公开(公告)号：US10160912B2

公开(公告)日：2018-12-25

申请号：US14465902

申请日：2014-08-22

申请人： PHILLIPS 66 COMPANY

发明人： Johnathan T. Gorke ,  Edgar Lotero

IPC分类号： C10G1/00 ,  C10G3/00 ,  C10B49/00 ,  C10G65/12 ,  C10B49/16 ,  C10B53/02

摘要： This disclosure relates to the fast pyrolysis of organic matter. More specifically, it relates to the catalytic modification of vapors created during the fast pyrolysis of organic matter to create transportation fuel or a transportation fuel component. At least a first portion of pyrolysis vapors is catalytically stabilized or converted, then combined with a portion of raw, unconverted bio-derived pyrolysis vapors at a temperature and pressure sufficient for molecules of the combined vapors to react and produce hydrocarbons of increased molecular weight that are suitable for use as a hydrocarbon transportation fuel or component thereof.

公开(公告)号：US09475031B2

公开(公告)日：2016-10-25

申请号：US14599020

申请日：2015-01-16

申请人： Biogenic Reagents Ventures, LLC

发明人： James A. Mennell ,  Daniel J. Despen ,  David Reamer

IPC分类号： C01B31/00 ,  C01B31/08 ,  C01B31/10 ,  B01J19/00 ,  B01J19/24 ,  B01J20/20 ,  B01J20/30 ,  B01J20/02 ,  C10B49/00 ,  C10B49/02 ,  C10B53/00 ,  C10B53/02

CPC分类号： B01J20/20 ,  B01J20/3078 ,  B01J2219/00013 ,  B01J2219/24 ,  C01B32/30 ,  C01B32/324 ,  C01B32/336 ,  C01B32/39 ,  C01B32/50 ,  C10B49/02 ,  C10B53/02 ,  Y02C10/08 ,  Y02E50/32 ,  Y02P20/136 ,  Y02P20/145

摘要： The present disclosure provides biorefining systems for co-producing activated carbon along with primary products. A host plant converts a feedstock comprising biomass into primary products and carbon-containing co-products; a modular reactor system pyrolyzes and activates the co-products, to generate activated carbon and pyrolysis off-gas; and an oxidation unit oxidizes the pyrolysis off-gas, generating CO2, H2O, and energy. The energy is recycled and utilized in the host plant, and the CO2 and H2O may be recycled to the reactor system as an activation agent. The host plant may be a saw mill, a pulp and paper plant, a corn wet or dry mill, a sugar production facility, or a food or beverage plant, for example. In some embodiments, the activated carbon is utilized at the host plant to purify one or more primary products, to purify water, to treat a liquid waste stream, and/or to treat a vapor waste stream.

摘要翻译： 本公开提供了与初级产物一起共同生产活性炭的生物精制系统。 宿主植物将包含生物质的原料转化成初级产物和含碳共同产物; 模块化反应器系统热解和激活副产物，产生活性炭和热解废气; 并且氧化单元氧化裂解废气，产生CO 2，H 2 O和能量。 该能量被再循环并在宿主植物中使用，并且CO 2和H 2 O可以作为活化剂再循环到反应器系统中。 主机厂可以是例如锯木厂，纸浆和造纸厂，玉米湿法或干磨机，糖生产设备或食品或饮料厂。 在一些实施方案中，活性炭在宿主植物中用于纯化一种或多种初级产物，净化水，处理液体废物流和/或处理蒸汽废物流。

公开(公告)号：US08312821B2

公开(公告)日：2012-11-20

申请号：US12304254

申请日：2006-11-02

申请人： Yeong Min Jeon

发明人： Yeong Min Jeon

IPC分类号： C10B49/00 ,  F23G5/027

CPC分类号： C08J11/12 ,  B29B17/02 ,  B29B2017/0496 ,  B29L2030/00 ,  C10B1/04 ,  C10B49/02 ,  C10B53/07 ,  C10G1/10 ,  C10G2300/1003 ,  Y02E20/12 ,  Y02P20/143 ,  Y02W30/622 ,  Y02W30/625 ,  Y02W30/703

摘要： Disclosed is a system for recycling waste tires, which are industrial wastes, so as to protect our environment against pollution and promote recycling of industrial material. The waste-tire recycling system includes a pyrolyzing unit for pyrolyzing a waste tire by using a pyrolysis reactor, in which a CO or N gas circulates as a carrier gas, a decomposed residue processing unit for crushing a decomposed residue pyrolyzed by the pyrolysis reactor to separate the decomposed residue into carbon and an iron core, an oil collecting unit for cooling and condensing an exhaust gas discharged from the pyrolysis reactor to recover heavy oil from the gas, a carbon processing unit for supplying a heat source to the circulating carrier gas by using a hot exhaust gas generated when the carbon separated from the decomposed residue is burned up, and operating a steam turbine and an absorption refrigerator to generate electricity and cold water, an exhaust gas processing unit for clarifying the exhaust gas discharged from the carbon processing unit to discharge the clarified gas in an atmosphere, and recovering a part of the CO or N gas from the exhaust gas.

摘要翻译： 公开了一种废旧轮胎回收系统，废轮胎是工业废物，以保护我们的环境免受污染，促进工业材料的回收利用。 废轮胎回收系统包括热解单元，用于通过使用其中CO或N气体作为载气循环的热解反应器来热解废轮胎，用于将由热解反应器热分解的分解残渣粉碎的分解残渣处理单元 将分解的残渣分离成碳和铁芯，用于冷却和冷凝从热解反应器排出的废气以从气体中回收重油的油收集单元，用于通过以下方式向循环载气提供热源的碳处理单元 使用从分解残渣中分离出的碳被燃烧时产生的热废气，并操作蒸汽轮机和吸收式冰箱以发电和冷水;废气处理单元，用于净化从碳处理单元排出的排气 在气氛中排出澄清气体，并从废气中回收一部分CO或N气体。

公开(公告)号：US07959765B2

公开(公告)日：2011-06-14

申请号：US12026993

申请日：2008-02-06

申请人： Dimitris Argyropoulos

发明人： Dimitris Argyropoulos

IPC分类号： C10B49/00 ,  C10G1/00

CPC分类号： C10B53/02 ,  C07H19/01 ,  C08B1/003 ,  C08H8/00 ,  C08L97/005 ,  C08L97/02 ,  C10B49/14 ,  C10G1/02 ,  C10G1/08 ,  Y02E50/14

摘要： Methods for the thermolysis of lignocellulosic materials, such as wood, cellulose, lignin, and lignocellulose are provided. Some methods comprise combining the lignocellulosic material with an ionic liquid and subjecting the mixture of the lignocellulosic material and the ionic media to thermolysis conditions to form a recoverable product, such as a commodity chemical.

摘要翻译： 提供木质纤维素材料如木材，纤维素，木质素和木质纤维素的热解的方法。 一些方法包括将木质纤维素材料与离子液体组合，并使木质纤维素材料和离子介质的混合物经受热解条件以形成可回收产品，例如商品化学品。

公开(公告)号：US20100247730A1

公开(公告)日：2010-09-30

申请号：US12794178

申请日：2010-06-04

申请人： Pierre HOLZSCHUH ,  Georg Buch ,  Jean-Jacques Weiland

发明人： Pierre HOLZSCHUH ,  Georg Buch ,  Jean-Jacques Weiland

IPC分类号： A23L1/232 ,  C10B49/00

CPC分类号： A23B4/044 ,  A23B4/0523

摘要： The present invention relates to the field of the production of smoke for agro-food usage and has for its object a process characterized in that it includes essentially the steps consisting in introducing organic material to be pyrolyzed into a reactor including essentially a substantially hermetically sealed heatable chamber containing at least one rotatable endless screw heated by the Joule effect receiving the material, heating the organic material to a temperature included between 200° C. and 800° C., preferably between 300° C. and 400° C., so as to cause the pyrolysis during its movement, under the influence of the rotation of the at least one screw and to extract the consumed material and the smoke products from the chamber.

摘要翻译： 本发明涉及用于农业食品使用的烟的生产领域，并且其目的是一个方法，其特征在于其基本上包括将要热解的有机材料引入反应器中的步骤，该反应器基本上包括基本上气密密封的可加热 包含至少一个由接收材料的焦耳效应加热的可旋转环形螺杆，将有机材料加热到包含在200℃和800℃之间的温度，优选在300℃和400℃之间，以便 在其运动期间在至少一个螺杆的旋转的影响下引起热分解，并从室中提取消耗的材料和烟产品。

公开(公告)号：US07645362B2

公开(公告)日：2010-01-12

申请号：US10938266

申请日：2004-09-10

申请人： Kenji Kato ,  Yukihiro Kubota ,  Takashi Arima ,  Masaki Sasaki ,  Makoto Matsuura ,  Hiroki Nakai

发明人： Kenji Kato ,  Yukihiro Kubota ,  Takashi Arima ,  Masaki Sasaki ,  Makoto Matsuura ,  Hiroki Nakai

IPC分类号： C10G1/00 ,  C10L5/00 ,  C10B49/00 ,  C10B53/00 ,  C10B55/00

CPC分类号： C10L5/04 ,  C10B57/005 ,  C10L9/08

摘要： Methods for pretreating and improving coking coal quality for producing blast-furnace coke by: (a) rapid-heating the coal charge in a fluidized-bed to a temperature range between not lower than 300° C. and not higher than the temperature at which the coal charge begins to soften, at a rate of 30 to 103 ° C./min., (b) classifying the rapid-heated coal charge to fine- and coarse-size coal, and then (c-1) briquetting the fine-size coal or (c-2) rapid-heating the fine- and coarse-size coal individually in a pneumatic preheater to a temperature range between not lower than 300° C. and not higher than the temperature at which the coal charge begins to soften, at a rate of 103 to 105 ° C./min., and (d) forming the fine-size coal.

摘要翻译： 用于预处理和提高生产高炉焦炭的焦煤质量的方法：（a）将流化床中的煤料快速加热到不低于300℃的温度，并且不高于 煤电费以30〜103℃/分钟的速度开始软化，（b）将快速加热的煤炭分类为细煤和粗煤，然后（c-1）将煤粉压块 将煤或（c-2）煤或（c-2）在气动预热器中单独快速加热到不低于300℃的温度范围，并且不高于煤开始温度的温度 以103〜105℃/分钟的速度软化，（d）形成细小的煤。

公开(公告)号：US20060076224A1

公开(公告)日：2006-04-13

申请号：US11220880

申请日：2005-09-07

申请人： Jae Ku

发明人： Jae Ku

IPC分类号： C10B49/00 ,  C10B51/00 ,  C10B35/00

CPC分类号： C10B47/44 ,  C10B53/07 ,  C10G1/10 ,  Y02P20/143

摘要： Disclosed is a successive pyrolysis system of waste synthetic-highly polymerized compound for successively pyrolizing combustible waste by indirect heating at a pyrolysis chamber maintaining an anaerobic or hypoxic environment, and producing refined oil like heavy oil and light oil according to boiling points at a distillation column to be used as heat source for the pyrolysis of the waste. The successive pyrolysis system comprises a hopper; an automatic waste injection device, which discharges a predetermined amount of waste from the hopper; a pyrolysis chamber for maintaining a high-temperature and hypoxic environment, and successively pyrolizing the waste by indirect heating; a gas burning chamber for burning noncondensable gas among pyrolysis gas produced at the time of the pyrolysis of the waste, and providing heat of a predetermined temperature to the outer surface of the pyrolysis chamber to be used as heat source for the pyrolysis of the waste; a refined oil producing means for producing refined oil from the pyrolysis gas reformed after going through catalyst reaction and providing residual noncondensable gas to the gas burning chamber; and an automatic discharging device for successively discharging ashes transported after being pyrolized from the pyrolysis chamber.

摘要翻译： 公开了一种废合成高分子化合物的连续热解系统，用于通过在保持厌氧或缺氧环境的热解室内间接加热连续地热解可燃废物，并根据蒸馏塔的沸点生产精炼油如重油和轻油 用作废物热解的热源。 连续的热解系统包括料斗; 自动废物注入装置，其从料斗排出预定量的废物; 用于维持高温和低氧环境的热解室，并通过间接加热连续热解废物; 用于在废物热分解时产生的裂解气中燃烧不凝气体的气体燃烧室，并将预定温度的热量提供给热解室的外表面以用作废物热解的热源; 一种精炼油生产装置，用于在通过催化剂反应重整后的裂解气中生产精制油，并向气体燃烧室提供残留的不凝气体; 以及自动排出装置，用于在从热解室中进行热解后连续排出输送的灰分。

公开(公告)号：US6126705A

公开(公告)日：2000-10-03

申请号：US171131

申请日：1998-10-13

申请人： Murray Howard Pryor ,  Jeremy James Lees

发明人： Murray Howard Pryor ,  Jeremy James Lees

IPC分类号： B03B9/00 ,  C10B47/00 ,  C10B49/00 ,  C10L9/00 ,  C10L9/08 ,  C10L5/00

CPC分类号： B03B9/005 ,  C10B47/00 ,  C10B49/00 ,  C10L9/00 ,  C10L9/08

摘要： A process for the recovery of coal particles from coal tailings is described. The process comprises the steps of initially treating the coal tailings to separate therefrom a proportion of the coal particles having sizes in a specified range, and then subjecting the coal particles to a heat treatment process. In one embodiment, the separated coal particles can undergo an agglomeration in oil prior to the heat treatment. The process provides a further means of recovering coal particles of certain sizes from slurries.

摘要翻译： PCT No.PCT / AU97 / 00226 Sec。 371日期：1998年10月13日 102（e）日期1998年10月13日PCT 1997年4月10日PCT PCT。 公开号WO97 / 38064 日期1997年10月16日描述了从煤尾矿回收煤颗粒的方法。 该方法包括以下步骤：首先处理煤尾矿以分离尺寸在规定范围内的一部分煤颗粒，然后对煤颗粒进行热处理。 在一个实施方案中，分离的煤颗粒在热处理之前可以在油中发生聚集。 该方法提供了从浆料中回收某些尺寸的煤颗粒的另一种方法。

公开(公告)号：US4523979A

公开(公告)日：1985-06-18

申请号：US569237

申请日：1984-01-09

申请人： Roland F. Deering ,  John H. Duir

发明人： Roland F. Deering ,  John H. Duir

IPC分类号： C10G1/02 ,  C10B49/00

CPC分类号： C10G1/02

摘要： Retorted shale particles are recovered from a retort and delivered to a gas lift for transport to a fluidized combustor by passage, serially, through a sealing vessel, a crusher preferably operating at retort pressure, and a surge vessel. In the sealing vessel, a sealing gas is introduced, and after commingling with the shale, the gas passes countercurrently to the shale and enters the retort, thus sealing the retort gases in the retort while separating the retorted shale from the retort gases. Retorted shale from the sealing vessel is transported to a crusher, wherein the shale is reduced in size to that suitable for combustion under fluidized conditions. To prevent the crushed shale from packing, the shale is passed to a surge vessel, wherein the crushed shale is held as a fluidized bed, from which the crushed shale is continuously withdrawn at a regulated rate and introduced into the gas lift leading to the fluidized combustor.

摘要翻译： 蒸馏页岩颗粒从蒸馏器中回收并输送到气举，以通过连续通过密封容器，优选在蒸煮压力下运行的破碎机和喘振容器通过流化燃烧器。 在密封容器中，引入密封气体，在与页岩混合之后，气体逆流地流入页岩并进入蒸馏器，从而将蒸馏的气体密封在蒸馏器中，同时将蒸馏页岩与蒸馏气体分离。 来自密封容器的蒸馏页岩被输送到破碎机，其中页岩​​尺寸减小到在流化条件下适合燃烧的页岩。 为了防止粉碎的页岩进行包装，页岩被传送到冲击容器，其中被粉碎的页岩被保持为流化床，从而从此从碎石页岩以规定的速率连续地取出页岩，并引入到通向流化床 燃烧器。

公开(公告)号：US4427529A

公开(公告)日：1984-01-24

申请号：US360064

申请日：1982-03-22

申请人： Hiroaki Nishio

发明人： Hiroaki Nishio

IPC分类号： C10B53/06 ,  C10G1/00 ,  C10G1/02 ,  C10G51/00 ,  C10B49/00 ,  C10B53/00

CPC分类号： C10G1/02

摘要： A method for distilling shale oil from oil shale, which comprises: supplying an oil shale together with a granular heat medium heated to a prescribed temperature in a heating furnace to a distiling furnace, where a gas containing a gaseous shale oil, hydrogen and carbon monoxide is separated by vaporization from said oil shale through heat exchange with said granular heat medium; separating the liquid shale oil from said gas, separating said granular heat medium from the waste oil shale after separation of said gas; and then, feeding back said granular heat medium into said heating furnace to reheat said heat medium again to said prescribed temperature and to use said heat medium in recycle. In said method, said granular heat medium comprises manganese oxides and iron oxides. The heat of said granular heat medium is replenished with the heat produced by exothermic reaction of said hydrogen and said carbon monoxide contained in said gas with Mn.sub.2 O.sub.3 contained in said granular heat medium and reducing by means of said hydrogen and said carbon monoxide contained in said gas, Fe.sub.2 O.sub.3 contained in said granular heat medium into Fe.sub.3 O.sub.4 and Fe to impart magnetism to said granular heat medium; and, magnetically separating said granular heat medium from said waste oil shale.

摘要翻译： 一种用于从油页岩中蒸馏页岩油的方法，包括：将油页岩与加热炉中加热到规定温度的颗粒状热介质一起供给到蒸馏炉，其中含有气态页岩油，氢气和一氧化碳 通过与所述颗粒状热介质的热交换从所述油页岩中蒸发而分离; 将液体页岩油与所述气体分离，在分离所述气体之后将所述颗粒状热介质与废油页岩分离; 然后将所述颗粒状热介质反馈到所述加热炉中，以再次将所述热介质再次加热到所述规定温度，并使用所述热介质进行再循环。 在所述方法中，所述粒状热介质包括氧化锰和氧化铁。 所述颗粒状热介质的热量由所述氢气和所述气体中所含的一氧化碳与所述颗粒状热介质中所含的Mn 2 O 3的放热反应产生的热量补充，并通过所述氢气和所述气体中所含的一氧化碳还原 ，所述粒状热介质中含有Fe 2 O 3，Fe 3 O 4和Fe，赋予所述粒状热介质磁性; 并且从所述废油页岩磁分离所述颗粒状热介质。