公开(公告)号：US09120977B1

公开(公告)日：2015-09-01

申请号：US13833758

申请日：2013-03-15

申请人： Harvey G. Buhr

发明人： Harvey G. Buhr

IPC分类号： C10B19/00 ,  C10B47/28 ,  C10B47/00 ,  C10B47/04 ,  C10B47/02 ,  C10B47/46 ,  C10B47/06 ,  C10G1/10 ,  B29B17/04

CPC分类号： C10B19/00 ,  B29B2017/0496 ,  C10B47/00 ,  C10B47/02 ,  C10B47/04 ,  C10B47/06 ,  C10B47/28 ,  C10B47/46 ,  C10B53/07 ,  C10G1/10 ,  C10G2300/1003 ,  Y02E50/30 ,  Y02E50/32 ,  Y02P20/143

摘要： A processor for vacuum distillation of whole tires including: an insulated housing having a door on one end, a central radiant heat tube and a plurality of peripheral heat tubes spaced about the central radiant heat tube and arranged with an inlet leg of each peripheral heat tube adjacent an outlet leg of another peripheral heat tube to maximize utilization of the radiant heat energy from the peripheral heat tubes. The central radiant heat tube has an unsupported end adjacent the door such that the tires loaded through door will pass over the central radiant heat tube and such that the central radiant heat tube is in a central opening of each tire.

摘要翻译： 一种用于整个轮胎的真空蒸馏的处理器，包括：一端具有门的绝缘壳体，中心辐射热管和围绕中心辐射热管间隔开的多个周边热管，并且设置有每个周边热管的入口腿 邻近另一个周边热管的出口腿，以最大限度地利用来自周边热管的辐射热能。 中央辐射热管在门附近具有不支撑的端部，使得通过门装载的轮胎将越过中心辐射热管并且使得中心辐射热管处于每个轮胎的中心开口中。

公开(公告)号：US4206186A

公开(公告)日：1980-06-03

申请号：US869147

申请日：1978-01-13

申请人： Heinz Holter ,  Heinz Gresch ,  Heinrich Igelbuscher

发明人： Heinz Holter ,  Heinz Gresch ,  Heinrich Igelbuscher

IPC分类号： B01D53/02 ,  B01D53/34 ,  B01D53/60 ,  B01D53/62 ,  B01D53/72 ,  C10B47/28 ,  C10B53/00 ,  C10K1/02 ,  C10K1/18 ,  C10K1/20 ,  F23G5/027

CPC分类号： C10G49/007 ,  B01D53/02 ,  B01D53/34 ,  B01D53/60 ,  B01D53/62 ,  B01D53/72 ,  C10B47/28 ,  C10B53/00 ,  C10K1/02 ,  C10K1/18 ,  C10K1/20 ,  F23G5/0273 ,  F23G2201/301 ,  F23G2201/303 ,  Y10S423/18

摘要： Organic refuse is pyrolyzed to form disposable solids and gas. The gas is washed at a temperature well above 100.degree. C. with wash oil, which is recirculated. Spent wash oil is pyrolyzed with contaminants and further organic refuse. The washed gas is filtered through sorption means to remove acid and or other noxious gases therefrom before being cooled well below 100.degree. C. to condense water vapor and other constituents having boiling points within the range of from, e.g., 75.degree. to 150.degree. C. After separating the resulting condensate, thus-purified combustion gas is used, e.g., as a fuel source for the organic-refuse pyrolysis.

摘要翻译： 有机垃圾被热解以形成一次性固体和气体。 气体在高于100℃的温度下用洗涤油进行洗涤，再循环。 废洗油被污染物和进一步的有机垃圾热解。 洗涤过的气体通过吸附装置过滤，以在冷却到100℃以下以冷凝水蒸气和沸点在例如75℃至150℃范围内的其它组分，从而除去酸和其它有害气体 在分离所得的冷凝物之后，使用如此纯化的燃烧气体，例如用作有机 - 垃圾热解的燃料源。

公开(公告)号：US11618854B1

公开(公告)日：2023-04-04

申请号：US17516295

申请日：2021-11-01

申请人： Myung Duck Ma

发明人： Myung Duck Ma

IPC分类号： C10B53/07 ,  C10B47/28 ,  C10B23/00 ,  H05B3/00 ,  B01D3/14

摘要： A process for converting waste plastic into oil includes: subjecting the waste plastic to be in contact with a plurality of far-infrared ray heating rods in a reactor which contains an agitator configured to distribute the waste plastic; converting the waste plastic into a liquid form resultant decomposition by thermal decomposition and pyrolysis in the reactor; fractionating the resultant decomposition product to obtain gas, light oil, and crude diesel oil; obtaining a sludge from a bottom portion of the reactor and transferring the sludge to a blending tank; transferring the light oil to the blending tank; mixing the sludge and the light oil using a high-speed shearing machine to produce a sludge and light oil mixture; transferring the sludge and light oil mixture to a homogenizer; and blending the sludge and light oil mixture at the homogenizer to form a blended oil.

公开(公告)号：US10377952B2

公开(公告)日：2019-08-13

申请号：US14896853

申请日：2013-07-11

申请人： MITSUBISHI HEAVY INDUSTRIES ENVIRONMENTAL & CHEMICAL ENGINEERING CO., LTD.

发明人： Yuuki Endou ,  Takehiro Kitta ,  Kazuaki Kakurata ,  Junichiro Abe

IPC分类号： C10B27/06 ,  F23G7/10 ,  C10B53/02 ,  F23L7/00 ,  F23G5/027 ,  C10B47/28 ,  C10B47/30

摘要： This method for inhibiting the occurrence of a pyrolysis deposit in a pyrolysis gasification system includes: gasifying biomass (S2) through pyrolysis in a pyrolysis gasification furnace (5); separating, in a solid-gas separation unit (7), a pyrolysis gas (G1) and a carbide (C) continuously formed through pyrolysis of the biomass (S2); feeding an oxygen-containing gas (G3) to the separated pyrolysis gas (G1); and introducing the pyrolysis gas (G1) together with the oxygen-containing gas (G3) to a combustion furnace (6) through a pipe (9) which constitutes a pyrolysis gas line (8).

公开(公告)号：US10131847B2

公开(公告)日：2018-11-20

申请号：US13517323

申请日：2010-12-20

申请人： David McNamara ,  Michael Murray

发明人： David McNamara ,  Michael Murray

IPC分类号： C10B47/28 ,  C10B47/32 ,  C10B53/07 ,  C10G1/00 ,  C10G1/02 ,  B01D3/14 ,  B01D3/24 ,  B01D5/00 ,  C10G1/10 ,  C10B47/18 ,  F23G5/02 ,  F23G7/12 ,  C10B47/34

摘要： A process is described for treating waste plastics material to provide at least one on-specification fuel product. Plastics material is melted and then pyrolyzed in an oxygen-free atmosphere to provide pyrolysis gases. The pyrolysis gases are brought into contact with plates in a contactor vessel so that some long chain gas components condense and return to be further pyrolyzed to achieve thermal degradation. Short chain gas components exit the contactor in gaseous form and proceed to distillation to provide one or more on-specification fuel products. A pipe directly links the pyrolysis chamber to the contactor, suitable for conveying upwardly-moving pyrolysis gases and downwardly-flowing long-chain liquid for thermal degradation.

公开(公告)号：US20240166951A1

公开(公告)日：2024-05-23

申请号：US17744619

申请日：2021-01-14

申请人： Engergy Research Institute of Shandong Academy of Sciences

发明人： Hongyu SI ,  Bing WANG ,  Xiaohui LIANG ,  Suxiang LIU ,  Meirong XU ,  Yonggang LI ,  Zhaojie CUI ,  Qiang YAO ,  Haichao WANG ,  Laizhi SUN ,  Shuangxia YANG ,  Likun HE ,  Dongliang HUA ,  Zhijie GU

IPC分类号： C10B47/28 ,  B01D3/14 ,  B01D53/26 ,  C10B21/12 ,  C10B21/18 ,  C10B27/06 ,  C10B39/02 ,  C10B57/10 ,  C10C1/00 ,  C10C5/00

CPC分类号： C10B47/28 ,  B01D3/143 ,  B01D53/265 ,  C10B21/12 ,  C10B21/18 ,  C10B27/06 ,  C10B39/02 ,  C10B57/10 ,  C10C1/00 ,  C10C5/00 ,  B01D2257/80 ,  B01D2258/0283 ,  B01D2259/65

摘要： A continuous solid organic matter pyrolysis polygeneration system and method for using the system is disclosed. The pyrolysis polygeneration system mainly includes a processing system, a drying furnace, a pyrolysis furnace, a cooling furnace, a tail gas treatment system, and a gas treatment system and a protective gas circulation system cooperate with each other to realize the multi-level rational utilization of energy, and are suitable for the continuous and rapid pyrolysis and carbonization of various solid organic matter in the actual production. While realizing the polygeneration of coke, wood vinegar and tar, the maximum utilization of overall heat is realized through process optimization.

公开(公告)号：US20160168471A1

公开(公告)日：2016-06-16

申请号：US14896853

申请日：2013-07-11

申请人： MITSUBISHI HEAVY INDUSTRIES ENVRONMENTAL & CHEMICAL ENGINEERING CO., LTD.

发明人： Yuuki ENDOU ,  Takehiro KITTA ,  Kazuaki KAKURATA ,  Junichiro ABE

IPC分类号： C10B27/06 ,  C10B47/28 ,  C10B53/02

CPC分类号： C10B27/06 ,  C10B47/28 ,  C10B47/30 ,  C10B53/02 ,  F23G5/0276 ,  F23G7/10 ,  F23G2201/303 ,  F23G2207/30 ,  F23L7/007 ,  Y02E20/344 ,  Y02E50/14 ,  Y02P20/145

摘要： This method for inhibiting the occurrence of a pyrolysis deposit in a pyrolysis gasification system includes: gasifying biomass (S2) through pyrolysis in a pyrolysis gasification furnace (5); separating, in a solid-gas separation unit (7), a pyrolysis gas (G1) and a carbide (C) continuously formed through pyrolysis of the biomass (S2); feeding an oxygen-containing gas (G3) to the separated pyrolysis gas (G1); and introducing the pyrolysis gas (G1) together with the oxygen-containing gas (G3) to a combustion furnace (6) through a pipe (9) which constitutes a pyrolysis gas line (8).

摘要翻译： 用于抑制热解气化系统中热解沉积物的发生的方法包括：通过热解气化炉（5）中的热解气化生物质（S2）; 在固体气体分离单元（7）中分离通过生物质（S2）的热解连续形成的热解气体（G1）和碳化物（C）; 向分离的热解气体（G1）供给含氧气体（G3）; 并通过构成热解气体管线（8）的管（9）将热解气体（G1）与含氧气体（G3）一起引入燃烧炉（6）。

公开(公告)号：US09039893B2

公开(公告)日：2015-05-26

申请号：US13378549

申请日：2010-06-14

申请人： Alberto Delbianco ,  Giambattista De Ghetto

发明人： Alberto Delbianco ,  Giambattista De Ghetto

IPC分类号： C10G1/04 ,  C10B49/02 ,  C10B47/28 ,  C10B49/14 ,  C10B53/06 ,  F24J2/07 ,  F24J2/46 ,  C10G1/00

CPC分类号： C10B49/02 ,  C10B47/28 ,  C10B49/14 ,  C10B53/06 ,  C10G1/047 ,  C10G2300/80 ,  C10G2300/805 ,  F24S20/20 ,  F24S80/20 ,  Y02E10/41 ,  Y02P20/134

摘要： Process for the extraction of hydrocarbons contained in oil sands and oil shale comprising feeding said oil sands or oil shale to a suitable apparatus in which they are heated, directly and/or by means of a suitable vector fluid, making use of solar energy collected by means of optical concentration systems.

摘要翻译： 包括在油砂和油页岩中的烃的提取方法，包括将所述油砂或油页岩直接和/或通过合适的载体流体加热到合适的装置中，使用由 光学浓度系统的手段。

公开(公告)号：US08377264B2

公开(公告)日：2013-02-19

申请号：US12521687

申请日：2007-12-28

申请人： Yoshiyuki Tokuda ,  Toshiaki Okauchi

发明人： Yoshiyuki Tokuda ,  Toshiaki Okauchi

IPC分类号： C10B47/28 ,  C10B1/00

CPC分类号： F23G5/027 ,  B01D53/77 ,  B01D2251/304 ,  B01D2251/604 ,  B09B3/00 ,  B09B3/0083 ,  C10B49/02 ,  C10B53/00 ,  F23G5/10 ,  F23G5/16 ,  F23G7/07 ,  F23J15/003 ,  F23J15/022 ,  F23J15/04 ,  F23J2219/10

摘要： Disclosed is an organic material disposal method comprising a step for thermally decomposing a raw organic material and a gas treatment step for treating a gas generated in the preceding step, wherein the thermal decomposition step comprises a substep of decomposing the raw organic material into a carbide and a gaseous component, and the gas treatment step comprises the following substeps (1) to (5): (1) catalytically oxidizing the gaseous component produced in the thermal decomposition step; (2) neutralizing/washing the oxidized gas; (3) subjecting a waste water produced in the neutralization/washing step to the solid-liquid separation; (4) further thermally decomposing a solid component separated in the solid-liquid separation step together with the raw organic material in the thermal decomposition step; and (5) re-using a liquid component separated in the solid-liquid separation step in the solid-liquid separation step and/or the neutralization/washing step.

摘要翻译： 公开了一种有机材料处理方法，其包括热分解原料有机材料的步骤和用于处理前述步骤中产生的气体的气体处理步骤，其中所述热分解步骤包括将原始有机材料分解成碳化物的子步骤， 气体处理步骤包括以下子步骤（1）至（5）：（1）催化氧化在热分解步骤中产生的气态组分; （2）中和/清洗氧化气体; （3）将在中和/洗涤步骤中产生的废水进行固液分离; （4）在热分解工序中，与固体成分分离步骤中分离出的固体成分与原料有机物一起进一步热分解; 和（5）在固液分离步骤和/或中和/洗涤步骤中重新使用在固液分离步骤中分离的液体组分。

公开(公告)号：US20240093094A1

公开(公告)日：2024-03-21

申请号：US18468324

申请日：2023-09-15

申请人： Carba Inc.

发明人： Andrew JONES ,  Robert CRANE

IPC分类号： C10B53/02 ,  C10B47/28

CPC分类号： C10B53/02 ,  C10B47/28

摘要： A process is hereby provided for permanently (>1000 years) reducing carbon dioxide in the atmosphere. The process involves the cultivation of tree and plant waste (biomass), the conversion of the biomass in a reactor to a carbon product, e.g., charcoal, and subsequent storage of the carbon product. The reactor used for conversion is run at a low temperature, e.g., 300-450° C. Thus, there is negligible cracking. The product is primarily a solid carbon product, which is safe and can be easily handled. The carbon product can also be safely stored. In one embodiment, the carbon product is buried in a location that is tested for limited oxygen at burial depths. The permanence of the CO2 reduction is therefore assured.