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    • 111. 发明授权
    • Process for thermal treatment, especially drying
    • 热处理工艺,特别是干燥
    • US4304049A
    • 1981-12-08
    • US151672
    • 1980-05-20
    • Friedrich Curtius
    • Friedrich Curtius
    • C02F11/12C05F7/00F26B3/084F26B21/04F27B15/00F26B3/08
    • C02F11/12C05F7/00F26B21/04F26B3/084F27B15/00
    • The invention relates to the thermal treatment of flowable material using heated contact surfaces in a fluidized bed. Known processes use a gas, often air, to fluidize the bed. This imposes limits on the temperatures that can be allowed to be reached as higher temperatures can cause the material to be treated to burn. It also often produces sterilization of the material. Further there is the problem of disposal of the gases generated in the treatment process. In an attempt to alleviate these problems, the present invention proposes a process generally of the above kind but in which the fluidizing gas comprises gases generated in the bed itself. This is economical as it reduces the heat losses, environmentally desirable as it reduces the amount of gas discharge and more efficient as these gases are generally inert, thus enabling higher temperatures to be generated in the bed without risk of the material burning, thus also facilitating sterilization of the material.
    • 本发明涉及使用流化床中的加热接触表面对可流动材料的热处理。 已知的方法使用气体,通常是空气来使床流化。 这对可以允许达到的温度施加限制,因为较高的温度可导致材料被处理燃烧。 它也经常对材料进行灭菌。 此外,存在处理过程中产生的气体的问题。 为了减轻这些问题,本发明提出了一种上述类型的方法,其中流化气体包括在床本身中产生的气体。 这是经济的,因为它减少了热损失,因为它减少了气体排放的量并且由于这些气体通常是惰性的而更有效,所以在环境上是有希望的,因此能够在床上产生更高的温度而没有材料燃烧的风险,因此也有助于 灭菌材料。
    • 112. 发明授权
    • Method of hot-air drying
    • 热风干燥方法
    • US4255870A
    • 1981-03-17
    • US83655
    • 1979-10-11
    • Lars Malmquist
    • Lars Malmquist
    • F26B21/04F26B23/00F26B3/04
    • F26B23/002F26B21/04Y02P70/405
    • The invention relates to a method of drying with hot air where the drying is divided into at least two partial processes, in parallel or in series with each other, and the circulation flows of the two partial processes are conditioned to substantially different wet temperature levels, and the spent air in the partial process with higher wet temperature is heat exchanged with the circulation air in the partial process with lower wet temperature, in combination with that the spent air flows from the two partial processes thereafter are mixed with each other and caused to pass a heat exchanger common for the processes in order to preheat the supply air to the partial process with low wet temperature and after the passage through the heat exchanger to partially constitute supply air for the partial process with high wet temperature.
    • 本发明涉及一种用热空气干燥的方法,其中干燥被分成至少两个彼此平行或串联的部分方法,并且两个部分方法的循环流被调节到基本上不同的湿温度水平, 并且在湿度较高的部分过程中的废气与部分过程中的循环空气与较低的湿温度进行热交换,结合来自其后的两个部分过程的废气相互混合并使其 通过该过程通用的换热器,以便将供应空气预热到具有低湿温度的部分过程,并且在通过热交换器之后,部分地构成用于具有高湿温度的部分过程的供应空气。
    • 113. 发明授权
    • Air flow reverser system
    • 气流反向器系统
    • US4250917A
    • 1981-02-17
    • US959832
    • 1978-11-13
    • Knud JespersenHans L. BergnerGuy E. Buller-Colthurst
    • Knud JespersenHans L. BergnerGuy E. Buller-Colthurst
    • A23B4/03A23B4/052A23B4/06F24F12/00F26B15/14F26B21/02F26B21/04
    • A23B4/031A23B4/052A23B4/066F24F12/001F26B15/14F26B21/028Y02B30/563Y02P60/851Y02P60/853Y02P70/40Y10T137/85954Y10T137/87442
    • An air flow reverser apparatus for use in association with an air flow system having air supply and return port means, said apparatus comprising a main supply duct, and a main return duct, said ducts being connectable to said respective supply and return port means of said air flow system, at least two branch supply ducts communicating with said main supply duct, at least two branch return ducts communicating with said main return duct, supply damper means for selectively shutting off at least one of said branch supply ducts, while leaving at least one said branch supply duct open, return damper means for selectively shutting off at least one of said branch return ducts while leaving at least one said branch return duct open, and means interconnecting said supply and return damper means whereby when a selected one of said branch supply ducts is closed, a selected one of said branch return ducts is open, and power operated means for moving the same from one position to another simultaneously.
    • 一种用于与具有供气和返回端口装置的空气流动系统相关联的气流反向器装置,所述装置包括主供应管道和主回流管道,所述管道可连接到所述相应的供应和返回端口装置 空气流动系统,与所述主供应管道连通的至少两个分支供应管道,与所述主回流管道连通的至少两个分支返回管道,供应阻尼装置,用于选择性地关闭至少一个所述分支供应管道,同时至少留下 一个所述分支供应管道打开,返回阻尼器装置,用于选择性地关闭至少一个所述分支返回管道,同时使至少一个所述分支回流管道敞开,以及将所述供应和返回阻尼器装置相互连接的装置,由此当所述分支 供应管道关闭,所选择的一个分支返回管道是打开的,并且用于将它们从一个位置移动到另一个位置的动力操作装置 不好意思
    • 115. 发明授权
    • Apparatus for drying fruit
    • 水果干燥装置
    • US4205460A
    • 1980-06-03
    • US927631
    • 1978-07-24
    • William J. Taylor
    • William J. Taylor
    • F26B9/06F26B21/04F26B9/02
    • F26B21/04F26B9/066
    • An apparatus for circulating high temperature air at approximately 20,000 cubic feet per minute through an enclosed room in which fruit are stacked in sweat boxes on pallets. A fan draws the heated air from a heat source into a plurality of inlet ports at the bottom of the housing. A damper position at each of the inlet ports deflects the hot air entering the drying room upwardly between the stacks of containers in the drying room and the corresponding side wall of the housing towards said top, the hot air passing between the top of the stacks of containers in the room and the top of the housing, and down between the stacks of containers in the room and the opposite side wall of the housing. A recirculating port in the first-named side wall through which the fan draws the air from the opposite side wall between the individual containers in the stacks and across the fruit within the containers and back to the inlet of said source.
    • 一种用于将高温空气以每分钟20,000立方英尺的速度循环通过封闭室的装置,其中水果堆叠在托盘上的汗盒中。 风扇将加热的空气从热源吸入壳体底部的多个入口。 在每个入口端口处的阻尼器位置使进入干燥室的热空气向上在干燥室中的容器堆叠与壳体的相应侧壁之间朝向所述顶部偏转,热空气通过 房间中的容器和壳体的顶部,以及房间中的容器堆叠和壳体的相对侧壁之间的下降。 在第一名称的侧壁中的再循环端口,风扇通过该循环端口从堆叠中的各个容器之间的相对侧壁抽吸空气,并跨过容器内的水果并返回到所述源的入口。
    • 116. 发明授权
    • Method of starting a hot air furnace
    • 启动热风炉的方法
    • US4123000A
    • 1978-10-31
    • US753702
    • 1976-12-23
    • Robert F. Miller
    • Robert F. Miller
    • F26B21/04F26B21/00
    • F26B21/04
    • An apparatus for starting a hot air recirculating furnace system. Reduced power is applied to the motor which drives the recirculating fan to cause the motor to turn at a reduced speed. The furnace is ignited during the application of the reduced power to the motor. As the temperature in the furnace increases, the warmer air recirculates and the load on the fan decreases. The power supplied to the fan motor is then increased, thereby increasing its speed as a function of the increased temperature as sensed by a thermostat in the furnace system. Full power is applied to the fan motor when the sensed temperature reaches a selected desired maximum. The apparatus and the method eliminate squeal of the belt which drives the fan and reduce wear common to those techniques which apply full voltage to the recirculating fan at furnace start-up. Also, this system reaches the desired operating temperature more quickly than prior art systems as a result of a reduced recirculating airflow during a longer acceleration period.
    • 一种用于启动热空气再循环炉系统的装置。 对驱动再循环风扇的电动机施加减小的功率,以使电动机以降低的速度转动。 在将电力降低到电机的过程中,炉子被点燃。 随着炉中的温度升高,较暖的空气再循环并且风扇上的负载减小。 然后提供给风扇马达的功率增加,从而随着炉系统中的恒温器感测到的升高的温度而增加其速度。 当感测到的温度达到所选择的最大值时,将对风扇电机施加全部功率。 该装置和方法消除了驱动风扇的带的尖叫,并降低了在炉启动时向再循环风扇施加全电压的技术所共有的磨损。 此外,由于在较长的加速期间减少的循环气流,该系统比现有技术的系统更快地达到期望的操作温度。
    • 117. 发明授权
    • Method and apparatus for drying moisture-containing solids  particularly
domestic refuse and sludge cakes
    • 用于干燥含水固体的方法和装置,特别是家用垃圾和污泥蛋糕
    • US3946495A
    • 1976-03-30
    • US426247
    • 1973-12-19
    • Asriel Osdor
    • Asriel Osdor
    • F26B17/14F26B21/04F26B23/02F26B5/04
    • F26B21/04F26B17/1483F26B23/028Y02P70/40
    • Method and apparatus are described for the production of solid fuel and steam by drying moisture-containing solids, such as refuse and sludge cakes, in a multi-stage heating zone by using the moisture-containing solids as the feed-water in a direct contact countercurrent flow pressurized boiler. After vaporizing the bulk of the moisture in the heating zone of the boiler, the solid residue is further dried in a multi-stage flashing zone. From the upper end of the heating zone is removed a nearly saturated steam including the water vapor evaporated from the moisture-contained solids by the heat of cooling of the introduced superheated steam. A portion of the removed steam equal to the vaporized moisture is heated and then directed to a turbine, generating all the power required to operate the system. The bulk of the removed steam equal to the introduced superheated steam is compressed, reheated and recycled through the heating zone. The dried solid is removed at the lower end of the flashing zone and is incinerated, and the recovered heat is utilized to supply the heat required for said drying, and to produce saturated steam for heating purposes, or superheated steam for power generation.In the latter case the heat of condensation of the turbine exhaust steam is utilized advantageously as a heat source in a distillation plant for fresh water production.
    • 描述了通过使用含水固体作为直接接触的给水来在多级加热区中干燥含湿固体如垃圾和污泥的方法和设备来生产固体燃料和蒸汽 逆流加压锅炉。 在蒸发锅炉加热区中的大部分水分后,固体残余物在多级闪蒸区进一步干燥。 通过引入的过热蒸汽的冷却热,从加热区的上端除去包含由含湿固体蒸发的水蒸气的近饱和蒸汽。 被移除的蒸汽的一部分等于蒸发的水分被加热,然后被引导到涡轮机,产生操作系统所需的所有功率。 除去的蒸汽等于引入的过热蒸汽的大部分被压缩,再加热并通过加热区再循环。 将干燥的固体在闪蒸区域的下端除去并进行焚烧,并且利用回收的热量来供应所述干燥所需的热量,并产生用于加热目的的饱和蒸汽或用于发电的过热蒸汽。
    • 119. 发明授权
    • Continuous vacuum drier
    • 连续真空干燥机
    • US3597850A
    • 1971-08-10
    • US3597850D
    • 1970-03-11
    • NAT SERVICE IND INC
    • JENKINS JOHN W
    • B29B13/06B29C47/10F26B17/12F26B21/04F26B3/08F26B17/00
    • B29B13/065B29C47/0009B29C47/1018B29C47/1027F26B17/128F26B21/04
    • A continuous vacuum drier for removing moisture from solid synthetic resins in granular form prior to manufacturing into finished products. The synthetic resinous material is continuously supplied to the top of a closed drying hopper and removed from the bottom of the hopper. In one embodiment air withdrawn from the top of the hopper is circulated through a heater and is returned to the bottom of the hopper, where it travels upwardly through the synthetic resinous material in the hopper. In a second embodiment, air is withdrawn from the bottom of the hopper and is returned to the top of the hopper, where it travels downwardly through the synthetic resinous material in the hopper. The circulated air and the material in the hopper are heated as they pass grids of pipes which are heated by circulated hot water. In both embodiments, a vacuum pump is connected to reduce the air pressure in the system for increasing the efficiency of the drier and for causing the hopper to automatically fill with material to a predetermined level from a primary feeder hopper. A small amount of dry air may be introduced into the hopper for carrying off evaporated moisture. The dry material is fed by gravity from the bottom of the hopper to a processor.