IL29503A - Condenser construction and fresh water recovery system - Google Patents

Condenser construction and fresh water recovery system

Info

Publication number
IL29503A
IL29503A IL29503A IL2950368A IL29503A IL 29503 A IL29503 A IL 29503A IL 29503 A IL29503 A IL 29503A IL 2950368 A IL2950368 A IL 2950368A IL 29503 A IL29503 A IL 29503A
Authority
IL
Israel
Prior art keywords
condenser
fresh water
tubes
water recovery
recovery system
Prior art date
Application number
IL29503A
Original Assignee
Saline Water Conversion Corp
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 Saline Water Conversion Corp filed Critical Saline Water Conversion Corp
Publication of IL29503A publication Critical patent/IL29503A/en

Links

Classifications

    • 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
    • F28B1/02Condensers in which the steam or vapour is separate from the cooling medium by walls, e.g. surface condenser using water or other liquid as the cooling medium
    • 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
    • B01D5/0012Vertical tubes
    • 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
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/02Treatment of water, waste water, or sewage by heating
    • C02F1/04Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C02F1/08Thin film evaporation
    • 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Organic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

Condenser construction and fresh water recovery SALUTE WATER CORPORATION 27945 S P E C I F I C A T I O N Invention relates to vapor condensation and more particularly it concerns novel surface condenser arrangements useful recovering fresh water from Surface condensers are used in connection with steam power plants in order to reduce the volume and therefore the back pressure of exhausted steam so that a greater measure of power may be obtained from the Surface condensers have also been used systems for the recovery of fresh water from saline o otherwise contaminated solutions The basic constructural configuration of a surface condenser involves an enclosure or outer elongated covering which is closed at each end by means of a tube A plurality of tubes extend along the interior of the enclosure and pass through the tube sheets at each end A cooling fluid is caused to pass through the condenser tubes and serves to maintain their surfaces at a low Steam or other vapor to be condensed then admitted into the and when it contacts the cooler surface of the condenser tubes it condenfies thereon into liquid form and drips down into a fresh water collection trough located below the In order to obtain maximum cooling it has been the practice to increase the condenser tube surface area to the greatest extent possible and to distribute this area throughout as much of the condenser interior as conventional condenser condenser tubes nested within the interior of the Typical prior art condensers have anywhere 22 to of the area of their tube sheets occupied by the condensing The large of condensing tubes used in prior condensers accounts for a major portion of the expense of these In structural problems from the use of a large number of condensing since very little the tube sheet remains at each end of the condenser to provide support for these condenser a reinforcing structures have to be This also contributes greatly to the cost of the The present Invention provides a surface condenser arrangement which is less complex and therefore is more economical to construct than prior condensers of comparable such condenser does not suffer from the structural difficulties encountered by prior art condenser According to one aspect of the present there provided a surface condenser unit within which a plurality of condenser tubes extend and are arranged such as to be in so that no condenser tube extends directly another With this the condensate which forms at any location along any of the drops directly down from that location and avoids all further contact with the a result the The present in another utilizes only about 2 to of the tuba sheet area to be occupied by the condenser While this a considerable reduction in area of the condensing it has been found that such reduction is more than for the increased availability increased heat transfer per square foot of tube surface of the condenser surfaces to the vapors to be In the where steam had to be forced through a congested nest of condenser it was not possible to utilise each tube to its fullest capacity since the incoming steam would initially contact the forwardmo3t tubes and be condensed prior to contacting the Further the rearward tubes vera contacted by steam to be condensed only after had forced through the entire tube and the rearward tubes would become effective to condense the steam only after the forward tubes were rendered less effective by the thereon of a film of in the conventional condenser there is a substantial press drop through the tube bank which i3 eliminated in this arrangement The present invention involves the use of relatively few condenser tubes so that incoming vapors to be condensed are not forced over one tube prior to contacting the upon which they are but instead they are caused to be condensed directl u on the first tube The present invention in a still further aspect involves the of the novel condensing concepts above into a controlled flash evaporation system to provide a structure for the recovery of fresh water from salt or other contaminated According to this aspect of the invention there are controlled flash evaporation channels down through which water to be evaporated from a higher to a lower In the lower pressure region there are provided condenser tubes and baffle along fresh vrater collection trough and unevaporated trough for separating and distributing the unevaporated solution and the recovered fresh This arrangement lends itself particularly well to in an constructed Specific of the invention have been chosen for purposes of illustration and and are shown in the accompanying forming a part of the 1 is a fragmentary section view of an evaporator system embodying novel condenser according to the present 2 is a side partially broken away illustratin water recovery system of 3 a section in elevation illustrating a second embodiment of the present is a partially broken illustrating a condenser arrangement to the present section view taken in elevation a portion of a multistage controlled flash evaporator type fr sh recovery system having integrated therein novel condenser means according to the present any liquid droplets from directly down the separator As shown in cross section in 1 there is provided an upper set of condenser tubes and 30c within the condenser region There is additionally a lower set of condensing tubes and 31c Just under the upper set within the condenser The condenser tubes extend horizontally from the front to the of the device are supplied with coolant liquid 32 from an external source It will be noted that the condenser tubes each of the sets are arranged along a triangula pattern so that no in set is directly above another tube in that This vertical disallgn ent of the tubes serves to prevent drippage of condensate from any one tube dovm upon another tube in the Λη intermediate baffle placed between the two sets of tubes 3 and in order to direct the condensate falls the upper set away from the tubes of the lower The system thu3 far described operates in the following The saline water 12 located above the upper is maintained at pressure and temperature conditions corresponding to That any Increase in temperature or any in pressure will cease of the water The saline water flows gradually down through the evaporation channels 20 in the channel members 18 toward the condenser regions 22 During such downward flow the water experiences a gradual In this controlled flash type a portion of the saline water thereby extracting heat from the unevaporated This vapor occupies a much greater volume and has much less inertia than the unevaporated Accordingly it is impelled at a rapid rate downwardly through the channel This rapid movement of vapor is accompanied by a smoothly distributed pressure gradient along the channel which results in a gradual or controlled flash along the This controlled flash evaporation is similar to that achieved according to Patent Both vapor and unevaporated saline water are discharged from the bottom of the channels 20 into the condenser region The unevaporated liquid tends to adhere to the liner 24 in the condenser region and thus for the most follows the walls of the condenser region 22 down to saline water collection trough 3 the bottom of the condenser region Any premature drippage of the unevaporated saline water is prevented by the upper baffle 28 from entering the interior of the separator The vapors which issue from the descending saline water in the channels 20 fill the greater portion of the interior of the condenser regions and through spaces the upper baffle 28 and the top of the o element These vapors enter into the interior of the separator element insufficientOCRQuality

Claims (1)

  1. A condenser comprising a chamber into which to be condensed can be and plurality of tally extending condenser tubes in the chaiaber arranged so that condensate forming on the exterior of any tube at any location along its length will drop down from the location into a condensate collection trough positioned under the tubes avoiding further contact with the other the condenser tubes occupying a volume in the range of substantially 2 to of the total volume of the A condenser according to claim 1 wherein at least some of the tubes are vertically staggered so that none of the tubes is directly above A condenser according to 1 or 2 wherein the a housing in the of a horizontally extending tubular and a generally horizontal inlet plate positioned above the tubes for dividing the housing into upper and lower the plate being perforated to effect distributed entry into the lower region of vapors introduced into the upper A fresh water recovery system using one or more condensers according to claims 1 or including an elongated supporting structure positioned above the the structure having an upper portion defining a reservoir surface for holding the fluid from which fresh water is to be and flow channels downwardly from the surface and connecting into the chambers of the A fresh water recovery system according to claim 4 wherein the fluid held by the supporting structure is a saline water solution at a teiaperature d presaure close to and the flow channels are of restricted area for effecting partial evaporation as the solution flows downwardly through the A fresh water recovery according to either of claims 4 or 5 wherein the condensate collection trough is A fresh water recovery according to any of claiias 5 and 6 wherein a shield is positioned above the condenser A fresh water recovery system according to any of claims 4 6 wherein the flow channels are displaced one above the other with interposed and are provided to direct unevaporated fluid upper flow channel around the condenser therebelow and the next lower flow condenser substantially as described above by way of example and with reference to the accompanying A fresh water recovery ste substantially as described above by way of example and with reference to the accompanying For the Applicants PARTNERS 19 insufficientOCRQuality
IL29503A 1967-02-21 1968-02-20 Condenser construction and fresh water recovery system IL29503A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US61764267A 1967-02-21 1967-02-21

Publications (1)

Publication Number Publication Date
IL29503A true IL29503A (en) 1972-01-27

Family

ID=24474437

Family Applications (1)

Application Number Title Priority Date Filing Date
IL29503A IL29503A (en) 1967-02-21 1968-02-20 Condenser construction and fresh water recovery system

Country Status (7)

Country Link
US (1) US3501382A (en)
DE (1) DE1601116A1 (en)
ES (1) ES350692A1 (en)
FR (1) FR1556000A (en)
GB (1) GB1212252A (en)
IL (1) IL29503A (en)
NL (1) NL6802385A (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IL37225A (en) * 1971-07-05 1974-05-16 Israel Desalination Eng Ltd Multieffect evaporator
US4218289A (en) * 1976-03-08 1980-08-19 The Upjohn Company Distillation apparatus with a grid partial condenser
US4880504A (en) * 1987-02-24 1989-11-14 Cellini John V Vacumm distillation system with spiralled cold coil
RU2392392C1 (en) * 2009-04-13 2010-06-20 Государственное образовательное учреждение высшего профессионального образования "Вологодский государственный технический университет" (ВоГТУ) Vessel to produce water from atmospheric air
CN110686524B (en) * 2018-07-04 2025-07-18 杭州沈氏节能科技股份有限公司 Coiled pipe type evaporative condenser
CN115286157B (en) * 2021-12-30 2023-11-17 武汉市政环境工程建设有限公司 Landfill leachate solidification preprocessing device

Family Cites Families (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1076410A (en) * 1912-09-30 1913-10-21 Martin L Dunnam Combined condenser and feed-water heater.
US1658143A (en) * 1924-07-12 1928-02-07 Chester D Tripp Oil-shale-distillation apparatus
US1698386A (en) * 1927-03-04 1929-01-08 Charles S Batdorf Water cooler
GB384741A (en) * 1931-10-12 1932-12-15 William Cuthill Mason Improvements in evaporators for distilling or concentrating apparatus
US1855231A (en) * 1931-11-19 1932-04-26 Worthington Pump & Mach Corp Surface condenser
NL78499C (en) * 1950-09-07
US2782150A (en) * 1953-10-23 1957-02-19 Westinghouse Electric Corp Evaporator apparatus
US3192131A (en) * 1960-06-20 1965-06-29 Aqua Chem Inc Multi-stage flash evaporator with removable stages
NL300398A (en) * 1962-11-22
US3214350A (en) * 1962-11-27 1965-10-26 Saline Water Conversion Corp Falling film still
US3275529A (en) * 1962-12-28 1966-09-27 Saline Water Conversion Corp Falling film still having convex film feeding spillways
US3330739A (en) * 1964-06-05 1967-07-11 Saline Water Conversion Corp Multi-cell flash distillation system
US3351119A (en) * 1965-01-05 1967-11-07 Rosenblad Corp Falling film type heat exchanger

Also Published As

Publication number Publication date
US3501382A (en) 1970-03-17
GB1212252A (en) 1970-11-11
NL6802385A (en) 1968-08-22
DE1601116A1 (en) 1970-05-21
FR1556000A (en) 1969-01-31
ES350692A1 (en) 1969-11-16

Similar Documents

Publication Publication Date Title
US4624747A (en) Process for the distillation of fresh water from sea water
US4585523A (en) Vapor compression distillation apparatus
US3834133A (en) Direct contact condenser having an air removal system
US2696465A (en) Thermocompression distilling plant
GB1021569A (en) Flash evaporators
JPH04244202A (en) Multi-stage flash evaporation device using uneven surface type plate heat exchanger
US3830293A (en) Tube and shell heat exchangers
US3529662A (en) Horizontal tube condenser
IL29503A (en) Condenser construction and fresh water recovery system
US2934477A (en) Flash-type distillation system
US2038002A (en) Heat exchanger
US3741879A (en) Apparatus for distillation of fluids
US5775129A (en) Heat exchanger
US5049199A (en) Potable water recovery and fluid preheater for syrup evaporator
US3214350A (en) Falling film still
GB2160115A (en) Sea water desalination apparatus
US2317234A (en) Refrigeration
US3330739A (en) Multi-cell flash distillation system
US3907629A (en) Multiple effect evaporator apparatus
US3619378A (en) Multistage vertical flash distillation apparatus having low heat consumption
JP3879407B2 (en) Fresh water generator
JPS6314293Y2 (en)
USRE32083E (en) Reduction of superheating
US1795601A (en) Apparatus for concentrating solutions
JPS6121701A (en) Flash evaporator