公开(公告)号：WO2005080640A2

公开(公告)日：2005-09-01

申请号：PCT/EP2005/001127

申请日：2005-02-04

Applicant: OUTOKUMPU OYJ ,  ANASTASIJEVIC, Nikola ,  NEPPER, Jean-Paul ,  KOENEKE, Martin ,  LOHRBERG, Dirk ,  MARTTILA, Tom ,  VIRTANEN, Henri

Inventor： ANASTASIJEVIC, Nikola ,  NEPPER, Jean-Paul ,  KOENEKE, Martin ,  LOHRBERG, Dirk ,  MARTTILA, Tom ,  VIRTANEN, Henri

IPC: C25C

CPC classification number: C25C7/06 ,  C25C1/12 ,  C25C7/02

Abstract: The present invention relates to a process for electrochemically winning or refining copper by electrodepositing copper from an electrolyte solution containing the metal in ionogenic form, in which the electrolyte is passed through an electrolysis plant compris­ing at least one electrolytic cell, which in an electrolyte tank for receiving the electrolyte has at least two electrodes serving as anode and cathode, which are alternately ar­ranged at a distance from each other, and to a corresponding plant. To increase the economic efficiency of such processes and plants, it is proposed in accordance with the invention to immerse the at least one cathode during operation of the electrolysis into the electrolyte over a length of at least 1.2 meters.

Abstract translation: 本发明涉及一种通过从含有离子型形式的金属的电解质溶液中电沉积铜来电化学获得或精炼铜的方法，其中电解液通过包含至少一个电解池的电解设备，所述电解设备在电解槽 接收电解质具有至少两个用作阳极和阴极的电极，它们彼此间隔一定距离交替布置，并且连接到相应的工厂。 为了提高这些工艺和设备的经济效率，根据本发明提出，在至少1.2米的长度内将电解操作期间的至少一个阴极浸入电解液中。

公开(公告)号：WO2002101314A1

公开(公告)日：2002-12-19

申请号：PCT/EP2002/005843

申请日：2002-05-28

Applicant: OUTOKUMPU OYJ ,  ANASTASIJEVIC, Nikola ,  DAUM, Karl-Heinz ,  SCHALK, Wolfram ,  LAIBACH, Stefan

Inventor： ANASTASIJEVIC, Nikola ,  DAUM, Karl-Heinz ,  SCHALK, Wolfram ,  LAIBACH, Stefan

IPC: F28F19/00

CPC classification number: F28F19/004 ,  C23F13/005

Abstract: To protect a plate-type heat exchanger (1) against corrosion due to the attack of sulfuric acid, it is proposed in accordance with the invention that the region through which flows sulfuric acid has at least one metal cathode (16, 17) and one reference electrode (27), that at least half the metal plates (7) have an electric contact (23) which is connected with the anode (21) of an electric d.c. voltage source of variable electric voltage, that the metal cathode (16, 17) likewise is electrically connected with the d.c. voltage source, and that the d.c. voltage source belongs to a potentiostat (20) which is electrically connected with the reference electrode (27).

Abstract translation: 为了防止板式热交换器（1）由于硫酸的侵蚀而受到腐蚀，根据本发明提出，流过硫酸的区域具有至少一个金属阴极（16,17）和一个 参考电极（27），至少一半的金属板（7）具有与阳极（21）连接的电气接触件（23） 可变电压的电压源，金属阴极（16,17）同样与直流电连接。 电压源，直流电源。 电压源属于与参考电极（27）电连接的恒电位仪（20）。

公开(公告)号：WO2014040634A1

公开(公告)日：2014-03-20

申请号：PCT/EP2012/068093

申请日：2012-09-14

Applicant: OUTOTEC OYJ ,  SCHAAF, Tanja ,  BINDER, Christian ,  ANASTASIJEVIC, Nikola ,  SCHNEIDER, Günter

Inventor： SCHAAF, Tanja ,  BINDER, Christian ,  ANASTASIJEVIC, Nikola ,  SCHNEIDER, Günter

IPC: C10G1/10 ,  C10B53/07 ,  C10B49/16 ,  C07C4/22 ,  C08J11/12 ,  C10B1/10 ,  C10K1/02

CPC classification number: C10K1/028 ,  C08J11/12 ,  C10B1/10 ,  C10B49/16 ,  C10B53/07 ,  C10G1/086 ,  C10G1/10 ,  C10K1/026 ,  Y02P20/129 ,  Y02P20/143 ,  Y02W30/703

Abstract: Plastic wastes which for at least 80 wt-% contain a polymer or a mixture of polymers from a group including polymethyl methacrylate, polypropylene, polyethylene, polystyrene, polyethylene terephthalate and/or polytetrafluoroethylene, are recycled using the following steps: (i) heating the plastic wastes to a temperature at which they are flowable; (ii) pyrolyzing the flowable plastics together with a catalyst and/or an adsorber and withdrawing the resulting gases; (iii) condensing the gases.

Abstract translation: 含有聚碳酸酯，聚丙烯，聚乙烯，聚苯乙烯，聚对苯二甲酸乙二醇酯和/或聚四氟乙烯的聚合物或聚合物混合物的至少80重量％的塑料废料使用以下步骤再循环：（i） 塑料废物达到可流动的温度; （ii）将可流动塑料与催化剂和/或吸附剂一起热解并抽出所得气体; （iii）冷凝气体。

公开(公告)号：WO2004056467A1

公开(公告)日：2004-07-08

申请号：PCT/EP2003/013163

申请日：2003-11-24

Applicant: OUTOKUMPU OYJ ,  STRÖDER, Michael ,  GERDES, Thorsten ,  WILLERT-PORADA, Monika ,  ANASTASIJEVIC, Nikola

Inventor： STRÖDER, Michael ,  GERDES, Thorsten ,  WILLERT-PORADA, Monika ,  ANASTASIJEVIC, Nikola

IPC: B01J8/42

CPC classification number: H05B6/806 ,  B01J8/1872 ,  B01J8/388 ,  B01J8/42 ,  B01J19/126 ,  B01J2208/00141 ,  B01J2208/00442 ,  B01J2208/00548 ,  B01J2219/1296 ,  C22B1/10 ,  C22B5/14 ,  F26B3/08 ,  F26B3/084 ,  F26B3/343 ,  H05B6/78 ,  H05B6/784

Abstract: This invention relates to a method for the thermal treatment of granular solids in a fluidized-bed reactor (1), in which microwave radiation from a microwave source (2) is fed into the reactor (1), and to a corresponding plant. To improve the utilization of energy and the introduction of the microwave radiation, a first gas or gas mixture is introduced from below through a preferably central gas supply tube (3) into a mixing chamber (7) of the reactor, the gas supply tube (3) being at least partly surrounded by a stationary annular fluidized bed (8) which is fluidized by supplying fluidizing gas. The microwave radiation is supplied to the mixing chamber (7) through the same gas supply tube (3).

Abstract translation: 本发明涉及一种用于热处理流化床反应器（1）中的颗粒状固体的方法，其中将来自微波源（2）的微波辐射送入反应器（1）以及相应的设备。 为了提高能量的利用和引入微波辐射，第一气体或气体混合物从下面通过优选的中心气体供应管（3）引入到反应器的混合室（7）中，气体供应管 3）至少部分地被固定的环形流化床（8）包围，所述固定的环形流化床通过供应流化气体被流化。 微波辐射通过相同的气体供给管（3）供应到混合室（7）。

公开(公告)号：WO2010066316A1

公开(公告)日：2010-06-17

申请号：PCT/EP2009/007620

申请日：2009-10-24

Applicant: OUTOTEC OYJ ,  GASAFI, Edgar ,  ANASTASIJEVIC, Nikola

Inventor： GASAFI, Edgar ,  ANASTASIJEVIC, Nikola

IPC: C04B7/28 ,  C04B7/30

CPC classification number: C04B7/28 ,  C04B7/30 ,  Y02P40/145

Abstract: This invention relates to a process for producing cement or cement substitutes on the basis of carbon-containing compounds with a carbon content of more than 10 wt-%, wherein the carbon-containing compounds are burnt in a furnace at a temperature of 600 to 900°C, and wherein beside the carbon-containing compounds at least one additional, inert and/or low-heating-value material, which already before or after a thermal treatment has cement properties, is introduced into the furnace and calcined.

Abstract translation: 本发明涉及一种基于碳含量大于10重量％的含碳化合物生产水泥或水泥替代物的方法，其中含碳化合物在炉中在600至900℃的温度下燃烧 ℃，并且除了含碳化合物之外，已经在热处理之前或之后具有水泥性质的至少一种另外的惰性和/或低热值材料被引入炉中并煅烧。

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

IPC: C10G1/00 ,  C10B49/22 ,  C10B53/06 ,  C10G1/02

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。

公开(公告)号：WO1998024950A1

公开(公告)日：1998-06-11

申请号：PCT/EP1997006505

申请日：1997-11-21

Applicant: METALLGESELLSCHAFT AKTIENGESELLSCHAFT ,  ANASTASIJEVIC, Nikola ,  LAIBACH, Stefan ,  WERNER, Dietrich ,  NEPPER, Jean-Paul ,  LANGSCHIED, Holger ,  CIESLAK, Heinrich

Inventor： METALLGESELLSCHAFT AKTIENGESELLSCHAFT

IPC: C25C07/02

CPC classification number: C25C7/00 ,  C25B9/063

Abstract: This invention concerns an electrolytic cell equipped with several bipolar electrodes which are connected in series during operation of the cell. Each of the bi-polar electrodes has a cathode side (K7, 8) and an anode side (A7, 8) between which an electrically conducting connection (11, 12) is established during operation. At least one bipolar electrode has a cathode side and an anode side which are displaceable towards one another. In particular, either the cathode side or the anode side can be separated and removed from the electrolyte.

Abstract translation: 电解池配备有多个其在电池工作过程中串联电连接的双极型电极。 每个双极性电极的具有阴极侧（K7，8）和阳极侧（A7，8）之间的导电连接（11，12）的操作期间。 至少一个双极电极具有阴极侧和阳极侧，其相互设计为可移动。 具体地，一个可以分离的阴极侧或阳极侧和从电解质将其拉出。

公开(公告)号：WO2010000383A1

公开(公告)日：2010-01-07

申请号：PCT/EP2009/004271

申请日：2009-06-13

Applicant: OUTOTEC OYJ ,  GASAFI, Edgar ,  SIEWERT, Frank ,  ANASTASIJEVIC, Nikola ,  WERNER, Dietrich

Inventor： GASAFI, Edgar ,  SIEWERT, Frank ,  ANASTASIJEVIC, Nikola ,  WERNER, Dietrich

IPC: C04B33/32

CPC classification number: C04B33/32 ,  F27B7/2033 ,  Y02P40/67

Abstract: The production of calcined clay is effected by using a plant known per se for producing cement by the dry or semiwet process, with a precalciner (1), for instance comprising at least one preheating line of series-connected preheating stages (2), such as cyclone preheaters or grate preheaters, and a rotary kiln or roaster (3). In accordance with the invention, the rotary kiln or roaster (3) for generating heating gas is utilized as combustion chamber (31), replaced by a combustion chamber (3') and/or completed by an additional combustion chamber.

Abstract translation: 煅烧粘土的生产通过使用本身已知的用于通过干法或半湿法生产水泥的设备进行，其中预煅烧器（1）例如包括至少一个串联连接的预热段（2）的预热管线，例如 作为旋风预热器或炉排预热器，以及回转窑或焙烧炉（3）。 根据本发明，用于产生加热气体的回转窑或焙烧炉（3）用作燃烧室（31），由燃烧室（3'）代替和/或由附加的燃烧室完成。

公开(公告)号：WO2009100840A2

公开(公告)日：2009-08-20

申请号：PCT/EP2009/000729

申请日：2009-02-04

Applicant: OUTOTEC OYJ ,  ANASTASIJEVIC, Nikola ,  MISSALLA, Michael ,  SCHNEIDER, Günter ,  ORTH, Andreas

Inventor： ANASTASIJEVIC, Nikola ,  MISSALLA, Michael ,  SCHNEIDER, Günter ,  ORTH, Andreas

IPC: C10B49/16 ,  C10B49/22 ,  C10B53/06 ,  C10G1/00 ,  C10G1/02

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 。

公开(公告)号：WO2009010157A2

公开(公告)日：2009-01-22

申请号：PCT/EP2008/005078

申请日：2008-06-24

Applicant: OUTOTEC OYJ ,  ANASTASIJEVIC, Nikola ,  SCHNEIDER, Günter ,  MISSALLA, Michael

Inventor： ANASTASIJEVIC, Nikola ,  SCHNEIDER, Günter ,  MISSALLA, Michael

IPC: C10G1/00 ,  C10G1/02 ,  C10B49/22 ,  C10B53/06

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: 为了精制含油固体，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中，并将含油蒸气在 温度为300-1000℃， - 将反应器中排出的含油蒸气供给裂解器，其中重油组分被分解，分离裂解器中获得的产物并抽出产物流，引入 固体留在反应器中，包括未经蒸发的重质烃馏分进入炉中，将炉中固体中留下的重质烃在600-1500℃，优选1050-1200℃的温度下燃烧，将热固体从 炉进入反应器，其中炉的氧化气氛通过阻挡装置与反应器的气氛分离。