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    • 3. 发明授权
    • Processes of producing cokes of large lump size and improved strength
from bituminous coals
    • 产生大块煤焦炭和烟煤强度提高的工艺
    • US3970523A
    • 1976-07-20
    • US534897
    • 1974-12-20
    • Kurt-Gunther BeckWolfgang RohdeHeinrich EchterhoffGerd Nashan
    • Kurt-Gunther BeckWolfgang RohdeHeinrich EchterhoffGerd Nashan
    • C10B47/10C10B57/02
    • C10B47/10
    • 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).
    • 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)。
    • 6. 发明授权
    • Method for dry cooling red-hot coke
    • 红热焦炭干燥方法
    • US4668343A
    • 1987-05-26
    • US649130
    • 1984-09-10
    • Gerd NashanJosef VolmariHorst DungsDieter BreidenbachKurt Lorenz
    • Gerd NashanJosef VolmariHorst DungsDieter BreidenbachKurt Lorenz
    • C10B39/02
    • C10B39/02Y02P20/129
    • 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.
    • 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。
    • 10. 发明授权
    • Method for cooling coke and generating superheated high pressure steam
    • 冷却焦炭并生成过热高压蒸汽的方法
    • US4668344A
    • 1987-05-26
    • US786944
    • 1985-10-11
    • Kurt LorenzHorst DungsGerd NashanDieter BreidenbachJosef Volmark
    • Kurt LorenzHorst DungsGerd NashanDieter BreidenbachJosef Volmark
    • C10B39/02F22B1/18F22G1/02F22G1/16F28G1/16
    • F22G1/16C10B39/02F22B1/1876Y02P20/129
    • 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.
    • 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。