公开(公告)号：US5364996A

公开(公告)日：1994-11-15

申请号：US53727

申请日：1993-04-27

Applicant: Craig J. Castagnoli ,  Suk-Bae Cha ,  Hong P. Wang

Inventor： Craig J. Castagnoli ,  Suk-Bae Cha ,  Hong P. Wang

IPC: C10J3/46 ,  C07C1/00

CPC classification number: C10J3/46 ,  C10J3/485 ,  C10J3/84 ,  C10J3/86 ,  C10K1/101 ,  C10J2300/0906 ,  C10J2300/1687 ,  C10J2300/1846 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/144

Abstract: Scrap rubber automobile tires, oil soluble plastics, as well as waste motor oil are disposed of by the process of the subject invention without polluting the nation's environment. Further, useful product synthesis gas, reducing gas, or fuel gas is produced. The rubber from the rubber tires and/or oil soluble plastics are dissolved in the waste motor oil to produce a homogeneous pumpable tire-oil which is separated from undissolved tire belt material containing undissolved rubber and/or oily material, solid residue, and off-gas comprising light hydrocarbons having a maximum atmospheric boiling point of 850.degree. F., and H.sub.2 S. The undissolved tire belt material is coked to produce off-gas, inorganic materials and carbon black. Off-gas form the liquefaction and coking reactors is cooled to produce organic condensate. The tire oil, carbon black, and condensate are mixed together and introduce into a partial oxidation gas generator for the production of synthesis gas, reducing gas, or fuel gas.

Abstract translation: 废橡胶汽车轮胎，油溶性塑料以及废机油通过本发明的方法处理而不污染国家的环境。 此外，产生有用的产物合成气体，还原气体或燃料气体。 来自橡胶轮胎和/或油溶性塑料的橡胶溶解在废机电机油中，以产生均匀的可泵送轮胎油，其从包含未溶解的橡胶和/或油性材料的未溶解的轮胎带材料，固体残余物和离心轮胎油分离出来， 气体包括最大常压沸点为850°F的轻质烃，和H2S。 未溶解的轮胎带材料被焦化以产生废气，无机材料和炭黑。 废气形成液化，焦化反应器被冷却以产生有机冷凝物。 将轮胎油，炭黑和冷凝物混合在一起，并引入到用于生产合成气，还原气体或燃料气体的部分氧化气体发生器中。

公开(公告)号：US5858033A

公开(公告)日：1999-01-12

申请号：US915322

申请日：1997-08-20

Applicant: Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

Inventor： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC: C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  C01B3/32 ,  F23J11/00 ,  F27B15/14

CPC classification number: C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

Abstract: A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in the peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen required for combustion. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

Abstract translation: 燃烧方法和装置，其中可燃物质例如废物，煤等被气化以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中央部形成有流化介质沉降扩散的移动床，在炉的周边部形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给到流化床炉的氧量设定为不高于燃烧所需的理论氧量的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉中产生的可燃性气体和细颗粒被供给到熔融燃烧炉中，在高温下燃烧，并使所得灰分熔化。

公开(公告)号：US5620488A

公开(公告)日：1997-04-15

申请号：US401370

申请日：1995-03-09

Applicant: Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

Inventor： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC: C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  B09B3/00 ,  F22B1/00 ,  F27B15/16

CPC classification number: C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

Abstract: A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in a central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in a peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen necessary to combust the combustible matter. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

Abstract translation: 燃烧方法和装置，其中可燃物质例如废物，煤等被气化以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中心部分形成流化介质沉降扩散的移动床，在炉的周边部分形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给流化床炉的氧气的量设定为不高于燃烧可燃物质所需的理论氧气的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉中产生的可燃性气体和细颗粒被供给到熔融燃烧炉中，在高温下燃烧，并使所得灰分熔化。

公开(公告)号：US06350288B1

公开(公告)日：2002-02-26

申请号：US09193127

申请日：1998-11-17

Applicant: Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

Inventor： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC: C10J300

CPC classification number: C10J3/723 ,  C10G2300/1003 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  F23J15/006 ,  F23L7/007 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

Abstract: A combustion method and apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt the ash by its own heat. A fluidized-bed furnace (2) has an approximately circular horizontal cross-sectional configuration. A moving bed (9), in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed (10), in which the fluidized medium is actively fluidized, is formed in the peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed (9) from the upper part of the fluidized bed (10), thus circulating through the two beds. Combustible matter (11) is cast into the upper part of the moving bed (9) and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace (2) is set so as to be the same contained in an amount of air not higher than 30% of the theoretical amount of combustion air. The temperature of the fluidized bed (10) is maintained at 450° C. to 650° C. so that the combustible gas produced contains a large amount of combustible component. The combustible gas and fine particles produced in the fluidized-bed furnace (2) are supplied to a melt combustion furnace where they are burned at high temperature, and the resulting ash is melted.

Abstract translation: 燃烧方法和装置，其中将可燃物质，例如废物，煤等气化，以产生含有足够大量可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉（2）具有近似圆形的横截面构造。 在炉的中心部分形成有流化介质沉降扩散的移动床（9），流化床主动流化的流化床（10）形成在周边部分 炉子。 流化介质从流化床（10）的上部翻转到移动床（9）的上部，从而循环通过两个床。 将可燃物（11）流入移动床（9）的上部并与流化介质一起循环而气化形成可燃气体。 供给到流化床炉（2）的氧气的量被设定为含有不高于理论量的燃烧空气的30％的空气量。 流化床（10）的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。 在流化床炉（2）中生产的可燃气体和细颗粒被供给到熔化炉中，在其中它们在高温下燃烧，并且所得到的灰分熔化。

公开(公告)号：US5725614A

公开(公告)日：1998-03-10

申请号：US547126

申请日：1995-10-24

Applicant: Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

Inventor： Yoshio Hirayama ,  Takahiro Oshita ,  Chikashi Tame ,  Shuichi Nagato ,  Tetsuhisa Hirose ,  Norihisa Miyoshi ,  Seiichiro Toyoda ,  Shugo Hosoda ,  Shosaku Fujinami ,  Kazuo Takano

IPC: C10J3/46 ,  C10J3/48 ,  C10J3/50 ,  C10J3/52 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23C10/00 ,  F23C10/02 ,  F23C10/12 ,  F23G5/00 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23G5/46 ,  F23J1/00 ,  F23J15/00 ,  F23L7/00 ,  C10J3/68 ,  C10J3/00 ,  F27B15/08

CPC classification number: C10J3/723 ,  C10J3/503 ,  C10J3/523 ,  C10J3/54 ,  C10J3/56 ,  C10J3/64 ,  C10J3/66 ,  C10J3/86 ,  F23G5/006 ,  F23G5/027 ,  F23G5/16 ,  F23G5/30 ,  F23G5/32 ,  F23J15/006 ,  F23L7/007 ,  C10G2300/1003 ,  C10J2200/09 ,  C10J2200/158 ,  C10J2300/0946 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0983 ,  C10J2300/1628 ,  C10J2300/1634 ,  C10J2300/1637 ,  C10J2300/165 ,  C10J2300/1675 ,  C10J2300/1687 ,  C10J2300/1838 ,  C10J2300/1846 ,  C10J2300/1853 ,  F23G2201/40 ,  F23G2202/101 ,  F23G2202/102 ,  F23G2202/103 ,  F23G2202/104 ,  F23G2202/20 ,  F23G2202/30 ,  F23G2203/30 ,  F23G2203/501 ,  F23G2206/00 ,  F23G2206/203 ,  F23G2209/12 ,  F23G2209/20 ,  F23G2209/26 ,  F23G2209/28 ,  F23G2209/281 ,  Y02E20/12 ,  Y02E20/16 ,  Y02E20/18 ,  Y02E20/344 ,  Y02P20/129 ,  Y02P20/144

Abstract: A combustion apparatus in which combustible matter, e.g., waste matter, coal, etc., is gasified to produce a combustible gas containing a sufficiently large amount of combustible component to melt ash by its own heat. A fluidized-bed furnace has an approximately circular horizontal cross-sectional configuration. A moving bed, in which a fluidized medium settles and diffuses, is formed in the central portion of the furnace, and a fluidized bed, in which the fluidized medium is actively fluidized, is formed in a peripheral portion in the furnace. The fluidized medium is turned over to the upper part of the moving bed from the upper part of the fluidized bed, thus circulating through the two beds. Combustible matter is cast into the upper part of the moving bed and gasified to form a combustible gas while circulating, together with the fluidized medium. The amount of oxygen supplied to the fluidized-bed furnace is set so as to be not higher than 30% of the theoretical amount of oxygen necessary to combust the combustible matter. The temperature of the fluidized bed is maintained at 450.degree. C. to 650.degree. C. so that the combustible gas produced contains a large amount of combustible component.

Abstract translation: 将燃烧物质，例如废物，煤等气化的燃烧装置，以产生含有足够大量的可燃组分的可燃气体，以通过其自身的热量来熔化灰分。 流化床炉具有近似圆形的横截面构造。 在炉的中央部形成有流化介质沉降扩散的移动床，在炉的周边部形成流化床主动流化的流化床。 流化介质从流化床的上部翻转到移动床的上部，从而循环通过两个床。 将可燃物投入到移动床的上部，并与流化介质一起气化以形成可燃气体同时循环。 供给流化床炉的氧气的量设定为不高于燃烧可燃物质所需的理论氧气的30％。 流化床的温度保持在450℃至650℃，使得产生的可燃气体含有大量的可燃组分。

公开(公告)号：US20020035804A1

公开(公告)日：2002-03-28

申请号：US09389851

申请日：1999-09-02

Inventor： ARMANDO GARCIA-SECOVIA ,  LUIS-RAMON FARIAS-MARTINEZ ,  JOSE-JAVIER GARZA-ONDARZA ,  JORGE BERRUN-CASTANON ,  HECTOR-AGUSTIN CANTU-MARTINEZ ,  ANGEL CUEVAS-MARTINEZ

IPC: C10J001/00 ,  C10K001/00 ,  F23G005/00

CPC classification number: C10J3/16 ,  C10J3/30 ,  C10J2300/1223 ,  F23G5/027 ,  F23G5/50 ,  F23G7/12 ,  F23G2207/112 ,  F23G2207/113 ,  F23G2209/281 ,  F23H3/02 ,  Y02P20/144

Abstract: An apparatus and a method for fractionating alternative solid fuels, specially whole tires, into volatiles and coal, to be used as alternative fuels, and metal, the apparatus comprising: a feeding zone wherein the solid fuels are feed to the apparatus, a gasifying zone into which the solid fuels are processed, obtaining a gaseous fraction, coal and metal; cooled grills controlling the bed permeability and permanence time of the solid fuels at the gasifying zone; and a discharging zone into which the resultant coal and metal are discharged.

Abstract translation: 一种用于将替代固体燃料，特别是整个轮胎分解成用作替代燃料的挥发物和煤以及金属的装置和方法，所述装置包括：供给区，其中固体燃料进料到装置，气化区 固体燃料被加工到其中，获得气体馏分，煤和金属; 控制气化区固体燃料的床渗透性和持久时间的冷却烤架; 以及排放区域，所得煤和金属排放到该排放区域中。

公开(公告)号：US2662816A

公开(公告)日：1953-12-15

申请号：US3973348

申请日：1948-07-20

Applicant: HYDROCARBON RESEARCH INC

Inventor： KALBACH JOHN C

IPC: C10J3/46

CPC classification number: C10J3/482 ,  C10J2200/158 ,  C10J2300/0933 ,  Y02P20/144 ,  Y10S48/04

公开(公告)号：US20170226436A1

公开(公告)日：2017-08-10

申请号：US15329303

申请日：2015-07-28

Applicant: Sustainable Waste Power Systems, Inc.

Inventor： Michael Joseph GILLESPIE ,  Christopher Paul GILLESPIE ,  Joseph J. ZAMBITO

IPC: C10J3/66 ,  C10J3/46

CPC classification number: C10J3/66 ,  C10J3/466 ,  C10J3/485 ,  C10J3/74 ,  C10J2300/094 ,  C10J2300/0946 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/0976 ,  C10L9/086 ,  Y02P20/144

Abstract: The invention concern methods for converting carbonaceous feedstock slurry into synthetic fuel gas comprising: (a) introducing a carbonaceous feed stock slurry into a first reaction vessel via a continuous feed; (b) converting said carbonaceous feed stock slurry to a carbon char slurry comprising carbon char, and water by allowing said carbonaceous feed stock slurry to have a residency time of between 5 and 30 minutes in said first reaction vessel, said carbonaceous feed stock slurry being heated to a temperature of between about 260 to about 320° C. at a pressure such that water does not flash to steam.

公开(公告)号：US20030150161A1

公开(公告)日：2003-08-14

申请号：US10228721

申请日：2002-08-26

Inventor： Armando Garcia-Segovia ,  Luis Ramon Farias-Martinez ,  Jose Javier Garza-Ondarza ,  Jorge Berrun-Castanon ,  Hector Agustin Cantun-Martinez ,  Angel Cuevas-Martinez

IPC: C10J003/20

CPC classification number: C10J3/16 ,  C10J3/30 ,  C10J2200/154 ,  C10J2300/1223 ,  C10J2300/1671 ,  F23G5/027 ,  F23G5/50 ,  F23G7/12 ,  F23G2207/112 ,  F23G2207/113 ,  F23G2209/281 ,  F23H3/02 ,  Y02P20/144

Abstract: An apparatus and a method fractionate solid fuels, especially whole tires, into metal as well as volatiles and coal to be used as alternative fuels. The apparatus includes a feeding zone wherein the solid fuels are fed to the apparatus, a gasifying zone into which the solid fuels are processed, obtaining a gaseous fraction, coal, and metal; cooled grills controlling the bed permeability and permanence time of the solid fuels at the gasifying zone; and a discharging zone into which the resultant coal and metal are discharged, in which the solid fuel coal and solid and gaseous fractions follow a path inside the apparatus through the feeding zone, the gasifying zone and discharging zone, and in which the gases inside the apparatus follow a path that is co-current with the solid fuel fractions path inside the apparatus.

Abstract translation: 一种装置和方法将固体燃料，特别是整个轮胎分馏成金属以及用作替代燃料的挥发物和煤。 该装置包括一个进料区，其中固体燃料被输送到该装置，一个气化区，固体燃料被加工到其中，得到一个气体馏分，煤和金属; 控制气化区固体燃料的床渗透性和持久时间的冷却烤架; 以及排放区域，其中所产生的煤和金属被排放到其中，其中固体燃料煤和固体和气体馏分通过进料区，气化区和排出区在设备内部通过路径，并且其中 设备遵循与设备内的固体燃料分数路径并流的路径。

公开(公告)号：US5904879A

公开(公告)日：1999-05-18

申请号：US908876

申请日：1997-08-08

Applicant: John Duckett Winter ,  Paul Ellis Brickhouse ,  Ronald Frederick Tyree ,  John S. Stevenson ,  Gregory Joseph Mayotte ,  Jerrold Samuel Kassman ,  Byron Von Klock

Inventor： John Duckett Winter ,  Paul Ellis Brickhouse ,  Ronald Frederick Tyree ,  John S. Stevenson ,  Gregory Joseph Mayotte ,  Jerrold Samuel Kassman ,  Byron Von Klock

IPC: C01B3/36 ,  C10J3/66 ,  C07C1/02 ,  C01B7/00

CPC classification number: C01B3/36 ,  C10J3/66 ,  C10J3/84 ,  C10K1/101 ,  C10J2300/0903 ,  C10J2300/0946 ,  C10J2300/1846 ,  Y02P20/144

Abstract: An integrated liquefaction and gasification process converts bulk particulate halogen-containing waste plastic materials with minimal particle size reduction into a synthesis gas and a non-leachable, vitreous environmentally nontoxic slag. The process involves melting and cracking bulk particulate halogen-containing waste plastic material to form a lower boiling point, lower molecular weight halogen-containing oil composition which then undergoes partial oxidation in a quench gasifier to produce a synthesis gas. Any hazardous gases, liquids or solids that are produced can be purified into commercially valuable byproducts or recycled to the process, which does not release hazardous materials to the environment.

Abstract translation: 集成的液化和气化过程将大量颗粒状含卤素废塑料材料转化为合成气和不可浸出的玻璃状环境无毒渣。 该方法包括熔化和裂解散装含颗粒的含卤素的废塑料材料以形成低沸点，低分子量含卤素的油组合物，然后在骤冷气化器中进行部分氧化以产生合成气。 所生产的任何危险气体，液体或固体都可以纯化成商业上有价值的副产物，或者再循环到不会向环境中释放有害物质的过程。