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    • 21. 发明授权
    • Adjustable potentiometer assembly
    • 可调电位器总成
    • US4110721A
    • 1978-08-29
    • US759346
    • 1977-01-14
    • Mutsuo NakanishiHans Schmidt
    • Mutsuo NakanishiHans Schmidt
    • H01C10/08H01C10/16H01C10/32
    • H01C10/32
    • A potentiometer assembly particularly suited for supplying tuning voltages for all of the bands of signals capable of receipt by a television receiver or the like, includes three segments of resistive material arranged in a circle on a support member. Each of the segments corresponds to a different band of frequencies to which the television receiver may be tuned. Band selection is effected by comparable conductive segments on the support member.In one embodiment, a single wiper is used to sweep all of the resistive segments to supply the desired tuning voltage output. A cam arrangement is used to adjust the detented position of the wiper relative to the support member to effect fine tuning at each position. Other embodiments utilize individually adjustable wipers for each station or detent position of the tuner, with each wiper being preset to effect the fine tuning at the detented position of the potentiometer assembly. The individual contacts or wipers for each position are arranged to overlap comparable resistances on the resistive material, so that the entire range of tuning voltages which appear across the resistive material is available from the outputs of the assembly.
    • 特别适用于为能够由电视接收机等接收的所有信号频带提供调谐电压的电位器组件包括在支撑构件上以圆圈布置的三个电阻材料段。 每个段对应于可以调谐电视接收机的不同的频带。 带选择由支撑构件上的相当的导电段实现。
    • 23. 发明授权
    • Method and apparatus for waste processing with multistage separation by air classification of light fractions from dried material
    • 通过从干燥材料中轻馏分的空气分类进行多级分离的废物处理方法和装置
    • US06264038B1
    • 2001-07-24
    • US09458345
    • 1999-12-10
    • Hans Schmidt
    • Hans Schmidt
    • B03B100
    • B03B9/06B07B9/00C10G1/00Y02E50/30Y02W30/521Y02W30/523Y02W30/525
    • To separate light organic fractions from waste which has undergone pretreatment consisting of precomminution, ferrous-metal separation, postcomminution, further ferrous-metal separation, drying and nonferrous-metal separation, multiple, preferably so-called zigzag air classifiers are arranged in cascading stages and are passed through sequentially by the material stream to be separated. The upward-stream speed of the air is adjusted in stages in the individual air classifiers such that the first air classifier receives the smallest and the last air-classifier the highest air speed. As a result, first the fine, then the medium and lastly the large organic light fractions are discharged to the top in sequence from each air-classifier stage. The separated organic light fractions represent fuel components of high calorific value. The remaining bottom-discharge from the air classifier group consists of a mixture of heavy organic fractions and minerals. This material mixture is separated by ballistic density separation into a heavy organic fraction and minerals. The separated heavy organic fraction also represents fuel components of high calorific value. The noncombustible groups such as ferrous metals, nonferrous metals, water and minerals collected throughout the entire process are utilizable as raw recycling materials.
    • 为了分离轻质有机部分与已经经过预处理,黑液金属分离,后处理,进一步黑色金属分离,干燥和有色金属分离的预处理的轻质有机部分,多个优选所谓的之字形空气分级器被布置在级联阶段, 依次通过待分离的物料流。 空气的上行速度在各个空气分级器中分阶段地调节,使得第一空气分级器接收最小和最后的空气分级器最高的空气速度。 结果,首先细,然后介质,最后大的有机轻馏分从每个空气分级器阶段依次排放到顶部。 分离的有机轻馏分代表高热值的燃料组分。 来自空气分级器组的剩余底部排放物由重质有机馏分和矿物质的混合物组成。 该材料混合物通过弹道密度分离分离为重质有机部分和矿物质。 分离的重质有机部分也代表高热值的燃料成分。 在整个过程中收集的黑色金属,有色金属,水和矿物质等不燃组合可用作原料回收材料。
    • 26. 发明授权
    • Process for liquefaction of natural gas
    • 天然气液化过程
    • US5551256A
    • 1996-09-03
    • US556195
    • 1995-11-09
    • Hans Schmidt
    • Hans Schmidt
    • F25J1/02F25J3/00
    • F25J1/0022F25J1/004F25J1/0045F25J1/0055F25J1/0212F25J2205/66F25J2220/60F25J2220/62F25J2220/64F25J2230/60F25J2245/90Y10S62/912
    • A pressurized natural gas flow, from which CO.sub.2 and H.sub.2 O are first removed using an adsorptive separation device, is subjected to liquefaction. The pre-purified natural gas flow is brought into heat exchange with at least one refrigerant routed in a refrigeration circuit and liquefied. The adsorptive separation device is regenerated by means of a regeneration gas containing a partial flow of the pre-purified natural gas flow and optionally additional residual gas flows such as a flash gas flow. During the cooling and liquefaction process of the natural gas flow at least the partial natural gas flow needed-for regeneration of the adsorptive separation device is separated when the temperature of the partial flow is such that the efficiency of cold use can be maximized by throttling to the regeneration gas pressure.
    • 使用吸附分离装置首先除去CO 2和H 2 O的加压天然气流被液化。 将预纯化的天然气流与在制冷回路中路由的至少一种制冷剂进行热交换并液化。 吸附分离装置通过再生气体再生,所述再生气体含有预纯化的天然气流的一部分流以及任选地附加的残余气体流如闪蒸气流。 在天然气流的冷却和液化过程中,当部分流动的温度使得冷的使用效率可以通过节流到最大化时,分离吸附分离装置的再生所需的至少部分天然气流量 再生气体压力。