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    Mobile apparatus for carbon-containing materials including biohazard wastes gasification by thermal decomposition and conversion into a liquid fuels.
    2.
    发明申请
    Mobile apparatus for carbon-containing materials including biohazard wastes gasification by thermal decomposition and conversion into a liquid fuels. 审中-公开

    公开(公告)号：US20170355909A1

    公开(公告)日：2017-12-14

    申请号：US15180061

    申请日：2016-06-12

    Applicant: Alexander Dementev

    Inventor： Alexander Dementev

    IPC: C10G2/00 ,  B09B3/00 ,  C25B1/02 ,  C10J3/20 ,  A61L2/07 ,  C10J3/06

    CPC classification number: C10G2/30 ,  A61L2/07 ,  B09B3/0075 ,  B09B3/0091 ,  C10G2300/4068 ,  C10J3/20 ,  C10J2200/31 ,  C10J2300/0906 ,  C10J2300/0946 ,  C10J2300/1659 ,  C10K1/12 ,  C10K1/165 ,  C10K1/20 ,  C10K3/04 ,  C25B1/02 ,  Y02E50/32 ,  Y02P20/124

    Abstract: The present invention relates to a method for gasification of carbon-containing materials including biohazard wastes, and more specifically, to a method for gasification of carbon-containing materials which allows an increase in carbon efficiency and a reduction in carbon dioxide emission, comprising the steps of: biohazard wastes grinding and sterilization, mix with carbon-containing materials for the gasification; and catalytic production of diesel fuel. A system having a movable platform including: material preparation block, gasification and catalytic of diesel fuel production reactors which are structurally and functionally integrated. In the practice of the process, a mixture of carbon-containing materials, a compressed air feed and process steam is fed to the gasifier to produce a synthesis gas. The synthesis gas is fed to the Fischer-Tropsch reactor where it is catalytically reacted to produce heavy hydrocarbons. The outlet from the Fischer-Tropsch reactor is separated into water, a low heating value tail gas, and the desired hydrocarbon liquid product. The water is pressurized and heated to generate process steam. The system further includes a plurality of heat exchangers that enable heat to be recovered from the outlet of the gasifier. The recovered heat is used to make the process steam as well as to preheat the hydrocarbon mix before it is fed to the gasifier and preheat the synthesis gas before it is fed to the Fischer-Tropsch reactor. The method of the present invention greatly increases carbon efficiency and reduces the generation of carbon dioxide.

    Method for steam reforming carbonaceous material
    6.
    发明授权
    Method for steam reforming carbonaceous material 有权
    蒸汽重整含碳材料的方法

    公开(公告)号：US09139787B2

    公开(公告)日：2015-09-22

    申请号：US12881057

    申请日：2010-09-13

    Applicant: Jayson Zwierschke ,  Earnest George Dueck

    Inventor： Jayson Zwierschke ,  Earnest George Dueck

    IPC: C01B3/02 ,  C10J3/72 ,  C10J3/00 ,  C10J3/06 ,  C10J3/20 ,  C10K3/00

    CPC classification number: C10J3/721 ,  C10J3/005 ,  C10J3/06 ,  C10J3/20 ,  C10J2200/158 ,  C10J2300/0916 ,  C10J2300/092 ,  C10J2300/0946 ,  C10J2300/0973 ,  C10J2300/1884 ,  C10K3/006 ,  Y02P20/145

    Abstract: A method for steam reforming carbonaceous material into a synthesis gas by using a single stage process of heating the carbonaceous material in a rotary kiln at an elevated reforming temperature so that the carbonaceous material undergoes substantially complete conversion to synthesis gas or by using a dual stream, multiple-stage process of heating carbonaceous material to a reforming temperature, below that at which metallic materials will typically vaporize, to form gaseous and solid materials; further reforming the gaseous materials in a second stage reforming kiln at an elevated reforming temperature to form synthesis gas; and separating carbon char from the solid material for further processing.

    Abstract translation: 一种通过使用在回转窑中以升高的重整温度加热含碳材料的单阶段方法将含碳材料蒸发转化成合成气的方法，使得碳质材料基本上完全转化为合成气或通过使用双流， 将碳质材料加热到金属材料通常蒸发的重整温度的多阶段过程，以形成气态和固体材料; 在升高的重整温度下进一步重整第二级重整炉中的气态物质，形成合成气; 并将碳炭与固体物质分离以进一步处理。

    Apparatus and Method for Gasifying Solid Fuel
    7.
    发明申请
    Apparatus and Method for Gasifying Solid Fuel 审中-公开
    用于气化固体燃料的装置和方法

    公开(公告)号：US20090249691A1

    公开(公告)日：2009-10-08

    申请号：US11883442

    申请日：2006-02-01

    Applicant: Toru Akiyama ,  Fumihiko Kiso ,  Shinji Tanaka ,  Hirofumi Okazaki ,  Fumihiko Hanayama ,  Kazunori Sato ,  Takahiro Nishida ,  Hiroshi Takezaki ,  Akio Ueda ,  Makoto Takeda

    Inventor： Toru Akiyama ,  Fumihiko Kiso ,  Shinji Tanaka ,  Hirofumi Okazaki ,  Fumihiko Hanayama ,  Kazunori Sato ,  Takahiro Nishida ,  Hiroshi Takezaki ,  Akio Ueda ,  Makoto Takeda

    IPC: C10J3/06 ,  C10J3/20

    CPC classification number: F23G5/02 ,  C10J3/487 ,  C10J3/506 ,  C10J2200/15 ,  C10J2300/09 ,  C10J2300/0903 ,  C10J2300/0909 ,  C10J2300/093 ,  C10J2300/1807 ,  F23G2201/301 ,  F23G2201/40 ,  F23G2201/80

    Abstract: Apparatus for gasifying a solid fuel that supplies a solid fuel such as coal by dry condition to a gasification furnace of an entrained-bed type is constructed so as to be able to collect the char discharged from the gasification furnace and re-supply the char to the furnace without using a lock hopper and without changing the char into slurry form.The char discharged from the gasification furnace along with produced gases 53 produced in the gasification furnace is brought into contact with water by a gas cooler 9 and collected. After being dehydrated by a dehydrator 10, the collected char is loaded into a mill 2 or a raw-coal bunker 1. For loading into the raw-coal bunker 1, the char is dried by a drying machine 14, preferably, after the dehydration.According to the present invention, a mixture of the collected char and water can be re-supplied to the gasification furnace without using a lock hopper or a dry feeder. After being dehydrated, the char preferably is further dried and then supplied to the gasification furnace. Since a great deal of moisture is not supplied to the inside of the gasification furnace, it is possible to prevent a temperature of the gasification furnace from decreasing, and thus improve gas conversion efficiency.

    Abstract translation: 将通过干燥状态将固体燃料例如煤供给到固定床型的气化炉的固体燃料的装置被构造成能够收集从气化炉排出的炭并将炭再供给 炉子不使用封闭料斗，而不改变焦炭成浆状。 从气化炉排出的焦炭以及在气化炉中产生的生成气体53通过气体冷却器9与水接触并收集。 在脱水机10脱水后，收集的炭被装载到磨机2或原煤仓1中。为了装载到原煤仓1中，优选用干燥机14干燥焦炭，脱水后 。 根据本发明，可以将收集的炭和水的混合物重新供给气化炉，而不使用锁定料斗或干式进料器。 脱水后，优选进一步干燥，然后供给到气化炉。 由于不向气化炉内部供给大量的水分，因此能够防止气化炉的温度下降，从而提高气体转换效率。

    High efficiency gasifier with recycle system
    8.
    发明授权
    High efficiency gasifier with recycle system 失效
    具有回收系统的高效气化炉

    公开(公告)号：US4881947A

    公开(公告)日：1989-11-21

    申请号：US212519

    申请日：1988-06-28

    Applicant: Thomas H. Parker ,  Virgil J. Flanigan

    Inventor： Thomas H. Parker ,  Virgil J. Flanigan

    IPC: C10B1/10 ,  C10J3/06 ,  C10J3/10

    CPC classification number: C10B1/10 ,  C10J3/005 ,  C10J3/06 ,  C10J3/10 ,  C10K1/024 ,  C10K3/04 ,  C10J2200/158 ,  C10J2300/1246 ,  C10J2300/1621 ,  C10J2300/1807 ,  C10J2300/1823

    Abstract: A high efficiency gasifier employs a rotary kiln having an indirect fired gasifier and a recycle system. The rotary kiln provides an essentially oxygen-free gasifying chamber into which raw feed material is introduced. Radiant tubes within the chamber transfer heat to the incoming raw feed material to pyrolyze it and convert it to char and product gas as the material advances toward the outlet end. The recycle system within the chamber returns both product gas and hot char to a receiving end of the kiln to aid in heat transfer to the raw feed material. The feed is thus heated more rapidly, and less heat input is required. Efficiency is further aided by providing additional residence time and gasification of the char.

    Abstract translation: 高效气化器采用具有间接燃烧气化器和循环系统的回转窑。 回转窑提供基本上无氧的气化室，其中引入原料。 室内的辐射管将热量转移到输入的原料进料中以将其热解并随着材料向出口端前进而将其转化成炭和产物气体。 室内的再循环系统将产品气和热炭都送回到窑的接收端，以帮助热量传递到原料。 因此，进料被更快地加热，并且需要较少的热量输入。 通过提供额外的焦炭停留时间和气化来进一步提高效率。

    Process for the cocurrent gasification of coal
    9.
    发明授权
    Process for the cocurrent gasification of coal 失效
    煤的并流气化过程

    公开(公告)号：US4813179A

    公开(公告)日：1989-03-21

    申请号：US33094

    申请日：1987-03-31

    Applicant: Jacques Ribesse

    Inventor： Jacques Ribesse

    IPC: C10J3/02 ,  C10J3/26 ,  F02B1/04 ,  C10J3/06

    CPC classification number: C10J3/26 ,  C10J2300/093 ,  F02B1/04

    Abstract: The invention relates to the cocurrent gasification of coal and to a gas generator. The gas generator (11) comprises a vertical sealed vessel, the lower third of which is divided into several identical vertical compartments (12). Coal is loaded at the top (17). The major part of the hot reactive gas under pressure is introduced at the top (18), and the remaining part at lower levels (21, 22). Gas evacuation (24) is stopped from one compartment (12) in turn, gas produced is blown in order to unclog the filters (25, 26) and to loosen the ash, the ash is extracted at the bottom (23) and cold reactive gas is blown countercurrently in order to complete the combustion and to cool the ash. This gas generator enables coal from any source to be used and does not require purification downstream.

    Abstract translation: 本发明涉及煤和气体发生器的并流气化。 气体发生器（11）包括垂直密封容器，其下三分之一被分成几个相同的垂直隔室（12）。 煤被装在顶部（17）。 在顶部（18）引入压力下的热反应气体的主要部分，其余部分在较低水平（21,22）。 依次将气体排出（24）从一个隔间（12）停止，吹出产生的气体，以阻止过滤器（25,26）的松开，并使灰分松动，灰分在底部（23）被抽出，冷反应 为了完成燃烧并冷却灰分，气体逆流吹扫。 该气体发生器使得能够使用来自任何来源的煤，并且不需要向下游净化。

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