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    Process for producing hydrocarbon derivative products from feedstock containing hydrocarbons
    32.
    发明授权
    Process for producing hydrocarbon derivative products from feedstock containing hydrocarbons 有权
    由含碳氢化合物的原料生产烃衍生物的方法

    公开(公告)号：US07728182B2

    公开(公告)日：2010-06-01

    申请号：US11184078

    申请日：2005-07-19

    Applicant: Larry Jack Melnichuk ,  Karen (Sue) Venita Kelly

    Inventor： Larry Jack Melnichuk ,  Karen (Sue) Venita Kelly

    IPC: C07C27/04

    CPC classification number: C07C29/156 ,  C01B2203/025 ,  C01B2203/0475 ,  C01B2203/061 ,  C07C29/1518 ,  C07C29/154 ,  C07C29/32 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/16 ,  C10J2300/1618 ,  C10J2300/1665 ,  C10J2300/1807 ,  C10K3/005 ,  C10K3/04 ,  Y02C10/04 ,  Y02E50/18 ,  Y02E50/32 ,  Y02P20/145 ,  C07C31/08 ,  C07C31/04

    Abstract: The process for producing a predetermined CXHYOZ product from a primary feedstock containing hydrocarbons and a secondary feedstock is disclosed, wherein X, Y and Z are integers. The process includes the steps of: providing primary feedstock; indirectly heating it generally in the absence of oxygen; cleaning the gas stream produced therefrom by removing CO2 and solids; determining the amount of CO and H2 therein; comparing the percentage of CO and H2 in the cleaned gas stream with the required CO and H2 to produce the predetermined CXHYOZ product; determining the additional of CO and H2 required; determining the secondary feedstock; calculating the amount of CO, H2 and heat produced from the secondary feedstock; partially oxidizing the secondary feedstock to produce heat and a secondary gas stream; combining the CO and H2 from both feedstocks to produce a mixed gas stream; adding a catalyst; and distilling to produce the predetermined CXHYOZ product.

    Abstract translation: 公开了从含有烃和二次原料的原料原料生产预定的CXHYOZ产物的方法，其中X，Y和Z是整数。 该方法包括以下步骤：提供初级原料; 通常在没有氧气的情况下间接加热; 通过除去CO 2和固体来清洗由其产生的气流; 确定其中的CO和H2的量; 将清洁气流中CO和H2的百分比与所需的CO和H2进行比较，以产生预定的CXHYOZ产物; 确定所需的CO和H2的附加值; 确定次级原料; 计算二次原料产生的CO，H2和热量; 部分氧化二次原料以产生热量和二次气流; 将来自两种原料的CO和H 2混合以产生混合气流; 加入催化剂; 并蒸馏生产预定的CXHYOZ产品。

    Multi-Stage Circulating Fluidized Bed Syngas Cooling
    37.
    发明申请
    Multi-Stage Circulating Fluidized Bed Syngas Cooling 审中-公开
    多级循环流化床合成气冷却

    公开(公告)号：US20170038152A1

    公开(公告)日：2017-02-09

    申请号：US15272667

    申请日：2016-09-22

    Applicant: Southern Company

    Inventor： Guohai Liu ,  Pannalal Vimalchand ,  Xiaofeng Guan ,  WanWang Peng

    IPC: F28D13/00 ,  C10J3/86 ,  F28D21/00

    CPC classification number: F28D13/00 ,  C10J3/86 ,  C10J2300/093 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K3/005 ,  F28D15/00 ,  F28D21/0001 ,  F28D2021/0075 ,  Y02E20/16 ,  Y02E20/18

    Abstract: A method and apparatus for cooling hot gas streams in the temperature range 800° C. to 1600° C. using multi-stage circulating fluid bed (CFB) coolers is disclosed. The invention relates to cooling the hot syngas from coal gasifiers in which the hot syngas entrains substances that foul, erode and corrode heat transfer surfaces upon contact in conventional coolers. The hot syngas is cooled by extracting and indirectly transferring heat to heat transfer surfaces with circulating inert solid particles in CFB syngas coolers. The CFB syngas coolers are staged to facilitate generation of steam at multiple conditions and hot boiler feed water that are necessary for power generation in an IGCC process. The multi-stage syngas cooler can include internally circulating fluid bed coolers, externally circulating fluid bed coolers and hybrid coolers that incorporate features of both internally and externally circulating fluid bed coolers.

    Abstract translation: 公开了一种使用多级循环流化床（CFB）冷却器在800℃至1600℃的温度范围内冷却热气流的方法和装置。 本发明涉及从煤气化炉冷却热合成气，其中热合成气夹带在传统冷却器中接触时污染，腐蚀和腐蚀传热表面的物质。 通过在CFB合成气冷却器中循环惰性固体颗粒提取并间接传递热量至传热表面来冷却热合成气。 CFB合成气冷却器分段，以便在IGCC工艺中发电所需的多种条件下生产蒸汽和热锅炉给水。 多级合成气冷却器可以包括内部循环流化床冷却器，外部循环流化床冷却器和混合冷却器，其结合内部和外部循环流化床冷却器的特征。

    Gasification of high ash, high ash fusion temperature bituminous coals
    39.
    发明授权
    Gasification of high ash, high ash fusion temperature bituminous coals 有权
    高灰分气化，高灰分聚合温度烟煤

    公开(公告)号：US09181502B2

    公开(公告)日：2015-11-10

    申请号：US13936457

    申请日：2013-07-08

    Applicant: The Southern Company

    Inventor： Guohai Liu ,  Pannalal Vimalchand ,  WanWang Peng

    IPC: C10J3/56 ,  C10J3/84 ,  C10J3/72 ,  C10K1/02 ,  C10K3/00

    CPC classification number: C10J3/56 ,  C10J3/721 ,  C10J3/84 ,  C10J2300/093 ,  C10J2300/094 ,  C10J2300/0976 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1884 ,  C10J2300/1892 ,  C10K1/024 ,  C10K1/026 ,  C10K3/005

    Abstract: This invention relates to gasification of high ash bituminous coals that have high ash fusion temperatures. The ash content can be in 15 to 45 weight percent range and ash fusion temperatures can be in 1150° C. to 1500° C. range as well as in excess of 1500° C. In a preferred embodiment, such coals are dealt with a two stage gasification process—a relatively low temperature primary gasification step in a circulating fluidized bed transport gasifier followed by a high temperature partial oxidation step of residual char carbon and small quantities of tar. The system to process such coals further includes an internally circulating fluidized bed to effectively cool the high temperature syngas with the aid of an inert media and without the syngas contacting the heat transfer surfaces. A cyclone downstream of the syngas cooler, operating at relatively low temperatures, effectively reduces loading to a dust filtration unit. Nearly dust- and tar-free syngas for chemicals production or power generation and with over 90%, and preferably over about 98%, overall carbon conversion can be achieved with the preferred process, apparatus and methods outlined in this invention.

    Abstract translation: 本发明涉及具有高灰熔融温度的高灰烟煤气化。 灰分含量可以在15至45重量％范围内，灰分熔化温度可以在1150℃至1500℃的范围以及超过1500℃。在一个优选的实施方案中，这种煤被处理为 二阶段气化过程 - 循环流化床输送气化器中的相对较低温度的一次气化步骤，接着是残留焦碳和少量焦油的高温部分氧化步骤。 处理这种煤的系统还包括内部循环流化床，借助惰性介质有效地冷却高温合成气，而不使合成气与传热表面接触。 合成气冷却器下游的旋风分离器在相对低的温度下运行，有效地减少了灰尘过滤装置的负荷。 使用本发明概述的优选方法，装置和方法可以实现化学品生产或发电的几乎无灰尘和焦油合成气，并且具有超过90％，优选超过约98％的总碳转化率。

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