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    • 2. 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)。
    • 3. 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。
    • 5. 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。
    • 6. 发明授权
    • Method of and an arrangement for pre-heating coking coal
    • 预热炼焦煤的方法和装置
    • US4102635A
    • 1978-07-25
    • US806277
    • 1977-06-13
    • Kurt-Gunther Beck
    • Kurt-Gunther Beck
    • C10B57/10C10B57/08F26B3/08
    • C10B57/08
    • Coal to be supplied to a coking oven is pre-heated, in a single pre-heating zone, such as in a conveying riser, first by heat yielded to it by a gaseous carrier medium entraining the coal for joint passage through the riser, and then additionally pre-heated by heat yielded to it by a gaseous fluid, such as hot combustion products, introduced into the pre-heating zone at a region thereof at which the temperature of the coal has already risen to a predetermined value, such as 80.degree. to 100.degree. C. The additional pre-heating of the coal results in a final temperature of the latter at the exit of the riser of more than 130.degree. C, preferably between 150.degree. and 250.degree. C. The stream of the carrier medium with the coal entrained therein flows upwardly through the riser which is substantially vertical, the coal being entrained at the lower end and separated from the mixture of the carrier medium with the gaseous fluid at the upper end of the riser. A part of the above-mentioned mixture may be circulated to the lower end of the riser for use as the carrier medium. The flow-through cross-sectional area of the pre-heating zone may be larger downstream than upstream of the region at which the gaseous fluid is introduced for maintaining the speed of flow through the pre-heating zone constant despite the addition of the gaseous fluid.
    • 供应到焦化炉的煤被预热,在单个预热区域中,例如在输送提升管中,首先通过由夹带煤的气态载体介质产生的热量通过提升管进行接合通道,以及 然后通过在煤的温度已经升高到预定值的区域(例如80℃)下被引入到预热区域中的气态流体(例如热燃烧产物)产生的热另外预热 DEG至100℃。煤的附加预加热导致提升管出口处的最终温度超过130℃,优选150℃至250℃。载体介质流 夹带在其中的煤通过基本垂直的提升管向上流动,煤被夹带在下端,并且与提升管上端的气态流体与载体介质的混合物分离。 上述混合物的一部分可以循环到提升管的下端以用作载体介质。 预热区域的流通横截面积可以比引入气态流体的区域的上游下游更大,以保持流过预热区域的流速恒定,尽管添加了气态流体 。