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公开(公告)号：WO2010083865A3
公开(公告)日：2010-10-21
申请号：PCT/EP2009009115
申请日：2009-12-18
Applicant: OUTOTEC OYJ , MISSALLA MICHAEL , HILTUNEN PEKKA , BLIGH ROGER , SCHMIDBAUER ERWIN , KLETT CORNELIS
Inventor： MISSALLA MICHAEL , HILTUNEN PEKKA , BLIGH ROGER , SCHMIDBAUER ERWIN , KLETT CORNELIS
Abstract: The present invention relates to the production of metal oxide from metal salts, in particular from aluminum hydroxide, wherein the metal salt is preheated in a first preheating stage, precalcined in a second preheating stage and calcined to metal oxide in a fluidized-bed reactor, and wherein the product obtained then is cooled in at least one suspension heat exchanger and subsequently in a multi- stage indirect cooler. To reduce the energy demand of a calcining plant, fluidizing air is supplied to the reactor with a temperature of up to 150 °C, and before entering the first preheating stage the metal salt is at least partly supplied to a hydrate drier in which it is indirectly heated with heat transfer medium from the first stage of the indirect cooler and dried.
Abstract translation: 本发明涉及从金属盐特别是氢氧化铝制备金属氧化物，其中金属盐在第一预热阶段预热，在第二预热阶段预煅烧并在流化床反应器中煅烧成金属氧化物， 并且其中然后获得的产物在至少一个悬浮式热交换器中冷却，随后在多级间接冷却器中冷却。 为了减少煅烧设备的能量需求，将流化空气以高达150℃的温度供给反应器，并且在进入第一预热阶段之前，将金属盐至少部分地供应到水合物干燥器 间接用间接加热的传热介质从第一级的间接冷却器中干燥。
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2.发明申请
公开(公告)号：WO2009100841A2
公开(公告)日：2009-08-20
申请号：PCT/EP2009000730
申请日：2009-02-04
Applicant: OUTOTEC OYJ , SCHMIDBAUER ERWIN
Inventor： SCHMIDBAUER ERWIN
CPC classification number: C10G1/002 , C10B49/22 , C10B53/06 , C10G1/02 , C10G11/05 , C10J3/482 , C10J3/66 , C10J2300/0909 , C10J2300/094 , C10J2300/16 , C10J2300/1606 , C10J2300/1637 , C10K1/02 , C10K3/023 , C10K3/04 , Y02P20/129
Abstract: In accordance with the invention, refining raw materials containing organic constituents, such as raw materials 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 an expulsion stage and expelling a hydrocarbonaceous, in particular oil-containing vapor at a temperature of e.g. about 300 to 1000°C, supplying the hydrocarbonaceous vapor expelled in the expulsion stage and/or in a gasification stage downstream of the expulsion stage to a processing stage, in which the same is further processed e.g. by cracking, coking and/or hydrotreating, separating the products obtained in the processing stage and withdrawing the same, introducing the solids left in the expulsion stage and/or in the gasification stage including the non-evaporated fractions of heavy hydrocarbons into a combustion stage, burning the heavy hydrocarbons left in the solids in the combustion stage at a temperature of e.g. about 600 to 1500°C, preferably e.g. about 1050 to 1200°C, recirculating hot solids from the combustion stage into the expulsion stage and/or the gasification stage, wherein the oxidizing atmosphere of the combustion stage is separated from the atmosphere of the expulsion stage and/or the gasification stage by means of a blocking device, and supplying water into the expulsion stage and/or the gasification stage.
Abstract translation: 根据本发明，用含有油和/或沥青的原料，特别是油或焦油砂或油页岩的含有有机成分的原料进行精制，步骤如下：将原料供应到排出阶段， 在例如温度下排出烃类，特别是含油蒸汽 约300至1000℃，将在排出阶段中排出的烃蒸气和/或在排出阶段下游的气化阶段供应到处理阶段，其中进一步处理该烃蒸气。 通过裂化，焦化和/或加氢处理，分离在处理阶段获得的产物并将其排出，将残留在排出阶段和/或包括非烃蒸馏馏分重质烃的气化阶段中的固体引入燃烧阶段 在例如燃烧阶段燃烧残留在固体中的重质烃 约600至1500℃，优选例如约600至1500℃。 约1050至1200℃，将热固体从燃烧阶段再循环到排出阶段和/或气化阶段，其中燃烧阶段的氧化气氛通过装置与排出阶段和/或气化阶段的气氛分离 的阻塞装置，并且将水供应到排出阶段和/或气化阶段。
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公开(公告)号：CA2745572C
公开(公告)日：2017-06-20
申请号：CA2745572
申请日：2009-12-18
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , HILTUNEN PEKKA , BLIGH ROGER , SCHMIDBAUER ERWIN , KLETT CORNELIS , SCHNEIDER GUENTER
Abstract: The present invention relates to the production of metal oxide from metal salts, in particular from aluminum hydroxide, wherein the metal salt is preheated in a first preheating stage, precalcined in a second preheating stage and calcined to metal oxide in a fluidized-bed reactor, and wherein the product obtained then is cooled in at least one suspension heat exchanger and subsequently in a multi-stage indirect cooler. To reduce the energy demand of a calcining plant, fluidizing air is supplied to the reactor with a temperature of up to 150 °C, and before entering the first preheating stage the metal salt is at least partly supplied to a hydrate dryer in which it is indirectly heated with heat transfer medium from the first stage of the indirect cooler and dried.
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公开(公告)号：GB2478240B
公开(公告)日：2014-04-30
申请号：GB201109904
申请日：2009-12-18
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , HILTUNEN PEKKA , BLIGH ROGER , SCHMIDBAUER ERWIN , KLETT CORNELIS , SCHNEIDER GUNTER
Abstract: A process for producing metal oxide from a metal salt includes supplying a first part of the metal salt to a hydrate drier so as to indirectly heat the first part of the metal salt in the hydrate drier using a heat transfer medium from a first stage of a multi-stage indirect cooler so as to dry the first part of the metal salt in the hydrate drier and so as to control a waste gas temperature of the process. A second part of the metal salt is guided as a partial stream past the hydrate drier. The metal salt is preheated in a first preheating stage and precalcined in a second preheating stage. The metal salt and a fluidizing gas having a temperature of 150° C. or less are supplied to a fluidized bed reactor so as to calcine the metal salt to form a metal oxide product. The metal oxide product is cooled in at least one suspension heat exchanger and then in the multi-stage indirect cooler.
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公开(公告)号：GB2478671B
公开(公告)日：2014-04-09
申请号：GB201109905
申请日：2010-01-14
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , SCHNEIDER GUNTER , JARZEMBOWSKI JAN , SCHMIDBAUER ERWIN
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Patent Agency Ranking
公开(公告)号：AU2008228481B2
公开(公告)日：2013-03-21
申请号：AU2008228481
申请日：2008-03-18
Applicant: OUTOTEC OYJ
Inventor： KLETT CORNELIS , SCHNEIDER GUENTER , MISSALLA MICHAEL , SCHMIDBAUER ERWIN
Abstract: When producing metal oxide from metal salts, the metal salt, in particular aluminum hydroxide, is dried and preheated in a first preheater (2) at a temperature of 100 to 200°C, precalcined in a second preheater (5) at a temperature of 300 to 400°C and then calcined in a reactor (8) at a temperature of 850 to 1100°C to obtain metal oxide, in particular alumina. After precalcination in the second preheater (5), a partial stream of the metal salt is branched off and supplied to a mixing tank (14), in which it is mixed with the metal oxide withdrawn from the reactor (8).
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公开(公告)号：EA016961B1
公开(公告)日：2012-08-30
申请号：EA200901271
申请日：2008-03-18
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , SCHNEIDER GUENTER , KLETT CORNELIS , SCHMIDBAUER ERWIN
Abstract: Описанспособполученияоксидаметаллаизсолейметалла, вчастностигидроксидаалюминия, вкоторомсольметалласушати предварительнонагреваютв первомподогревателе (2) притемпературеот 100 до 200°С, предварительнопрокаливаютвовторомподогревателе (5) притемпературеот 300 до 400°Си затемпрокаливаютв реакторе (8) притемпературеот 850 до 1100°С, получаяоксидметалла, вчастностиоксидалюминия. Послепредварительногопрокаливаниявовторомподогревателе (5) частьпотокасолиметаллаотводятв сторонуи подаютв бак-смеситель (14), вкоторомонсмешиваетсяс оксидомметалла, выводимымизреактора (8).
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公开(公告)号：DE102009006094A1
公开(公告)日：2010-07-29
申请号：DE102009006094
申请日：2009-01-26
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , SCHNEIDER GUENTER , JARZEMBOWSKI JAN , SCHMIDBAUER ERWIN
IPC: C01F7/44
Abstract: Die vorliegende Erfindung betrifft die Herstellung von Metalloxid aus Metallsalzen, insbesondere aus Aluminiumhydroxid, wobei das Metallsalz in einer Trockeneinrichtung getrocknet, in wenigstens einer Vorwärmstufe vorgewärmt und in einem Wirbelschichtreaktor zu Metalloxid kalziniert wird, und wobei das gewonnene Metalloxid dann abgekühlt wird. Um den Energiebedarf einer Kalzinieranlage zu verringern, wird das Metallsalz vor der Trocknung in wenigstens einem Filter gereinigt und in der Trockeneinrichtung gebildeter Dampf in den Filter zurückgeführt.
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公开(公告)号：AU2010206320B2
公开(公告)日：2014-10-09
申请号：AU2010206320
申请日：2010-01-14
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , SCHNEIDER GUNTER , JARZEMBOWSKI JAN , SCHMIDBAUER ERWIN
Abstract: The present invention relates to the production of metal oxide from metal salts, in particular from aluminum hydroxide, wherein the metal salt is dried in a drying means, preheated in at least one preheating stage, and calcined to metal oxide in a fluidized-bed reactor, and wherein the metal oxide obtained then is cooled. To reduce the energy demand of a calcining plant, the metal salt is cleaned in at least one filter before being dried and steam formed in the drying means is recirculated into the filter.
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公开(公告)号：DE102009006095A1
公开(公告)日：2010-07-29
申请号：DE102009006095
申请日：2009-01-26
Applicant: OUTOTEC OYJ
Inventor： MISSALLA MICHAEL , HILTUNEN PEKKA , BLIGH ROGER , SCHMIDBAUER ERWIN , KLETT CORNELIS , SCHNEIDER GUENTER
IPC: C01F7/44
Abstract: Die vorliegende Erfindung betrifft die Herstellung von Metalloxid aus Metallsalzen, insbesondere aus Aluminiumhydroxid, wobei das Metallsalz in einer ersten Vorwärmstufe vorgewärmt, in einer zweiten Vorwärmstufe vorkalziniert und in einem Wirbelschichtreaktor zu Metalloxid kalziniert wird, und wobei das gewonnene Produkt dann in wenigstens einem Suspensionswärmetauscher und anschließend in einem mehrstufigen indirekten Kühler abgekühlt wird. Um den Energiebedarf einer Kalzinieranlage zu verringern, wird dem Reaktor Fluidisierungsluft mit einer Temperatur von bis zu 150°C zugeführt und das Metallsalz vor dem Eintritt in die erste Vorwärmstufe wenigstens teilweise einem Hydrattrockner zugeführt, in welchem es mit Wärmeträgermedium aus der ersten Stufe des indirekten Kühlers indirekt erwärmt und getrocknet wird.
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