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    Ash And Solids Cooling In High Temperature And High Pressure Environment
    3.
    发明申请
    Ash And Solids Cooling In High Temperature And High Pressure Environment 有权
    灰和固体在高温高压环境中的冷却

    公开(公告)号：US20120031584A1

    公开(公告)日：2012-02-09

    申请号：US13198745

    申请日：2011-08-05

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    IPC: F28F9/00 ,  F28F19/00

    CPC classification number: F28D21/001 ,  C10J3/523 ,  C10J3/76 ,  C10J2300/093 ,  C10J2300/1625 ,  C10J2300/1861 ,  C10J2300/1892 ,  C10K1/022 ,  C10K1/024 ,  F23C10/24 ,  F23C2900/10006 ,  F23J1/02 ,  F23J2900/01002 ,  F28D7/12 ,  F28D13/00 ,  F28D2021/0045

    Abstract: Disclosed are cooling and depressurization system equipment, arrangement and methods to cool solid particles from a coal gasifier operating at high temperature and pressure. Ash from the coal needs to be continuously withdrawn from a circulating fluidized bed gasifier to maintain the solids inventory in the gasifier. The system disclosed enables use of conventional materials of construction for heat transfer surfaces. The supports for the cooling surfaces are located on the lower temperature upper section of the primary cooler. The cooled solids along with the fluidizing gas exits the primary cooler to a secondary receiving vessel where the solids can be further cooled by conventional means. The fluidizing and entrained gas entering the secondary vessel is filtered and vented through a vent pressure control valve. The column of cooled solids in the secondary vessel is depressurized by a continuous depressurization system to low pressures which are sufficient for conveying the solids to silos for disposal. The system and methods proposed are equally applicable to many high temperature, high pressure processes that require cooling and depressurization of process solids.

    Abstract translation: 公开了冷却和减压系统设备，从高温和高压下运行的煤气化炉中固体颗粒冷却的方法。 需要从循环流化床气化器中连续取出煤中的灰分，以保持气化炉中的固体物质。 所公开的系统使得能够使用用于传热表面的常规建筑材料。 用于冷却表面的支撑件位于主冷却器的较低温度上部。 冷却的固体与流化气体一起离开初级冷却器到二次接收容器，其中固体可以通过常规方式进一步冷却。 进入二次容器的流化和夹带的气体被过滤并通过排气压力控制阀排出。 二次容器中冷却的固体柱通过连续减压系统减压至足以将固体输送到筒仓进行处理的低压。 所提出的系统和方法同样适用于需要对工艺固体进行冷却和减压的许多高温高压方法。

    Dispersed Bubble Reactor For Enhanced Gas-Liquid-Solids Contact And Mass Transfer
    4.
    发明申请
    Dispersed Bubble Reactor For Enhanced Gas-Liquid-Solids Contact And Mass Transfer 有权
    分散气泡反应器用于增强气液固体接触和质量传递

    公开(公告)号：US20120216680A1

    公开(公告)日：2012-08-30

    申请号：US13402908

    申请日：2012-02-23

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng ,  Alexander Bonsu

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng ,  Alexander Bonsu

    IPC: B01D53/14 ,  B01F3/04

    CPC classification number: B01J8/228 ,  B01D53/1475 ,  B01D53/18 ,  B01D53/62 ,  B01D2251/206 ,  B01J8/1827 ,  B01J8/1836 ,  B01J8/1872 ,  B01J19/1881 ,  B01J2208/00141 ,  B01J2208/00548 ,  B01J2219/00083 ,  B01J2219/00164 ,  B01J2219/00182 ,  B01J2219/00247 ,  Y02A50/2342 ,  Y02C10/04 ,  Y02C10/06 ,  Y02P20/152

    Abstract: An apparatus to promote gas-liquid contact and facilitate enhanced mass transfer. The dispersed bubble reactor (DBR) operates in the dispersed bubble flow regime to selectively absorb gas phase constituents into the liquid phase. The dispersion is achieved by shearing the large inlet gas bubbles into fine bubbles with circulating liquid and additional pumped liquid solvent when necessary. The DBR is capable of handling precipitates that may form during absorption or fine catalysts that may be necessary to promote liquid phase reactions. The DBR can be configured with multistage counter current flow sections by inserting concentric cylindrical sections into the riser to facilitate annular flow. While the DBR can absorb CO2 in liquid solvents that may lead to precipitates at high loadings, it is equally capable of handling many different types of chemical processes involving solids (precipitates/catalysts) along with gas and liquid phases.

    Abstract translation: 促进气液接触并促进增强传质的装置。 分散的气泡反应器（DBR）以分散的气泡流动方式操作，以选择性地吸收气相成分进入液相。 通过在需要时将大的入口气泡剪切成具有循环液体的细小气泡和附加的泵送液体溶剂来实现分散。 DBR能够处理可能在吸收过程中形成的沉淀物或可能促进液相反应所需的细小催化剂。 DBR可以通过将同心圆柱形部分插入提升管中以便于环形流动而配置多级逆流部分。 虽然DBR可以在可能导致高负载下沉淀的液体溶剂中吸收二氧化碳，但同样能够处理涉及固体（沉淀物/催化剂）以及气相和液相的许多不同类型的化学过程。

    Method and apparatus for the separation of a gas-solids mixture in a circulating fluidized bed reactor
    5.
    发明授权
    Method and apparatus for the separation of a gas-solids mixture in a circulating fluidized bed reactor 有权
    用于在循环流化床反应器中分离气体 - 固体混合物的方法和装置

    公开(公告)号：US07771585B2

    公开(公告)日：2010-08-10

    申请号：US11684405

    申请日：2007-03-09

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    IPC: B01D45/12 ,  B01D50/00 ,  C10G11/00

    CPC classification number: B01D45/12 ,  B01J8/0055 ,  B01J8/0065

    Abstract: The system of the present invention includes a centripetal cyclone for separating particulate material from a particulate laden gas solids stream. The cyclone includes a housing defining a conduit extending between an upstream inlet and a downstream outlet. In operation, when a particulate laden gas-solids stream passes through the upstream housing inlet, the particulate laden gas-solids stream is directed through the conduit and at least a portion of the solids in the particulate laden gas-solids stream are subjected to a centripetal force within the conduit.

    Abstract translation: 本发明的系统包括用于从载有颗粒的气体固体物流中分离颗粒材料的向心旋流器。 旋风分离器包括限定在上游入口和下游出口之间延伸的管道的壳体。 在操作中，当载有颗粒的气体 - 固体物流通过上游壳体入口时，载有颗粒的气体 - 固体物流被引导通过管道，并且将含有颗粒的气体 - 固体物流中的至少一部分固体经受 导管内的向心力。

    Oxycombustion in transport oxy-combustor
    6.
    发明授权
    Oxycombustion in transport oxy-combustor 有权
    运输氧燃烧器中的氧燃烧

    公开(公告)号：US08689709B2

    公开(公告)日：2014-04-08

    申请号：US13405312

    申请日：2012-02-26

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    IPC: F23G5/00 ,  F23J11/00 ,  F23C10/00

    CPC classification number: F23C10/10 ,  B01J8/0055 ,  B01J8/388 ,  B01J2208/00141 ,  F22B1/22 ,  F22B35/002 ,  F23C2206/103 ,  F23C2900/10006 ,  Y02E20/344

    Abstract: A pressurized transport oxy-combustor with different configurations is disclosed. Substantially pure oxygen is fed to the transport oxy-combustor under pressure to combust fossil fuels, generating steam for power generation. The end product is the flue gas containing substantially pure CO2 after moisture condensation. The low excess oxygen necessary to achieve complete combustion in the combustor is scavenged by adding another fuel so that substantially all oxygen fed to the combustor is completely consumed. The capability to operate the transport oxy-combustor as a circulating fluidized bed combustor at very high solids circulation rates makes it unnecessary to use recycled CO2 or flue gas as a means to moderate and control the combustion temperature. The temperature in the combustor is effectively controlled by relatively cooler circulating solids that enter the combustion zone. A small amount of CO2 is recycled for aeration and to convey solids fuel to the combustor.

    Abstract translation: 公开了具有不同结构的加压输送氧 - 燃烧器。 在压力下将基本上纯的氧气输送到运输氧气燃烧器以燃烧化石燃料，产生用于发电的蒸汽。 最终产品是在水分冷凝后含有基本上纯的二氧化碳的烟气。 通过添加另外的燃料来清除在燃烧器中实现完全燃烧所需的低的过量氧气，以使供给燃烧器的大部分氧气被完全消耗。 作为循环流化床燃烧器以非常高的固体循环速率操作运输氧燃烧器的能力使得不需要使用再循环的CO 2或烟道气作为调节和控制燃烧温度的手段。 通过进入燃烧区的相对较冷的循环固体有效地控制燃烧器中的温度。 再循环少量的二氧化碳进行曝气并将固体燃料输送到燃烧器。

    Oxycombustion In Transport Oxy-Combustor
    7.
    发明申请
    Oxycombustion In Transport Oxy-Combustor 有权
    运输氧气燃烧器中的氧气

    公开(公告)号：US20130055936A1

    公开(公告)日：2013-03-07

    申请号：US13405312

    申请日：2012-02-26

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  WanWang Peng

    IPC: F23C10/08 ,  F23B80/00 ,  F23B10/00 ,  F23C10/18 ,  F23L7/00 ,  F23J15/02

    CPC classification number: F23C10/10 ,  B01J8/0055 ,  B01J8/388 ,  B01J2208/00141 ,  F22B1/22 ,  F22B35/002 ,  F23C2206/103 ,  F23C2900/10006 ,  Y02E20/344

    Abstract: A pressurized transport oxy-combustor with different configurations is disclosed. Substantially pure oxygen is fed to the transport oxy-combustor under pressure to combust fossil fuels, generating steam for power generation. The end product is the flue gas containing substantially pure CO2 after moisture condensation. The low excess oxygen necessary to achieve complete combustion in the combustor is scavenged by adding another fuel so that substantially all oxygen fed to the combustor is completely consumed. The capability to operate the transport oxy-combustor as a circulating fluidized bed combustor at very high solids circulation rates makes it unnecessary to use recycled CO2 or flue gas as a means to moderate and control the combustion temperature. The temperature in the combustor is effectively controlled by relatively cooler circulating solids that enter the combustion zone. A small amount of CO2 is recycled for aeration and to convey solids fuel to the combustor.

    Abstract translation: 公开了具有不同结构的加压输送氧 - 燃烧器。 在压力下将基本上纯的氧气输送到运输氧气燃烧器以燃烧化石燃料，产生用于发电的蒸汽。 最终产品是在水分冷凝后含有基本上纯的二氧化碳的烟气。 通过添加另外的燃料来清除在燃烧器中实现完全燃烧所需的低的过量氧气，以使供给燃烧器的大部分氧气被完全消耗。 以非常高的固体循环速率操作作为循环流化床燃烧器的运输氧燃烧器的能力使得不需要使用再循环的CO 2或烟道气作为调节和控制燃烧温度的手段。 通过进入燃烧区的相对较冷的循环固体有效地控制燃烧器中的温度。 再循环少量的二氧化碳进行曝气并将固体燃料输送到燃烧器。

    One-Way Check Valve for Solid Particulate Flow Pipeline
    9.
    发明申请
    One-Way Check Valve for Solid Particulate Flow Pipeline 审中-公开
    固体颗粒流量管道单向止回阀

    公开(公告)号：US20160290517A1

    公开(公告)日：2016-10-06

    申请号：US14737419

    申请日：2015-06-11

    Applicant: Wanwang Peng

    Inventor： Wanwang Peng

    IPC: F16K15/03

    CPC classification number: F16K15/03 ,  F16K15/021 ,  F16K17/12

    Abstract: A one-way check valve for solid particulate flow pipeline is disclosed suitable for use in a pressure fluid line containing fine particles of solids. The one way valve increases the reliability and safety of the process operations and simplifies the pipeline detection and control requirements.

    Abstract translation: 公开了一种用于固体颗粒流动管道的单向止回阀，适合用于含有细颗粒固体的压力流体管线。 单向阀增加了过程操作的可靠性和安全性，并简化了管道检测和控制要求。

    Ash and solids cooling in high temperature and high pressure environment
    10.
    发明授权
    Ash and solids cooling in high temperature and high pressure environment 有权
    灰和固体在高温高压环境下冷却

    公开(公告)号：US09335100B2

    公开(公告)日：2016-05-10

    申请号：US13198745

    申请日：2011-08-05

    Applicant: Pannalal Vimalchand ,  Guohai Liu ,  Wanwang Peng

    Inventor： Pannalal Vimalchand ,  Guohai Liu ,  Wanwang Peng

    IPC: F22B1/18 ,  F28D21/00 ,  F23C10/24 ,  F23J1/02 ,  C10J3/52 ,  C10J3/76 ,  C10K1/02 ,  F28D7/12 ,  F28D13/00

    CPC classification number: F28D21/001 ,  C10J3/523 ,  C10J3/76 ,  C10J2300/093 ,  C10J2300/1625 ,  C10J2300/1861 ,  C10J2300/1892 ,  C10K1/022 ,  C10K1/024 ,  F23C10/24 ,  F23C2900/10006 ,  F23J1/02 ,  F23J2900/01002 ,  F28D7/12 ,  F28D13/00 ,  F28D2021/0045

    Abstract: Disclosed are cooling and depressurization system equipment, arrangement and methods to cool solid particles from a coal gasifier operating at high temperature and pressure. Ash needs to be continuously withdrawn from a circulating fluidized bed gasifier to maintain the solids inventory in the gasifier. The supports for the cooling surfaces are located on the lower temperature upper section of the primary cooler. The cooled solids along with the fluidizing gas exits the primary cooler to a secondary receiving vessel where the solids can be further cooled by conventional means. The fluidizing and entrained gas entering the secondary vessel is filtered and vented through a vent pressure control valve. The column of cooled solids in the secondary vessel is depressurized by a continuous depressurization system to low pressures which are sufficient for conveying the solids to silos for disposal.

    Abstract translation: 公开了冷却和减压系统设备，从高温和高压下运行的煤气化炉中固体颗粒冷却的方法。 灰分需要从循环流化床气化器中连续取出，以保持气化炉中的固体物质。 用于冷却表面的支撑件位于主冷却器的较低温度上部。 冷却的固体与流化气体一起离开初级冷却器到二次接收容器，其中固体可以通过常规方式进一步冷却。 进入二次容器的流化和夹带的气体被过滤并通过排气压力控制阀排出。 二次容器中冷却的固体柱通过连续减压系统减压至足以将固体输送到筒仓进行处理的低压。

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