KR840004872A - 물질 전달 접촉장치 - Google Patents

물질 전달 접촉장치 Download PDF

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Publication number
KR840004872A
KR840004872A KR1019830002823A KR830002823A KR840004872A KR 840004872 A KR840004872 A KR 840004872A KR 1019830002823 A KR1019830002823 A KR 1019830002823A KR 830002823 A KR830002823 A KR 830002823A KR 840004872 A KR840004872 A KR 840004872A
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South Korea
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liquid
velocity
lattice
grating
lattice element
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KR1019830002823A
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KR900007320B1 (ko
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시이쉬프트너 케네스
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헬멋트 엠쉘링
켐-프로 코오포레이션
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Application filed by 헬멋트 엠쉘링, 켐-프로 코오포레이션 filed Critical 헬멋트 엠쉘링
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/14—Fractional distillation or use of a fractionation or rectification column
    • B01D3/16—Fractionating columns in which vapour bubbles through liquid
    • B01D3/22—Fractionating columns in which vapour bubbles through liquid with horizontal sieve plates or grids; Construction of sieve plates or grids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D47/00—Separating dispersed particles from gases, air or vapours by liquid as separating agent
    • B01D47/12—Washers with plural different washing sections
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18—Absorbing units; Liquid distributors therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/32—Packing elements in the form of grids or built-up elements for forming a unit or module inside the apparatus for mass or heat transfer
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32206—Flat sheets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32203—Sheets
    • B01J2219/32237—Sheets comprising apertures or perforations
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/32—Details relating to packing elements in the form of grids or built-up elements for forming a unit of module inside the apparatus for mass or heat transfer
    • B01J2219/322—Basic shape of the elements
    • B01J2219/32279—Tubes or cylinders

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

내용 없음

Description

물질 전달 접촉장치
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도 본 발명의 원리를 채택한 기-액 접촉장치 즉 기체 세정장치를 묘사하는 부분적으로 절개된 입면도.
제2도 유동 개체의 속도분포와 격자 요소장치간의 관계를 묘사하는 도식.
제6도 본 발명의 격자 모듈(module)을 바꾼 사분면의 평면도.

Claims (10)

  1. 격자요소는 상호연결용 덕트 위크에서의 기체류의 미리 결정된 속도 압력분포와 분배된 액체의 정두 및 동두의 속도압력분포의 합과 이상적으로 동일한 단면적 분포를 갖도록 만들어졌으며, 액체는 격자 요소의 오목면 위로 분배되며, 선택된 액체류의 속도(L)는 주어진 평균 기체속도에 대해 격자요소의 오목면 위의 유동상이 조절되기에 충분하도록 한, 격자요소에서의 기체흐름의 방향에 수직하게 배치되어 덕트 워크에 달려있는 최소한 하나의 격자요소와 이 격자요소에 선택된 유속(L)으로 액체를 분배하는 수단을 특징으로 하는 입구와 출구사이의 상호연결덕트 워크와 입구와 출구를 포함하는 하우징 요소로 구성된 기-액접촉장치.
  2. 각 모듈내의 격자요소는 각 요소에서의 기류와 분배된 액체의 정 및 동두의 미리결정된 이론적 속도 압력 분포의 합과 이상적으로 동일한 단면적 분포를 갖도록 만들어졌으며, 액체는 격자요소의 오목한 면위로 분배되며, 선택된 액체류의 속도(L)는 주어진 평균기체속도에 대해 격자요소의 오목면위에 유동상이 조절되기에 충분하도록 한, 입구 및 출구를 갖는 자체의 하우징요소와 거기에 매달린 최소한 하나의 격자요소를 포함하는 모듈의 최소한 한 그룹의 모듈, 각 모듈에 있는 격자요소는 기류의 방향에 수직하게 배치되어 있으며 각 모듈을 통과하는 기체류의 속도는 덕트 워크를 통과하는 기체류의 속도를 모듈의 수로 나눈 것과 거의 동일한, 기류에 수직한 면에 모듈의 그룹을 고정시키는 수단 및 각 모듈에 있는 격자 요소로 선택된 속도의 액체류를 분배하는 장치를 특징으로 하는 입구와 출구사이의 상호연결 덕트워크와 입구및 출구를 포함하는 하우징 요소로 구성된 기-액접촉 장치.
  3. 제1 또는 2항에 있어서, 분배된 액체의 에너지 수준과 기류의 에너지수준간에 분배된 액체에 유리한 에너지 불균형을 조성하여 마침내 격자요소를 통해서 조절된 유동상으로 부터 액체가 배수되도록한 격자 요소가 추가적인 깊이를 갖는 장치.
  4. 제3항에 있어서, 격자요소가 식 dc=PVC+HSR+HPL+d+(여기서 PVC는 근지점에서 기체의 속도 압력이며, HSL은 분배된 액체의 정두이고, HDL은 분배된 액체의 동두이고, d+는 분배된 액체에 유리한 에너지 불균형을 창출하기 위한 추가적인 깊이이다)로 결정된 근지점 깊이, 즉 dc를 갖는 격자요소가 고리모양인 장치.
  5. 제3항에 있어서, 격자요소의 단면적 분포가 이상적인 설계에 충분히 가까워서 조절된 유동상이 되도록 한 장치.
  6. 제3항에 있어서, 각쌍의 격자요소들이 서로 미리 결정된 거리에 위치하는, 덕트 워크 또는 모듈 하우징 요소에서 최소한 하나의 격자쌍이 있는 장치.
  7. 제3항에 있어서, 격자요소가 굴곡성 물질로 직조되어서 누적된 물질이 격자요소의 굴곡에 제거 되도록한 장치.
  8. 제3항에 있어서, 격자의 개방 면적이 50-85%인 장치.
  9. 제3항에 있어서, 격자의 저방면적이 50-75%인 장치.
  10. 제3항에 있어서, 추가적인 깊이가 5-40%의 범위인 장치.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019830002823A 1982-06-23 1983-06-23 기액 접촉 장치 KR900007320B1 (ko)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US39113982A 1982-06-23 1982-06-23
US391139 1982-06-23
US496054 1983-05-19
US06/496,054 US4432914A (en) 1982-06-23 1983-05-19 Mass transfer contact apparatus

Publications (2)

Publication Number Publication Date
KR840004872A true KR840004872A (ko) 1984-10-31
KR900007320B1 KR900007320B1 (ko) 1990-10-08

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KR1019830002823A KR900007320B1 (ko) 1982-06-23 1983-06-23 기액 접촉 장치

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Country Link
US (1) US4432914A (ko)
EP (1) EP0099656B1 (ko)
KR (1) KR900007320B1 (ko)
CA (1) CA1207225A (ko)
DE (1) DE3380620D1 (ko)

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Publication number Publication date
DE3380620D1 (en) 1989-11-02
EP0099656A2 (en) 1984-02-01
EP0099656B1 (en) 1989-09-27
KR900007320B1 (ko) 1990-10-08
US4432914A (en) 1984-02-21
CA1207225A (en) 1986-07-08
EP0099656A3 (en) 1986-11-20

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