KR900012651A - 진공 증류 방법 - Google Patents

진공 증류 방법 Download PDF

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Publication number
KR900012651A
KR900012651A KR1019900001482A KR900001482A KR900012651A KR 900012651 A KR900012651 A KR 900012651A KR 1019900001482 A KR1019900001482 A KR 1019900001482A KR 900001482 A KR900001482 A KR 900001482A KR 900012651 A KR900012651 A KR 900012651A
Authority
KR
South Korea
Prior art keywords
liquid
vacuum distillation
distillation method
delivery conduit
distillation column
Prior art date
Application number
KR1019900001482A
Other languages
English (en)
Other versions
KR0145698B1 (ko
Inventor
알베르투스 하머 요하네스
반 데어 헤예덴 피이터
Original Assignee
오노 알버어스
셀 인터나쵸나아레 레사아치 마아츠 샤피 비이부이
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 오노 알버어스, 셀 인터나쵸나아레 레사아치 마아츠 샤피 비이부이 filed Critical 오노 알버어스
Publication of KR900012651A publication Critical patent/KR900012651A/ko
Application granted granted Critical
Publication of KR0145698B1 publication Critical patent/KR0145698B1/ko

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Classifications

    • 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
    • B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
    • B01D3/322—Reboiler specifications
    • 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
    • B01D3/10—Vacuum distillation
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00—Distillation: processes, separatory
    • Y10S203/09—Plural feed
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S203/00—Distillation: processes, separatory
    • Y10S203/90—Particular type of heating

Abstract

내용 없음

Description

진공 증류 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 진공 증류 컬럼(1)의 종단면도이다.

Claims (2)

  1. 증기 및 액체를 함유한 공급물을 감압으로 조작된 증류컬럼 내로 도입시키고, 증기를 증류컬럼 내부로 상승시키고, 액체를 증류컬럼의 바닥 부분으로 낙하시키고, 액체를 전달 도관을 통해 바닥부분으로부터 외부수집용기로 보내고, 수집용기로부터 액체를 제거시키고, 수집 용기로부터 제거된 액체를 냉각시키고, 냉각된 액체의 부분을 전달 도관을 통과하는 액체 내로 도입시키는 것으로 구성된 진공 증류 방법.
  2. 제1항에 있어서, 전달 도관 내로 도입되는 냉각된 액체의 분율이 냉각된 액체의 30-70부피%인 진공 증류 방법.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019900001482A 1989-02-10 1990-02-07 진공 증류 방법 KR0145698B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB898903013A GB8903013D0 (en) 1989-02-10 1989-02-10 Vacuum distillation process
GB8903013.4 1989-02-10

Publications (2)

Publication Number Publication Date
KR900012651A true KR900012651A (ko) 1990-09-01
KR0145698B1 KR0145698B1 (ko) 1998-08-17

Family

ID=10651465

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019900001482A KR0145698B1 (ko) 1989-02-10 1990-02-07 진공 증류 방법

Country Status (12)

Country Link
US (1) US5019219A (ko)
EP (1) EP0382316B1 (ko)
JP (1) JP3026575B2 (ko)
KR (1) KR0145698B1 (ko)
AU (1) AU620495B2 (ko)
CA (1) CA2009565C (ko)
DE (1) DE69005140T2 (ko)
ES (1) ES2047817T3 (ko)
GB (1) GB8903013D0 (ko)
MY (1) MY106051A (ko)
SA (1) SA90100267B1 (ko)
ZA (1) ZA90935B (ko)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20010032804A1 (en) * 1995-04-21 2001-10-25 Becht Engineering Company Inc. Fractionator with liquid-vapor separation arrangement
DE60033759T2 (de) * 1999-10-29 2007-12-06 Nippon Shokubai Co. Ltd. Destillationsapparat und Destillationsmethode
JP4558870B2 (ja) 1999-11-08 2010-10-06 株式会社日本触媒 塔式処理方法および装置
DE10241482A1 (de) * 2002-09-07 2004-03-18 Cognis Deutschland Gmbh & Co. Kg Anlage und Verfahren zum Durchführen einer diskontinuierlichen Rektifikation oder Reaktion
US7383828B2 (en) * 2004-06-24 2008-06-10 Emission & Power Solutions, Inc. Method and apparatus for use in enhancing fuels
US7428896B2 (en) * 2004-06-24 2008-09-30 Emission & Power Solutions, Inc. Method and apparatus for use in enhancing fuels
US20090134004A1 (en) * 2007-11-27 2009-05-28 Asprey William J Driving or driven distiller with heat pump function

Family Cites Families (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2664391A (en) * 1952-03-28 1953-12-29 Dow Chemical Co Continuous distillation of heat sensitive compounds
DE1052359B (de) * 1955-10-24 1959-03-12 Metallgesellschaft Ag Verfahren und Vorrichtung zur Gewinnung von Kristallen aus Loesungen durch Vakuumkuehlung
DE1258358B (de) * 1960-08-31 1968-01-04 American Mach & Foundry Vorrichtung zur Gewinnung von Suesswasser aus Seewasser durch die Waerme und Kaelte eines Kuehlmittelkreislaufes
US3334027A (en) * 1963-12-26 1967-08-01 Aqua Chem Inc Separation of entrained liquid droplets from vapors
US3480515A (en) * 1964-04-03 1969-11-25 Aqua Chem Inc Method and apparatus for vapor compression distillation and vapor washing of impure water
US3749647A (en) * 1970-12-07 1973-07-31 Standard Oil Co Apparatus for stripping solvent from and dehydrating trimellitic acid content of fluid effluent from catalytic liquid phase oxidation of pseudocumene in presence of acetic acid
AU501376B2 (en) * 1976-02-23 1979-06-21 Dow Chemical Company, The Liquid desiccants and absorbants when acid gases are present or mixtures thereof
US4166773A (en) * 1977-12-22 1979-09-04 Union Carbide Corporation Continuous process for separating high boiling, heat sensitive materials
JPS5925771B2 (ja) * 1979-08-06 1984-06-21 住友化学工業株式会社 高融点化合物の精製法
US4568428A (en) * 1983-07-05 1986-02-04 General Signal Corporation Method and apparatus for vacuum distillation
GB8903009D0 (en) * 1989-02-10 1989-03-30 Shell Int Research Vacuum distillation process

Also Published As

Publication number Publication date
GB8903013D0 (en) 1989-03-30
SA90100267B1 (ar) 1999-05-30
JP3026575B2 (ja) 2000-03-27
ES2047817T3 (es) 1994-03-01
ZA90935B (en) 1990-10-31
CA2009565C (en) 2000-05-30
KR0145698B1 (ko) 1998-08-17
DE69005140T2 (de) 1994-05-11
MY106051A (en) 1995-03-31
DE69005140D1 (de) 1994-01-27
AU4937990A (en) 1990-08-16
US5019219A (en) 1991-05-28
JPH02273501A (ja) 1990-11-08
EP0382316A2 (en) 1990-08-16
EP0382316B1 (en) 1993-12-15
EP0382316A3 (en) 1992-04-15
CA2009565A1 (en) 1990-08-10
AU620495B2 (en) 1992-02-20

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