公开(公告)号：WO2016089235A3

公开(公告)日：2016-09-09

申请号：PCT/PT2015000051

申请日：2015-11-30

Applicant: FINERTEC FUELS CENTRO LDA

Inventor： SILVA VALENTE ANTÓNIO JOSÉ ,  KADRI GULYURTLU IBRAHIM

IPC: C10G1/10 ,  C10B47/24

CPC classification number: C10G1/10 ,  C10B47/24 ,  C10B53/07 ,  C10G2400/04 ,  Y02P20/143

Abstract: The present invention is relate to environment and energy areas and ultimately lead to the production of liquid fuel from the thermochemical recycling of plastic materials, based on a new fast pyrolysis process. The invention consists of an external reactor (1), an internal reactor (12), two gas burners (9) located in the walls of the external reactor (1), an external furnace (2) is located where the main burner (7), a circular distribution box (5), a heat exchanger (13), a gas compressor and a cooling system by water. A novelty is the use of two concentric and circular reactors, wherein the external reactor (1) provides the heat for the pyrolysis process. Besides the mechanism, it is also intended patenting operation method thereof.

Abstract translation: 本发明涉及环境和能量领域，并且最终导致基于新的快速热解过程从塑料材料的热化学回收生产液体燃料。 本发明由外部反应器（1），内部反应器（12），位于外部反应器（1）壁内的两个气体燃烧器（9），外部炉（2）位于主燃烧器（7） ），圆形分配箱（5），热交换器（13），气体压缩机和冷却系统。 新颖之处在于使用两个同心圆形反应器，其中外部反应器（1）为热解过程提供热量。 除了这种机制外，它也是专利化的操作方法。

公开(公告)号：WO2012013735A1

公开(公告)日：2012-02-02

申请号：PCT/EP2011/062962

申请日：2011-07-28

Applicant: BASF SE ,  PANTOUFLAS, Emmanouil ,  PROCHAZKA, Roman ,  SCHUNK, Stephan

Inventor： PANTOUFLAS, Emmanouil ,  PROCHAZKA, Roman ,  SCHUNK, Stephan

IPC: C08L97/00 ,  C10B47/24 ,  C10B53/02 ,  C10B57/06 ,  C10C5/00 ,  C10L5/44 ,  B01J21/18 ,  B01J29/40 ,  B01J31/06 ,  B01J37/00 ,  B01J37/04 ,  B01J37/08 ,  C10G1/00 ,  C08L97/02 ,  C08H8/00

CPC classification number: C08L97/005 ,  B01J21/02 ,  B01J21/18 ,  B01J29/06 ,  B01J29/40 ,  C08H6/00 ,  C08H8/00 ,  C08K3/32 ,  C08K3/34 ,  C08K3/38 ,  C08L97/02 ,  C10B47/24 ,  C10B53/02 ,  C10B57/06 ,  C10C5/00 ,  C10G2300/1014 ,  C10G2300/308 ,  C10G2300/807 ,  C10G2400/30 ,  C10L5/44 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/30 ,  Y02P30/20

Abstract: Die vorliegende Erfindung betrifft eine Zusammensetzung ("Komposit"), die Lignin und wenigstens einen in der Zusammensetzung verteilten Katalysator enthlt. Die Erfindung betrifft weiterhin ein Verfahren zur Herstellung einer solchen katalysator- und ligninhaltigen Zusammensetzung und deren Verwendung zur Herstellung einer Aromatenzusammensetzung.

Abstract translation: 本发明涉及一种组合物（“复合”），分布于组合物中的木质素和至少一种含有催化剂。 本发明还涉及一种用于制造这样的催化剂和含木质素的组合物及其用于制备芳族化合物的方法。

公开(公告)号：WO2022089704A1

公开(公告)日：2022-05-05

申请号：PCT/DK2021/050317

申请日：2021-10-27

Applicant: FRICHS HOLDING 2 APS

Inventor： KUDAHL MUNCH, Ove

IPC: C10B53/02 ,  C10B47/24 ,  B01J8/18 ,  C10G1/02

Abstract: A method and a pyrolysis plant are described, comprising a reactor (2) for producing pyrolysis gas (28) from biomass (30). The reactor (2) comprises one or more reaction channels (3) linked thermally with at least one heating circuit (18), which is configured to heat the reaction channels (3) to a temperature that is high enough to gasify the biomass (30). The reactor (2) comprises a feed section (6) configured for feeding the biomass (30) into the reaction channels (3). The pyrolysis plant comprises a gas accelerator (20) configured for recirculating the gas (28) that is present in the at least one reaction channel (3) and for providing a gas flow velocity (15) that is able to distribute the biomass (30) in the reaction channel (3).

公开(公告)号：WO2021102519A1

公开(公告)日：2021-06-03

申请号：PCT/AU2020/051287

申请日：2020-11-27

Applicant: ROYAL MELBOURNE INSTITUTE OF TECHNOLOGY

Inventor： SHAH, Kalpit ,  KUNDU, Sazal, Kumar ,  PATEL, Savankumar, Rajnikantbhai ,  WINTER, John, David

IPC: F23G7/12 ,  F23G7/14 ,  F23G5/027 ,  C02F1/58 ,  C02F11/10 ,  C10B47/24 ,  C10B49/10 ,  C10B53/02 ,  B01J8/24 ,  B01J6/00

Abstract: The invention provides a system for pyrolysis, comprising: (i) a gas producer comprising a gasification zone and a producer gas outlet, wherein the gas producer is configured to: oxidise at least one carbon-containing feed in the presence of an oxidising gas in the gasification zone to form a producer gas; and discharge the producer gas from the gasification zone via the producer gas outlet, wherein a residual oxygen content of the producer gas is substantially depleted or maintained below a maximum predetermined amount by controlling a ratio of oxygen fed to the gasification zone to the carbon-containing feed, (ii) a pyrolyzer comprising a pyrolysis zone and one or more pyrolyzer gas outlets, wherein the pyrolyzer is configured to: feed the producer gas discharged from the gasification zone to the pyrolysis zone; pyrolyze a pyrolyzable organic feed in the pyrolysis zone in the presence of the producer gas to produce a carbonaceous pyrolysis product and a gas mixture comprising combustible components comprising pyrolysis gas; and discharge the gas mixture from the pyrolysis zone via the one or more pyrolyzer gas outlets, and (iii) a first combustor comprising a combustion zone, wherein the first combustor is configured to: receive the gas mixture discharged from the pyrolysis zone in the combustion zone; feed an oxygen-containing gas to the combustion zone; and combust at least a portion of the combustible components present in the gas mixture in the combustion zone to produce a combustion product gas.

公开(公告)号：WO2011026631A3

公开(公告)日：2012-06-28

申请号：PCT/EP2010005409

申请日：2010-09-03

Applicant: TETZLAFF KARL-HEINZ

Inventor： TETZLAFF KARL-HEINZ

IPC: C10B47/24 ,  C10B53/02 ,  C10J3/66

CPC classification number: C10J3/66 ,  C10B19/00 ,  C10B47/24 ,  C10B53/02 ,  C10J3/482 ,  C10J3/84 ,  C10J2300/0916 ,  C10J2300/0956 ,  C10J2300/0959 ,  C10J2300/0973 ,  C10J2300/1276 ,  C10J2300/1684 ,  C10J2300/1846 ,  C10K3/006 ,  Y02E50/14 ,  Y02P20/145

Abstract: The invention relates to a device (1) for producing syngas (4) from substantially solid fuels, preferably biomass (2), by steam reforming, using at least one pyrolysis reactor (16) for the formation of pyrolysis gas containing tar and coke particles. In order to produce a syngas that is substantially devoid of tar in a simple, cost-effective manner, the device is provided with at least one coke cloud reactor (11) and said coke cloud reactor (11) has at least one heating device (18) for the catalytic cracking of the tar in the pyrolysis gas.

Abstract translation: 公开了一种用于生产合成气的装置（1）（4）基本上由固体燃料，优选的生物质（2），通过蒸汽与含焦油的裂解气和焦炭颗粒的形成的至少一个热解反应器（16）重整。 为了能够容易且廉价地产生基本上焦油 - 自由合成气，它提供了至少一个Kokswolkenreaktor（11）存在，以及Kokswolkenreaktor（11）具有用于热解气体的焦油的催化裂化至少一个加热装置（18）。

公开(公告)号：WO2017128943A1

公开(公告)日：2017-08-03

申请号：PCT/CN2017/070473

申请日：2017-01-06

Applicant: 王志成

Inventor： 王志成

IPC: C10B53/00 ,  C10B57/10 ,  C10B47/24

CPC classification number: C10B47/24 ,  C10B53/00 ,  C10B57/10 ,  Y02P20/129

Abstract: 一种固体垃圾无氧催化热裂解方法，其步骤有，垃圾预处理：将外运垃圾放入垃圾池除去废水后，依次进行粗破、脱水、粉碎成小于3厘米的垃圾颗粒；再利用余热和再生可燃气和/或外加热来加热垃圾颗粒，在干燥将垃圾颗粒的水分含量降低到10-30％范围内，得到干燥垃圾颗粒。垃圾裂化分解：将干燥垃圾颗粒投入流化裂解炉，在无氧的条件下，利用余热和再生可燃气和/或外加热来加热流化裂解炉，使得裂解的温度和升温速度达到要求，加催化剂，使得干燥垃圾颗粒中的有机物质分解成无机物、可燃气、生物碳和液体化合物。裂化分解后的产物再加工：将无机物、可燃气、生物碳和液体化合物，分离、净化、合成加工成建材、燃气、成品肥料、燃油。该方法在中低温、催化、完全没有氧气的条件下，可以处理复杂的混合垃圾，连续进料，实现高效热裂解，产生燃气和碳等，同时，对产生的焦油进行二次裂解，消除管道堵塞和提高燃气热值等。

公开(公告)号：WO2012083431A1

公开(公告)日：2012-06-28

申请号：PCT/CA2011/001392

申请日：2011-12-23

Applicant: ETX SYSTEMS INC. ,  BROWN, Wayne

Inventor： BROWN, Wayne

IPC: C10B47/24 ,  C10B31/00 ,  C10B33/00 ,  C10G9/32

CPC classification number: C10B47/24 ,  C10B49/22 ,  C10B55/10

Abstract: A fluidized bed coking reactor apparatus comprises a reaction vessel; a temperature sensor inside the reaction vessel for measuring a reactor temperature, a solids feed mechanism for feeding solid particles into the reactor vessel at a mass flow rate, a feed material feed mechanism for feeding feed material into the reactor at an operating feed rate; and a supervisory controller programmed to determine an upper feed material feed rate of the reactor when operating at the reactor temperature and receiving solid particles at the mass flow rate. The upper feed material feed rate is defined as a feed rate of feed material deposited onto a selected fraction of a fluidized bed of solid particles that causes defluidization in the reactor when the reactor is operating under conditions having a selected degree of backmixing in the fluidized bed, wherein the degree of backmixing is modeled as a selected number of reactors arranged in series and each operating under continuous well-mixed conditions, with the selected number of reactors being an integer between one and infinity.

Abstract translation: 流化床焦化反应器装置包括反应容器; 用于测量反应器温度的反应容器内的温度传感器，用于以质量流量将固体颗粒输送到反应器容器中的固体进料机构，用于以进给速率将进料输送到反应器中的进料机构; 以及一个监控控制器，其被编程以确定当在反应器温度下操作并以质量流量接收固体颗粒时反应器的上进料输送速率。 上饲料进料速率定义为沉积在固体颗粒流化床的选定馏分中的进料的进料速率，当反应器在流化床中具有选择的回混程度的条件下在反应器中引起脱流时 其中将回混程度建模为串联布置的选定数量的反应器，并且每个反应器在连续充分混合的条件下运行，所选择的反应器数量是在一个和一个无穷大之间的整数。

公开(公告)号：WO2010059799A1

公开(公告)日：2010-05-27

申请号：PCT/US2009/065106

申请日：2009-11-19

Applicant: KIOR INC. ,  O'CONNOR, Paul

Inventor： O'CONNOR, Paul

IPC: C10B47/24

CPC classification number: C10B53/02 ,  C05D9/00 ,  C05G3/0047 ,  C10B49/22 ,  C10G2300/1011 ,  C10L1/02 ,  Y02E50/14 ,  Y02P30/20 ,  C05D9/02

Abstract: A process is disclosed for the catalytic conversion of biomass material whereby particulate biomass material is contacted with a particulate heat carrier material in a fluidized bed. Ash formed in the process may be present in vaporized liquid reaction products and in the char. The process comprises steps of removing ash from the various reaction product components. In a preferred embodiment, ash recovered from the process is recycled into the process.

Abstract translation: 公开了用于生物质材料的催化转化的方法，由此颗粒生物质材料与流化床中的颗粒状热载体材料接触。 在该过程中形成的灰可能存在于蒸发的液体反应产物和焦炭中。 该方法包括从各种反应产物组分中除去灰分的步骤。 在优选的实施方案中，从该方法回收的灰分被再循环到该方法中。

公开(公告)号：WO2009090335A2

公开(公告)日：2009-07-23

申请号：PCT/FR2008001456

申请日：2008-10-17

Applicant: INST FRANCAIS DU PETROLE ,  ROLLAND MATTHIEU ,  LOURET SYLVAIN

Inventor： ROLLAND MATTHIEU ,  LOURET SYLVAIN

IPC: C10B49/10 ,  B01J8/24 ,  B01J8/30 ,  B01J8/32 ,  B02C23/02 ,  B02C23/24 ,  C10B47/24 ,  C10B53/02 ,  C10J3/50 ,  C10L5/44 ,  F26B3/08

CPC classification number: C10L5/44 ,  B01J8/1872 ,  C10B49/10 ,  C10B53/02 ,  C10J3/54 ,  C10J2300/0903 ,  C10J2300/0916 ,  C10L9/083 ,  F26B3/082 ,  F26B2200/02 ,  F26B2200/24 ,  Y02E50/10 ,  Y02E50/14 ,  Y02E50/15 ,  Y02E50/30 ,  Y02P20/145

Abstract: The invention relates to a method and a device for the fluidised-bed roasting and grinding of a load mainly containing a biomass in order to feed the same into a unit for the gasification or combustion of said load.

Abstract translation: 本发明涉及一种用于对主要含有生物质的负载进行流化床焙烧和研磨的方法和设备，以便将其馈送到用于所述负载的气化或燃烧的单元中。

公开(公告)号：WO2022233747A1

公开(公告)日：2022-11-10

申请号：PCT/EP2022/061615

申请日：2022-04-29

Applicant: UCL BUSINESS LTD

Inventor： MATERAZZI, Massimiliano

IPC: C10B47/24 ,  C10B53/00 ,  C10G1/10 ,  C10B57/18 ,  C10B57/02

Abstract: A reactor is described which is useful for the generation of hydrocarbon products by thermochemical treatment. The reactor comprises a feeding means for the addition of feedstock material to the reactor; an outlet for the extraction of hydrocarbon products from the reactor; a devolatilization zone; and a cracking zone; wherein the devolatilization zone comprises a first gas distribution base plate for the generation of a fluidised bed of material in the devolatilization zone, the cracking zone comprises a second gas distribution base plate for the generation of a fluidised bed of material in the cracking zone, and the devolatilization zone is in fluid communication with the cracking zone through a plurality of apertures within the second gas distribution base plate permitting the passage of gas from the devolatilization zone into the cracking zone. Processes of producing hydrocarbon products by thermochemical treatment are also described. The hydrocarbon products may be useful as drop-in fuel products and/or chemical feedstock.