公开(公告)号：WO1985001953A1

公开(公告)日：1985-05-09

申请号：PCT/EP1984000325

申请日：1984-10-24

Applicant: FIRMA CARL STILL GMBH & CO. KG ,  STALHERM, Dieter ,  HAACK, Reimer ,  STEWEN, Wilhelm ,  LUKASZEWICZ, Helmut

Inventor： FIRMA CARL STILL GMBH & CO. KG

IPC: C10B39/18

CPC classification number: C10B39/18

Abstract: The present invention enables to detect and record the coke temperature throughout the surface of the drawing ramp (1) by means of temperature sensors (3) mounted above the ramp and, when portions of coke which are too hot are discovered, to automatically and over the shortest possible duration only on those hot portions by using a concentrated water jet.

Abstract translation: 本发明能够通过安装在斜坡上方的温度传感器（3）和当发现太热的焦炭部分自动地和超过这一点，来检测和记录整个拉伸斜坡（1）表面的焦炭温度 通过使用浓缩水射流，在这些热部分上的最短持续时间。

公开(公告)号：WO1989007636A1

公开(公告)日：1989-08-24

申请号：PCT/EP1989000093

申请日：1989-02-02

Applicant: STILL OTTO GMBH ,  STALHERM, Dieter ,  TIPPMER, Kurt ,  LOHMANN, Dieter

Inventor： STILL OTTO GMBH

IPC: C10B39/04

CPC classification number: C02F1/441 ,  B01D61/022 ,  B01D61/04 ,  B01D2311/04 ,  C10B39/00 ,  C10J3/02 ,  C10J2300/169 ,  C10J2300/1884 ,  B01D2311/106 ,  B01D2311/25 ,  B01D2311/2649 ,  B01D2311/2669

Abstract: In a process for treating coal pyrolysis effluent, the effluent is filtered (6, 10), distilled (13) and separated by reverse osmosis (20, 21, 22) into a permeate of low salt concentration which can be recycled to the coking process and a concentrated salt solution. The concentrated salt solution (32) is split either wholly or in part, in a hot reducing atmosphere (41), and the salts separated. According to the invention, the concentrated salt solution is placed, either wholly or in part, in contact with the hot chamber coke in a closed, gasifying, coke cooling stage (50) in order to decompose the noxious substances in said salt solution and to utilize the oxygen fraction by the formation of oxygen and carbon monoxide.

公开(公告)号：WO1988003549A1

公开(公告)日：1988-05-19

申请号：PCT/EP1987000693

申请日：1987-11-09

Applicant: STILL OTTO GMBH ,  LORENZ, Kurt ,  STALHERM, Dieter ,  DUNGS, Horst ,  SCHUMACHER, Werner ,  BRINKMANN, Willi

Inventor： STILL OTTO GMBH

IPC: C10B39/00

CPC classification number: C10B39/00 ,  C10B39/02 ,  C10B39/04

Abstract: A process for the cooling of and the removal of dust from high-temperature coke in at least two stages, whereby the coke is cooled in the first stage to less than about 800 DEG C. In this first cooling stage (1), the coke is cooled to a temperature of between 200 DEG and 800 DEG C, and preferably to between about 400 and 650 DEG C; it is then quickly and continuously drawn through a water bath (8), after which it is held in the steam-laden atmosphere of a sealed re-evaporation chamber (14).

Abstract translation: 一种在至少两个阶段中从高温焦炭冷却和除去灰尘的方法，其中焦炭在第一阶段被冷却至小于约800℃。在该第一冷却阶段（1）中，焦炭 冷却至200〜800℃，优选为400〜650℃左右; 然后将其快速连续地通过水浴（8），然后将其保持在密封的再蒸发室（14）的蒸汽充满的气氛中。

公开(公告)号：WO1989004730A1

公开(公告)日：1989-06-01

申请号：PCT/EP1988001043

申请日：1988-11-17

Applicant: STILL OTTO GMBH ,  STALHERM, Dieter ,  DUNGS, Horst ,  HOLLENHORST, Dieter ,  TARON, Herbert

Inventor： STILL OTTO GMBH

IPC: B09B05/00

CPC classification number: F23G5/20 ,  B09C1/06 ,  F23G5/0273 ,  F23G7/14 ,  F23G2201/50

Abstract: In a process for thermal treatment of contaminated bulk materials in a calcination step in order to dispose of or remove toxic comonents, the gases containing the toxic substances which are evolved during the calcination step are evacuated to atmosphere after a final purification step. The invention also concerns a device for implementing the process. The calcination of contaminated bulk materials is carried out in an indirectly and/or directly heated and in particular continuously operated vertical shaft oven (3).

Abstract translation: 在煅烧步骤中用于热处理污染的散装材料以处置或去除有毒的共聚物的过程中，在最终纯化步骤之后将含有在焙烧步骤中放出的有毒物质的气体抽空至大气中。 本发明还涉及用于实现该过程的装置。 污染的散装材料的煅烧是在间接和/或直接加热的，特别是连续操作的立式竖炉（3）中进行的。

公开(公告)号：WO1988004681A1

公开(公告)日：1988-06-30

申请号：PCT/EP1987000798

申请日：1987-12-18

Applicant: BERGWERKSVERBAND GMBH ,  NASHAN, Gerd ,  WESSIEPE, Klaus ,  BERTLING, Heribert ,  ROHDE, Wolfgang ,  BLASE, Manfred ,  GALOW, Manfred ,  KOCHANSKI, Ulrich ,  DÜRSELEN, Heinz ,  JANICKA, Johannes ,  STALHERM, Dieter ,  HOITZ, Joachim ,  TIETZE, Jürgen ,  SCHUMACHER, Ralf

Inventor： BERGWERKSVERBAND GMBH

IPC: C10B05/02

CPC classification number: C10B5/10 ,  C10B5/02 ,  Y02P20/129

Abstract: In a coking system, charges of carbonizing mixtures, in particular on the basis of hard coal, are supplied to a reactor (1) indirectly heated by heat recovery in regenerators (I, II) or recuperators. The reactor is a large volume coking reactor (100), several large volume coking reactors are gathered in a reactor block and the large volume coking reactors form each an independent module. Each module can be operated and if necessary exchanged independently from its adjacent modules, with little or no interference with the operation of the adjacent modules. The individual reactors can be statically and thermally operated independently from each other. The regenerators or recuperators (I, II, R, R') can be arranged next to or below the reactor chamber. Adjacent reactors can share a common separating wall (2).

公开(公告)号：WO1995019405A1

公开(公告)日：1995-07-20

申请号：PCT/EP1995000125

申请日：1995-01-13

Applicant: THYSSEN STILL OTTO ANLAGENTECHNIK GMBH ,  STALHERM, Dieter ,  OFFERMANN, Ludwig ,  SCHUMACHER, Ralf ,  VOGEL, Werner ,  LANGE, Georg ,  NASHAN, Gerd ,  GUDENAU, Heinrich, Wilhelm ,  HEDDEN, Kurt ,  WESSIEPE, Klaus

Inventor： THYSSEN STILL OTTO ANLAGENTECHNIK GMBH

IPC: C10B57/18

CPC classification number: C10B5/02 ,  C10B27/00 ,  C10B57/18

Abstract: A process is disclosed for treating crude coking gas at high temperatures. Coal charges are coked in a large-capacity coking reactor or in a conventional battery of multiple-earth coke ovens, and the thus obtained crude gas is subjected to a high temperature treatment. The resulting crude cracked gas replaces conventional coke oven gas as an ecological source of energy or may be used as reduction gas for ore reduction. Also disclosed is a device for carrying out the process. This process should permanently improve the economic and ecological situation of coking plants associated to steel works. The high temperature treatment is integrated into the coking system and carried out at temperatures above 800 DEG C, preferably from 900 to 1300 DEG C, with admixture of the required amount of oxidising agent within the coking chamber and/or the hot area of the oven block.

Abstract translation: 本发明涉及用于高温处理Verkokungsrohgas的过程中，所述进料煤在一个Grossraumverkokungsreaktor或常规Vielkammerkoksofenbatterie焦化和对原料气体以高温处理如此获得，从而顶替获得Rohspaltgas生态能源，传统的焦炉煤气或供给作为矿石还原的还原性气体， 和用于执行该方法的装置。 通过这种方法，在复合材料的焦化厂的经济和环境状况的持续改善与冶金设备来实现。 的高温处理实现作为焦化的在温度高于800℃，优选900-1300℃的一个组成部分，在添加碳化室中和/或炉块的热区内氧化剂按需量的。

公开(公告)号：WO1990014408A1

公开(公告)日：1990-11-29

申请号：PCT/EP1990000838

申请日：1990-05-23

Applicant: DIDIER OFU ENGINEERING GMBH ,  KRUPP KOPPERS GMBH ,  STILL OTTO GMBH ,  BLASE, Manfred ,  KOCHANSKI, Ulrich ,  WAGENER, Dietrich ,  MEYER, Günther ,  DÜRSELEN, Heinz ,  STALHERM, Dieter ,  HOITZ, Joachim ,  OFFERMANN, Ludwig ,  TIETZE, Jürgen

Inventor： DIDIER OFU ENGINEERING GMBH ,  KRUPP KOPPERS GMBH ,  STILL OTTO GMBH

IPC: C10B21/20

CPC classification number: C10B21/22 ,  Y02P20/129

Abstract: Heating system for regenerative coke oven batteries heatable with rich, and/or lean or mixed gas, comprising vertical flues grouped in pairs connected to regenerators for preheating the air or, in lean gas operation, the lean gas or mixed gas. The invention comprises a combination of the following features: a) The combustion air is introduced through outlet openings arranged at at least three different heights in each flue. One outlet opening at the base of the flow is connected directly to the regenerators and the outlet openings arranged above the first are connected to the regenerators via hollow connecting passages arranged in the connecting walls or via separate passages. b) The regenerators for preheating the air are divided in the longitudinal direction of the oven. One part is connected to the outlet openings at the base of the flue, the other part is connected to the hollow connecting passages or to the separate passages, and the volumes of air for the two parts can be adjusted separately from outside. c) The outlet openings above the bottom of the flue are provided with externally adjustable sliding blocks for adjusting the distribution of air. d) Closable openings (cross-flow openings) which direct the internal flue gas flow are arranged at the base of the flue in the connecting wall between the upward-conducting and downward-conducting flues.

Abstract translation: 用于可再生焦炉电池的加热系统，其可用富含和/或贫或混合气体加热，包括成对连接的成对连接到再生器的垂直烟道，用于预热空气，或者在贫气操作中，将贫气或混合气体连接。 本发明包括以下特征的组合：a）燃烧空气通过布置在每个烟道中的至少三个不同高度的出口开口引入。 在流动底部的一个出口开口直接连接到再生器，并且布置在第一个上方的出口开口通过布置在连接壁中或通过单独通道的中空连接通道连接到再生器。 b）用于预热空气的再生器沿烘箱的纵向分开。 一部分连接到烟道底部的出口，另一部分连接到中空连接通道或分离通道，两部分空气的体积可以与外面分开调节。 c）烟道底部上方的出口开口设有可调节空气分配的外部可调滑块。 d）引导内部烟气流动的封闭开口（横流开口）布置在烟道底部的向上和向下导流的烟道之间的连接壁中。

公开(公告)号：WO1988004682A1

公开(公告)日：1988-06-30

申请号：PCT/EP1987000799

申请日：1987-12-18

Applicant: BERGWERKSVERBAND GMBH ,  NASHAN, Gerd ,  WESSIEPE, Klaus ,  BERTLING, Heribert ,  ROHDE, Wolfgang ,  BLASE, Manfred ,  GALOW, Manfred ,  KOCHANSKI, Ulrich ,  DÜRSELEN, Heinz ,  JANICKA, Johannes ,  STALHERM, Dieter ,  HOITZ, Joachim ,  TIETZE, Jürgen ,  SCHUMACHER, Ralf

Inventor： BERGWERKSVERBAND GMBH

IPC: C10B05/02

CPC classification number: C10B5/10 ,  C10B5/02 ,  Y02P20/129

Abstract: In a coking system, charges of carbonising mixtures, in particular on the basis of hard coal, are supplied to a reactor (1) indirectly heated by heat recovery in regenerators (I, II) or recuperators. The reactor is a large-volume coking reactor (100), several large volume coking reactors are gathered in a reactor block and the large volume coking reactors form independent modules. Each module can be operated and if necessary exchanged independently from its adjacent modules, with little or no interference with the operation of the adjacent modules. The individual reactors can be statically and thermally operated independently of each other. The regenerators or recuperators (I, II, R, R') can be arranged next to or below the reactor chamber. Adjacent reactors can share a common separating wall (2).

Abstract translation: 在焦化系统中，特别是基于硬煤的碳化混合物的装料被供给到通过再生器（I，II）或换热器中的热回收间接加热的反应器（1）。 反应器是大容量焦化反应器（100），几个大体积的焦化反应器聚集在反应器块中，大体积的焦化反应器形成独立的模块。 每个模块可以被操作，如果必要的话，与其相邻的模块相互独立地交换，对相邻模块的操作几乎没有干扰。 各个反应器可以彼此独立地静态和热操作。 再生器或再生器（I，II，R，R'）可以布置在反应室旁边或下方。 相邻的反应器可以共享一个共同的隔离墙（2）。