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公开(公告)号：WO2009010157A3
公开(公告)日：2009-04-09
申请号：PCT/EP2008005078
申请日：2008-06-24
Applicant: OUTOTEC OYJ , ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
Inventor： ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
CPC classification number: C10G1/02 , C10B49/22 , C10B53/06 , C10G7/00 , C10G9/00 , C10G2300/4006 , Y02P20/129
Abstract: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil- containing vapor at a temperature of 300 to 1000 °C, - supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500 °C, preferably 1050 to 1200 °C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.
Abstract translation: 为了精炼含油固体，特别是油砂或油页岩，提出了一种具有以下步骤的方法：将含油固体供应到反应器并在300-1000℃的温度下排出含油蒸汽 将在反应器中排出的含油蒸气供应到裂化器中，其中重油组分被分解，分离裂化器中获得的产物并抽出产物流，引入包含未蒸发部分的反应器中残留的固体 的重质烃进入炉中，在600至1500℃，优选1050至1200℃的温度下将留在炉中固体中的重质烃燃烧，将热固体从炉再循环到反应器中，其中氧化气氛 通过阻挡装置将炉与反应器的气氛分离。
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2.发明申请PROCESS AND PLANT FOR THE THERMAL TREATMENT OF PARTICULATE SOLIDS, IN PARTICULAR FOR PRODUCING METAL OXIDE FROM METAL HYDROXIDE 审中-公开用于热处理颗粒状固体的方法和设备，特别是用于从金属氢氧化物生产氧化金属
公开(公告)号：WO2008077462A3
公开(公告)日：2008-09-18
申请号：PCT/EP2007010680
申请日：2007-12-07
Applicant: OUTOTEC OYJ , STROEDER MICHAEL , STOCKHAUSEN WERNER , MISSALLA MICHAEL , SCHNEIDER GUENTER
Inventor： STROEDER MICHAEL , STOCKHAUSEN WERNER , MISSALLA MICHAEL , SCHNEIDER GUENTER
CPC classification number: F23L7/007 , B01J4/002 , B01J8/0055 , B01J8/006 , B01J8/1809 , B01J8/1827 , B01J8/1872 , B01J8/44 , B01J19/26 , B01J2208/00141 , B01J2208/00495 , B01J2208/00504 , B01J2208/0053 , B01J2208/00548 , B01J2208/0069 , B01J2219/00006 , C01B13/18 , C01F7/445 , C22B1/10 , F23C10/10 , Y02E20/344 , Y02P20/129
Abstract: This invention relates to a process for producing e.g. anhydrous metal oxide from metal hydroxide, wherein the metal hydroxide is at least partly dehydrated and preheated, before the metal hydroxide is introduced into a fluidized-bed reactor (19), in which the metal hydroxide is heated to a temperature of about 650 to about 1250°C by combustion of fuel, and metal oxide is generated, wherein primary air and/or secondary air enriched with oxygen is supplied to the fluidized-bed reactor (19). To achieve a rather low dust emission and a small amount of grain disintegration, the oxygen or the gas enriched with oxygen is introduced into the fluidized-bed reactor (19) with a low gas velocity.
Abstract translation: 本发明涉及一种生产方法。 在金属氢氧化物被引入到流化床反应器（19）中之前，金属氢氧化物至少部分脱水和预热，其中金属氢氧化物被加热至约650至约 通过燃料燃烧产生1250℃，产生金属氧化物，其中将一氧化碳和/或二氧化碳的空气供给至流化床反应器（19）。 为了实现相当低的粉尘排放和少量的颗粒分解，将氧气或富氧气体以低气体速度引入流化床反应器（19）。
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公开(公告)号：WO2009010157A8
公开(公告)日：2010-04-22
申请号：PCT/EP2008005078
申请日：2008-06-24
Applicant: OUTOTEC OYJ , ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
Inventor： ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
CPC classification number: C10G1/02 , C10B49/22 , C10B53/06 , C10G7/00 , C10G9/00 , C10G2300/4006 , Y02P20/129
Abstract: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil- containing vapor at a temperature of 300 to 1000 °C, - supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500 °C, preferably 1050 to 1200 °C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.
Abstract translation: 为了精炼含油固体，特别是油砂或油页岩，提出了一种具有以下步骤的方法：将含油固体供应到反应器并在300-1000℃的温度下排出含油蒸汽 将在反应器中排出的含油蒸气供应到裂化器中，其中重油组分被分解，分离裂化器中获得的产物并抽出产物流，引入包含未蒸发部分的反应器中残留的固体 的重质烃进入炉中，在600至1500℃，优选1050至1200℃的温度下将留在炉中固体中的重质烃燃烧，将热固体从炉再循环到反应器中，其中氧化气氛 通过阻挡装置将炉与反应器的气氛分离。
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4.发明申请
公开(公告)号：WO2009100840A3
公开(公告)日：2010-02-25
申请号：PCT/EP2009000729
申请日：2009-02-04
Applicant: OUTOTEC OYJ , ANASTASIJEVIC NIKOLA , MISSALLA MICHAEL , SCHNEIDER GUENTER , ORTH ANDREAS
Inventor： ANASTASIJEVIC NIKOLA , MISSALLA MICHAEL , SCHNEIDER GUENTER , ORTH ANDREAS
CPC classification number: B01J8/1818 , B01J2208/00752 , C10G1/02
Abstract: In accordance with the invention, refining raw materials containing organic constituents, such as solids containing oil and/or bitumen, in particular oil or tar sand or oil shale, is effected with the following steps: - supplying the raw materials to a reactor and expelling fuel gases at a temperature of about 300 to 1000°C, preferably about 500 to 800°C, introducing the solids left in the reactor including the non-evaporated fractions of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500°C, preferably 700 to 900°C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by means of a blocking device.
Abstract translation: 根据本发明，包含含有机油成分的原料，例如含有油和/或沥青的固体，特别是油或焦油砂或油页岩的原料，是通过以下步骤进行的： - 将原料供应到反应器并排出 将温度在约300至1000℃，优选约500至800℃的燃料气体引入包含非蒸发馏分的重质烃的反应器中的固体进入炉中，将残留在固体中的重质烃燃烧 该炉在600至1500℃，优选700至900℃的温度下，将来自炉的热固体再循环到反应器中，其中通过阻塞装置将炉的氧化气氛与反应器的气氛分离 。
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公开(公告)号：EA025146B1
公开(公告)日：2016-11-30
申请号：EA201291250
申请日：2011-05-30
Applicant: OUTOTEC OYJ
Inventor： ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER
Abstract: Изобретениеотноситсяк снижениюсодержанияуглеродав золе, согласнокоторомузолу, содержаниеуглеродав которойсоставляетот 1 до 20 мас.%, вводятв реактори сжигаютв реакторепритемпературах, составляющихот 700 до 1100°С. Вовремясжиганияв реакторнаправляютмикроволновоеизлучениеи, поменьшеймере, частичнорекуперируютэнергию, высвобождаемуювовремясжигания.
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Patent Agency Ranking
公开(公告)号：CA2692571C
公开(公告)日：2015-08-11
申请号：CA2692571
申请日：2008-06-24
Applicant: OUTOTEC OYJ
Inventor： ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
Abstract: For refining oil-containing solids, in particular oil sand or oil shale, there is proposed a process with the following steps: supplying the oil-containing solids to a reactor and expelling an oil-containing vapor at a temperature of 300 to 1000 °C, - -supplying the oil-containing vapor expelled in the reactor to a cracker, in which the heavy oil components are broken down, separating the products obtained in the cracker and withdrawing the product streams, introducing the solids left in the reactor including the unevaporated fraction of heavy hydrocarbons into a furnace, burning the heavy hydrocarbons left in the solids in the furnace at a temperature of 600 to 1500 °C, preferably 1050 to 1200 °C, recirculating hot solids from the furnace into the reactor, wherein the oxidizing atmosphere of the furnace is separated from the atmosphere of the reactor by a blocking device.
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公开(公告)号：BRPI0814237A2
公开(公告)日：2015-01-06
申请号：BRPI0814237
申请日：2008-06-24
Applicant: OUTOTEC OYJ
Inventor： ANASTASIJEVIC NIKOLA , SCHNEIDER GUENTER , MISSALLA MICHAEL
Abstract: The solids (1) are heated in a reactor (6) to 300-1000[deg] C, to drive off an oil-containing vapor, which is sent to a cracker (9). There, heavy oil components are cracked. Products held in the cracker are separated and the product vapor stream is drawn off. Solids from the reactor, together with the non-vaporized fraction, are sent to a furnace (12). Here, residual heavy hydrocarbons are burned-off at 1050-1200[deg] C. Hot solids from the furnace are recycled (15) into the reactor, whilst excluding the oxidizing atmosphere of the furnace. An independent claim IS INCLUDED FOR corresponding plant.
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公开(公告)号：EA020656B1
公开(公告)日：2014-12-30
申请号：EA201001697
申请日：2009-04-20
Applicant: OUTOTEC OYJ
Inventor： GASAFI EDGAR , SCHNEIDER GUENTER , MISSALLA MICHAEL
Abstract: Притермическойобработкетвердыхмелкозернистыхминеральныхматериалов, вчастностидлякальцинированияглиныилигипса, твердыечастицыпропускаютсячерезфлаш-реактор (5), вкоторомониприводятсяв контактс горячимигазамипритемпературеот 450 до 1500°С, изатемтвердыечастицыматериаловпроходятчерезреактор (7) выдержкипритемпературеот 500 до 890°С, изкоторогоонивыводятсяпоистечениивременипребыванияот 1 до 600 мини принеобходимостинаправляютсянастадиюдальнейшейобработки.
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公开(公告)号：FI20110260A
公开(公告)日：2011-08-09
申请号：FI20110260
申请日：2011-08-09
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , SCHNEIDER GUENTER , JARZEMBOWSKI JAN , SCHMIDBAUER ERWIN
IPC: B01J20060101
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公开(公告)号：DE102006062151A1
公开(公告)日：2008-06-26
申请号：DE102006062151
申请日：2006-12-22
Applicant: OUTOTEC OYJ
Inventor： STROEDER MICHAEL , STOCKHAUSEN WERNER , MISSALLA MICHAEL , SCHNEIDER GUENTER
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