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    • 31. 发明授权
    • Process for inhibiting the polymerization of easily-polymerizable compounds
    • 抑制易聚合化合物聚合的方法
    • US06409886B1
    • 2002-06-25
    • US09549531
    • 2000-04-14
    • Yukihiro MatsumotoTakeshi Nishimura
    • Yukihiro MatsumotoTakeshi Nishimura
    • B01D314
    • C07C51/50B01D3/148B01D3/20C07C51/44C07C67/54Y10S203/22C07C57/04C07C69/54
    • In distillation of easily polymerizable compounds such as (meth)acrylic acid and (meth)acrylic esters using a distillation unit, a liquid having substantially the same composition with that of a liquid surrounding a constitutive member placed in the distillation unit is sprayed by a spraying and supplying device. The liquid supplied by the spraying and supplying device preferably has a wetting liquid rate (of the sprayed and supplied liquid, a flow rate of a liquid attaching to and wetting the constitutive member) of 0.5 m3/m2hr or more relative to the surface area of the constitutive member. The liquid supplied by the spraying and supplying device preferably contains a polymerization inhibitor. It is also preferred to supply a gas containing molecular oxygen to the distillation unit. This process can effectively inhibit the polymerization of the easily polymerizable compounds, which polymerization is liable to occur inside the distillation unit.
    • 在使用蒸馏单元蒸馏易于聚合的化合物如(甲基)丙烯酸和(甲基)丙烯酸酯)时,通过喷雾喷雾与包含在蒸馏单元中的构成成分的液体基本相同的组成的液体 和供应装置。 由喷雾供给装置供给的液体优选相对于表面积为0.5m 3 / m 2·小时以上的润湿液体率(喷射和供给液体的润湿液体,附着并润湿构成部件的液体的流量) 组成成员。 由喷雾供给装置供给的液体优选含有阻聚剂。 还优选向蒸馏单元供应含有分子氧的气体。 该方法可以有效地抑制容易聚合的化合物的聚合,该聚合在蒸馏单元内容易发生聚合。
    • 35. 发明授权
    • Process for inhibiting a polymerization in a vacuum section of an easily polymerizable compound purification system
    • 在容易聚合的化合物净化系统的真空部分中抑制聚合的方法
    • US06878239B1
    • 2005-04-12
    • US09587387
    • 2000-06-05
    • Yukihiro MatsumotoTakeshi Nishimura
    • Yukihiro MatsumotoTakeshi Nishimura
    • B01D3/00C07B61/00C07B63/00C07B63/04C07C51/50C07C57/07C07C57/075C07C67/62C07C69/54C08F2/38B01D3/10B01D3/34C07C57/025
    • C07B63/04C07C67/62Y10S203/11Y10S203/16Y10S203/22C07C69/54
    • A process for inhibiting a polymerization of an easily polymerizable compound purification system is disclosed.According to the present invention, the polymerization of the easily polymerizable compound such as (meth)acrylic acid and (meth)acrylate flowed into a vacuum section can be inhibited by contacting a liquid containing a polymerization inhibitor with the compound directly in the vacuum section.When the vacuum section includes a gas and liquid contact chamber (usually a condenser), the liquid containing a polymerization inhibitor may be supplied to the chamber. When the vacuum section includes a liquid ejector and/or a nash pump as a vacuuming device, the liquid containing a polymerization inhibitor may be circulated by the liquid ejector and/or the nash pump for reducing a pressure of a purifying section. Examples of easily polymerizable compounds are (meth)acrylic acid and (meth)acrylates. The process of the invention is capable of inhibiting the polymerization of the easily polymerizable compound such as (meth)acrylic acid and (meth)acrylate in a vacuum section of a purifying system. The system of the invention is suitable for purifying the easily polymerizable compound.
    • 公开了抑制容易聚合的化合物净化系统的聚合的方法。根据本发明,可以抑制流入真空部分的(甲基)丙烯酸和(甲基)丙烯酸酯等易聚合性化合物的聚合, 将含有聚合抑制剂的液体直接与真空部分接触。当真空部分包括气体和液体接触室(通常为冷凝器)时,可以将含有阻聚剂的液体供应到室中。 当真空部分包括作为抽真空装置的液体喷射器和/或纳什泵时,含有聚合抑制剂的液体可以通过液体喷射器和/或纳什泵循环,以降低净化部分的压力。 易聚合性化合物的实例是(甲基)丙烯酸和(甲基)丙烯酸酯。 本发明的方法能够在纯化系统的真空部分中抑制易聚合化合物如(甲基)丙烯酸和(甲基)丙烯酸酯的聚合。 本发明的系统适用于纯化容易聚合的化合物。
    • 36. 发明授权
    • Method for absorbing acrylic acid and method for purifying acrylic acid
    • 丙烯酸的吸收方法和丙烯酸的净化方法
    • US06713648B2
    • 2004-03-30
    • US09780787
    • 2001-02-09
    • Harunori HiraoYoshitake IshiiYukihiro MatsumotoTakeshi Nishimura
    • Harunori HiraoYoshitake IshiiYukihiro MatsumotoTakeshi Nishimura
    • C07C5142
    • C07C51/44B01D3/225C07C51/48C07C57/04
    • This invention concerns a method for absorbing acrylic acid, characterized by supplying an acrylic acid-containing reaction gas component obtained by the reaction of catalytic gas phase oxidation to an acrylic acid absorption column and advancing a high boiling inert hydrophobic organic liquid into counter-flow contact with said reaction gas in said acrylic acid absorption column with the mass flow rate of the organic liquid fixed in the range of 0.2-4.5 times the mass flow rate of the acrylic acid in the reaction gas thereby absorbing acrylic acid in said organic liquid and obtaining an acrylic acid-containing solution and a method for purifying acrylic acid, comprising a step for purifying the acrylic acid-containing organic liquid obtained by the step mentioned above. By this invention, a product of acrylic acid containing a low boiling substance at a low concentration can be produced.
    • 本发明涉及一种吸收丙烯酸的方法,其特征在于将通过催化气相氧化反应获得的含丙烯酸的反应气体组分供给丙烯酸吸收塔,并将高沸点惰性疏水性有机液体推入逆流接触 所述丙烯酸吸收塔中的所述反应气体的有机液体的质量流量固定在反应气体中丙烯酸的质量流量的0.2-4.5倍的范围内,从而吸收所述有机液体中的丙烯酸,并获得 含丙烯酸的溶液和丙烯酸的精制方法,其特征在于,含有通过上述工序得到的含丙烯酸的有机液的纯化工序。 通过本发明,可以制备含有低浓度低沸点物质的丙烯酸的产物。
    • 38. 发明授权
    • Method for distilling polymerizable compound or liquid containing polymerizable compound
    • 蒸馏可聚合化合物或含有可聚合化合物的液体的方法
    • US06666956B1
    • 2003-12-23
    • US09506715
    • 2000-02-18
    • Takeshi NishimuraYukihiro Matsumoto
    • Takeshi NishimuraYukihiro Matsumoto
    • B01D332
    • B01D3/322C07C51/44Y10S203/11Y10S203/22C07C57/04
    • In distillation of a polymerizable compound such as (meth)acrylic acid or a liquid containing such a polymerizable compound with use of a distillation column equipped with a reboiler, (a) a vertical multi-tube reboiler whose outlet nozzle inside diameter (D1) is 0.2 to 1 time its reboiler shell inside diameter (D2) is used as the reboiler, (b) an outlet of an outlet nozzle of the reboiler to a gas-phase section of the distillation column is provided at a position such that a distance L from the top tubesheet of the reboiler to the lower end of the outlet of the outlet nozzle satisfies L=(0.4 to 3)×D1, and (c) a liquid level in the distillation column is maintained in a range such that a height H of the liquid level from the top tubesheet of the reboiler satisfies H=(0.1 to 0.8)×L.
    • 在使用装备有再沸器的蒸馏塔的可聚合化合物如(甲基)丙烯酸或含有这种聚合性化合物的液体的蒸馏中,(a)出口喷嘴内径(D1)的垂直多管再沸器 将其再沸器壳体内径(D2)的0.2至1次用作再沸器,(b)在蒸馏塔的气相部分的出口喷嘴的出口设置在距离L 从再沸器的顶部管板到出口喷嘴的出口的下端满足L =(0.4〜3)×D 1,(c)蒸馏塔中的液面保持在高度H 来自再沸器的顶部管板的液面满足H =(0.1〜0.8)×L。