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    • 6. 发明授权
    • Method and apparatus for treating oil-water-solids sludges and refinery
waste streams
    • 用于处理油水固体污泥和炼油废物流的方法和装置
    • US4881473A
    • 1989-11-21
    • US303324
    • 1989-01-30
    • James L. Skinner
    • James L. Skinner
    • B01D17/00C02F11/12E21B21/06E21B41/00F23G5/04F23G7/00F26B3/24F26B17/20
    • F26B17/20B01D17/00C02F11/06C02F11/12E21B21/066E21B41/005F23G5/04F23G7/001F26B1/00F26B11/16F26B3/24C02F1/40C02F2101/20C02F2101/32C02F2103/008C02F2103/365F23G2900/50008F26B2200/18Y02W10/40
    • Heavy hydrocarbon containing sludges such as refinery waste streams, oil storage tank sludges and marine oil tanker ballast are treated by passing the sludges in a flow stream through an indirect dryer to vaporize liquids having a boiling point at atmospheric pressure of less than about 700.degree. C. and to provide substantially dried solid particles discharged from the dryer. The dried particles, containing heavy hydrocarbons as a coating or as a part of the solids, are conducted to a combuster/oxidizer and exposed to a high velocity flow stream of oxygen containing gas, typically low pressure forced air, to burn the residual hydrocarbons in the solids and to reduce heavy metals and the like to oxides thereof. A sludge handling system includes a rotary disk type indirect dryer connected to a lift pipe type combustor/oxidizer for thorough exposure of the dried solids to an oxygen containing atmosphere. A centrifigal or cyclone type gas-solids separator receives the flow stream discharged from the lift pipe and a portion of the dried solids may be diverted after discharge from the dryer back to the dryer inlet to reduce the moisture content of the sludge flow stream introduced to the dryer to minimize caking and clogging of the dryer itself.
    • 通过将流过的淤泥通过间接的干燥器来使处于大气压下的沸点小于约700℃的液体蒸发,来处理含有重质烃的污泥,例如炼油废物流,储油罐淤泥和海洋油罐车镇流器 并提供从干燥器排出的基本干燥的固体颗粒。 将含有作为涂层的重烃或作为固体的一部分的干燥颗粒进入燃烧器/氧化剂并暴露于含氧气体(通常为低压强制空气)的高速流动流中,以将 固体并且将重金属等还原成其氧化物。 污泥处理系统包括连接到提升管式燃烧器/氧化器的旋转盘式间接干燥器,用于将干燥固体彻底暴露于含氧气氛。 离心式或旋风型气固分离器接收从提升管排出的流动流,并且一部分干燥的固体可以在从干燥器排放到干燥器入口之后转向,以减少引入到干燥器中的污泥流的水分含量 干燥器,以最大限度地减少烘干机本身的结块和堵塞。
    • 7. 发明授权
    • Heat exchanger
    • 热交换器
    • US4660628A
    • 1987-04-28
    • US852948
    • 1986-03-20
    • Per SolbergJan Gronhaug
    • Per SolbergJan Gronhaug
    • F28F5/04F26B3/24F26B17/20F28D11/02
    • F26B17/20F26B3/24F28D11/02Y10S165/152
    • A heat exchanger (10) for indirectly heating, drying and cooling materials comprises a hollow rotor (40) having an inlet (46) of heating and cooling medium and an outlet (47) of the medium or its condensate, a casing mounted on the hollow rotor, a plurality of disc-shaped base boards (20), a plurality of annular ducts (21, 23; 22, 24) projected from both side surfaces (11, 12) of the base boards (20), the duct forming a passage communicating with the inlet (46) and the outlet (47), arranged so as to be partly superposed sequentially on both front and back surfaces (11, 12) of the base board (20) from the inner peripheral edges to the outer peripheral edges of the base boards (20) in such a manner that partition plates for shielding the ducts (21, 23; 22, 24) being provided in the superposed positions.
    • PCT No.PCT / NO85 / 00045 Sec。 371日期1986年3月20日 102(e)1986年3月20日PCT PCT日期:1985年7月29日PCT公布。 出版物WO86 / 01284 日本1986年2月27日。用于间接加热,干燥和冷却材料的热交换器(10)包括中空转子(40),其具有加热和冷却介质的入口(46)和介质或其介质的出口(47) 冷凝物,安装在中空转子上的壳体,多个盘形基板(20),从基板的两个侧表面(11,12)突出的多个环形导管(21,23; 22,24) (20),所述管道形成与所述入口(46)和所述出口(47)连通的通道,所述通道被布置成顺序地部分地重叠在所述基板(20)的前表面和后表面(11,12)上, 所述基板(20)的外周边缘的内周缘以这样的方式设置,所述隔板用于屏蔽所述导管(21,23; 22,24)的隔板设置在叠置位置。
    • 9. 发明授权
    • High speed paper drying
    • US4359827A
    • 1982-11-23
    • US234288
    • 1981-02-17
    • Keith V. Thomas
    • Keith V. Thomas
    • D21F5/04F26B3/24
    • D21F5/042D21F5/04
    • An improved paper drying process and machine are described in which the paper web is supported independently of velocity-induced stresses thus permitting operation at speeds significantly in excess of the prior art for each paper grade. The process requires: (1) transporting the web on a supporting fabric that travels from the last press nip through at least the initial portion of a drying section; and (2) holding the web onto its supporting fabric by employing forces normal to the major web surfaces sufficient to overcome those forces which tend to lift the web from its supporting fabric. The web on its supporting fabric travels a serpentine path through the drying section about drying cylinders with the web alternating between direct contact with a drying cylinder followed by indirect contact with the subsequent cylinder. The principal holding forces are preferably pressure differentials created by vacuum boxes arranged to effectively hold the web to its supporting fabric on all portions of the web-fabric combination where the web is not in direct wrapping contact with the drying cylinders. The fabric supports the web at least until the web has attained sufficient strength through increased dryness to resist breaking stresses at the selected machine speed. The products made by the process of this invention possess a unique toughness or stretchability not found in conventionally prepared papers that have been strained or stretched during manufacture. Processes and machine arrangements designed to balance stretchability with certain desirable stiffness properties are disclosed. Pulp furnishes may now be selected for their contribution to product qualities, such as higher finished product tensile strength, rather than principally for wet strength. For example, chemical pulps may be significantly reduced or eliminated from newsprint furnishes where their purpose has been principally to permit economic paper machine speeds. The invention makes attainable speeds approaching twice current operating levels for each paper grade.
    • 10. 发明授权
    • Process of drying and calcining bulk materials
    • 干燥和煅烧散装材料的工艺
    • US4354826A
    • 1982-10-19
    • US212285
    • 1980-12-03
    • Gerhard KrugerWerner Kepplinger
    • Gerhard KrugerWerner Kepplinger
    • B01J6/00F26B3/00F26B3/24F26B11/02F27B7/16F27B7/34F27B7/02
    • F26B3/00F26B11/028F26B3/24F27B7/16F27B7/34
    • A process for drying and/or calcining bulk material in a rotary kiln when hot gases are passed countercurrent to the flow of bulk material thereto, and the bulk material is dried and/or calcined in the rotary kiln is disclosed. According to the invention, the bulk material is dried and/or calcined, as it passes from the feed end of the rotary kiln to the discharge end thereof, by contacting the same with hot gases and thereafter, as the bulk material passes towards the discharge end of the rotary kiln, the bulk material is heated by indirect heat exchange with such hot gases. An apparatus for carrying out such process is also disclosed. The apparatus is a rotary kiln equipped with a centrally disposed tube, disposed axially within the rotary kiln toward the bulk material discharge end of the rotary kiln whereby an annular space is defined between the outer wall of the central tube and inner wall of the rotary kiln. The apparatus is equipped with means for passing hot gases within the central tube, means for passing bulk material on the outer wall of the central tube whereby the bulk material can be heated by indirect heat exchange with hot gases within the tube.
    • 当热气体与散装材料的流动逆流通过时,在回转窑中干燥和/或煅烧散装材料的方法,并且公开了在回转窑中干燥和/或煅烧的本体材料。 根据本发明,散装材料在从旋转窑的进料端通过其排出端时被干燥和/或煅烧,通过使其与热气体接触,此后,随着散装材料通过放电 回转窑的端部,通过与这种热气体的间接热交换来加热散装材料。 还公开了一种用于执行这种处理的装置。 该设备是配备有中心设置的管的回转窑,其轴向设置在回转窑内朝向回转窑的散装物料排放端,由此在中心管的外壁和回转窑的内壁之间形成环形空间 。 该装置装备有用于将中心管内的热气体通过的装置,用于将散装材料通过中心管的外壁上的装置,由此可以通过与管内的热气体的间接热交换来加热散装材料。