쇼핑제의 제조방법 및 그 제조방법에 의한 쇼핑제
    31.
    发明公开
    쇼핑제의 제조방법 및 그 제조방법에 의한 쇼핑제 有权
    用相同方法制造的皂洗剂和皂洗剂的制造方法

    公开(公告)号:KR20180020562A

    公开(公告)日:2018-02-28

    申请号:KR20160105096

    申请日:2016-08-18

    Inventor: CHO CHANG SUB

    CPC classification number: C11D11/0017 C11D7/26 C11D7/50 C11D11/0094 D06L1/08

    Abstract: 본발명은정제수일부에디알킬나프탈렌설폰산나트륨, 소르비톨및 소듐벤조에이트를용해및 혼합하는 1차반응단계; 상기 1차반응단계에서형성된혼합물에소듐글루코네이트, 구연산및 나머지정제수를첨가하고용해및 혼합하는 2차반응단계; 상기 2차반응단계에서형성된혼합물에서불순물을제거하는여과단계; 상기여과된혼합물을숙성시키는숙성단계를포함하는쇼핑제제조방법및 상기제조방법에의하여제조되는쇼핑제에관한것이다.

    Abstract translation: 本发明涉及一种组合物的制备方法,该组合物包括将一些十四烷基萘磺酸钠,山梨糖醇和苯甲酸钠溶解并混入精制水中的第一反应步骤; 第二反应步骤,将葡糖酸钠,柠檬酸和剩余的纯化水加入到在第一反应步骤中形成的混合物中,溶解并混合该混合物; 从第二反应步骤中形成的混合物中除去杂质的过滤步骤; 老化过滤后的混合物的老化步骤和通过该制造方法制备的购物代理商。

    염색 물성이 개선된 폴리에스테르 직물의 염색방법
    32.
    发明授权
    염색 물성이 개선된 폴리에스테르 직물의 염색방법 有权
    用于改善染色特性的涤纶纺织品的染色方法

    公开(公告)号:KR101216482B1

    公开(公告)日:2012-12-31

    申请号:KR1020110106976

    申请日:2011-10-19

    CPC classification number: D06P3/36 D06L1/08 D06M15/03

    Abstract: PURPOSE: A method for dyeing a polyester fabric is provided to modify the surface of the polyester fabric using chitosan-acetic acid solution and to improve leveling property and color fastness. CONSTITUTION: A method for dyeing a polyester fabric comprises: a step of modifying the surface of the polyester fabric using an antimony free nontoxic catalyst; a step of dyeing the polyester fabric using a dyeing solution containing a chitosan-acetic acid solution and a solution containing one or more disperse dyes; and step of reduction-cleaning the fabric using sodium hydrosulfite or sodium hydroxide.

    Abstract translation: 目的:提供一种染色聚酯织物的方法,以使用壳聚糖 - 乙酸溶液改性聚酯织物的表面,并改善流平性和色牢度。 构成:用于染色聚酯织物的方法包括:使用无锑无毒催化剂改性聚酯织物的表面的步骤; 使用含有壳聚糖 - 乙酸溶液的染色溶液和含有一种或多种分散染料的溶液染色聚酯织物的步骤; 以及使用连二亚硫酸钠或氢氧化钠还原清洗织物的步骤。

    CLEANING SYSTEM UTILIZING AN ORGANIC CLEANING SOLVENT AND A PRESSURIZED FLUID SOLVENT
    35.
    发明公开
    CLEANING SYSTEM UTILIZING AN ORGANIC CLEANING SOLVENT AND A PRESSURIZED FLUID SOLVENT 审中-公开
    使用有机清洁溶剂和加压流体溶剂的清洁系统

    公开(公告)号:EP1381728A1

    公开(公告)日:2004-01-21

    申请号:EP02736584.0

    申请日:2002-04-18

    Abstract: A cleaning system that utilizes an organic cleaning solvent and pressurized fluid solvent is disclosed. The system has no conventional evaporative hot air drying cycle. Instead, the system utilizes the solubility of the organic solvent in pressurized fluid solvent as well as the physical properties of pressurized fluid solvent. After an organic solvent cleaning cycle, the solvent is extracted from the textiles at high speed in a rotating drum (112, 122) in the same way conventional solvents are extracted from textiles in conventional evaporative hot air dry cleaning machines. Instead of proceeding to a conventional drying cycle, the extracted textiles are then immersed in pressurized fluid solvent to extract the residual organic solvent from the textiles. This is possible because the organic solvent is soluble in pressurized fluid solvent. After the textiles are immersed in pressurized fluid solvent, pressurized fluid solvent is pumped from the drum (112, 122). Finally, the drum is de-pressurized to atmospheric pressure to evaporate any remaining pressurized fluid solvent, yielding clean, solvent free textiles. The organic solvent is preferably selected from terpenes, halohydrocarbons, certain glycol ethers, polyols, ethers, esters of glycol ethers, esters of fatty acids and other long chain carboxylic acids, fatty alcohols and other long-chain alcohols, short-chain alcohols, polar aprotic solvents, siloxanes, hydrofluoroethers, dibasic esters, and aliphatic hydrocarbons solvents or similar solvents or mixtures of such solvents and the pressurized fluid solvent is preferably densified carbon dioxide.

    Abstract translation: 公开了一种利用有机清洁溶剂和加压流体溶剂的清洁系统。 该系统没有传统的蒸发式热风干燥循环。 相反,该系统利用有机溶剂在加压流体溶剂中的溶解度以及加压流体溶剂的物理性质。 在有机溶剂清洁循环之后,以与传统蒸发热空气干燥清洁机中从纺织品中提取常规溶剂相同的方式,在旋转鼓(112,122)中以高速从纺织品中提取溶剂。 代替进行常规的干燥循环,然后将提取的纺织品浸入加压的流体溶剂中以从纺织品中提取残留的有机溶剂。 这是可能的,因为有机溶剂可溶于加压流体溶剂。 在纺织品浸入加压流体溶剂之后,加压流体溶剂从滚筒(112,122)泵入。 最后,将滚筒减压至大气压力以蒸发剩余的加压流体溶剂,产生清洁的无溶剂纺织品。 有机溶剂优选选自萜烯,卤代烃,某些乙二醇醚,多元醇,醚,乙二醇醚的酯,脂肪酸和其它长链羧酸的酯,脂肪醇和其它长链醇,短链醇,极性 非质子溶剂,硅氧烷,氢氟醚,二元酯和脂族烃溶剂或类似溶剂或这些溶剂的混合物,并且加压流体溶剂优选是致密化的二氧化碳。

    SYSTEM AND METHOD FOR EXTRACTING WATER IN A DRY CLEANING PROCESS INVOLVING A SILOXANE SOLVENT
    36.
    发明公开
    SYSTEM AND METHOD FOR EXTRACTING WATER IN A DRY CLEANING PROCESS INVOLVING A SILOXANE SOLVENT 审中-公开
    在CHEMISCHREINIGUNG的VORRICHTUNG UND VERFAHREN ZUR WASSER EXTRAKTION

    公开(公告)号:EP1194630A4

    公开(公告)日:2002-11-20

    申请号:EP00945390

    申请日:2000-07-13

    Abstract: A system and method are provided for separating water from solvent during dry cleaning. Included is an inlet (52) capable of receiving a mixture of dry cleaning fluid and water from a basket of a dry cleaning apparatus. The dry cleaning fluid includes a siloxane composition. Also provided is a flow controller (60) for urging flow of the mixture received from the outlet. Coupled to the flow controller (60) is a coalescent media (64) that receives the mixture urged by the flow controller (60). A chamber (68) is coupled to the coalescent media (64) for receiving the mixture from the coalescent media (64) to separate the water and the dry cleaning fluid. Also coupled to the chamber (68) is an outlet (69) to remove the dry cleaning fluid from the chamber (68) in the absence of water.

    Abstract translation: 提供了一种用于在干洗期间从溶剂中分离水的系统和方法。 包括能够从干洗设备的篮子接收干洗液和水的混合物的入口(52)。 干洗液包含硅氧烷组合物。 还提供了一种流量控制器(60),用于推动从出口接收的混合物的流量。 与流量控制器(60)耦合的是聚结介质(64),其接收由流量控制器(60)推动的混合物。 室(68)联接到聚结介质(64),用于接收来自聚结介质(64)的混合物以分离水和干洗液。 在室(68)上还连接有一个出口(69),用于在没有水的情况下从室(68)中取出干洗液。

    CLEANING SYSTEM UTILIZING AN ORGANIC CLEANING SOLVENT AND A PRESSURIZED FLUID SOLVENT
    39.
    发明授权
    CLEANING SYSTEM UTILIZING AN ORGANIC CLEANING SOLVENT AND A PRESSURIZED FLUID SOLVENT 有权
    清洗系统与有机以及加压液体溶剂

    公开(公告)号:EP1224351B1

    公开(公告)日:2006-08-23

    申请号:EP00970901.5

    申请日:2000-10-13

    Abstract: A cleaning system that utilizes an organic cleaning solvent and pressurized fluid solvent is disclosed. The system has no conventional evaporative hot air drying cycle. Instead, the system utilizes the solubility of the organic solvent in presurized fluid solvent as well as the physical properties of pressurized fluid solvent. After an organic solvent cleaning cycle, the solvent is extracted from the textiles at high speed in a rotating drum in the same way conventional solvents are extracted from textiles in conventional evaporating hot air dry cleaning machines. Instead of proceeding to a conventional drying cycle, the extracted textiles are then immersed in pressurized fluid solvent to extract the residual organic solvent from the textiles. This is possible because the organic solvent is soluble in pressurized fluid solvent. After the textiles are immersed in pressurized fluid solvent, pressurized fluid solvent is pumped from the drum. Finally, the drum is de-pressurized to atmospheric pressure to evaporate any remaining pressurized fluid solvent, yielding clean, solvent free textiles. The organic solvent is preferably dipropylene glycol n-butyl ether, tripropylene glycol n-butyl ether or tripropylene glycol methyl ether, a mixture thereof, or a similar solvent and the pressurized fluid solvent is preferably densified carbon dioxide.

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