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    • 35. 发明授权
    • Gas-tight closure
    • 气密封闭
    • US4313704A
    • 1982-02-02
    • US32495
    • 1979-04-23
    • Werner KucharzykWolfgang Rohde
    • Werner KucharzykWolfgang Rohde
    • B65D90/54B08B9/08B08B9/087B65D90/62C10B31/02C10J3/50
    • C10B31/02B65D90/626
    • The gas-tight closure comprises a thin walled tubular piece projecting from a feeding duct into a filling space, a thin walled conical jacket having its larger bottom base provided with a rigid seal reinforcing member cooperating with the lower rim of the intake tubular piece. The outer periphery of the reinforcing member is slanted about a small angle to snugly fit into the tubular piece and adjust the form thereof when upward pull is exerted upon the conical jacket by means of an actuation rod passing outwardly through the wall of the feeding duct. The actuation rod has preferably the form of a hollow shaft which accommodates the manipulation rod of a scraper projecting radially below the reinforcing member into the filling space. The outside portion of the actuation rod is provided with a control device in the form of clamping plates cooperating with abutment plates resting on the guiding sleeve for the actuation rod. The clamping plates are manipulated by means of separate levers.
    • 气密闭合件包括从进料管道突出到填充空间的薄壁管状件,薄壁锥形夹套,其较大的底部基部设置有与进气管件的下边缘配合的刚性密封加强件。 加强构件的外周边以小的角度倾斜以紧密地配合到管状件中,并且当通过向外穿过供给管的壁的致动杆向上拉动作用在锥形护套上时调节其形状。 致动杆优选地具有中空轴的形式,该空心轴容纳在加强构件的径向下方突出到填充空间中的刮刀的操纵杆。 致动杆的外侧部分设有一个控制装置,该控制装置与夹持在用于致动杆的导向套筒上的抵靠板配合。 夹板通过单独的杠杆操纵。
    • 36. 发明授权
    • Process and apparatus for drying and preheating of coking coal in a
single flight stream tube
    • 炼焦煤在单一飞行流管中的干燥和预热的工艺和装置
    • US4241513A
    • 1980-12-30
    • US070993
    • 1979-08-30
    • Wolfgang Rohde
    • Wolfgang Rohde
    • C10B57/10F27B3/08F27B17/00
    • C10B57/10
    • A process and an apparatus for the drying and preheating of coking coal is described, in which a coarser grain fraction of the starting coal is separated out at least at one location in a flight stream tube through which the coal and a heat carrier gas are fed, and in which this larger grain fraction is subsequently reintroduced into the main stream containing only the finer grain fraction of the coal and the predominant portion of the heat carrier gas. The method and the apparatus through which the method may be carried out allow for a single-step process for both drying and preheating of the coal, make it possible to substantially reduce the length of the flight stream tube necessary, and increase the uniformity of the degree of pretreatment of the variously-sized fractions of the starting material.
    • 描述了用于焦化煤的干燥和预热的方法和装置,其中至少在飞行流管中的一个位置处分离起始煤的较粗颗粒部分,通过该排气管中的煤和热载体被供给 ,并且其中该较大的晶粒分数随后被再次引入到仅含有煤的较细晶粒部分和热载体的主要部分的主流中。 可以进行该方法的方法和装置允许用于煤的干燥和预热的单步过程,使得可以显着地减少所需的飞行流管的长度,并且增加 起始原料的各种级分的预处理程度。
    • 37. 发明授权
    • Arrangement for pneumatically regulating the introduction of substances
into chambers
    • US4058230A
    • 1977-11-15
    • US662017
    • 1976-02-27
    • Heinz BellenbergWerner KucharzykWolfgang RohdeWerner Siebert
    • Heinz BellenbergWerner KucharzykWolfgang RohdeWerner Siebert
    • G01F17/00C10B31/00F23K3/00
    • C10B31/00C10B41/005
    • An arrangement for regulating the introduction of substances into chambers is disclosed and is particularly well-suited for the feeding of coal into coke ovens. The arrangement includes a chamber which is to be filled to a predetermined level and a feeding device is provided for feeding material into the chamber. The feeding device has a switch which stops the introduction of the material to the chamber when the level of the material reaches the predetermined level. The switch for the feeding device is electrically connected with a differential pressure switch which is actuated upon the generating of a predetermined pressure differential across it. The requisite pressure differential is generated by introducing pressurized gas into the chamber and an air compressor may be provided for this purpose. A sensing conduit, which is connected with one terminal of the differential pressure switch, extends into the chamber and has an end positioned at the predetermined level to which the chamber is to be filled. The pressurized gas admitted into the chamber sets up certain pressure characteristics in the sensing conduit which are changed when the level of material in the chamber reaches the predetermined level so that the gas no longer has free access to the open end of the sensing conduit. The change in the pressure characteristics causes a pressure differential to be established across the differential pressure switch which, in turn, activates the feeding device switch to stop the introduction of material into the chamber. In order to compensate for shock waves which may be generated in the chamber by the feeding of the material and which may cause a false signal to be transmitted to the switch of the feeding device, a compensating conduit is provided which has an end in the chamber and is connected with the terminal of the differential pressure switch opposite that to which the sensing conduit is connected. A supply conduit for the pressurized gas is also provided and introduces the pressurized gas into the chamber in the vicinity of the end of the sensing conduit.
    • 39. 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)。