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公开(公告)号：US4990220A
公开(公告)日：1991-02-05
申请号：US399527
申请日：1989-08-22
Applicant: Gerd Nashan , Klaus Wessiepe , Heribert Bertling , Wolfgang Rohde , Manfred Blase , Manfred Galow , Ulrich Kochanski , Heinz Durselen , Johannes Janicka , Dieter Stalherm , Joachim Holtz , Jurgen Tietze , Ralf Schumacher
Inventor： Gerd Nashan , Klaus Wessiepe , Heribert Bertling , Wolfgang Rohde , Manfred Blase , Manfred Galow , Ulrich Kochanski , Heinz Durselen , Johannes Janicka , Dieter Stalherm , Joachim Holtz , Jurgen Tietze , Ralf Schumacher
CPC classification number: C10B5/10 , C10B5/02 , Y02P20/129
Abstract: Coking system, wherein the coking blends particularly based on hard coal, are fed batchwise to a reactor (1), which is heated indirectly by heat recovery in regenerators (I, II) or recuperators, whereby the reactor is built as a high-capacity coking reactor (100), several high-capacity coking reactors are combined to form a reactor block and the high-capacity coking reactors are built as mutually independent modules, whereby each module can be operated or optionally replaced independently of the neighboring modules, with little or no impairment of the operation of the neighboring modules. The individual reactors are independently operatable in terms of statics and heat supply. The regenerators, or recuperators (I, II, R, R') can be arranged laterally or underneath the reactor chamber. Neighboring reactors can have a common intermediate wall (2). The reactor chambers have a width of at least 0.7 m, a height of at least 8.5 m and a length of at least 18 m.
Abstract translation: 焦化系统，其中特别是基于硬煤的焦化混合物分批进料到反应器（1），反应器（1）通过再生器（I，II）或换热器中的热回收间接加热，由此将反应器建成为高容量 焦化反应器（100），几个大容量焦化反应器组合形成反应器块，大容量焦化反应器被构建为相互独立的模块，由此每个模块可以独立于相邻模块进行操作或可选地替换，几乎没有 或没有损害相邻模块的操作。 各个反应堆在静态和供热方面可独立运行。 再生器或再生器（I，II，R，R'）可以横向或在反应器室的下方布置。 相邻反应器可以具有共同的中间壁（2）。 反应室的宽度至少为0.7米，高度至少为8.5米，长度至少为18米。
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公开(公告)号：US5395485A
公开(公告)日：1995-03-07
申请号：US956774
申请日：1992-12-17
Applicant: Gerd Nashan , Klaus Wessiepe , Heribert Bertling , Werner Abendroth , Helmut Dohle , Manfred Friedrichs , Gerd Klinkenberg , Manfred Blase , Heinz Durselen , Gunter Meyer , Wolfgang Rohde
Inventor： Gerd Nashan , Klaus Wessiepe , Heribert Bertling , Werner Abendroth , Helmut Dohle , Manfred Friedrichs , Gerd Klinkenberg , Manfred Blase , Heinz Durselen , Gunter Meyer , Wolfgang Rohde
CPC classification number: C10B25/06
Abstract: A large-scale coking reactor including a housing provided with a chamber and with outer and inner chamber frames, a displaceable outer door elastically compressed against the outer frame and formed with a respective elastic peripheral seal compressible against the frame and with an outer high temperature membrane interposed between the door and the seal and elastically pressed thereagainst to seal the door opening, a displaceable inner door spaced from the outer door and formed with an inner high temperature membrane interposed between the inner door and the inner frame to fit elastically the inner frame, the inner and outer doors being releasably interconnected upon displacing the outer door, so that the doors are mounted in the housing to be operatable either selectively or in combination with one another.
Abstract translation: PCT No.PCT / EP91 / 00739 Sec。 371日期1992年12月17日 102（e）日期1992年12月17日PCT 1991年4月18日PCT PCT。 出版物WO91 / 16404 日本1991年10月31日。一种大型焦化反应器，包括设有室的外壳和外室框架和内室框架，可移动的外门弹性地压靠外框架并形成有相对的弹性周边密封件， 并且外部的高温隔膜插入在门和密封件之间并且被弹性地压在其上以密封门开口，与外门间隔开并形成有插入在内门和内框架之间的内部高温隔膜的可移动的内门 为了弹性地装配内框架，内门和外门在移动外门时可释放地互连，使得门被安装在壳体中以便可选择性地或彼此组合地操作。
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公开(公告)号：US4211533A
公开(公告)日：1980-07-08
申请号：US894846
申请日：1978-04-10
Applicant: Gerd Nashan , Josef Langhoff , Joachim Lehmann , Kurt Kleisa , Dieter Makrutzki
Inventor： Gerd Nashan , Josef Langhoff , Joachim Lehmann , Kurt Kleisa , Dieter Makrutzki
CPC classification number: C10L5/04
Abstract: Coke is mixed with bituminous coal and the mixture is converted into briquettes. To obtain high-quality and high-strength briquettes, the temperature of the coke is adjusted, prior to mixing, to such a level that when the mixing takes place, the coke/coal mixture will have a precisely predetermined temperature within the scope of 400.degree.-500.degree. C. The exact temperature within this range is selected in dependence upon the characteristics of the coke and the coal.
Abstract translation: 焦炭与烟煤混合，将混合物转化为压块。 为了获得高质量和高强度的团块，在混合之前将焦炭的温度调节到这样的水平，即当发生混合时，焦炭/煤混合物将具有在400范围内的精确预定温度 DEG-500℃。根据焦炭和煤的特性选择该范围内的精确温度。
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4.发明授权
公开(公告)号：US3970523A
公开(公告)日：1976-07-20
申请号：US534897
申请日：1974-12-20
Applicant: Kurt-Gunther Beck , Wolfgang Rohde , Heinrich Echterhoff , Gerd Nashan
Inventor： Kurt-Gunther Beck , Wolfgang Rohde , Heinrich Echterhoff , Gerd Nashan
CPC classification number: C10B47/10
Abstract: Improvements in the process of producing coke from bituminous coal in high-efficiency coking ovens, whereby the size of the lumps of coke and their strength are both increased, which comprises maintaining a coking rate between 1.2 and 2.8, and preferably between 1.44 and 2.0, inches per hour, based upon the width in inches of the coking chamber and the time required to complete the coking operation, and maintaining a rate of temperature increase between 1.6 and 3.3 centigrade degrees per minute during the heating of the coal while it is in the plastic range. The coal preferably is also preliminarily heated to a temperature between 160.degree. and 250.degree.C, preferably between 180.degree. and 200.degree.C, before being charged to the high-efficiency coking oven, and the width of the coking chamber of the high-efficiency oven that is used is at least 500 millimeters (19.7 inches).
Abstract translation: 在高效焦化炉中从烟煤生产焦炭的方法的改进，由此焦炭块的尺寸及其强度都增加，其包括保持焦化速率在1.2和2.8之间，优选在1.44和2.0之间， 基于焦化室的英寸宽度和完成焦化操作所需的时间，并且在煤的加热期间保持在每分钟加热1.6至3.3摄氏度之间的温度升高速率 塑料范围。 煤优选也预先加热至160℃至250℃，优选180℃至200℃的温度，然后将其加入到高效焦化炉中，并将焦化室的宽度高效 使用的烤箱至少为500毫米（19.7英寸）。
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公开(公告)号：US5039379A
公开(公告)日：1991-08-13
申请号：US276268
申请日：1988-11-25
Applicant: Gerd Nashan
Inventor： Gerd Nashan
IPC: C10B39/02
CPC classification number: C10B39/02
Abstract: A preferred method of dry cooling coke includes the steps of removing the coke from the coke oven, crushing the coke with a crushing device to increase a surface area thereof, transporting the coke after crushing to a dry cooling apparatus, and dry cooling the coke by the transfer of heat at the surface area which has been increased by the crushing.
Abstract translation: 干冷却焦炭的优选方法包括以下步骤：从焦炉中除去焦炭，用破碎装置粉碎焦炭以增加其表面积，将粉碎后的焦炭输送到干燥冷却装置，并将焦炭干燥冷却 在通过破碎而增加的表面积处的热量传递。
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Patent Agency Ranking
公开(公告)号：US4668343A
公开(公告)日：1987-05-26
申请号：US649130
申请日：1984-09-10
Applicant: Gerd Nashan , Josef Volmari , Horst Dungs , Dieter Breidenbach , Kurt Lorenz
Inventor： Gerd Nashan , Josef Volmari , Horst Dungs , Dieter Breidenbach , Kurt Lorenz
IPC: C10B39/02
CPC classification number: C10B39/02 , Y02P20/129
Abstract: A method of dry cooling red-hot coke in a vessel having an antechamber with a small discharge leading to a vertically elongated cooling chamber which is of larger dimension than the discharge and with both the cooling chamber and the antechamber having fluid cooling tubes in one or more walls and the ceiling thereof and also having cooling tube bank diverging downwardly from the discharge of the antechamber into the cooling chamber, comprises directing the red-hot coke to be cooled downwardly through the antechamber and into the cooling chamber so as to maintain a charge of coke in the cooling chamber to the conical charge cone of the cooling tubes adjacent the top of the cooling chamber which extends downwardly below the discharge, thereafter circulating a coolant through the cooling tubes to effect transfer of sensible heat from the coke to the fluid and directing a cooling gas from the bottom of the cooling upwardly through the coke and above the entire area of the coke charging cone and then into an exhaust duct to one or more waste heat boilers.
Abstract translation: 在容器中干燥冷却红热焦炭的方法，该容器具有具有小排放物的前室，导致垂直细长的冷却室，其尺寸大于排出物，并且冷却室和前室都具有流体冷却管， 更多的墙壁和天花板，还有从前厅排放到冷却室中的向下扩散的冷却管组，包括将红热焦炭引导向下冷却通过前厅并进入冷却室，以保持电荷 在冷却室中的焦炭的锥形加料锥体与冷却室的顶部相邻，该冷却管的顶部向下延伸到排放物下方，然后使冷却剂循环通过冷却管，以使显热从焦炭传递到流体， 将冷却气体从冷却的底部向上引导通过焦炭并在焦炭充电器的整个区域的上方 e然后进入排气管道到一个或多个废热锅炉。
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公开(公告)号：US4647341A
公开(公告)日：1987-03-03
申请号：US683934
申请日：1984-12-20
Applicant: Kurt Lorenz , Horst Dungs , Gerd Nashan , Dieter Breidenbach , Josef Volmari
Inventor： Kurt Lorenz , Horst Dungs , Gerd Nashan , Dieter Breidenbach , Josef Volmari
IPC: C10B39/02
CPC classification number: C10B39/02
Abstract: A dry coke cooling apparatus comprises an antechamber with a bottom hole for charging coke into a cooling chamber which accommodates vertical outer cooling walls and inner cooling walls which extend within the coke charge. The lower part accommodates coke discharge equipment and conduits for supplying circulated cooling gas which passes upwardly through the charge, to be exhausted at the top. The inner cooling walls are supported on hollow beams which are cooled by the circulated cooling gas directly or indirectly.
Abstract translation: 一种干焦炭冷却装置包括一个具有底孔的前室，用于将焦炭装入冷却室，冷却室容纳垂直外冷却壁和在焦炭装料内延伸的内冷却壁。 下部容纳焦炭排放设备和用于供应循环冷却气体的管道，该冷却气体向上通过电荷，在顶部排出。 内部冷却壁支撑在由直接或间接地循环的冷却气体冷却的中空梁上。
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公开(公告)号：US4421604A
公开(公告)日：1983-12-20
申请号：US314259
申请日：1981-10-23
Applicant: Wilhelm Weskamp , Gerd Nashan , Wilhelm Stewen
Inventor： Wilhelm Weskamp , Gerd Nashan , Wilhelm Stewen
Abstract: The quality of coke is improved by measuring the width of a plastic zone of a given type of coal, comparing said measured zone with a predetermined zone width known to result in good quality coke, adjusting certain characteristics of said given coal prior to charging it into the coke oven to cause a change in said zone width of the coal that will ultimately result in improved coke quality. Typical adjusting steps include preheating the coal and/or the addition of coal binders, such as, various carbon and petro-based binding agents, for example, pitch.
Abstract translation: 通过测量给定类型的煤的塑性区域的宽度来改善焦炭的质量，将所测量的区域与已知导致优质焦炭的预定区域宽度进行比较，调整所述给定煤的某些特性，然后再将其充入 焦炉导致煤的所述区域宽度的变化，这将最终导致改善的焦炭质量。 典型的调整步骤包括预热煤和/或添加煤粘合剂，例如各种碳和石油基粘合剂，例如沥青。
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公开(公告)号：US4699693A
公开(公告)日：1987-10-13
申请号：US764931
申请日：1985-08-12
Applicant: Gerd Nashan , Josef Volmari , Horst Dungs , Dieter Breidenbach , Kurt Lorenz
Inventor： Gerd Nashan , Josef Volmari , Horst Dungs , Dieter Breidenbach , Kurt Lorenz
IPC: C10B39/02
CPC classification number: C10B39/02 , Y02P20/129
Abstract: An apparatus for dry cooling red-hot coke having an antechamber with a small discharge leading to a vertically elongated cooling chamber which is of larger dimension than the discharge and with both the cooling chamber and the antechamber having fluid cooling tubes in one or more walls and the ceiling thereof and also having a cooling tube bank in the shape of truncated pyramid comprising trapezoidal walls diverging downwardly from the discharge of the antechamber into the cooling chamber.
Abstract translation: 一种用于干燥红热焦炭的设备，其具有具有小排放物的前室，其导致垂直细长的冷却室，其尺寸大于排放物，并且冷却室和前室在一个或多个壁中具有流体冷却管， 其顶部还具有截顶棱锥形状的冷却管堤，其包括从前厅的排放口向下散开到冷却室中的梯形壁。
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公开(公告)号：US4668344A
公开(公告)日：1987-05-26
申请号：US786944
申请日：1985-10-11
Applicant: Kurt Lorenz , Horst Dungs , Gerd Nashan , Dieter Breidenbach , Josef Volmark
Inventor： Kurt Lorenz , Horst Dungs , Gerd Nashan , Dieter Breidenbach , Josef Volmark
CPC classification number: F22G1/16 , C10B39/02 , F22B1/1876 , Y02P20/129
Abstract: A waste heat boiler system includes a vertically elongated waste heat boiler having an upper portion with a waste gas inlet and a lower portion with an exhaust line connection which in addition to its vapor generating tubes includes evaporator tube nests and a water preheater. The waste gases are received from a dry coke cooling vessel and they are delivered through a separator by a blower to the lower end of the coke cooling vessel for flow upwardly through the hot coke. The superheater is mounted over the waste heat boiler and has a connection through a controllable valve to the top of the waste heat boiler. The superheater includes its own burner and air and external gas supply are supplied to the combustion chamber for the superheater along with bypass portion of the circulated waste gases. The steam generated by the boiler is delivered from a steam cylinder or drum in the superheated tubes of the superheater. Some of the gases from the superheater are selectively delivered to the waste heat boiler and some are discharged through atmosphere.
Abstract translation: 废热锅炉系统包括垂直细长的废热锅炉，其具有具有废气入口的上部和具有排气管线连接的下部，除了其蒸气发生管之外，还包括蒸发器管巢和水预热器。 废气从干焦炭冷却容器接收，并且通过鼓风机通过分离器输送到焦炭冷却容器的下端，以向上流过热焦炭。 过热器安装在废热锅炉上，并通过可控阀连接到废热锅炉的顶部。 过热器包括自己的燃烧器和空气，并且外部气体供应被供应到用于过热器的燃烧室以及循环废气的旁路部分。 锅炉产生的蒸汽从过热器的过热管中的蒸汽筒或滚筒输送。 来自过热器的一些气体被选择性地输送到废热锅炉，一些通过大气排出。
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