[go: up one dir, main page]

KR920002191A - 액화 개스를 비등시키는 방법 - Google Patents

액화 개스를 비등시키는 방법 Download PDF

Info

Publication number
KR920002191A
KR920002191A KR1019910013093A KR910013093A KR920002191A KR 920002191 A KR920002191 A KR 920002191A KR 1019910013093 A KR1019910013093 A KR 1019910013093A KR 910013093 A KR910013093 A KR 910013093A KR 920002191 A KR920002191 A KR 920002191A
Authority
KR
South Korea
Prior art keywords
liquefied gas
heat exchange
heat
passages
passage
Prior art date
Application number
KR1019910013093A
Other languages
English (en)
Other versions
KR0185587B1 (ko
Inventor
테렌스 라빈 죤
Original Assignee
마이클 위크햄
더 비오씨 그룹 피엘씨
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 마이클 위크햄, 더 비오씨 그룹 피엘씨 filed Critical 마이클 위크햄
Publication of KR920002191A publication Critical patent/KR920002191A/ko
Application granted granted Critical
Publication of KR0185587B1 publication Critical patent/KR0185587B1/ko

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • F28F13/18Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
    • F28F13/185Heat-exchange surfaces provided with microstructures or with porous coatings
    • F28F13/187Heat-exchange surfaces provided with microstructures or with porous coatings especially adapted for evaporator surfaces or condenser surfaces, e.g. with nucleation sites
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0003Condensation of vapours; Recovering volatile solvents by condensation by using heat-exchange surfaces for indirect contact between gases or vapours and the cooling medium
    • B01D5/0015Plates
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0033Other features
    • B01D5/0036Multiple-effect condensation; Fractional condensation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0078Condensation of vapours; Recovering volatile solvents by condensation characterised by auxiliary systems or arrangements
    • B01D5/0081Feeding the steam or the vapours
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04406Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
    • F25J3/04412Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04763Start-up or control of the process; Details of the apparatus used
    • F25J3/04866Construction and layout of air fractionation equipments, e.g. valves, machines
    • F25J3/04872Vertical layout of cold equipments within in the cold box, e.g. columns, heat exchangers etc.
    • F25J3/04884Arrangement of reboiler-condensers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J5/00Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants
    • F25J5/002Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger
    • F25J5/005Arrangements of cold exchangers or cold accumulators in separation or liquefaction plants for continuously recuperating cold, i.e. in a so-called recuperative heat exchanger in a reboiler-condenser, e.g. within a column
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F28D9/0068Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements with means for changing flow direction of one heat exchange medium, e.g. using deflecting zones
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/02Bath type boiler-condenser using thermo-siphon effect, e.g. with natural or forced circulation or pool boiling, i.e. core-in-kettle heat exchanger
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/04Down-flowing type boiler-condenser, i.e. with evaporation of a falling liquid film
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/10Boiler-condenser with superposed stages
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2250/00Details related to the use of reboiler-condensers
    • F25J2250/20Boiler-condenser with multiple exchanger cores in parallel or with multiple re-boiling or condensing streams
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/32Details on header or distribution passages of heat exchangers, e.g. of reboiler-condenser or plate heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/44Particular materials used, e.g. copper, steel or alloys thereof or surface treatments used, e.g. enhanced surface

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Separation By Low-Temperature Treatments (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

내용 없음

Description

액화 개스를 비등시키는 방법
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 고압 컬럼 및 저압 컬럼을 포함하는 공기 분리 장치의 본 발명 형성부에 따른 콘덴서-리보일러를 부분절개한 개략적인 정면도이고,
제2도는 액체산소의 낙하막(falling film) 이 부분적으로 비등시키는 종류인, 제1도에 도시된 장치의 열교환기 형성부의 개략적인 투시도이다.

Claims (14)

  1. 액화 개스를 비등시키기 위한 제1열교환 통로 셋트를 한정하는 다수의 제1열전달 표면 각각의 아래쪽으로 액화 개스의 낙화막(falling film)을 생성시키는 단계, 하강하는 액체의 일부가 비등되도록 상기 제1표면을 가열하는 단계, 액화 개스를 비등시키기 위한 제2통로 셋트를 한정하는 다수의 제2열전달 표면이 적어도 부분적으로 침지되어 있는 대량의 액화 개스속으로 비등되지 않은 액화 개스를 통과시키는 단계, 액화 개스가 상기 제2통로를 통해 흐르도록 하는 단계, 및 상기 제2통로를 통과하는 액화 개스의 적어도 일부가 비등되도록 상기 제2열전달 표면을 가열하는 단계를 포함하는, 액화개스를 비등시키는 방법.
  2. 제1항에 있어서, 상기 제1및 제2열전달 표면을 액화 개스와 상이한 조성을 갖는 응축 증기를 포함하는 열교환 유체를 사용하여 각각 가열하고, 상기 제1열교환 통로를 적어도 하나의 제1열교환기내에서 상기 열교환 유체가 통과할 수 있는 열교환 통로와 교대로 배열하고, 상기 제2열교환 통로를 적어도 하나의 제2열교환기내에서 상기 열교환 유체가 통과할 수 있는 열교환 통로와 교대로 배열하는 방법.
  3. 제2항에 있어서, 상기 액화 개스가 액체 산소이고, 상기 열교환 유체가 질소인 방법.
  4. 제3항에 있어서, 액체산소의 공급원이 공기가 분리되는 정류 컬럼내의 액체-증기 접촉수단이고, 제1열교환 통로를 액체 산소가 중력에 의해 공급될 수 있도록 액체-증기 접촉수단 아래쪽에 위치시키는 방법.
  5. 제4항에 있어서, 상기 대량의 액화 개스가 저압 정류 컬럼, 및 질소를 포함하는 열교환 유체를 공급하는 고압 정류 컬럼을 포함하는 이중 정류 컬럼의 상기 저압 컬럼 형성부분인 저압 정류 컬럼의 배수조(sump)내에 함유된 방법.
  6. 제3항 내지 제5항중 어느 한 항에 있어서, 제2열교환 통로를 통한 액화 개스의 흐름을, 각각의 상기 제2열교환 통로를 그의 기저부에서 대량의 액화 개스에 대해 개방시키고, 제2열전달 표면을 가열하여 액화 개스를 비등시킴으로서 열사이펀 효과(thermosiphon effect)에 의해 이들 통로를 통하여 액화 개스의 연속 흐름이 야기되도록 액화 개스의 높이를 유지시킴으로서 달성하는 방법.
  7. 제1항 내지 제6항중 어느 한 항에 있어서, 각각의 제1열교환 표면이, 기공이 개방되어 서로 연통되어 있는 다공성 금속 피막에 의해 제공된, 증기포(vapor bubble)의 형성을 위한 핵형성 부위를 갖는 방법.
  8. 사용시에 대량의 액화 개스를 함유하는데 적합한 용기내로 비등되지 않은 액체가 흐르도록 배열된 출구를 갖는, 액화 개스의 낙화막을 각각 비등시키기 위한 제1열교환 통로 셋트를 한정하는 다수의 제1열전달 표면,운전시에 하강하는 액체의 일부가 비등되도록 상기 제1열전달 표면을 가열하기 위한 수단, 액화 개스가 통하여 흐르는데 적합하며, 사용시에 용기내의 대량의 액화개스내에 적어도 부분적으로 침지되도록 배치되어 있는, 액화 개스를 비등시키기 위한 제2열교환 통로 셋트를 한정하는 다수의 제2열전달 표면, 및 통과하는 액화 개스의 적어도 일부가 비등되도록 상기 제2열전달 표면을 가열하기 위한 수단을 포함하는, 액화 개스를 비등시키기 위한 장치.
  9. 제8항에 있어서, 상기 제1열교환 통로를 적어도 하나의 제1열교환기내에서 열교환 유체가 통과할 수 있는 열교환 통로와 교대로 배열하고, 상기 제2열교환 통로를 적어도 하나의 제2열교환기내에서 상기 열교환 유체가 통과할 수 있는 열교환 통로와 교대로 배열한 장치.
  10. 제9항에 있어서, 열교환기가 정류 컬럼내에 위치하는 장치.
  11. 제10항에 있어서, 정류 컬럼내의 액체-증기 접촉수단으로부터 수득한 액체 산소를 상기 적어도 하나의 제1열교환기로 공급하기 위한 중간 탱크를 추가로 포함하는 장치.
  12. 제11항에 있어서, 상기 대량의 액화 개스를 함유하는 용기가 저압 정류 컬럼 및 고압 정류 컬럼을 포함하는 이중 정류 컬럼의 저압 정류 컬럼 형성부분인 저압 정류 컬럼의 배수조인 장치.
  13. 제8항 내지 제12항중 어느 한 항에 있어서, 제2열교환 통로가 그의 저부에서 개방되어 있고, 용기내의 액화 개스의 높이가 운전시에는 제2열전달 표면을 가열하여 액화 개스를 비등시킴으로서 열사이펀 효과에 의해 상기 통로를 액화 개스의 연속 흐름이 야기되도록 유지되는 장치.
  14. 제8항 내지 제13항중 어느 한 항에 있어서, 각각의 제1열교환 표면이, 기공이 개방되어 서로 연통되어 있는 다공성 피막에 의해 제공된, 증기포의 형성을 위한 핵 형성 부위를 가진 장치.
    ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
KR1019910013093A 1990-07-31 1991-07-30 액화 개스를 비등시키는 방법 KR0185587B1 (ko)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB909016766A GB9016766D0 (en) 1990-07-31 1990-07-31 Boiling liquefied gas
GB9016766.9 1990-07-31

Publications (2)

Publication Number Publication Date
KR920002191A true KR920002191A (ko) 1992-02-28
KR0185587B1 KR0185587B1 (ko) 1999-04-15

Family

ID=10679926

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1019910013093A KR0185587B1 (ko) 1990-07-31 1991-07-30 액화 개스를 비등시키는 방법

Country Status (8)

Country Link
EP (1) EP0469780B1 (ko)
KR (1) KR0185587B1 (ko)
CN (1) CN1058643A (ko)
AU (1) AU8138291A (ko)
CA (1) CA2048254A1 (ko)
DE (1) DE69103709T2 (ko)
GB (1) GB9016766D0 (ko)
ZA (1) ZA915029B (ko)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9315061D0 (en) * 1993-07-19 1993-09-01 Boc Group Plc Fractional distillation
US5438836A (en) * 1994-08-05 1995-08-08 Praxair Technology, Inc. Downflow plate and fin heat exchanger for cryogenic rectification
US5699671A (en) * 1996-01-17 1997-12-23 Praxair Technology, Inc. Downflow shell and tube reboiler-condenser heat exchanger for cryogenic rectification
DE19605500C1 (de) * 1996-02-14 1997-04-17 Linde Ag Vorrichtung und Verfahren zum Verdampfen einer Flüssigkeit
FR2774755B1 (fr) * 1998-02-09 2000-04-28 Air Liquide Condenseur a plaques brasees perfectionne et son application aux doubles colonnes de distillation d'air
EP1094286B1 (de) * 1999-10-20 2005-06-15 Linde Aktiengesellschaft Verfahren und Vorrichtung zur Tieftemperaturzerlegung von Luft
DE19950570A1 (de) 1999-10-20 2001-04-26 Linde Ag Verfahren und Vorrichtung zur Tieftemperaturzerlegung von Luft
FR2876441B1 (fr) * 2004-10-08 2017-07-21 Thermi Consult Condenseur de vapeur a plaques soudees notamment pour tour de condensation et de decantation

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1949609C3 (de) * 1969-10-01 1978-05-11 Linde Ag, 6200 Wiesbaden Kondensatorverdampfer für einen Doppelsäulenrektifikator
JPS60253782A (ja) * 1984-05-30 1985-12-14 日本酸素株式会社 大型空気分離装置用凝縮器
US4699209A (en) * 1986-03-27 1987-10-13 Air Products And Chemicals, Inc. Heat exchanger design for cryogenic reboiler or condenser service
FR2650379B1 (fr) * 1989-07-28 1991-10-18 Air Liquide Appareil de vaporisation-condensation pour double colonne de distillation d'air, et installation de distillation d'air comportant un tel appareil

Also Published As

Publication number Publication date
CA2048254A1 (en) 1992-02-01
EP0469780B1 (en) 1994-08-31
CN1058643A (zh) 1992-02-12
ZA915029B (en) 1992-06-24
EP0469780A1 (en) 1992-02-05
DE69103709D1 (de) 1994-10-06
AU8138291A (en) 1992-02-13
GB9016766D0 (en) 1990-09-12
KR0185587B1 (ko) 1999-04-15
DE69103709T2 (de) 1994-12-22

Similar Documents

Publication Publication Date Title
US4585523A (en) Vapor compression distillation apparatus
DE3474059D1 (en) Device for evaporating a liquid by heat exchange with a second fluid and air distillation unit comprising such a device
US4118285A (en) Separation of liquid mixtures
JPH05138008A (ja) 液体源バブラー
KR920002191A (ko) 액화 개스를 비등시키는 방법
RU98116061A (ru) Способ и испаритель для испарения легко окисляющихся соединений
KR910002111B1 (ko) 이중 영역에 의한 비등방법과 열교환기
US2070100A (en) Fractionating tower
JPS5821521B2 (ja) 液体気化装置
US5014773A (en) Liquefied gas boilers
GB1311232A (en) Heat exchanger
KR840008296A (ko) 이중용기 열교환 장치
US5667643A (en) Heat exchanger and double distillation column
GB2164577A (en) Carbonating apparatus having liquid distribution trough
Somer et al. Heat transfer to an immiscible liquid mixture and between liquids in direct contact
JPS6033521B2 (ja) 縦型多管式の液膜降下式蒸発装置
JPS63502566A (ja) リボイラおよびその使用方法
FR2233584A1 (en) Vertical heat exchanger with low liquid level - has distributors directing film of condensate under gravity onto heated surface at bottom
JPS54140254A (en) Heat exchanger
Cho et al. Steam bubble formation at a submerged orifice in quiescent water
US2393387A (en) Milk cooler
JPH0755281B2 (ja) 蒸発器
RU2036684C1 (ru) Устройство для испарения жидкости в процессе периодической ректификации
AU638607B2 (en) Urn with airlock
SU1212470A1 (ru) Термический дегазатор

Legal Events

Date Code Title Description
PA0109 Patent application

Patent event code: PA01091R01D

Comment text: Patent Application

Patent event date: 19910730

PG1501 Laying open of application
A201 Request for examination
PA0201 Request for examination

Patent event code: PA02012R01D

Patent event date: 19960730

Comment text: Request for Examination of Application

Patent event code: PA02011R01I

Patent event date: 19910730

Comment text: Patent Application

E701 Decision to grant or registration of patent right
PE0701 Decision of registration

Patent event code: PE07011S01D

Comment text: Decision to Grant Registration

Patent event date: 19980924

GRNT Written decision to grant
PR0701 Registration of establishment

Comment text: Registration of Establishment

Patent event date: 19981226

Patent event code: PR07011E01D

PR1002 Payment of registration fee

Payment date: 19981226

End annual number: 3

Start annual number: 1

PG1601 Publication of registration
LAPS Lapse due to unpaid annual fee
PC1903 Unpaid annual fee

Termination category: Default of registration fee

Termination date: 20021011