연속적인 흡착 및 탈착공정으로 폐극성용매의 처리방법
    81.
    发明授权
    연속적인 흡착 및 탈착공정으로 폐극성용매의 처리방법 失效
    采用连续吸附/解吸法回收废极性溶剂的方法

    公开(公告)号:KR100905796B1

    公开(公告)日:2009-07-02

    申请号:KR1020070103248

    申请日:2007-10-12

    CPC classification number: Y02W10/15

    Abstract: 본 발명은 흡착탑을 이용한 흡착 및 탈착 공정을 연속적으로 수행하여 폐 극성용매 중에 다량으로 함유된 수분을 제거하는 방법에 관한 것으로, 상기 흡착 시 특정의 분자체를 표면개질 또는 이온교환한 흡착제를 사용하여 저온에서 흡착반응을 수행하고, 탈착 시 마이크로파를 조사하여 수분제거율이 높은 순수한 극성용매의 재생 및 단시간의 주기로 흡착제의 효과적인 반복 사용이 가능한 연속적인 흡착 및 탈착공정으로 폐 극성용매를 처리하는 방법에 관한 것이다.
    극성용매, 탈착, 흡착, 마이크로파

    연속적인 흡착 및 탈착공정으로 폐극성용매의 처리방법
    82.
    发明公开
    연속적인 흡착 및 탈착공정으로 폐극성용매의 처리방법 失效
    使用连续吸附/解吸过程回收废气溶液的方法

    公开(公告)号:KR1020090037746A

    公开(公告)日:2009-04-16

    申请号:KR1020070103248

    申请日:2007-10-12

    CPC classification number: Y02W10/15 B01D15/00 C02F1/28 C02F3/10

    Abstract: A method for treating a waste polar solvent by a continuous adsorption and a desorption processes is provided to reproduce pure polar solvent in which a moisture elimination rate is high and to use an adsorption agent effectively and successively. A method for treating a waste polar solvent by a continuous adsorption and a desorption processes comprises the following steps of: adsorbing water contained to a waste polar solvent at 45~25 °C by supplying the waste polar solvent in which water contained; detaching the water by irradiating a microwave in an adsorption column while maintaining temperature of the adsorption column in a range of -45~25 °C; and obtaining a surface of a molecular sieve having a specific surface area of 80 to 1200 m^2/g with a hydrophilic group.

    Abstract translation: 提供了通过连续吸附和脱附方法处理废极性溶剂的方法,以再现其中除水速率高的纯极性溶剂,并且有效和连续地使用吸附剂。 通过连续吸附和解吸法处理废极性溶剂的方法包括以下步骤:通过提供含有水的废极性溶剂,在45〜25℃下对包含在废极性溶剂中的水进行吸附; 将吸附塔的温度保持在-45〜25℃的范围内,通过在吸附塔中照射微波来分离水; 并用亲水基团得到比表面积为80〜1200m 2 / g的分子筛的表面。

    입자형 다결정실리콘 제조용 고압 유동층반응기
    83.
    发明公开
    입자형 다결정실리콘 제조용 고압 유동층반응기 有权
    用于制备颗粒状聚硅氧烷的高压流化床反应器

    公开(公告)号:KR1020070080306A

    公开(公告)日:2007-08-10

    申请号:KR1020060011493

    申请日:2006-02-07

    Abstract: A high pressure fluidized bed reactor for manufacturing a granular polycrystalline silicon is provided to minimize the contamination due to particles, to obtain easily silicon grains of high purity and to keep the difference of pressure between inner and outer regions of an inner space of the fluidized bed reactor itself in a low range by using a pressure difference control unit. A reactor cell encloses a reaction tube(2), so that an inner space of the reactor cell is divided into an inner region and an outer region by the reaction tube. A silicon grain layer is formed and a silicon precipitation is generated in the inner region of the inner space of the reactor cell except the outer region. A gas inlet unit is used for supplying a predetermined gas to the silicon grain layer. A product exhaust unit is used for exhausting polycrystalline grains and an exhaust gas from the inner region. An inert gas connection unit is used for keeping the outer region under an inert gas condition. A pressure control unit is used for measuring and controlling the pressures of the inner and outer regions. A pressure difference control unit keeps the difference of pressure between the inner and outer regions in a predetermined range of 0 to 1 bar.

    Abstract translation: 提供了一种用于制造粒状多晶硅的高压流化床反应器以最小化由于颗粒引起的污染,从而容易获得高纯度的硅晶粒并且保持流化床内部空间的内部和外部区域之间的压力差 反应器本身通过使用压力差控制单元在低范围内。 反应器单元包围反应管(2),使得反应器单元的内部空间被反应管分成内部区域和外部区域。 形成硅晶粒层,并且在除了外部区域之外的反应器电池的内部空间的内部区域中产生硅沉淀。 气体入口单元用于向硅晶粒层提供预定的气体。 产品排气单元用于从内部区域排出多晶颗粒和排气。 惰性气体连接单元用于将外部区域保持在惰性气体条件下。 压力控制单元用于测量和控制内部和外部区域的压力。 压力差控制单元将内外区域之间的压力差保持在0〜1巴的预定范围内。

    폐 이소프로필 알코올 재생 장치 및 방법
    84.
    发明授权
    폐 이소프로필 알코올 재생 장치 및 방법 失效
    废异丙醇再生的装置和方法

    公开(公告)号:KR100561738B1

    公开(公告)日:2006-03-15

    申请号:KR1020030020501

    申请日:2003-04-01

    Abstract: 본 발명은 TFT-LCD(박막트랜지스터 액정디스플레이) 제조공정, 반도체 제조공정, 솔-젤(Sol-Gel process) 공정, 알콕사이드(alkoxide) 제조, 제약 및 유기합성 등에서 다량 발생하는 폐 이소프로필 알코올의 재생 장치 및 방법에 관한 것이다.
    본 발명은 폐액 이소프로필 알코올로 부터 물과 고비점 물질을 제거하여 순수 이소프로필 알코올을 생성하는 고비점 공비증류탑; 상기 고비점 공비증류탑의 후단에 연결되어, 상기 순수 이소프로필 알코올로 부터 수분을 흡착,제거하여 무수 이소프로필 알코올을 생성하는 흡착탑; 상기 흡착탑 후단에 연결되어, 상기 무수 이소프로필 알코올에 포함된 저비점 물질을 제거하는 저비점 공비증류탑; 상기 저비점 공비증류탑 후단에 연결되어, 상기 저비점 물질이 제거된 무수 이소프로필 알코올에 포함된 이온 물질 및 입자상 물질을 제거하는 필터장치;를 포함하여 구성된 것을 특징으로 한다.
    IPA, 공비혼합물, 흡착, 증류, 필터

    구형입자의 연속 제조방법
    85.
    发明授权
    구형입자의 연속 제조방법 失效
    구형입자의연속제조방법

    公开(公告)号:KR100466803B1

    公开(公告)日:2005-01-24

    申请号:KR1020020052242

    申请日:2002-08-31

    Abstract: PURPOSE: A continuous method for preparing spheric particles by means of wet-process is provided to obtain fine powdery and spherical particles having desirable viscous property and flexibility for catalyst and/or adsorbents. CONSTITUTION: The method comprises steps of admixing fine powders having less then 10 micrometers to organic/inorganic binder or kneading only the find powders into pasta status; injecting the pasta dough into continuous strands having 0.5-15mm thickness; equally cutting the injected continuous strands; introducing the cut strands between both of upper plate and lower plate to form spherical product having 0.5-15mm thickness; removing solvent contained in the spherical particles through drying process to inhibit modification of the particles; and calcining the spherical particles to remove impurities at 400-1000 deg.C under air or inert atmosphere condition.

    Abstract translation: 目的:提供一种通过湿法制备球形颗粒的连续方法,以获得对催化剂和/或吸附剂具有所需粘性和柔性的细粉状和球形颗粒。 构成:该方法包括以下步骤:将具有小于10微米的细粉混合到有机/无机粘合剂中或仅将发现粉末捏合成面食状态; 将面团生面团注入具有0.5-15mm厚度的连续股线中; 同样切割注入的连续股; 在上板和下板之间引入切割线以形成厚度为0.5-15mm的球形产品; 通过干燥过程去除球形颗粒中所含的溶剂以抑制颗粒的改性; 并在空气或惰性气氛条件下在400-1000℃下煅烧球形颗粒以除去杂质。

    폐 이소프로필 알코올 재생 장치 및 방법
    86.
    发明公开
    폐 이소프로필 알코올 재생 장치 및 방법 失效
    用于再生废水异丙醇的装置和方法制造具有超高纯度的无水IPA

    公开(公告)号:KR1020040085710A

    公开(公告)日:2004-10-08

    申请号:KR1020030020501

    申请日:2003-04-01

    Abstract: PURPOSE: Provided are an apparatus and a method for regenerating waste isopropyl alcohol(IPA), derived from processes for making thin film transistor LCDs, manufacturing semiconductors and alkoxides, sol-gel processes and pharmaceutical or organic synthetic processes, to obtain anhydrous IPA with ultrahigh purity. CONSTITUTION: The apparatus comprises: an azeotropic distillation tower(71) for removing water and substances with high boiling point from waste IPA to provide pure IPA; an adsorption tower(74) connected to the distal end of the azeotropic distillation tower(71), which adsorbs and removes water from the pure IPA to provide anhydrous IPA; a second azeotropic distillation tower(76) connected to the distal end of the adsorption tower(74), which removes substances with low boiling point from the anhydrous IPA; and a filter unit connected to the distal end of the second azeotropic distillation tower(76), which removes ionic and particulate materials contained in the anhydrous IPA from which low-boiling point substances have already been removed.

    Abstract translation: 目的:提供衍生自制造薄膜晶体管LCD,制造半导体和醇盐的方法,溶胶 - 凝胶法和药物或有机合成工艺的废异丙醇(IPA)的再生设备和方法,以获得具有超高分子量的无水IPA 纯度。 构成:该装置包括:用于从废物IPA中除去水和高沸点物质的共沸蒸馏塔(71)以提供纯IPA; 连接到共沸蒸馏塔(71)的远端的吸附塔(74),其吸收并除去纯IPA中的水以提供无水的IPA; 连接到吸附塔(74)的远端的第二共沸蒸馏塔(76),其从无水IPA中除去低沸点物质; 以及连接到第二共沸蒸馏塔(76)的远端的过滤器单元,其去除了已经从中除去低沸点物质的无水IPA中所含的离子和颗粒物质。

    연속 구형화 장치
    87.
    发明公开
    연속 구형화 장치 失效
    连续的全球化设备

    公开(公告)号:KR1020040011738A

    公开(公告)日:2004-02-11

    申请号:KR1020020044837

    申请日:2002-07-30

    CPC classification number: B01J2/02

    Abstract: PURPOSE: A continuous globulization apparatus is provided, which is effectively used in mass production of spherical particles by continuously globulizing molded material having certain size range after mixing fine particles with liquid in the kneaded state into spherical particles having a diameter of about 0.5 to 15 mm. CONSTITUTION: The apparatus comprises an upper plate(2) for repeating eccentric circular motion to a certain angular velocity; a lower plate(3) moved to a certain direction; an inlet through which molded material(5') is spatially introduced on the basis of a moving direction of the molded material(5') moved with being put on the surface of the lower plate; a globulization part for globulizing the molded material between the upper plate and lower plate; and an outlet for discharging spherical particles(6) formed in the globulization part to the outside, wherein the upper and lower plates contacted with the molded material maintain a certain distance therebetween, and the surface(4) of the upper plate and the surface of the lower plate are respectively inclined to certain angles (a, b) from the inlet and outlet.

    Abstract translation: 目的:提供一种连续的全球化装置,其通过连续地将具有一定尺寸范围的成型材料在捏合状态下将细颗粒与液体混合后,直径为约0.5至15mm的球形颗粒,有效地用于大规模生产球形颗粒 。 构成:该装置包括用于以一定角速度重复偏心圆周运动的上板(2) 下板(3)移动到一定方向; 基于模制材料(5')的移动方向在空间上引入模制材料(5')的入口,其被放置在下板的表面上; 用于在上板和下板之间使成型材料球化的球形部分; 以及用于将形成在球形部分中的球形颗粒(6)排出到外部的出口,其中与模制材料接触的上板和下板在它们之间保持一定距离,并且上板的表面(4)和 下板分别从入口和出口倾斜到一定角度(a,b)。

    희박농도의 메탄 산화촉매 및 그 제조방법
    88.
    发明授权
    희박농도의 메탄 산화촉매 및 그 제조방법 失效
    通过金属负载沸石选择性除去烟道气中的甲烷

    公开(公告)号:KR100343550B1

    公开(公告)日:2002-07-20

    申请号:KR1019990053104

    申请日:1999-11-26

    Abstract: 본발명은희박농도의메탄산화촉매의제조방법에관한것으로서, 높은실리카함량의제올라이트에팔라듐(Pd), 백금(Pt), 로듐(Rh), 금(Au)을포함하는활성귀금속성분을담지하는데있어서제올라이트세공을보호할수 있는특정의유기물을미리제올라이트세공내에채워넣은상태에서활성귀금속촉매성분을담지하여메탄산화에필수적인귀금속성분을제올라이트세공의원하는위치에정확히담지되도록하며, 이렇게제조된촉매는제올라이트세공을보호하지않은상태에서활성귀금속성분을담지하여제조한촉매에비하여저온에서높은메탄산화활성을나타내고, 특히희박농도의메탄이포함되어있는배출가스로부터의메탄을효과적으로산화제거하는데유용한메탄산화촉매의제조방법에관한것이다.

    수소와 산소에 의한 직접적 수산화 방향족 화합물의 제조방법
    89.
    发明公开
    수소와 산소에 의한 직접적 수산화 방향족 화합물의 제조방법 失效
    用氢氧化合物制备羟基芳族化合物的方法

    公开(公告)号:KR1020000001930A

    公开(公告)日:2000-01-15

    申请号:KR1019980022415

    申请日:1998-06-15

    CPC classification number: C07C37/58 Y02P20/52 C07C39/04

    Abstract: PURPOSE: Title compounds are directly prepared by hydrogen and oxygen, not using perhydroxide in the presence of binary catalyst. CONSTITUTION: Title compounds are prepared by hydrogen and oxygen at -10- 60°C, atmospheric pressure in the presence of binary catalyst comprising zeolite catalyst including VIII-B transition metals and alkyl anthraquinone derivatives and zeolite catalyst containing the transition metal having tetrahedron coordinated structures. Thus, 15 ml benzene and 15 ml acetic acid are mixed in the velocity of 16 ml/min of hydrogen and oxygen at 60°C for 5 hours to give a phenol.

    Abstract translation: 目的:标题化合物直接由氢和氧制备,在二元催化剂存在下不使用全氢氧化物。 构成:标题化合物是在氢气和氧气的制备下,在-10〜60℃,大气压下,在二元催化剂存在下,包含沸石催化剂,包括VIII-B过渡金属和烷基蒽醌衍生物,以及含有具有四面体配位结构的过渡金属的沸石催化剂 。 因此,将15ml苯和15ml乙酸以16ml / min的氢气和氧气的速度在60℃下混合5小时,得到苯酚。

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