公开(公告)号：US11345859B2

公开(公告)日：2022-05-31

申请号：US17255725

申请日：2019-06-18

Applicant: BIOFORCE TECH CORPORATION

Inventor： Dario Presezzi ,  Valentino Villa ,  Marco Mosciarello ,  Stefano Pessina ,  Mattia Bonfanti

IPC: C10B47/18 ,  C10B47/44 ,  C10B19/00 ,  C10B1/06 ,  C10B5/10 ,  C10B7/10 ,  F28D7/16 ,  H02K7/18

Abstract: A system and method for performing pyrolysis comprises a reactor through which organic material is conveyed from an upstream end toward a downstream end and within which said pyrolysis will occur; a combustion chamber fluidically connected to the downstream end of the reactor; an output pipe fluidically connected to the downstream end of the reactor; a capsule surrounding a first part of the reactor and into an internal portion of which heated thermal fluids are disposed for heating the first part of said reactor; and a plurality of electrical resistors disposed around a second part of the reactor for heating the second part of the reactor; whereby, as a result of the pyrolysis occurring within the reactor, the syngas is conducted toward the combustion chamber while the carbonized material is conducted outwardly from the reactor through the output pipe.

公开(公告)号：US11118114B2

公开(公告)日：2021-09-14

申请号：US16804570

申请日：2020-02-28

Applicant: RES POLYFLOW LLC

Inventor： Jay Schabel ,  Richard A. Schwarz ,  Charles W. Grispin ,  Mehmet A. Gencer ,  Joseph D. Hensel

IPC: C10G1/10 ,  C10B47/06 ,  C08J11/12 ,  C10B47/44 ,  C10B47/32 ,  C10B47/18 ,  G05D23/00 ,  G05D23/19 ,  C10G1/00 ,  C10B5/00 ,  C10B7/10 ,  C10B45/00 ,  C10B49/02 ,  C10B53/07 ,  C10G1/02

Abstract: A process and an apparatus for pyrolysis of mixed plastic feedstock producing petroleum products are described. In one example, a process for producing petroleum products includes charging feedstock of mixed polymer materials into a reactor apparatus. Heat energy is applied to the feedstock while advancing the feedstock through the reactor apparatus in an anaerobic operation. The energy input to the reactor apparatus is controlled by controlling a temperature gradient within the reactor vessel to produce petroleum gas product. The process involves in situ chemical reactions comprising cracking and recombination reactions that that are controlled to convert solid hydrocarbonaceous portion of the feedstock to molten fluids and gases inside the reactor vessel and to produce gaseous petroleum products which exit the reactor vessel. The separated solid residue from the pyrolysis process is also removed from the reactions vessel.

公开(公告)号：US10968394B2

公开(公告)日：2021-04-06

申请号：US16309870

申请日：2017-06-19

Applicant: SUEZ GROUPE

Inventor： Andrzej Posmyk ,  James Gray ,  Jonathan Hall

IPC: C10B53/07 ,  B01D3/06 ,  B01D3/32 ,  C10G1/10 ,  C10B47/18 ,  B01D3/22 ,  B01D3/16 ,  B01D5/00 ,  C10G1/02 ,  C10G1/06 ,  C10L1/04

Abstract: A process for thermal cracking of a feedstock of plastic materials, in particular waste materials, includes the steps of melting the feedstock, conveying melted feedstock in a pyrolysis chamber where the melted feedstock is heated in a substantially oxygen purged environment, to convert it into pyrolysis gases, the process further comprising the steps of: driving pyrolysis gases from the pyrolysis chamber into a tray reflux column comprising a partial condenser at its upper extremity, returning pyrolysis gases condensed in the tray reflux column into the pyrolysis chamber, distilling pyrolysis gases exiting the partial condenser of the reflux column, to provide one or more fuel products.

公开(公告)号：US20190256781A1

公开(公告)日：2019-08-22

申请号：US16401380

申请日：2019-05-02

Applicant: Future Energy Investments Pty Ltd

Inventor： Garry Baker

IPC: C10B53/07 ,  C10G1/10 ,  C10G11/02 ,  C10G11/05 ,  C10G11/10 ,  C10L1/06 ,  C10B47/18 ,  C10B27/06 ,  C10G1/02 ,  C10L1/08

Abstract: A process and plant for the thermocatalytic conversion of waste materials into reusable fuels and a fuel produced by the process, involving the steps of delivering melted waste material to one or more pyrolysis chambers via heated and valved manifolds and effecting pyrolysis of the waste material into a gaseous state in an oxygen purged and pressure controlled environment. Pyrolytic gases are then transferred to a catalytic converter where the molecular structure of the gaseous material is altered in structure and form, with gases then transferred to one or more condensers to distil and cool gases in to their respective fractions. After post pyrolysis treatment, fuel fractions form a useable fuel.

公开(公告)号：US10023804B2

公开(公告)日：2018-07-17

申请号：US13738173

申请日：2013-01-10

Applicant: Fredrick Taylor

Inventor： Fredrick Taylor

IPC: C10G1/00 ,  C10G1/02 ,  C10G1/10 ,  C10B1/10 ,  C10B47/00 ,  C10B47/18 ,  C10B47/30 ,  C10B53/00 ,  C10B53/07 ,  C09C1/48 ,  C22B7/00 ,  C01B31/02

Abstract: A system and method of converting tires or other solid carbon based material is disclosed, including providing a chamber, feeding the solid carbon based material into the chamber, rotating the chamber, heating and reducing the material in the chamber, collecting solid residue from the chamber, collecting vapor from the chamber, and converting vapor collected from the chamber to a liquid. In an embodiment, the material includes a whole tire. The tire is heated in the chamber causing the tire to collapse and liquefy, exposing the metal in the tire which aids in grinding the carbon material in the tire as it tumbles, collecting solid residue, for example tire carbons, and collecting vapor, for example vaporized oil, and benzene and methane gas from the chamber and converting the oil. The chamber may be heated to a temperature from about 350° F. to about 1100° F. using gases reclaimed from the material.

公开(公告)号：US20160333271A1

公开(公告)日：2016-11-17

申请号：US15221713

申请日：2016-07-28

Applicant: PYROWAVE INC.

Inventor： Jocelyn DOUCET ,  Jamal CHAOUKI ,  Amr SOBHY

IPC: C10B53/07 ,  C10B47/18 ,  C10G1/10 ,  C10G1/02 ,  C10G1/00 ,  C10B19/00 ,  C10B27/06

CPC classification number: C10B53/07 ,  B01J21/18 ,  C10B19/00 ,  C10B27/06 ,  C10B47/18 ,  C10B53/00 ,  C10B53/02 ,  C10G1/002 ,  C10G1/02 ,  C10G1/10 ,  C10G2300/1003 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10K1/024 ,  C10K3/02 ,  C10L9/083 ,  F23G5/0276 ,  F23G2201/303 ,  F23G2204/203 ,  F23G2900/50202 ,  Y02E50/14 ,  Y02E50/15

Abstract: The present document describes a catalyst to initiate microwave pyrolysis of waste, a process for the microwave pyrolysis of waste using the catalyst, as well as a microwave pyrolysis system.

Abstract translation: 本文件描述了引发废物的微波热解的催化剂，使用催化剂的废物微波热解的方法以及微波热解系统。

公开(公告)号：US09309464B2

公开(公告)日：2016-04-12

申请号：US13878884

申请日：2011-10-10

Applicant: Rolf Ljunggren

Inventor： Rolf Ljunggren

IPC: C10J3/00 ,  C10B21/00 ,  C10B47/18 ,  C10J3/48

CPC classification number: C10B21/00 ,  C10B47/18 ,  C10J3/485 ,  C10J2300/093 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1207 ,  C10J2300/1269 ,  C10J2300/1625 ,  C10J2300/1884 ,  C10J2300/1892 ,  Y02P20/129

Abstract: Method and equipment for producing coke (PC) during indirectly heated gasification, in which coal particles are supplied to a gasification reactor (1) and process gas (P) supplied during the gasification is reduced in it to synthesis gas (S), whereby the synthesis gas (S) is removed from the gasification reactor (1). The method is distinguished in that at the same time a gasification takes place, a coking of coal takes place in an inner reactor (4) arranged inside the gasification reactor (1), that the inner reactor (4) is indirectly heated, that coke (PC) and combustible gases are produced in the inner reactor (4) during the coking, and that the combustible gases are used for the indirect heating in the gasification in the gasification reactor (1).

Abstract translation: 在气化过程中将煤粒子供给到气化反应器（1）和处理气体（P）的间接加热气化过程中生产焦炭（PC）的方法和设备减少到合成气体（S），由此 从气化反应器（1）除去合成气（S）。 该方法的特征在于，同时发生气化，煤焦化在布置在气化反应器（1）内的内反应器（4）中发生，内反应器（4）被间接加热，焦炭 （PC）和可燃气体在焦化期间在内反应器（4）中产生，并且可燃气体用于气化反应器（1）中的气化中的间接加热。

公开(公告)号：US5976484A

公开(公告)日：1999-11-02

申请号：US935543

申请日：1997-09-23

Applicant: Chien-Lang Teng ,  Feng-Sung Wang

Inventor： Chien-Lang Teng ,  Feng-Sung Wang

IPC: C01B31/08 ,  C01B31/10 ,  C10B1/04 ,  C10B47/18 ,  C10B53/00 ,  C10B53/07 ,  B01J20/02

CPC classification number: C10B47/18 ,  C01B31/081 ,  C01B31/10 ,  C10B1/04 ,  C10B53/07 ,  Y02P20/143

Abstract: A method and device is provided which is capable of producing gasified substance and solid-shaped carbonized substances from solid-shaped wastes such as waste tyres by a series of heating, dry distillation and splitting decomposition. After discharging out from the bottom of a splitting decomposition reactor, the solid-shaped carbonized substances are subject to a series of treatments: water washing, magnetic separating, alkaline cleaning and acid pickling (treatment) to separate out iron wire and to remove heavy metal-bearing ash contents. The carbonized substances are next pulverized to the desired particle size so that highly purified carbon black is formed. Subsequently, the carbon black granules are led into an activation furnace and are heated and activated at the atmosphere of steam being passed in to produce powder particulate activated carbon. On the other hand, from the gasified substance produced by-products of the combustible oil and gas are respectively formed. This combustible oil and/or combustible gas can be led into the splitting decomposition reactor and the activation furnace as fuels for heating on the outside of the furnace and where the remaining portion of which may be sold to the outside. The above process of treatments is accomplished at an intermittent and continuous way and recovery rate of the activated carbon is high whereas the treatment time is shortened.

Abstract translation: 提供了一种方法和装置，其能够通过一系列加热，干馏和分解分解从固体废物例如废轮胎产生气化物质和固体碳化物质。 从分解分解反应器的底部排出后，固体碳化物质经过一系列处理：水洗，磁分离，碱洗和酸洗（处理）以分离出铁丝并除去重金属 - 含灰分。 接着将碳化物质粉碎至所需的粒度，从而形成高度纯化的炭黑。 随后，将炭黑颗粒引入活化炉中，并在通入蒸汽的气氛中加热和活化以产生粉末颗粒活性炭。 另一方面，分别形成由可燃油和气体产生的副产物的气化物质。 该可燃油和/或可燃气体可以作为燃料在分解分解反应器和活化炉中被引入到炉的外部加热，其余部分可以出售到外部。 上述处理过程以间歇连续的方式完成，活性炭的回收率高，而处理时间缩短。

公开(公告)号：US5464503A

公开(公告)日：1995-11-07

申请号：US142014

申请日：1993-10-28

Applicant: Vahan Avetisian ,  Craig J. Castagnoli ,  Suk B. Cha

Inventor： Vahan Avetisian ,  Craig J. Castagnoli ,  Suk B. Cha

IPC: B09B3/00 ,  C10B7/10 ,  C10B33/00 ,  C10B47/44 ,  C10B53/00 ,  C10B53/07 ,  C10G1/00 ,  C10G1/10 ,  C10B47/18

CPC classification number: C10G1/10 ,  C10B33/00 ,  C10B47/44 ,  C10B53/07 ,  C10B7/10 ,  C10G1/002 ,  Y02P20/143

Abstract: A discharge system is used with a tire liquefaction process using a reactor. The system includes a receiver receiving unreacted components, including oil coated metal, from the reactor. The unreacted components are moved through a pyrolysis reactor where they are heated to a temperature sufficient to convert the unreacted hydrocarbon components to a liquid and to gas by way of pyrolysis. The liquid and the majority of gas are drawn off from the pyrolysis reactor. Discharge apparatus connected to the pyrolysis reactor converts the remaining gas to a condensate and discharges the metal. The condensate is also removed for further use.

Abstract translation: 排气系统与使用反应器的轮胎液化过程一起使用。 该系统包括从反应器接收未反应组分（包括油涂金属）的接收器。 将未反应的组分移动通过热解反应器，在其中将其加热到足以通过热解将未反应的烃组分转化为液体和气体的温度。 液体和大部分气体从热解反应器中排出。 连接到热解反应器的排放装置将剩余气体转化为冷凝物并排出金属。 冷凝水也被去除以供进一步使用。

公开(公告)号：US4465556A

公开(公告)日：1984-08-14

申请号：US402641

申请日：1982-07-28

Applicant: Mack D. Bowen ,  Kenneth R. Purdy

Inventor： Mack D. Bowen ,  Kenneth R. Purdy

IPC: C10B49/06 ,  C10B53/02 ,  C10G1/02 ,  C10B1/04 ,  C10B47/18

CPC classification number: C10B49/06 ,  C10B53/02 ,  C10G1/02 ,  Y02E50/14 ,  Y02P20/129 ,  Y02P20/145

Abstract: A process and system for continuously pyrolyzing organic feedstock produces a solid carbonaceous residue of controlled volatility, in a manner that is highly energy efficient. The value of the gaseous product and of the pyrolytic oil produced are also optimized.

Abstract translation: 用于连续热解有机原料的方法和系统以高能量的方式产生受控挥发性的固体碳质残余物。 气态产物和所产生的热解油的价值也得到优化。