Method of purifying liquor and purification apparatus
    1.
    发明申请
    Method of purifying liquor and purification apparatus 有权
    纯化液和净化装置的方法

    公开(公告)号:US20060292262A1

    公开(公告)日:2006-12-28

    申请号:US10573906

    申请日:2004-09-16

    Applicant: Yuji Asakawa

    Inventor: Yuji Asakawa

    CPC classification number: C12H1/0432 C12H1/14

    Abstract: After passing alcoholic liquors 20 through an HSO3 type strongly basic anion exchange resin layer 14, or after adding an HSO3 salt to alcoholic liquors; the alcoholic liquors are passed through a mixed bed layer 18 containing of an H type strongly acidic cation exchange resin and a free base type weakly basic anion exchange resin, or the alcoholic liquors are successively passed through an H type strongly acidic cation exchange resin layer and a free base type weakly basic anion exchange resin layer. According to this way, it is possible to remove aldehydes and inorganic salts from alcoholic liquors such as brewed alcoholic liquors and distilled alcoholic liquors, while strongly retaining a peculiar fragrance or retaining a manneristic flavor.

    Abstract translation: 在通过HSO 3类强碱性阴离子交换树脂层14或在向酒精中加入HSO 3盐之后使酒精液20通过后, 酒精液通过包含H型强酸性阳离子交换树脂和游离碱型弱碱性阴离子交换树脂的混合层18,或者醇液依次通过H型强酸性阳离子交换树脂层, 游离碱型弱碱性阴离子交换树脂层。 按照这种方式,可以从醇酒和蒸馏酒精等醇酒中除去醛和无机盐,同时强烈地保持特殊的香味或保持风味。

    Mixed bed type sugar solution refining system and regeneration method for such apparatus

    公开(公告)号:US06508939B2

    公开(公告)日:2003-01-21

    申请号:US10000589

    申请日:2001-10-22

    Applicant: Yuji Asakawa

    Inventor: Yuji Asakawa

    CPC classification number: C13B20/142 B01J49/09 B01J49/50

    Abstract: By passing an alkali regenerating agent A through a basic anion exchange resin (3), and through a strongly acidic cation exchange resin (4), the basic anion exchange resin can be regenerated while amphoteric organic materials such as the amino acids captured at the strongly acidic cation exchange resin can be desorbed. Then, an acid regenerating agent B is passed through the strongly acidic cation exchange resin to regenerate the strongly acidic cation exchange resin.

    ELECTRODEIONIZATION APPARATUS FOR PRODUCING DEIONIZED WATER
    3.
    发明申请
    ELECTRODEIONIZATION APPARATUS FOR PRODUCING DEIONIZED WATER 有权
    用于生产水分的电极化装置

    公开(公告)号:US20140202867A1

    公开(公告)日:2014-07-24

    申请号:US14236690

    申请日:2012-08-01

    Abstract: Provided is an electrodeionization apparatus for producing deionized water, capable of removing or reducing a biased flow of electric current in a deionization chamber. In the electrodeionization apparatus for producing deionized water, at least one deionization treatment unit including the deionization chamber and a pair of concentration chambers adjacent to both sides of the deionization chamber is disposed between a cathode and an anode. In the deionization chamber, anion exchanger layers and cation exchanger layers are stacked in an order in which a last ion exchanger layer through which water to be treated passes is an anion exchanger layer. A bipolar membrane is formed on the cathode side of the anion exchanger layer in the deionization chamber. The anion exchange membrane of the bipolar membrane is in contact with the anion exchanger layer.

    Abstract translation: 提供一种用于产生去离子水的电去电离装置,其能够去除或减少去离子室中的电流的偏置流动。 在用于产生去离子水的电去离子装置中,至少一个包括去离子室的去离子处理单元和与去离子室两侧相邻的一对浓缩室设置在阴极和阳极之间。 在去离子室中,阴离子交换层和阳离子交换层的顺序层叠,其中待处理水的最后一个离子交换层是阴离子交换层。 在去离子室中的阴离子交换层的阴极侧形成双极性膜。 双极性膜的阴离子交换膜与阴离子交换层接触。

    ELECTRODEIONIZATION APPARATUS FOR PRODUCING DEIONIZED WATER
    4.
    发明申请
    ELECTRODEIONIZATION APPARATUS FOR PRODUCING DEIONIZED WATER 有权
    用于生产水分的电极化装置

    公开(公告)号:US20130068624A1

    公开(公告)日:2013-03-21

    申请号:US13701819

    申请日:2011-05-20

    Abstract: An electrodeionization apparatus for producing deionized water comprises a deionization treatment unit including deionization chamber D and a pair of concentration chambers C1 and C2 placed adjacent to deionization chamber D on opposite sides thereof and those concentration chambers are filled with anion exchangers. The deionization chamber D is partitioned by an ion exchange membrane into first small deionization chamber D-1 adjacent to concentration chamber C1 and second small deionization chamber D-2 adjacent to concentration chamber C2. First small deionization chamber D-1 is filled with an anion exchanger. Second small deionization chamber D-2 is filled with an anion exchanger and a cation exchanger in a sequence such that the ion exchanger, through which water that is to be treated finally passes, is the anion exchanger.

    Abstract translation: 用于制造去离子水的电去离子装置包括去离子处理单元,其包括去离子室D和在其相对侧上与去离子室D相邻放置的一对浓缩室C1和C2,并且这些浓缩室填充有阴离子交换剂。 去离子室D被离子交换膜分隔成与浓缩室C1相邻的第一小去离子室D-1和与浓缩室C2相邻的第二小去离子室D-2。 第一个小的去离子室D-1填充有阴离子交换剂。 第二个小去离子室D-2以一个顺序填充阴离子交换剂和阳离子交换剂,使得最终通过待处理的水的离子交换剂是阴离子交换剂。

    Electrodeionization apparatus for producing deionized water
    6.
    发明授权
    Electrodeionization apparatus for producing deionized water 有权
    用于生产去离子水的电去离子装置

    公开(公告)号:US08871073B2

    公开(公告)日:2014-10-28

    申请号:US13701819

    申请日:2011-05-20

    Abstract: An electrodeionization apparatus for producing deionized water comprises a deionization treatment unit including deionization chamber D and a pair of concentration chambers C1 and C2 placed adjacent to deionization chamber D on opposite sides thereof and those concentration chambers are filled with anion exchangers. The deionization chamber D is partitioned by an ion exchange membrane into first small deionization chamber D-1 adjacent to concentration chamber C1 and second small deionization chamber D-2 adjacent to concentration chamber C2. First small deionization chamber D-1 is filled with an anion exchanger. Second small deionization chamber D-2 is filled with an anion exchanger and a cation exchanger in a sequence such that the ion exchanger, through which water that is to be treated finally passes, is the anion exchanger.

    Abstract translation: 用于制造去离子水的电去离子装置包括去离子处理单元,其包括去离子室D和在其相对侧上与去离子室D相邻放置的一对浓缩室C1和C2,并且这些浓缩室填充有阴离子交换剂。 去离子室D被离子交换膜分隔成与浓缩室C1相邻的第一小去离子室D-1和与浓缩室C2相邻的第二小去离子室D-2。 第一个小的去离子室D-1填充有阴离子交换剂。 第二个小去离子室D-2以一个顺序填充阴离子交换剂和阳离子交换剂,使得最终通过待处理的水的离子交换剂是阴离子交换剂。

    Mixed-bed type sugar solution refining system and regeneration method for such apparatus

    公开(公告)号:US06362240B1

    公开(公告)日:2002-03-26

    申请号:US09740594

    申请日:2000-12-19

    Applicant: Yuji Asakawa

    Inventor: Yuji Asakawa

    Abstract: By passing an alkali regenerating agent A through a basic anion exchange resin (3), and through a strongly acidic cation exchange resin (4), the basic anion exchange resin can be regenerated while amphoteric organic materials such as the amino acids captured at the strongly acidic cation exchange resin can be desorbed. Then, an acid regenerating agent B is passed through the strongly acidic cation exchange resin to regenerate the strongly acidic cation exchange resin.

    Method and apparatus for purifying alcoholic liquors
    10.
    发明授权
    Method and apparatus for purifying alcoholic liquors 有权
    净酒精液的方法和装置

    公开(公告)号:US07326349B2

    公开(公告)日:2008-02-05

    申请号:US10573906

    申请日:2004-09-16

    Applicant: Yuji Asakawa

    Inventor: Yuji Asakawa

    CPC classification number: C12H1/0432 C12H1/14

    Abstract: After passing alcoholic liquors 20 through an HSO3 type strongly basic anion exchange resin layer 14, or after adding an HSO3 salt to alcoholic liquors; the alcoholic liquors are passed through a mixed bed layer 18 containing of an H type strongly acidic cation exchange resin and a free base type weakly basic anion exchange resin, or the alcoholic liquors are successively passed through an H type strongly acidic cation exchange resin layer and a free base type weakly basic anion exchange resin layer. According to this way, it is possible to remove aldehydes and inorganic salts from alcoholic liquors such as brewed alcoholic liquors and distilled alcoholic liquors, while strongly retaining a peculiar fragrance or retaining a manneristic flavor.

    Abstract translation: 在通过HSO 3类强碱性阴离子交换树脂层14或在向酒精中加入HSO 3盐之后使酒精液20通过后, 酒精液通过包含H型强酸性阳离子交换树脂和游离碱型弱碱性阴离子交换树脂的混合层18,或者醇液依次通过H型强酸性阳离子交换树脂层, 游离碱型弱碱性阴离子交换树脂层。 按照这种方式,可以从醇酒和蒸馏酒精等醇酒中除去醛和无机盐,同时强烈地保持特殊的香味或保持风味。

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