US2425669A - Condenser - Google Patents

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Publication number
US2425669A
US2425669A US547883A US54788344A US2425669A US 2425669 A US2425669 A US 2425669A US 547883 A US547883 A US 547883A US 54788344 A US54788344 A US 54788344A US 2425669 A US2425669 A US 2425669A
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United States
Prior art keywords
steam
condenser
jacket
water
outlet
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Legal status (The legal status 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 status listed.)
Expired - Lifetime
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US547883A
Inventor
Brock Raymond Barrington
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Townson & Mercer Ltd
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Townson & Mercer Ltd
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Publication of US2425669A publication Critical patent/US2425669A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28BSTEAM OR VAPOUR CONDENSERS
    • F28B1/00Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser
    • 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
    • B01D5/0006Coils or serpentines
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D5/00Condensation of vapours; Recovering volatile solvents by condensation
    • B01D5/0057Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes
    • B01D5/006Condensation of vapours; Recovering volatile solvents by condensation in combination with other processes with evaporation or distillation
    • B01D5/0063Reflux condensation
    • GPHYSICS
    • G01MEASURING; TESTING
    • G01NINVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
    • G01N25/00Investigating or analyzing materials by the use of thermal means
    • G01N25/14Investigating or analyzing materials by the use of thermal means by using distillation, extraction, sublimation, condensation, freezing, or crystallisation
    • G01N25/145Accessories, e.g. cooling devices
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S165/00Heat exchange
    • Y10S165/184Indirect-contact condenser
    • Y10S165/205Space for condensable vapor surrounds space for coolant
    • Y10S165/206Space for condensable vapor surrounds space for coolant including coiled heat exchange tube

Definitions

  • This invention consists of improvements in or relating to condensers. It has been suggested from time to time that distilled water could be obtained from various steam mains; and indeed it is well known on board a steam ship to condense steam from Various steam mains so that distilled water is produced. However the steam in many steam mains is generally dirty or carries a certain proportion of oily or solid particles in suspension.
  • the object of this invention is to provide a simple and economical method and apparatus for producing distilled water from steam from mains which may be contaminated or which may have some proportion of oily or solid particles in suspension.
  • the raw steam from the mains is passed into the bottom of an aircooled jacket surrounding a water-cooled condenser and the top of the jacket opens direct into the steam space of the water-cooled condenser, so that a minor proportion of the raw steam is condensed in the jacket and entrains the oil or other suspended matter which is thus brought to the bottom of the jacket and carried away to waste while the cleaned steam is condensed by the water-cooled condenser and yields clean distilled water.
  • the apparatus shown is a vertical condenser made in hard glass.
  • An outer jacket has an outer cylindrical wall H and an inner cylindrical wall l2 united to the outer wall at the bottom as at l3 but open at the top as at I4.
  • the inlet for raw steam l5 enters the outer jacket at a point It near the bottom and the raw steam passes upwards in the outer jacket and is subjected to the cooling action of the air round the apparatus so that a certain proportion, say to 20% of the raw steam is condensed and the condensed water in the outer jacket brings down dirt or oil to the bottom of the outer jacket where it is discharged to waste through the outlet H.
  • the steam thus cleaned now passes down inside the wall 12 in contact with a water-cooled condenser comprising a central cylindrical chamber IS with external connection l9 and a helical tube 20 with external connection 2!, the coil 20 and chamber l8 being connected at the bottom as shown at 22.
  • the coil 20 occupies a large part of the space between the chamber is and the wall I 2 and the cleaned steam in its descent is therefore brought into intimate contact with the watercooled condenser.
  • the distilled water collects in the tube 23 and is discharged therefrom.
  • the bottom of the outer jacket illustrated acts as a trap for the waste stripping water, and it is a feature of this invention that such a trap may be used in any form of primary condenser.
  • this trap contributes to the efficiency, but it is within the scope of this invention to omit the actual trap, e g. to reduce the distance from the point l3 to the steam inlet conduit [5 and to use a restricted outlet at IT so that all the condensed dirty water plus a small proportion of steam are blown off to waste. Whether an actual trap is used or not, the outlet I1 is such as to prevent any undesired escape of raw steam therethrough.
  • the condenser is supplied with steam from mains and trouble from furring does not arise because the feed water i generally softened, so that even if the raw steam is wet it will not produce furring.
  • a condenser having an outer casing closed at one end and a single-walled inner casing disposed within said outer casing and united with said outer casing to form a jacket space, the said inner casing having its end which is adjacent the closed end of the outer casing open to said jacket space, the said outer casing having adjacent its end which is remote from its closed end an inlet for the fluid to be distilled into the said jacket space and an outlet from said jacket space at said end of said outer casing for impurities stripped from said fluid, the said outer casing having on its closed end inlet and outlet connections for a coolant, and a straight tube disposed within said inner casing and connected at one end to one of said coolant connections and connected at its other end to one end of a helical tube surrounding said straight tube, said helical tube being connected at its other end to the other of said coolant connections, and the said inner casing having at its end opposite to the end thereof open to said 3 jacket space an outlet for the distillate therefrom.

Description

Aug. 12, 1947. R, B, BROCK 2,425,669
CONDENSER Filed Aug. 3,1944
Patented Aug. 12, 1947 CONDENSER.
Raymond Barrington Brock, Croydon, England,
assignor to Townson & Mercer Limited, Croydon, England, a British company Application August 3, 1944, Serial No. 547,883 In Great Britain August 26, 1943 2 Claims.
This invention consists of improvements in or relating to condensers. It has been suggested from time to time that distilled water could be obtained from various steam mains; and indeed it is well known on board a steam ship to condense steam from Various steam mains so that distilled water is produced. However the steam in many steam mains is generally dirty or carries a certain proportion of oily or solid particles in suspension. The object of this invention is to provide a simple and economical method and apparatus for producing distilled water from steam from mains which may be contaminated or which may have some proportion of oily or solid particles in suspension.
According to this invention the raw steam from the mains is passed into the bottom of an aircooled jacket surrounding a water-cooled condenser and the top of the jacket opens direct into the steam space of the water-cooled condenser, so that a minor proportion of the raw steam is condensed in the jacket and entrains the oil or other suspended matter which is thus brought to the bottom of the jacket and carried away to waste while the cleaned steam is condensed by the water-cooled condenser and yields clean distilled water.
The nature of this invention and the manner in which it is performed will be appreciated from the following description of a specific example which is illustrated in the accompanying drawmg.
The apparatus shown is a vertical condenser made in hard glass. An outer jacket has an outer cylindrical wall H and an inner cylindrical wall l2 united to the outer wall at the bottom as at l3 but open at the top as at I4. The inlet for raw steam l5 enters the outer jacket at a point It near the bottom and the raw steam passes upwards in the outer jacket and is subjected to the cooling action of the air round the apparatus so that a certain proportion, say to 20% of the raw steam is condensed and the condensed water in the outer jacket brings down dirt or oil to the bottom of the outer jacket where it is discharged to waste through the outlet H. The steam thus cleaned now passes down inside the wall 12 in contact with a water-cooled condenser comprising a central cylindrical chamber IS with external connection l9 and a helical tube 20 with external connection 2!, the coil 20 and chamber l8 being connected at the bottom as shown at 22. As shown the coil 20 occupies a large part of the space between the chamber is and the wall I 2 and the cleaned steam in its descent is therefore brought into intimate contact with the watercooled condenser. The distilled water collects in the tube 23 and is discharged therefrom.
It will be seen that the bottom of the outer jacket illustrated acts as a trap for the waste stripping water, and it is a feature of this invention that such a trap may be used in any form of primary condenser.
Under normal conditions it is found that the provision of this trap contributes to the efficiency, but it is within the scope of this invention to omit the actual trap, e g. to reduce the distance from the point l3 to the steam inlet conduit [5 and to use a restricted outlet at IT so that all the condensed dirty water plus a small proportion of steam are blown off to waste. Whether an actual trap is used or not, the outlet I1 is such as to prevent any undesired escape of raw steam therethrough.
The use of glass for the apparatus has proved eirective but other materials can be employed if convenient.
With many forms of stills at present in use trouble arises from furring and the cleaning of furred stills is difficult. The furring occurs because the ordinary stills are supplied with tap water which is often hard.
In using the present invention the condenser is supplied with steam from mains and trouble from furring does not arise because the feed water i generally softened, so that even if the raw steam is wet it will not produce furring.
I claim:
1. A condenser having an outer casing closed at one end and a single-walled inner casing disposed within said outer casing and united with said outer casing to form a jacket space, the said inner casing having its end which is adjacent the closed end of the outer casing open to said jacket space, the said outer casing having adjacent its end which is remote from its closed end an inlet for the fluid to be distilled into the said jacket space and an outlet from said jacket space at said end of said outer casing for impurities stripped from said fluid, the said outer casing having on its closed end inlet and outlet connections for a coolant, and a straight tube disposed within said inner casing and connected at one end to one of said coolant connections and connected at its other end to one end of a helical tube surrounding said straight tube, said helical tube being connected at its other end to the other of said coolant connections, and the said inner casing having at its end opposite to the end thereof open to said 3 jacket space an outlet for the distillate therefrom.
2. A condenser according to claim 1, wherein the outlet for impurities at the end of the outer casing is restricted.
RAYMOND BARRINGTON BROCK.
REFERENCES CITED The following references are of record in the file of this patent:
UNITED STATES PATENTS Name Date Caps Feb. 15, 1910 Number OTHER REFERENCES Industrial and Engineering Chemistry Magazine, Sept. 1941, page 1107. (Copy in Division 25.)
US547883A 1943-08-26 1944-08-03 Condenser Expired - Lifetime US2425669A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB13947/43A GB571558A (en) 1943-08-26 1943-08-26 Improvements in or relating to the production of distilled water

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Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2475857A (en) * 1947-02-17 1949-07-12 Armin E Reinert Sampling device
US2675346A (en) * 1949-11-04 1954-04-13 Celanese Corp Concentration of formaldehyde by distillation and fractional condensation
US2705218A (en) * 1951-01-18 1955-03-29 Canicoba Saul Distilling apparatus of the continuous production type
US3015474A (en) * 1956-09-19 1962-01-02 George A Dalin Condensing apparatus
US3022241A (en) * 1957-02-15 1962-02-20 Cambridge Instr Company Inc Method and apparatus for measurement of dissolved oxygen
US3057603A (en) * 1958-03-11 1962-10-09 Technicon Instr Glass tube coil assemblies and heating baths
US3228667A (en) * 1963-04-16 1966-01-11 Ingersoll Rand Co Reserve capacity attemperator
US3871444A (en) * 1971-08-02 1975-03-18 Beckman Instruments Inc Water quality analysis system with multicircuit single shell heat exchanger
US3951175A (en) * 1972-09-14 1976-04-20 Eberhart Wolfgang R External internal channels in glass tubing
US4009751A (en) * 1973-11-09 1977-03-01 Slovenska Vysoka Skola Technika Method of and apparatus for high intensity heat and/or mass transfer between two or more phases
US4257479A (en) * 1979-04-02 1981-03-24 Sunburst Solar Energy Corp. Heat exchanger and drain down for solar collector
US4471836A (en) * 1982-01-15 1984-09-18 Arthur C. Knox, Jr. Vent condenser
US4681066A (en) * 1985-01-21 1987-07-21 Anton Steinecker Maschinenfabrik Gmbh Boiler for boiling mash or wort
US4749030A (en) * 1987-09-28 1988-06-07 Knox Jr Arthur C Device for condensing organic solvents
US5033541A (en) * 1989-11-17 1991-07-23 Cetac Technologies, Inc. Double pass tandem cooling aerosol condenser
US5046548A (en) * 1987-10-20 1991-09-10 Leif Tilly Device for preparing putty and similar masses
ES2116165A1 (en) * 1994-08-05 1998-07-01 Lopez De Coca Lopez De Sancho Dual-effect condenser
US5885313A (en) * 1996-09-12 1999-03-23 Shionogi & Co., Ltd. Temperature-gradient type multistage condenser
US20070089870A1 (en) * 2005-10-26 2007-04-26 Dobos James G Two part condenser for varying the rate of condensing and related method
US20070295493A1 (en) * 2004-12-18 2007-12-27 Neue Energie-Verwertungsge-Sellschaft Mbh Heat Exchanger
CN102327700A (en) * 2011-07-06 2012-01-25 蚌埠市周氏蜂业有限责任公司 Condensation device
CN106643201A (en) * 2016-12-26 2017-05-10 涂人哲 Cooling mechanism for organic reaction
USD910141S1 (en) * 2018-09-29 2021-02-09 Gary D Stadler Separation tool
CN114007677A (en) * 2019-04-03 2022-02-01 欧希金尼姆有限公司 Portable system for oxygen generation

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US898980A (en) * 1908-04-08 1908-09-15 Leo Loewenstein Proces for the fractional condensation of vapors.
US949217A (en) * 1908-02-15 1910-02-15 Chapin A Cartwright Steam-condenser, water-heater, and oil-separator.
US1073302A (en) * 1911-09-28 1913-09-16 Carl Still Cooler for condensing mixtures of hydrocarbon and steam.
US1641660A (en) * 1926-10-28 1927-09-06 Ellsworth S Bryant Condenser
US2232394A (en) * 1938-07-08 1941-02-18 Ko Tsu-Liang Jointed condenser with several delivery tubes
US2324257A (en) * 1942-07-02 1943-07-13 Ekert Werner Condensing and distilling device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US949217A (en) * 1908-02-15 1910-02-15 Chapin A Cartwright Steam-condenser, water-heater, and oil-separator.
US898980A (en) * 1908-04-08 1908-09-15 Leo Loewenstein Proces for the fractional condensation of vapors.
US1073302A (en) * 1911-09-28 1913-09-16 Carl Still Cooler for condensing mixtures of hydrocarbon and steam.
US1641660A (en) * 1926-10-28 1927-09-06 Ellsworth S Bryant Condenser
US2232394A (en) * 1938-07-08 1941-02-18 Ko Tsu-Liang Jointed condenser with several delivery tubes
US2324257A (en) * 1942-07-02 1943-07-13 Ekert Werner Condensing and distilling device

Cited By (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2475857A (en) * 1947-02-17 1949-07-12 Armin E Reinert Sampling device
US2675346A (en) * 1949-11-04 1954-04-13 Celanese Corp Concentration of formaldehyde by distillation and fractional condensation
US2705218A (en) * 1951-01-18 1955-03-29 Canicoba Saul Distilling apparatus of the continuous production type
US3015474A (en) * 1956-09-19 1962-01-02 George A Dalin Condensing apparatus
US3022241A (en) * 1957-02-15 1962-02-20 Cambridge Instr Company Inc Method and apparatus for measurement of dissolved oxygen
US3057603A (en) * 1958-03-11 1962-10-09 Technicon Instr Glass tube coil assemblies and heating baths
US3228667A (en) * 1963-04-16 1966-01-11 Ingersoll Rand Co Reserve capacity attemperator
US3871444A (en) * 1971-08-02 1975-03-18 Beckman Instruments Inc Water quality analysis system with multicircuit single shell heat exchanger
US3951175A (en) * 1972-09-14 1976-04-20 Eberhart Wolfgang R External internal channels in glass tubing
US4009751A (en) * 1973-11-09 1977-03-01 Slovenska Vysoka Skola Technika Method of and apparatus for high intensity heat and/or mass transfer between two or more phases
US4257479A (en) * 1979-04-02 1981-03-24 Sunburst Solar Energy Corp. Heat exchanger and drain down for solar collector
US4471836A (en) * 1982-01-15 1984-09-18 Arthur C. Knox, Jr. Vent condenser
US4681066A (en) * 1985-01-21 1987-07-21 Anton Steinecker Maschinenfabrik Gmbh Boiler for boiling mash or wort
US4749030A (en) * 1987-09-28 1988-06-07 Knox Jr Arthur C Device for condensing organic solvents
US5046548A (en) * 1987-10-20 1991-09-10 Leif Tilly Device for preparing putty and similar masses
US5033541A (en) * 1989-11-17 1991-07-23 Cetac Technologies, Inc. Double pass tandem cooling aerosol condenser
ES2116165A1 (en) * 1994-08-05 1998-07-01 Lopez De Coca Lopez De Sancho Dual-effect condenser
US5885313A (en) * 1996-09-12 1999-03-23 Shionogi & Co., Ltd. Temperature-gradient type multistage condenser
US20070295493A1 (en) * 2004-12-18 2007-12-27 Neue Energie-Verwertungsge-Sellschaft Mbh Heat Exchanger
US7306029B2 (en) * 2005-10-26 2007-12-11 Westinghouse Savannah River Company Llc Two part condenser for varying the rate of condensing and related method
US20070089870A1 (en) * 2005-10-26 2007-04-26 Dobos James G Two part condenser for varying the rate of condensing and related method
CN102327700A (en) * 2011-07-06 2012-01-25 蚌埠市周氏蜂业有限责任公司 Condensation device
CN106643201A (en) * 2016-12-26 2017-05-10 涂人哲 Cooling mechanism for organic reaction
CN106643201B (en) * 2016-12-26 2019-03-26 杨雪 A kind of cooling body for organic reaction
USD910141S1 (en) * 2018-09-29 2021-02-09 Gary D Stadler Separation tool
CN114007677A (en) * 2019-04-03 2022-02-01 欧希金尼姆有限公司 Portable system for oxygen generation

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