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    • 2. 发明授权
    • Method for catalytic gas phase oxidation
    • 催化气相氧化方法
    • US06613940B1
    • 2003-09-02
    • US09648950
    • 2000-08-25
    • Takeshi NishimuraMasakatsu MoriMasatsugu KitauraOsamu DodoDaisuke Nakamura
    • Takeshi NishimuraMasakatsu MoriMasatsugu KitauraOsamu DodoDaisuke Nakamura
    • C07C5116
    • B01J8/008B01J8/067B01J2208/00212B01J2208/00221B01J2208/00256C07C45/35C07C51/215C07C51/252C07C51/255C07C51/265C07C47/22C07C57/145C07C63/16C07C57/02
    • In the reaction of catalytic gas phase oxidation by means of a shell-and-tube type reactor adapted to circulate a heating medium to the shell of the reactor through the medium of a circulation device connecting an annular conduit connected thereto, a method for the catalytic gas phase oxidation characterized by subjecting a part of the heating medium extracted from the shell of the reactor to heat exchange, introducing the heating medium resulting from the heat exchange into the proximity of a heating medium circulation inlet on the inlet side of the circulation device or the annular conduit on the outlet side of the reactor. The flow rate of the heating medium after the heat exchange is preferred to be in the range of 2-40 vol. % based on the flow rate of the heating medium within the shell of the reactor and the temperature difference of the heating medium at the inlet and the outlet to be in the range of 15-150° C. According to this invention, it is made possible to reduce evenly the hot spots in the reaction tubes, improve the yield of the product aimed at, and implement a reaction of catalytic gas phase oxidation of propylene or isobutylene.
    • 在通过壳管式反应器进行催化气相氧化的反应中,该反应器适于通过连接连接其的环形导管的循环装置的介质将加热介质循环到反应器的壳体,催化剂的方法 气相氧化特征在于使从反应器壳体中提取的一部分加热介质进行热交换,将由热交换产生的加热介质引入循环装置入口侧的加热介质循环入口附近,或 反应器出口侧的环形导管。 热交换后的加热介质的流量优选为2-40体积%。 基于反应器壳体内的加热介质的流量,入口和出口处的加热介质的温度差在15-150℃的范围内。根据本发明,制成 可能均匀地减少反应管中的热点,提高目标产品的产率,并实现丙烯或异丁烯的催化气相氧化反应。
    • 5. 发明授权
    • Device and process for crystallizing (meth)acrylic acid
    • 用于结晶(甲基)丙烯酸的装置和方法
    • US08859809B2
    • 2014-10-14
    • US13381449
    • 2010-06-24
    • Kazuhiko SakamotoKoji UenoYoshitake IshiiMasatsugu Kitaura
    • Kazuhiko SakamotoKoji UenoYoshitake IshiiMasatsugu Kitaura
    • C07C51/42B01D9/00C07C51/43
    • B01D9/0013B01D9/0063C07C51/43C07C57/04
    • A crystallization device and a crystallization process are provided for obtaining (meth)acrylic acid with higher purity without causing leakage of a crude solution by preventing complete clogging in a crystallization tube from occurring. The device for crystallizing (meth)acrylic acid includes a crude (meth)acrylic acid solution supply part, a crystallization tube, a heat medium supply tube, a heat medium discharge tube, a storage part of a crude (meth)acrylic acid solution passed through the crystallization tube, a tube for circulating and supplying the crude (meth)acrylic acid solution to the supply part from the storage part, and a pump for circulating and supplying the crude (meth)acrylic acid solution to the supply part from the storage part, and also includes a pressure meter in the circulate-supply tube. The device is used for carrying out dynamic crystallization in a batch manner by circulating the crude (meth)acrylic acid solution to flow the crude solution downward along the inner wall of the crystallization tube in a coating film-like state.
    • 提供了一种结晶装置和结晶方法,用于获得高纯度的(甲基)丙烯酸,而不会通过防止结晶管中发生完全堵塞而导致粗溶液泄漏。 用于结晶(甲基)丙烯酸的装置包括粗(甲基)丙烯酸溶液供应部分,结晶管,热介质供应管,热介质放电管,粗(甲基)丙烯酸溶液的储存部分通过 通过结晶管,将来自储存部的粗(甲基)丙烯酸溶液循环供给到供给部的管,以及从储存部向供给部循环供给粗(甲基)丙烯酸溶液的泵 并且还包括在循环供应管中的压力计。 该装置用于以分批方式进行动态结晶,通过循环粗制(甲基)丙烯酸溶液使涂料膜状态沿着结晶管的内壁向下流动粗溶液。
    • 8. 发明申请
    • DEVICE AND PROCESS FOR CRYSTALLIZING (METH) ACRYLIC ACID
    • 用于结晶(甲基)丙烯酸的装置和方法
    • US20120108847A1
    • 2012-05-03
    • US13381449
    • 2010-06-24
    • Kazuhiko SakamotoKoji UenoYoshitake IshiiMasatsugu Kitaura
    • Kazuhiko SakamotoKoji UenoYoshitake IshiiMasatsugu Kitaura
    • C07C51/43B01J19/00
    • B01D9/0013B01D9/0063C07C51/43C07C57/04
    • The objective of the present invention is to provide a crystallization device and a crystallization process for obtaining (meth)acrylic acid with higher purity without causing leakage of a crude solution by preventing complete clogging in a crystallization tube from occurring. The device for crystallizing (meth)acrylic acid according to the present invention is characterized in comprising a crude (meth)acrylic acid solution supply part, a crystallization tube, a heat medium supply tube, a heat medium discharge tube, a storage part of a crude (meth)acrylic acid solution passed through the crystallization tube, a tube for circulating and supplying the crude (meth)acrylic acid solution to the supply part from the storage part, and a pump for circulating and supplying the crude (meth)acrylic acid solution to the supply part from the storage part; and further comprising a pressure meter in the circulate-supply tube; wherein the device is used for carrying out dynamic crystallization in a batch manner by circulating the crude (meth)acrylic acid solution to flow the crude solution downward along the inner wall of the crystallization tube in a coating film-like state.
    • 本发明的目的是提供一种结晶装置和结晶方法,用于通过防止结晶管中发生完全堵塞而获得更高纯度的(甲基)丙烯酸,而不会导致粗溶液泄漏。 根据本发明的用于结晶(甲基)丙烯酸的装置的特征在于包含粗(甲基)丙烯酸溶液供应部分,结晶管,热介质供给管,热介质放电管, 粗(甲基)丙烯酸溶液通过结晶管,将来自储存部分的粗(甲基)丙烯酸溶液循环供给到供应部分的管和用于循环供给粗(甲基)丙烯酸 从储存部分解决供应部件; 并且还包括在所述循环供应管中的压力计; 其中所述装置用于通过循环粗制(甲基)丙烯酸溶液以使涂层膜状状态沿着结晶管的内壁向下流动的方式以间歇方式进行动态结晶。
    • 9. 发明申请
    • METHOD FOR PRODUCING (METH) ACRYLIC ACID
    • 生产(甲基)丙烯酸的方法
    • US20120077947A1
    • 2012-03-29
    • US13320567
    • 2010-04-30
    • Masatsugu Kitaura
    • Masatsugu Kitaura
    • C08F20/06C07C57/04
    • C07C51/43C07C57/04
    • The objective of the present invention is to provide a method for efficiently producing (meth)acrylic acid by crystallization using a plurality of crystallizer to purify (meth)acrylic acid and a refrigerator for supplying both of a cooling medium and a heating medium, while the refrigerator is stably operated for supplying media having a proper temperature and the temperature of the crystallizers is maintained. The method for producing (meth)acrylic acid according to the present invention is characterized in comprising the steps of at least crystallizing (meth)acrylic acid and melting the (meth)acrylic acid crystal obtained in the crystallization step; wherein two or more crystallizers are employed; when both of the crystallization step and the melting step are concurrently carried out in separate crystallizers, from a refrigerator, a cooling medium is supplied to a crystallizer for carrying out the crystallization step to crystallize (meth)acrylic acid and a heating medium is supplied to other crystallizer for carrying out the melting step to melt the (meth)acrylic acid crystal; and when only the crystallization step is carried out before the melting step is carried out, a temperature of a heating medium to be returned to the refrigerator is previously decreased to be lower than a set temperature for the melting step before only the crystallization step is carried out.
    • 本发明的目的是提供一种使用多个结晶器通过结晶高效制备(甲基)丙烯酸以纯化(甲基)丙烯酸的方法和用于供应冷却介质和加热介质两者的制冷机,同时 为了供给具有适当温度的介质并保持结晶器的温度,冰箱被稳定地操作。 本发明的(甲基)丙烯酸的制造方法的特征在于,至少使(甲基)丙烯酸结晶并使在结晶工序中得到的(甲基)丙烯酸结晶熔融的步骤; 其中采用两种或多种结晶器; 当结晶步骤和熔融步骤同时在单独的结晶器中从冰箱中进行时,将冷却介质供应到结晶器,以进行结晶步骤以使(甲基)丙烯酸结晶,并将加热介质供应至 用于进行熔融步骤以熔化(甲基)丙烯酸晶体的其它结晶器; 并且仅在进行熔融步骤之前仅进行结晶步骤时,将返回到冰箱的加热介质的温度预先降低至低于在仅进行结晶步骤之前的熔融步骤的设定温度 出来