在床内，生物质原料转化为含有烃分子和其他工艺蒸气的气相产物，以及夹带的固体焦炭产物，其在蒸气流已经从蒸汽流的顶部排出之后与蒸气流分离 反应堆。 当产物蒸气流被冷却到环境温度时，产物蒸气流中的相当大比例的烃可作为疏水性烃的液体流回收，其特性与汽油，煤油和柴油燃料的性质一致。 也可以通过每种类型的燃料的选择性冷凝，或通过后来的组合烃液体的蒸馏来获得单独的汽油，煤油和柴油燃料。

    USE OFCARBON DIOXIDE GENERATED BY HYDROPYROLYSIS FOR PROCESS INERTIZATION
    3.
    发明申请
    USE OFCARBON DIOXIDE GENERATED BY HYDROPYROLYSIS FOR PROCESS INERTIZATION 有权
    使用氢过氧化物生成的二氧化碳进行过程自动化

    公开(公告)号：US20160068758A1

    公开(公告)日：2016-03-10

    申请号：US14479246

    申请日：2014-09-05

    申请人： GAS TECHNOLOGY INSTITUTE

    发明人： Martin B. LINCK ,  Terry L. MARKER ,  Michael J. ROBERTS ,  Larry G. FELIX

    IPC分类号： C10G1/00 ,  C01B3/16 ,  C10G65/12 ,  C10G1/06 ,  C10G47/02

    CPC分类号： C10G1/002 ,  C01B2203/0216 ,  C01B2203/0405 ,  C01B2203/043 ,  C10G1/06 ,  C10G3/50 ,  C10G47/02 ,  C10G65/12 ,  C10G2300/1011 ,  Y02P20/145 ,  Y02P30/20

    摘要： A hydropyrolysis process comprises feeding both (i) hydrogen and (ii) a biomass-containing feedstock or a biomass-derived feedstock, to a hydropyrolysis reactor vessel. The process comprises producing a CO2-containing vapor stream and at least one liquid product. A CO2 product, separated from the CO2-containing vapor stream, is advantageously used for at least one inertization function of the hydropyrolysis process. Representative inertization functions include operation of solids transport equipment, blanketing of liquid containers, drying of biomass-containing feedstock or biomass-derived feedstock, conveying or separating solids, and combinations thereof. Importantly, CO2 products utilized for these inertization functions may be obtained predominantly, if not completely (depending on the nature of the feedstock), from renewable carbon in biomass.

    摘要翻译： 加氢热解过程包括将（i）氢和（ii）含生物质的原料或生物质衍生的原料进料到加氢热解反应器容器中。 该方法包括产生含CO 2的蒸汽流和至少一种液体产物。 与含CO 2的蒸汽流分离的CO 2产物有利地用于加氢热解过程的至少一种惰性化功能。 代表性的惰性化功能包括固体输送设备的操作，液体容器的覆盖，含生物质的原料或生物质衍生的原料的干燥，输送或分离固体及其组合。 重要的是，用于这些惰性化功能的二氧化碳产品可以主要地从生物质中的可再生碳获得，如果不是完全（取决于原料的性质）。

    HYDROPYROLYSIS OF BIOMASS-CONTAINING FEEDSTOCKS
    9.
    发明申请
    HYDROPYROLYSIS OF BIOMASS-CONTAINING FEEDSTOCKS 有权
    含生物量的饲料的水解

    公开(公告)号：US20160002540A1

    公开(公告)日：2016-01-07

    申请号：US14321147

    申请日：2014-07-01

    申请人： GAS TECHNOLOGY INSTITUTE

    发明人： Larry G. FELIX ,  Martin B. LINCK ,  Terry L. MARKER ,  Michael J. ROBERTS

    IPC分类号： C10G1/00

    CPC分类号： C10G1/002 ,  C01B3/34 ,  C01B2203/0233 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/062 ,  C01B2203/1235 ,  C01B2203/1264 ,  C01B2203/148 ,  C10G1/06 ,  C10G3/42 ,  C10G3/46 ,  C10G3/50 ,  C10G3/52 ,  C10G2300/1003 ,  C10K1/32 ,  Y02P30/20

    摘要： Various techniques are disclosed for pretreating municipal solid waste (MSW) and other biomass-containing feedstocks that may be of a poorer quality and consequently more difficult, or even impossible, to convert to higher value liquid products (e.g., transportation fuels) using conventional processes. Such conventional processes may otherwise be satisfactory for the conversion of the biomass portion of the feedstock alone. The pretreatment of biomass-containing feedstocks may generally include steps carried out prior to a hydropyrolysis step and optionally further steps, in order to change one or more characteristics of the feedstock, rendering it more easily upgradable.

    摘要翻译： 公开了各种技术用于预处理城市固体废物（MSW）和其他可能具有较差质量的生物质原料，因此更难或甚至不可能使用常规方法转化为更高价值的液体产品（例如运输燃料） 。 否则这种常规方法可能对于单独的原料的生物质部分的转化是令人满意的。 含生物质的原料的预处理通常可以包括在加氢热解步骤之前进行的步骤和任选的进一步的步骤，以改变原料的一种或多种特性，使其更容易升级。