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    • 22. 发明授权
    • Continuous crystallization
    • 持续结晶
    • US3981739A
    • 1976-09-21
    • US501862
    • 1974-08-30
    • Morris DmitrovskyAntoine H. Kokke
    • Morris DmitrovskyAntoine H. Kokke
    • C13B30/02C13K1/10C13F1/02C13K5/00C13K11/00
    • C13B30/022C13K1/10
    • A crystallizable solute is crystallized from a solution containing the same by introducing a solution of said solute into a first stage evaporative-crystallization zone together with seed solute crystals. Within the first stage evaporative-crystallization zone the solution is concentrated to yield a saturated first stage concentrate containing crystals of said solute. The crystals of said solute are substantially larger than said seed crystals and are suspended in a solution more concentrated with respect to said solute than the solution supplied to said first evaporative-crystallization zone. A stream of said first concentrate is removed from said first evaporative-crystallization zone and transferred to a second evaporative-crystallization zone for further concentration or crystallization of solute and for the production of solute crystals of increased size. There is continuously recovered from the second evaporative-crystallization zone a slurry having a total solute or solids content of about 86-94 percent by weight and containing the solute crystals of desired crystal size.
    • 通过将所述溶质的溶液与种子溶质晶体一起引入第一阶段蒸发结晶区,从含有该溶质的溶液中结晶可结晶溶质。 在第一阶段的蒸发结晶区域内,将溶液浓缩,得到含有所述溶质晶体的饱和第一阶段浓缩物。 所述溶质的晶体基本上大于所述晶种,并且相对于所述溶质悬浮在比所提供给所述第一蒸发结晶区的溶液更浓的溶液中。 将所述第一浓缩物流从所述第一蒸发结晶区域中移出并转移到第二蒸发结晶区域,以进一步浓缩或结晶溶质和用于生产增大尺寸的溶质晶体。 从第二蒸发结晶区连续回收总溶质或固体含量为约86-94重量%并含有所需晶体尺寸的溶质晶体的浆料。
    • 24. 发明申请
    • PROCESS AND EQUIPMENT FOR SUGAR CRYSTALLIZATION BY CONTROLLED COOLING
    • 通过控制冷却进行糖果结晶的工艺和设备
    • US20140000586A1
    • 2014-01-02
    • US13930650
    • 2013-06-28
    • DEDINI S/A INDUSTRIAS DE BASE
    • Paulo Eduardo Mantelatto
    • C13K13/00
    • C13K13/00B01D9/0013B01D9/004B01D9/0063C13B30/022
    • A process is proposed for crystallizing, by progressively cooling, in multiple stages arranged in series in a crystallization vessel (10), a descending continuous flow of a saturated sucrose solution at a temperature from about 78° to about 120° C., each stage maintaining the sucrose solution being crystallized at a predetermined temperature, until reaching a temperature from about 25 to 40° C., obtaining substantially pure sucrose crystals. A suspension containing sugar seeds is introduced in the crystallizing equipment, in the first stage, jointly with the saturated sucrose solution of 1.05-1.15. In another embodiment of the invention, the saturated solution is fed and its temperature is controlled, already in the first stage of the vessel (10), to obtain a supersaturation between 1.05 and 1.15, inducing the formation of small crystals used as crystallization seeds.
    • 提出了一种通过逐步冷却在结晶容器(10)中串联排列的多个阶段结晶的方法,在约78℃至约120℃的温度下,饱和蔗糖溶液的下降连续流动,每个阶段 保持蔗糖溶液在预定温度下结晶,直到达到约25至40℃的温度,得到基本上纯的蔗糖晶体。 将含有糖种子的悬浮液在第一阶段中与饱和蔗糖溶液1.05-1.15一起引入结晶设备中。 在本发明的另一个实施方案中,进料饱和溶液,并且已经在容器(10)的第一阶段中控制其温度,以获得1.05-1.15的过饱和度,诱导形成用作结晶种子的小晶体。
    • 25. 发明申请
    • Continuous Vacuum Pan
    • 连续真空盘
    • US20110297331A1
    • 2011-12-08
    • US13125243
    • 2009-09-10
    • David J. LoveStephen D. Peacock
    • David J. LoveStephen D. Peacock
    • B01D1/00B01D1/06
    • C13B30/022B01D9/0022
    • This invention relates to a continuous vacuum pan for use in the sugar processing industry, and more particularly but not exclusively, to a vertical, double calandria, continuous vacuum pan. The vacuum pan includes a vessel having a first enclosed chamber and a second enclosed chamber. A first heat exchanger is located in the first chamber, with a first vapour space defined in the first chamber above the first heat exchanger. A second heat exchanger located in the second chamber, with a second vapour space defined in the second chamber above the second heat exchanger. The first heat exchanger and the second heat exchanger both have heat transfer medium inlets, and the vacuum pan is characterized therein that the heat transfer medium inlet of the second heat exchanger is in flow communication with the first vapour space, in order for vapour contained in the first vapour space to be conveyed through the second heat exchanger as heat transfer medium.
    • 本发明涉及一种用于糖加工工业的连续真空盘,更具体但非排他地涉及一种垂直双重排气管连续式真空锅。 真空盘包括具有第一封闭室和第二封闭室的容器。 第一热交换器位于第一室中,第一蒸气空间限定在第一热交换器上方的第一室中。 位于第二室中的第二热交换器,在第二热交换器上方的第二室中限定有第二蒸气空间。 第一热交换器和第二热交换器都具有传热介质入口,并且其特征在于,第二热交换器的传热介质入口与第一蒸气空间流动连通,以便包含在 作为传热介质通过第二热交换器输送的第一蒸气空间。
    • 28. 发明授权
    • Sugar refining process
    • 糖精炼过程
    • US4119436A
    • 1978-10-10
    • US799268
    • 1977-05-23
    • Milovan Bosnjak
    • Milovan Bosnjak
    • C13B25/00C13B30/02C13F1/00C13G1/02
    • C13B30/002C13B30/022Y10S159/39
    • A process for the production of sugar from either sugar beets or cane wherein of the total amount of thin juice processed, only that amount required to produce the vapor needed for the sugar boiling phase and the desired density of thick juice is directly evaporated while the remainder or excess over and above these requirements is recompressed. Essentially only that fraction of the latent heat of vaporization required for process heating is extracted from the already limited amount of vapor employed in sugar boiling by transferring the heat contained in a portion of this vapor to a refrigerant which is then recompressed so as to raise the temperature thereof to a level of approximately 95.degree. C.
    • 从糖甜菜或甘蔗生产糖的方法,其中加工的精制果汁的总量只有生产糖沸点所需的蒸气所需的量和所需浓稠果汁的浓度才直接蒸发,而其余的 或超过这些要求的超量被重新压缩。 基本上只有通过将该蒸汽的一部分中所含的热量转移到然后被再压缩的制冷剂中,从糖煮沸中使用的已经有限量的蒸气中提取了蒸发需要的部分潜热, 温度至约95℃
    • 29. 发明授权
    • Crystallization apparatus
    • 水晶装置
    • US3837811A
    • 1974-09-24
    • US29285872
    • 1972-09-28
    • FIVES LILLE CAIL
    • WINDAL G
    • B01D9/02B01D9/00C13B30/02
    • C13B30/022B01D9/0031
    • A crystallization apparatus with a horizontal tank subdivided into a plurality of intercommunicating compartments has a plurality of walls parallel to the longitudinal axis of the tank arranged in each compartment to form therein two cells laterally adjacent the tank walls and at least one central cell. The neighboring cells in each compartment also communicate with each other, as does each cell laterally adjacent the tank walls with a like cell upstream or downstream, the ports in the dividing walls being so arranged that the product in the tank circulates therethrough in a sinuous path. Radiators are positioned in the lower part of the tank and pass through all compartments, the radiators being divided into several sections each positioned in one of the cells and forming in each cell a return passage for the product under the radiators.
    • 具有细分成多个相互连通的隔间的水平箱的结晶装置具有平行于每个隔室中的箱的纵向轴线的多个壁,以在其中形成横向邻近罐壁和至少一个中心室的两个单元。 每个隔室中的相邻电池也相互连通,每个电池横向邻近罐壁,在上游或下游具有类似的电池,分隔壁中的端口被布置成使得容器中的产品在弯曲的路径中循环通过 。 散热器定位在罐的下部并穿过所有隔室,散热器被分成几个部分,每个部分定位在一个电池中,并在每个电池中形成用于产品在散热器下方的返回通道。