KR830005881A - Method and apparatus for mass transportation and disassembly through selective barrier - Google Patents

Method and apparatus for mass transportation and disassembly through selective barrier Download PDF

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KR830005881A
KR830005881A KR1019810002450A KR810002450A KR830005881A KR 830005881 A KR830005881 A KR 830005881A KR 1019810002450 A KR1019810002450 A KR 1019810002450A KR 810002450 A KR810002450 A KR 810002450A KR 830005881 A KR830005881 A KR 830005881A
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barrier
cracker
liquid
mixing
reservoir
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가이스 미첼
시모니 모세
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가이스 미첼
시모니 모세
원본미기재
테크니은 리서어치 엔드 디벨로프먼트 파운데이션 리미티드 미칩 슈세임
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Priority to KR1019810002450A priority Critical patent/KR830005881A/en
Publication of KR830005881A publication Critical patent/KR830005881A/en
Priority to KR2019840014251U priority patent/KR850000341Y1/en

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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
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    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/022—Filtration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/02—Solvent extraction of solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08—Selective adsorption, e.g. chromatography
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D33/00—Filters with filtering elements which move during the filtering operation
    • B01D33/01—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons
    • B01D33/015—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons with flat filtering elements
    • B01D33/0183—Filters with filtering elements which move during the filtering operation with translationally moving filtering elements, e.g. pistons with flat filtering elements supported
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/08—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • B01D63/087—Single membrane modules
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
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    • G01N33/50—Chemical analysis of biological material, e.g. blood, urine; Testing involving biospecific ligand binding methods; Immunological testing
    • G01N33/53—Immunoassay; Biospecific binding assay; Materials therefor
    • G01N33/536—Immunoassay; Biospecific binding assay; Materials therefor with immune complex formed in liquid phase
    • G01N33/537—Immunoassay; Biospecific binding assay; Materials therefor with immune complex formed in liquid phase with separation of immune complex from unbound antigen or antibody
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
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    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
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    • B01D2315/06—Submerged-type; Immersion type
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    • B01D—SEPARATION
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    • B01D2317/02—Elements in series
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    • G01—MEASURING; TESTING
    • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
    • G01N30/02—Column chromatography
    • G01N30/50—Conditioning of the sorbent material or stationary liquid
    • G01N30/52—Physical parameters
    • G01N2030/524—Physical parameters structural properties
    • G01N2030/527—Physical parameters structural properties sorbent material in form of a membrane

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Abstract

내용 없음No content

Description

선택장벽을 통한 대량운반과 분해를 위한 방법 및 장치Method and apparatus for mass transportation and disassembly through selective barrier

본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음Since this is an open matter, no full text was included.

제1도는 리덱스(LIDEX) 피 에스(침전분리기)의 예시도.Figure 1 is an illustration of the LIDEX (Sedimentation Separator).

제2도는 리덱스 피 에스 분해기의 작동상태도.2 is an operating state of the Redex PS cracker.

제3도는 제1도 1나의 하부 화대 단면도.3 is a cross-sectional view of the lower flower bed of FIG.

제4도는 4가 및 4나는 본 발명의 정치장치의 예시도.4 is an illustration of the stationary device of the present invention, 4 and 4 are.

제5도는 제1도의 복합장치의 예시도.5 is an illustration of the composite device of FIG.

제6도는 6가는 제5도의 복합장치 사이의 차단장치 예시도.Figure 6 is an illustration of the blocking device between the composite device of Figure 6 thinner.

제7도는 리덱스 피 에스의 예시도.Figure 7 is an illustration of the Redox PS.

Claims (33)

그상들이 둘다 액체이건 액체와 고체이건 액체-가스-고체이건 또는 액체-가스-액체이건 한상에서 다른 상으로부터의 하나 또는 그 이상의 성분들의 대량운반작업을 수행하는 개량된 방법, 다시 말해서 대량운반 및 물리적 분해작업은 혼합저장기(1)내에 접촉되어지는 상의 소개, 성분의 혼합, 최소한개의 특별히 설계된 장벽을 침투 통과하는 것과 밀폐요소의 구멍 그리고 장벽상에 가하여지는 압력을 감하기 위하여 혼합분해기(2)가 가스포켓의 수진을 위한 방법이 준비된용기(5)내로 최소한 한개의 채널로 통과운반 되어지는 개량된 방법으로 수행된다.Improved methods of carrying out mass transport of one or more components from one phase to another, whether liquid, liquid and solid, liquid-gas-solid, or liquid-gas-liquid, ie mass transport and physical Decomposition involves the introduction of the phases in contact with the mixing reservoir, the mixing of the components, the penetration of at least a specially designed barrier, the opening of the sealing element and the pressure exerted on the barrier to reduce the pressure exerted on the barrier. The method for collecting the gas pockets is carried out in an improved manner in which it is carried through at least one channel into the prepared container (5). 전술한 장벽은 흡착상, 구멍이난 섬유, 막, 치밀한 판의 형식의 저항하는 고정 또는 이동상으로 이루어진 청구범위 1에 의한 방법.The above-mentioned barrier is a method according to claim 1 consisting of an adsorbent bed, perforated fiber, membrane, resistant fixed or mobile bed in the form of a dense plate. 전술한 장벽은 구멍이 뚫려있고 이들 구멍은 기계통에서 분해되어야 할 고체물보다 적어야 되는 청구범위 1,2에 의한 방법.The method according to claims 1 and 2, wherein the aforementioned barriers are perforated and these holes must be less than the solids to be broken down in the machine. 전술한 막은 유공성 바이코오, 활성탄 또는 압축된 분말상의 실리가겔로서 만들어진 청구범위 2에 의한 방법.The method according to claim 2, wherein the membrane described above is made as a porous vicoo, activated carbon or compressed powdered siligagel. 전술한 장벽은 화학적으로 반응적인 물질로서 삼투구성 물질로서 반응하는 청구범위 2에 의한 방법.The method according to claim 2, wherein said barrier is reacted as an osmotic material as a chemically reactive material. 전술한 장벽은 확산성 용해성을 소유한 중합물질, 유동금속성, 막이거나 유리, 친화현상에 기포를 둔 분해로부터 만들어진 청구범위 2에 의한 방법.The above-mentioned barrier is a method according to claim 2 made from polymerized material possessing diffusible solubility, flow metallicity, membrane or glass, and decomposition based on affinity. 전술한 장벽은 이온교환 형식 즉 양이온-교환수지 그리고 음이온-교환수지와 같은 청구범위 2에 의한 방법.The above-mentioned barrier is a method according to claim 2, such as ion exchange type, ie cation-exchange resin and anion-exchange resin. 전술한 막은 정규 삼투 형식전자 삼투형식이거나 역삼투형식으로 되는 청구범위 2에 의한 방법.The method according to claim 2, wherein the membrane described above is a normal osmotic or reverse osmosis type. 전술한 장벽은 급냉시킨 유리이거나 여과기 그리고 스크린 같은 내부특성을 소유한 물질로서 만들어진 청구범위 2에 의한 방법.The method according to claim 2, wherein said barrier is made of quenched glass or a material possessing internal properties such as filters and screens. 청구범위 1중에는 둘 또는 그 이상 겹친 단위로 구성된 폭포형 장치가 사용되고 한 단위에서 두번째 단위로 통과할 때는 투명 핵체상이다.In Claim 1, a cascading device consisting of two or more overlapping units is used and when passed from one unit to the second unit is transparent nucleus. 이상들이 둘다 액체이건, 고체 또는 액체-가스-액체 또는 액체-가스-고체이건 한상에서 다른상으로 한 성분 또는 더 많은 성분의 대량운반 작동을 수행하는 장치 다시 말해서 동일한 장치로 수행된 대량운반과 물리적 분해작동으로서 수직 혼합저장기(1)로서 구성된 혼합분해기(2)에 꼭 끼워졌고 최소한 한개의 장벽과 그 두께를 통과하 최소한 1개의 구멍을 기초로 한 밀폐물질을 가지고 있고 전술한 구멍은 최소한 한개의 채널(3)과 연결되어 있어야 하며 혼합분해기(2)는 용기(5)의 상단부에 연결되었어야 하고 이 속에는 혼합저장기(1)로부터 분해된 상부액상이 집적되어 있으며 막과 채널(3)로 침투되었고 혼합분해기(2)가 혼합저장기(1)쪽으로 눌러내려져 갈때 혼합분해기(2)상에 준비되어진 가스 포켓의 집적을 위한 방법이다.Both of these devices, whether liquid or solid or liquid-gas-liquid or liquid-gas-solid, carry out mass transport operations of one or more components from one phase to another, ie mass transport and physical As a cracking operation, it is fitted in a mixer cracker (2) configured as a vertical mixer reservoir (1) and has a sealing material based on at least one barrier and at least one hole through its thickness, the hole being at least one described above. Must be connected to the channel (3) of the mixing cracker (2), which must be connected to the upper end of the vessel (5), in which the upper liquid phase decomposed from the mixing reservoir (1) is integrated, and the membrane and channel (3) Is a method for the accumulation of gas pockets prepared on the mixed cracker (2) when it has been infiltrated into the mixed cracker (2) and is pressed down into the mixed reservoir (1). 막대기(18)는 수집용기(5)속으로 그의 동일량의 액상으로 치환하기 위하여 혼합분해기(2)의 채널(3)내로 삽입하는 청구범위 2에 의한 장치.The device according to claim 2, wherein the rod (18) is inserted into the channel (3) of the mixed cracker (2) to replace the same amount of liquid phase into the collecting vessel (5). 혼합저장기(1)는 원통형상인 청구범위 11에 의한 장치.The mixing reservoir (1) is a device according to claim 11, which is cylindrical in shape. 혼잡분해기(2) 속에서는 2개 이상의 좁은 지역몰이 존재하는 청구범위 11에 의한 장치.Apparatus according to claim 11 in which at least two narrow area malls are present in the condenser 2. 가락지는 혼합저장기(1)의 상단부와 요소(5) 사이 가운데 위치하고 있고 이것은 혼합분해기(2)상으로 미끄러질 수 있고 이것이 혼합분해기(2)의 하향운동의 수준을 결정하는 청구범위 11에 의한 장치.The gas stop is located midway between the upper end of the mixing reservoir 1 and the element 5, which can slide onto the mixing cracker 2, which device according to claim 11, which determines the level of downward motion of the mixing cracker 2. . 용기(5)는 혼합분해기(2)의 상단부로부터의 어떤 높이에 있는 혼합저장기(1)의 직경보다 넓은 청구범위 11에 의한 장치The vessel 5 is a device according to claim 11 which is wider than the diameter of the mixing reservoir 1 at some height from the top of the mixing cracker 2. 수집용기(5)는 둘 또는 그 이상의 분해된 칸막이로 구분되어 있는 청구범위 11에 의한 정치.The collection vessel 5 is stationary according to claim 11 which is divided into two or more disassembled partitions. 혼합저장기(1)의 내부격을 따라 미끄러지는 밀폐성분은 혼합저장기(1)의 내부벽이라고 말하는 것과 좋은 접촉을 유지하고 있는 청구범위 11에 의한 장치.Apparatus according to claim 11 in which the hermetic component sliding along the inner space of the mixed reservoir 1 is in good contact with said internal wall of the mixed reservoir 1. 이를테면 고무오-링으로 구성된 밀폐요소는 채널(3)과 연결된 구멍을 가지고 있다. 그리고 이를테면 혼합저장기(1)의 내부벽을 따라 미끄러지는데 이 가락지를 응용하는 청구범위 18에 의한 장치.The sealing element, for example composed of a rubber o-ring, has a hole connected to the channel 3. And an apparatus according to claim 18 which applies, for example, a slippery slide along the inner wall of the mixing reservoir 1. 전술한 장치는 비활성물질로서 만들어진 청구범위 11에 의한 장치.The device according to claim 11 made as an inert material. 전술한 비활성 물질이란 금속, 유리, 폴리에치렌 또는 어떤 다른 적절한 플라스틱물질로 구성된 집단으로부터 선택되어진 청구범위 20에 의한 장치.The above-mentioned inert material is a device according to claim 20 selected from the group consisting of metal, glass, polyethylene or any other suitable plastics material. 전술한 가스포켓의 집적방법은 수평, 수직, 나사형의 홈들로서 혼합분해기(2)상에 위치해 있는 청구범위 11에 의한 장치.The method of incorporating the above described gas pockets is a device according to claim 11, located on the mixer cracker as horizontal, vertical, threaded grooves. 전술한 수평 수직 또는 나사형의 홈들이란 밀폐요소와 장벽사이에 위치하는 청구범위 22에 의한 장치.The device according to claim 22, wherein said horizontal vertical or threaded grooves are located between the sealing element and the barrier. 전술한 가스포켓 수집방법이란 한개 또는 그 이상의 채널관의 준비로서 되어진 청구범위에 의한 장치.The above-described gas pocket collection method is a device according to the claims made in preparation of one or more channel tubes. 전술한 장벽은 흡착상이거나 구멍뚫린 섬유, 막, 치밀한 판의 형태로 저항 고정상 또는 이동상으로 구성되어진 청구범위 11에 의한 장치.The device according to claim 11, wherein said barrier consists of a resistive stationary phase or a mobile phase in the form of adsorbed or perforated fibers, membranes, dense plates. 설명 25에 의한 장치중에서 이를테면 막은 구멍이 있는 바이코오, 활성목탄, 또는 압축된 분말상의 시리카겔로서 만들어진 청구범위 25에 의한 장치.The device according to claim 25, wherein the membrane is made of pore-shaped bicoo, activated charcoal, or compressed powdery silica gel in the device according to description 25. 설명 25에 의한 장치중에서 전술한 바와같이 장벽을 삼투구성물의 하나의 반응하는 화학적으로 반응하는 물질로 만든 청구범위 25에 의한 장치.25. An apparatus according to claim 25, wherein the barrier is made of one reactive chemically reacting material of the osmotic component as described above in the apparatus according to description 25. 전술한 장벽은 확산성 용해성을 가진 중할물질, 유동금속막, 그리고 유리막으로서 분해되는 친화현상에 기초를 둔 것으로 만들어진 청구범위 25에 의한 장치.The device according to claim 25, wherein the aforementioned barrier is based on affinity phenomena that decompose as heavy metals, flowable metal films, and glass films with diffusible solubility. 설명 25에 의한 장치중에서 전술한 장벽은 양이온 교환 그리고 음이온 교환과 같은 이온 교환 수지를 함유한 통으로서 되는 청구범위 25에 의한 장치.The device according to claim 25, wherein the barrier described above in the device according to description 25 is a container containing ion exchange resins such as cation exchange and anion exchange. 전술한 장벽은 정상적 삼투형 전기-삼투형 그리고 초여과형의 막으로서 되는 청구범위 25에 의한 장치.The device according to claim 25, wherein the barrier described above is a membrane of normal osmotic electro-osmotic and ultrafiltration. 전술한 장벽은 급속히 냉각시킨 유리 여과나 또는 그물같은 비활성의 특성을 소유한 물질로서 만들어진 청구범위 25에 의한 장치.The device according to claim 25, wherein said barrier is made of a material possessing inert properties such as rapidly cooled glass filtration or netting. 설명 11에 의하여 전술한 장치를 첨용도면 1,2,5,6 및 7로서 예시한 청구범위 11에 의한 장치.Apparatus according to claim 11 which exemplifies the apparatus described above by way of explanation 11 as appended drawings 1,2,5,6 and 7. 대량운반 작업을 수행하는 방법을 예시한 청구범위 1 내지 10에 의한 장치.Apparatus according to claims 1 to 10 illustrating a method of performing mass transport operations. ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.※ Note: The disclosure is based on the initial application.
KR1019810002450A 1980-07-21 1981-07-06 Method and apparatus for mass transportation and disassembly through selective barrier KR830005881A (en)

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