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    Process for the gasification of carbonaceous agglomerates in a fixed bed reactor
    1.
    发明授权
    Process for the gasification of carbonaceous agglomerates in a fixed bed reactor 失效
    在固定床反应器中碳质附聚物气化的方法

    公开(公告)号：US4599092A

    公开(公告)日：1986-07-08

    申请号：US559725

    申请日：1983-12-09

    申请人： Michael Eichelsbacher ,  Rudolph Kohlen ,  Rainer Reimert ,  Carl Hafke ,  Wolfgang Schafer

    发明人： Michael Eichelsbacher ,  Rudolph Kohlen ,  Rainer Reimert ,  Carl Hafke ,  Wolfgang Schafer

    IPC分类号： C10J3/02 ,  C10J3/30

    CPC分类号： C10J3/30 ,  C10J3/32 ,  C10J3/723 ,  C10J3/78 ,  C10J2200/36 ,  C10J2300/093 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0976

    摘要： A process for the gasification of carbonaceous agglomerates in a reactor at a pressure of the range of 5 to 150 bar. The agglomerates are fed into said reactor from a storage zone located above the reactor and form a fixed bed in the reactor, in which they slowly descend when gasified. At least two gasification agents selected from the group consisting of oxygen, air, steam and carbon dioxide are introduced into said reactor through the bottom and rise through said fixed bed. Solid ash or liquid slag is discharged below said fixed bed and a steam-containing product gas is tapped from the reactor above said fixed bed. In order to minimize or prevent the condensation of steam on the agglomerates in the storage zone, the invention provides for a controlled atmosphere almost entirely free of oxygen and steam which is introduced into the storage zone at a pressure approximately equal to the pressure of the product gas.

    摘要翻译： 在5至150巴的压力下在反应器中气化碳质团聚体的方法。 将附聚物从位于反应器上方的储存区域进料到所述反应器中，并在反应器中形成固定床，当气化时它们缓慢下降。 选自氧，空气，蒸汽和二氧化碳的至少两种气化剂通过底部引入所述反应器并且通过所述固定床上升。 固体灰或液态炉渣在所述固定床下方排出，并且含有蒸汽的产物气体从所述固定床上方的反应器中抽出。 为了最小化或防止蒸汽在储存区域中的附聚物上的冷凝，本发明提供几乎完全没有氧气和蒸汽的受控气氛，其在大约等于产品压力的压力下被引入储存区 加油站。

    Method of and apparatus for discharging solids from a pressurized container
    3.
    发明授权
    Method of and apparatus for discharging solids from a pressurized container 失效
    从加压容器排出固体的方法和设备

    公开(公告)号：US4753565A

    公开(公告)日：1988-06-28

    申请号：US882277

    申请日：1986-07-07

    申请人： Rainer Reimert ,  Heinz Wolf

    发明人： Rainer Reimert ,  Heinz Wolf

    IPC分类号： B65G53/40 ,  B65G53/46 ,  C10J3/00

    CPC分类号： B65G53/4683

    摘要： The container communicates through an outlet, which is adapted to be closed with a lock chamber, which is adapted to be emptied and is provided with a pressure-relief valve. When it is desired to empty the lock chamber the volume which is available in the lock chamber for the gas is initially increased so that the pressure in the lock chamber is reduced. Thereafter the lock chamber is opened.

    摘要翻译： 容器通过出口连通，该出口适于用适于排空的锁定室封闭，并设置有减压阀。 当需要清空锁定室时，最初增加用于气体的锁定室中可获得的体积，使得锁定室中的压力减小。 此后，锁室打开。

    Apparatus for extracting valuable substances from a granular feedstock
    5.
    发明授权
    Apparatus for extracting valuable substances from a granular feedstock 失效
    用于从颗粒原料中提取有价值物质的装置

    公开(公告)号：US4741807A

    公开(公告)日：1988-05-03

    申请号：US907542

    申请日：1986-09-15

    申请人： Joachim Wilhelm ,  Rainer Reimert ,  Georg Penk

    发明人： Joachim Wilhelm ,  Rainer Reimert ,  Georg Penk

    IPC分类号： B01D11/02 ,  C11B1/10

    CPC分类号： B01D11/0203

    摘要： In a reactor, granular feedstock having particle sizes in the range from about 0.5 to 15 mm is subjected in a moving bed to a countercurrent extraction at a temperature in the range from 20.degree. to 150.degree. C. and under a pressure in the range from 50 to 400 bars by a continuously supplied solvent which is in a liquid or supercritical state. A mixture of valuable substances and solvent is withdrawn from the upper portion of the reactor. The solvent is separated from the valuable substances by a pressure relief and/or temperature rise and is recycled to the reactor. The extraction residue is withdrawn from the lower end of the reactor. Respective locks are used to charge the feedstock into the reactor and to discharge the extraction residue from the reactor. Solvent and an entrainer are supplied to the reactor at different locations. Outlet ducts having a length of 0.1 to 1 m are preferably used to deliver the feedstock onto a moving bed in the reactor so that a free space is provided over the bed.

    摘要翻译： 在反应器中，将粒度在约0.5至15mm范围内的粒状原料在移动床中进行逆流萃取，温度范围为20-150℃，压力范围为 通过处于液体或超临界状态的连续供应的溶剂，50至400巴。 有价值物质和溶剂的混合物从反应器的上部排出。 通过减压和/或升温将溶剂与有价值物质分离，并再循环到反应器中。 萃取残余物从反应器的下端排出。 使用各种锁将原料装入反应器并从反应器排出萃取渣。 溶剂和夹带剂在不同的位置供应到反应器。 优选使用长度为0.1至1μm的出口管道将原料输送到反应器中的移动床上，使得在床上设置自由空间。

    Process of gasifying solid fuels
    6.
    发明授权
    Process of gasifying solid fuels 失效
    气化固体燃料的工艺

    公开(公告)号：US4426810A

    公开(公告)日：1984-01-24

    申请号：US337345

    申请日：1982-01-06

    申请人： Paul Rudolph ,  Rainer Reimert ,  Osman Turna

    发明人： Paul Rudolph ,  Rainer Reimert ,  Osman Turna

    IPC分类号： C10J3/02 ,  C10J3/08 ,  C10J3/16 ,  C10J3/54 ,  C10J3/78

    CPC分类号： C10J3/482 ,  C10J3/02 ,  C10J3/08 ,  C10J3/16 ,  C10J3/54 ,  C10J3/78 ,  C10K1/10 ,  C10K1/101 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0973 ,  C10J2300/1606 ,  C10J2300/1665 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/129

    摘要： Coarse-grained solid fuels in particle sizes of at least 2 mm are gasified under a pressure of 5 to 150 bars in a fixed bed which is slowly descending and into which the gasifying agents are introduced from below whereas the incombustible mineral constituents are withdrawn as solid ash or liquid slag from the lower end of the bed. Fine-grained solid fuels are gasified in a fluidized bed under a pressure of 1 to 100 bars. Oxygen, steam and/or carbon dioxide are used as gasifying agents for the gasification in the fixed bed and in the fluidized bed. The product gas from the fluidized-bed gasifier has a temperature of 700.degree. to 1200.degree. C. and is indirectly cooled with water. The resulting steam is fed as gasifying agent to the fixed-bed gasifier. The product gas from the fixed-bed gasifier can be indirectly cooled to produce steam and at least part of said steam is fed as gasifying agent to the fluidized-bed gasifier. The steam fed as gasifying agent to the fixed-bed gasifier has a temperature of about 300.degree. to 600.degree. C., preferably of about 400.degree. to 500.degree. C.The steam produced by an indirect heat exchange with the product gas from the fixed-bed gasifier can be superheated by an indirect heat exchange with the product gas from the fluidized-bed gasifier before said steam is fed as gasifying agent to the fluidized-bed gasifier.

    摘要翻译： 颗粒尺寸至少为2mm的粗粒固体燃料在5至150巴的压力下在固定床中气化，固定床缓慢下降，气化剂从下方引入，而不燃性矿物组分作为固体排出 灰烬或液体渣从床的下端。 细粒固体燃料在1至100巴的压力下在流化床中气化。 氧气，蒸汽和/或二氧化碳用作固定床和流化床中气化的气化剂。 来自流化床气化器的产物气体的温度为700℃至1200℃，并用水间接冷却。 将所得蒸汽作为气化剂进料至固定床气化器。 来自固定床气化器的产物气体可以被间接冷却以产生蒸汽，并且至少部分所述蒸汽作为气化剂供给到流化床气化器。 作为气化剂供给到固定床气化器的蒸汽的温度为约300℃至600℃，优选为约400℃至500℃。通过与来自固定床的气体的产物间接热交换产生的蒸汽 在将气体作为气化剂供给到流化床气化器之前，可以通过与来自流化床气化器的产物气体的间接热交换来过热加热。

    Process and apparatus for feeding particulate solids into a pressure reactor
    7.
    发明授权
    Process and apparatus for feeding particulate solids into a pressure reactor 失效
    将颗粒固体进料到压力反应器中的方法和装置

    公开(公告)号：US4033730A

    公开(公告)日：1977-07-05

    申请号：US693043

    申请日：1976-06-04

    申请人： Gerhard Baron ,  Carl Hafke ,  Dietrich Engler ,  Rainer Reimert ,  Eberhard Blaum

    发明人： Gerhard Baron ,  Carl Hafke ,  Dietrich Engler ,  Rainer Reimert ,  Eberhard Blaum

    IPC分类号： B01J3/02 ,  C10J3/30

    CPC分类号： C10J3/30 ,  B01J3/02 ,  C10J3/50 ,  C10J3/78 ,  C10J2200/09 ,  C10J2300/093 ,  C10J2300/0959 ,  C10J2300/0969 ,  C10J2300/0976 ,  Y10S48/04

    摘要： Particulate solids are fed into a pressure reactor operated under a pressure of 5-150 bars by means of a guide cylinder which is secured to the reactor and surrounds the reactor inlet. The guide cylinder is adapted to be closed and a stationary feed conduit is directed towards the guide cylinder. A cylinder container, which is gastightly guided in the guide cylinder and has a bottom which is adapted to be closed, is moved up and down in the guide cylinder and when the bottom of the cylinder is open and the reactor inlet is closed the material flows out of the container into the guide cylinder whereas the bottom of the container is closed and the same is moved toward the open reactor inlet to displace gases into the reactor. The device for carrying out the process includes a guide cylinder secured to the reactor and surrounding the reactor inlet. The guide cylinder is adapted to be closed. A stationary feed conduit is directed towards the guide cylinder and a container is gastightly guided in the guide cylinder and is movable up and down therein and has a bottom that is adapted to be closed.

    摘要翻译： 将颗粒状固体进料到压力反应器中，该压力反应器通过导向圆柱体在5-150巴的压力下操作，所述导向圆筒固定到反应器并且围绕反应器入口。 引导筒适于闭合，并且固定进料导管指向导向筒。 气缸容器在导向气缸中气密地引导并且具有适于封闭的底部，在导向气缸中上下移动，当气缸的底部打开并且反应器入口关闭时，材料流动 从容器中排出到导向筒中，而容器的底部是封闭的，并且将其移动到开放的反应器入口以将气体置入反应器中。 用于执行该方法的装置包括固定到反应器并围绕反应器入口的导向圆筒。 引导筒适合关闭。 固定进料导管指向导向筒，并且容器在引导筒中被气密地引导并且可上下移动并具有适于关闭的底部。

    In-line gas pre-heating
    8.
    发明授权
    In-line gas pre-heating 有权
    在线气体预热

    公开(公告)号：US06730272B2

    公开(公告)日：2004-05-04

    申请号：US09242473

    申请日：1999-11-30

    申请人： Rainer Reimert

    发明人： Rainer Reimert

    IPC分类号： F17D100

    CPC分类号： F23C13/00 ,  F02C1/00 ,  F02C3/36 ,  F23D2900/21003 ,  Y10T137/0396

    摘要： A process for heating fuel gas under high pressure before it is expanded. The gas is directly heated by burning part of the gas in the gas pipeline.

    摘要翻译： 在膨胀之前在高压下加热燃料气体的方法。 气体通过燃烧气体管道中的部分气体直接加热。

    Process of treating the gasification residue formed by the gasification of solid fuels in a fluidized bed
    9.
    发明授权
    Process of treating the gasification residue formed by the gasification of solid fuels in a fluidized bed 失效
    在流化床中处理由固体燃料气化形成的气化残渣的方法

    公开(公告)号：US5635147A

    公开(公告)日：1997-06-03

    申请号：US409254

    申请日：1995-03-23

    申请人： Peter Herbert ,  Rainer Reimert ,  Michael Stroder

    发明人： Peter Herbert ,  Rainer Reimert ,  Michael Stroder

    IPC分类号： C10J3/54 ,  C01B17/16 ,  C10B57/00

    CPC分类号： C10J3/54 ,  C10J3/463 ,  C10J3/523 ,  C10K1/026 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1807

    摘要： In addition to ash and coke, the gasification residue contains alkaline earth metal sulfide and alkaline earth metal oxide because desulfuring agents have been supplied to the gasifier. At temperatures from 5.degree. to 80.degree. C. the gasification residue is mixed with an acid-containing aqueous solution so that a gas which is rich in H.sub.2 S is produced. Ash, coke, and alkaline earth metal salt are supplied to a flotation zone, in which coke is separated. A solid residue which contains ash and alkaline earth metal salt is withdrawn from the flotation zone. Carbonic acid or dilute sulfuric acid is preferably used as an acid.

    摘要翻译： 除了灰分和焦炭之外，气化残渣含有碱土金属硫化物和碱土金属氧化物，因为已经向气化器供应了脱硫剂。 在5〜80℃的温度下，将气化残渣与含酸水溶液混合，制成富含H 2 S的气体。 灰分，焦炭和碱土金属盐被供应到浮选区域，其中焦炭被分离。 从浮选区抽出含有灰分和碱土金属盐的固体残渣。 优选使用碳酸或稀硫酸作为酸。