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    • 1. 发明授权
    • Method of operating coke ovens
    • 操作焦炉的方法
    • US4064017A
    • 1977-12-20
    • US597917
    • 1975-07-21
    • Kurt-Gunther BeckWolfgang RohdeDieter StalhermVolker Kolitz
    • Kurt-Gunther BeckWolfgang RohdeDieter StalhermVolker Kolitz
    • C10B21/20C10B57/00C10B21/10
    • C10B21/20
    • A cokable substance such as coal is admitted into a coking chamber. A quantity of heat which is sufficient to cause coking of the cokable substance is supplied to the chamber during preselected time intervals within the coking period in which coking of the cokable substance progresses in response to the supply of heat. On the other hand, during other time intervals within the coking period in which coking of the cokable substance is essentially unaffected by the supply of heat, the quantity of heat supplied to the chamber is reduced to a level below that required to sustain coking of the cokable substance during the preselected time intervals. In this manner, savings in energy may be realized. The supply of heat to the chamber during those time intervals in which coking of the cokable substance is unaffected by the supply of heat may be discontinued completely.
    • 可燃物质如煤炭进入焦化室。 足以引起可溶性物质焦化的热量在焦化期间内的预选时间间隔内供应到室内,在该焦化期间,可溶性物质的焦化响应于供热而进行。 另一方面,在可焦化物质的焦化基本上不受供热影响的焦化期间内的其它时间间隔内,供给到室的热量降低到低于维持焦化所需的热量 在预选的时间间隔内的可卡因物质。 以这种方式,可以节省能源。 在可燃物质的焦化不受热量的影响的那些时间间隔期间,可以完全停止在室中供应热量。
    • 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)。
    • 4. 发明授权
    • Process and system for the dry quenching of coke
    • 焦炭干法淬火的工艺和系统
    • US4627174A
    • 1986-12-09
    • US725048
    • 1985-04-19
    • Kurt HeddenKurt-Gunther BeckWolfgang RohdeHorst Schumacher
    • Kurt HeddenKurt-Gunther BeckWolfgang RohdeHorst Schumacher
    • C10B39/02C10B57/10F26B3/16
    • C10B57/10C10B39/02
    • Glowing coke descending through a cooling duct in a coking plant is quenched by two gas flows respectively traversing an upper compartment and a lower compartment of the duct, the two compartments meeting at a restricted gate for the passage of the coke. At least the lower gas flow, passing in countercurrent to the descending coke charge, is also circulated through a drying and preheating oven for coal to be fed to a coke-oven battery of the plant, thus containing some water vapor. When the upper flow is also constituted by coal-drying gas, it is passed downward through the upper compartment in order to reduce the height of a high-temperature zone in which combustion and thus loss of coke could occur. The coke gate is formed by a funnel-shaped upper partition and an upwardly pointing conical lower partition between which a scavenger gas passes in cross-flow.
    • 通过焦化装置中的冷却管道下降的发光焦炭通过分别穿过管道的上隔室和下隔室的两个气流骤冷,两个隔室在限制门处会合以供焦炭通过。 至少与下降焦炭装置逆流通过的较低气体流量也通过干燥和预热炉循环,以将煤供给到设备的焦炉电池,从而含有一些水蒸汽。 当上部流动也由干燥气体构成时,其通过上部区域向下通过,以便降低可能发生燃烧和因此可能发生焦炭的高温区域的高度。 焦炭门由漏斗形的上部隔板和向上指向的圆锥形下部隔板形成,在该隔板中,清除剂气体在其间交叉流动。