CN103204557B - Vacuum evaporation desalination device - Google Patents
Vacuum evaporation desalination device Download PDFInfo
- Publication number
- CN103204557B CN103204557B CN201310015277.7A CN201310015277A CN103204557B CN 103204557 B CN103204557 B CN 103204557B CN 201310015277 A CN201310015277 A CN 201310015277A CN 103204557 B CN103204557 B CN 103204557B
- Authority
- CN
- China
- Prior art keywords
- mentioned
- sea water
- condenser
- preheater
- water
- Prior art date
- 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.)
- Active
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63J—AUXILIARIES ON VESSELS
- B63J1/00—Arrangements of installations for producing fresh water, e.g. by evaporation and condensation of sea water
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
-
- 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Ocean & Marine Engineering (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The present invention provides a kind of Vacuum evaporation desalination device.The thermal efficiency of this Vacuum evaporation desalination device is excellent.Vacuum evaporation desalination device（1）Including：Heater（3）, it is heated to the raw material seawater being supplied to using the heat carrying out self-heat power and is generated steam；The container body of hermetic type（2）, it is for utilizing heater（3）The steam producing imports；Decompression member（Water ejector）（7）, it is used for container body（2）Inside reduced pressure；Condenser（4）, it is used for using cooling sea water to container body（2）Interior steam is cooled down and is generated fresh water；Preheater（5）, it is used for utilizing container body（2）Interior steam is to condenser（4）The cooling ejecting is heated with a part for sea water and is supplied to heater as raw material seawater（3）.Condenser（4）And preheater（5）In each heat pipe of at least one（40、50）Inner surface or outer surface carried out convex-concave processing.
Description
Technical field
The present invention relates to a kind of Vacuum evaporation desalination device for manufacturing fresh water from sea water, more particularly to a kind of
There is the Vacuum evaporation desalination device of preheater.
Background technology
In the ship generally at sea running, carry out following process from the past：By from the boiler being equipped on ship
Steam or the used heat from diesel engine, other devices are used as thermal source, make to steam under a high vacuum from the marine sea water drawing up
Send out and manufacture fresh water.This Vacuum evaporation desalination device generally includes：Heater, its pass through to the raw material seawater being supplied to
Carry out heat exchange between the hot water of the cooling for diesel engine etc. the raw material seawater being supplied to is heated and made it evaporate；
The container body of hermetic type, remains decompression using decompression member by inside it（Vacuum）State, this container body is used for producing
Raw steam condenses and makes its desalination.It is built-in with the condenser with multiple heat pipes in container body, by steam
And heat pipe internal flow cooling with sea water between carry out heat exchange and make steam cool down condensation so that its fresh water
Change.And, a part for the cooling sea water that condenser is discharged is supplied to heater as raw material seawater.
Be supplied to the heat exchange that the raw material seawater of heater is passed through between the steam in itself and condenser, its temperature some
Permitted to raise, but, still far below the evaporating temperature of sea water.Therefore, in the Vacuum evaporation desalination device of said structure it is impossible to
Efficiently the raw material seawater in heater is heated and so that it is evaporated.It is therefore proposed that there being following vacuum evaporation type desalination dresses
Put：This Vacuum evaporation desalination device includes preheater, and this preheater is used for the cooling sea water discharged from condenser（Raw material
Sea water）After heating further, by the cooling sea water after heating（Raw material seawater）Supply to heater（See, for example patent literary composition
Offer 1）.
In the Vacuum evaporation desalination device of patent documentation 1, it is provided with the knot same with condenser above condenser
The multibarrel preheater of structure.The cooling that condenser imports in the heat pipe of preheater passes through it and in container master with sea water
Carry out heat exchange between the internal steam producing and be further heated, thus being supplied as raw material seawater using state at higher temperature
To heater.Thus, in the Vacuum evaporation desalination device of patent documentation 1, seek to improve the thermal efficiency of heater, and
Seek the overall miniaturization of device.
Patent documentation 1：Japanese Unexamined Patent Publication 6-254534 publication
But, in the Vacuum evaporation desalination device of patent documentation 1, by arranging preheater, make to be supplied to heating
The temperature of the raw material seawater of device is higher, thus seeking to improve the thermal efficiency of heater, but, due to not especially being used for structure to improving
Become preheater（And condenser）The aspect of the heat conductivility of each heat pipe discuss, therefore, still suffer from improveing in this aspect
Leeway.
Content of the invention
The present invention is conceived to above-mentioned problem and makes, and its object is to provide a kind of thermal efficiency excellent vacuum evaporation
Formula desalter.
The above-mentioned purpose of the present invention can be realized by a kind of Vacuum evaporation desalination device.This vacuum evaporation type desalination
Device, using the heat from the thermal source being equipped on ship, manufactures fresh water, wherein, this vacuum from the sea water being introduced in ship
Vaporation-type desalter includes：Heater, it is heated to the raw material seawater being supplied to using the heat carrying out self-heat power and is given birth to
Become steam；The container body of hermetic type, it is imported for the steam being produced using above-mentioned heater；Decompression member, its be used for
State in container body and reduced pressure；Condenser, it has multiple heat pipes, for using cooling sea water to said vesse main body
Interior steam is cooled down and is generated fresh water；Preheater, it has multiple heat pipes, for using the steaming in said vesse main body
Vapour is supreme to supplying as raw material seawater after being heated from the cooling that above-mentioned condenser ejects with a part for sea water
State heater,
In above-mentioned condenser and above-mentioned preheater, the inner surface of above-mentioned each heat pipe of at least one or outer surface are carried out
Cross convex-concave processing.
Set in the preferred technical scheme of the present invention it is characterised in that between above-mentioned condenser and above-mentioned preheater
Have donkey pump, this donkey pump be used for make from the cooling sea water that above-mentioned condenser ejects a part boosting after be supplied to
Above-mentioned preheater.
In the preferred technical scheme of the present invention it is characterised in that this Vacuum evaporation desalination device include for
By the cooling pump of sea water supply to above-mentioned condenser, said pump is for by from the marine sea water supply drawing up to comprising
Each sea water of the ship of diesel engine uses the sea water pump at position.
It is characterised in that this Vacuum evaporation desalination device includes using in the preferred other technologies scheme of the present invention
In by cooling with sea water supply to above-mentioned condenser pump, above-mentioned decompression member is the water ejector being driven by sea water, and, on
Stating pump is for by the ejector pump of driving sea water supply to above-mentioned water ejector, the driving discharged from above-mentioned water ejector is extra large
Water is by as cooling sea water supply to above-mentioned condenser.
According to the Vacuum evaporation desalination device of technique scheme, preferably above-mentioned heat pipe is made up of corrugated tube.Or,
Preferably above-mentioned heat pipe is to carry out convex-concave processing by being integrally provided projection or groove on its inner surface or outer surface
's.
And, it is characterised in that above-mentioned decompression member is to be driven by sea water in the preferred other technologies scheme of the present invention
Dynamic water ejector, this Vacuum evaporation desalination device also include for by driving sea water supply to above-mentioned water ejector spray
Penetrate pump, above-mentioned ejector pump is supplied to supreme after being used for making boosting from a part for the cooling sea water that above-mentioned condenser ejects
State water ejector and above-mentioned preheater.It is preferred that this Vacuum evaporation desalination device also includes using in this technical scheme
In by cooling with sea water supply to above-mentioned condenser pump, said pump be for will from the marine sea water supply drawing up to wrap
Each sea water of the ship containing diesel engine uses the sea water pump at position.And, it is further preferred that above-mentioned heat pipe is by corrugated tube structure
Become, or above-mentioned heat pipe is to be added by being integrally provided projection or groove on its inner surface or outer surface and carry out convex-concave
Work.
And, it is preferred that above-mentioned heating utensil in the Vacuum evaporation desalination device of above-mentioned all of technical scheme
Have multiple heating tubes, raw material seawater can be imported to the inside of the plurality of heating tube, the inner surface of above-mentioned each heating tube or
Outer surface carried out convex-concave processing.
Using the Vacuum evaporation desalination device of the present invention, due to each heat conduction at least one in condenser and preheater
The inner surface of pipe or outer surface carried out convex-concave processing, therefore, it is possible to improve the heat conductivility of each heat pipe.Thus, with profit
Compared with the existing vacuum evaporation type desalter that smooth pipe constitutes each heat pipe, can make to supply to heater from preheater
Raw material seawater temperature be higher temperature.Therefore, it is possible to improve the thermal efficiency of heater further.
Brief description
Fig. 1 is the summary construction diagram of the Vacuum evaporation desalination device of one embodiment of the present invention.
Fig. 2 is the longitudinal section of the apparatus main body of Fig. 1.
Fig. 3 is the sectional view of I-I line along Fig. 2.
Fig. 4 is the sectional view of II-II line along Fig. 2.
Fig. 5 is the sectional view of heat pipe.
Fig. 6 is the longitudinal section of the apparatus main body of other embodiment.
Fig. 7 is the sectional view of heating tube.
Fig. 8 is the summary construction diagram of the Vacuum evaporation desalination device of the other embodiment of the present invention.
Fig. 9 is the summary construction diagram of the Vacuum evaporation desalination device of the other embodiment of the present invention.
Figure 10 is the summary construction diagram of the Vacuum evaporation desalination device of the other embodiment of the present invention.
Specific embodiment
Hereinafter, referring to the drawings while illustrating to embodiments of the present invention.Fig. 1 is an embodiment party of the present invention
The summary construction diagram of the Vacuum evaporation desalination device 1 of formula, Fig. 2 is the longitudinal section of the apparatus main body 6 of Fig. 1.As Fig. 1 and Fig. 2
Shown, the Vacuum evaporation desalination device 1 of present embodiment include by the container body 2 of hermetic type, heater 3, condenser 4 and
Apparatus main body 6 that preheater 5 is constituted and for container body 2 is remained decompression（Vacuum）The decompression member 7 of state.In addition,
In FIG, reference 10 is the hull of ship, and reference 11 is disposed in ship and for from the marine sea water that draws
Sea water pump.The sea water being drawn up by sea water pump 11 is except being reserved as cooling down various sea water using the chuck that position cools down
Outside the diesel engine that water supplies to various sea water using position, be for example equipped in ship, also by as vacuum evaporation type desalination
The cooling water supply of the desalination of device 1 is to condenser 4.
For container body 2, connect having heaters 3 in its underpart, and, be built-in with condenser 4 and preheating at an upper portion thereof
Device 5.And, it is provided with exhaustor 102 on the top of container body 2, and, the ratio heater 3 in the bottom of container body 2 is high
Position is provided with brine outlet 103.
Exhaustor 102 is connected to decompression member 7 by gas piping 17.Decompression member 7 is sprayed by water in the present embodiment
Emitter is constituted, and the non-condensing gas of the inside of container body 2 are attracted out from exhaustor 102 by water ejector 7, container master
It is retained as the decompression forced down than air in body 2（Vacuum）State, in container body 2, can be in decompression（Vacuum）Under state
Carry out the evaporative condenser of raw material seawater described later.And, brine outlet 103 is connected to water injection by brine discharge tube road 18
Device 7, the saline after evaporation in container body 2 described later（Sea water）Attracted out from brine outlet 103 by water ejector 7
Afterwards, it is discharged to outside ship.
Heater 3 includes the heating chamber 30 of hermetic type and the multiple heating tubes 31 being arranged in heating chamber 30.Multiple heating
Pipe 31 is configured in the way of being extends in the vertical direction, two ends of this heating tube 31 be connected to heating chamber 30 upper wall surface and under
Wall.It is connected with sea water supply room 32 in the bottom of heating chamber 30, be provided with for leading raw material seawater in sea water supply room 32
Enter to the raw material seawater introducing port 33 of each heating tube 31.Hot water introducing port 34 and hot water row are provided with the side wall of heating chamber 30
Outlet 35, this hot water introducing port 34 can import the hot water such as the chuck cooling water of the cooling for diesel engine etc., this hot water outlet
35 can discharge the hot water such as the chuck cooling water of the cooling for diesel engine etc..It is directed into each heating tube from raw material seawater introducing port 33
31 raw material seawater is directed between the hot water in heating chamber 30 by it and from hot water introducing port 34 and carries out heat exchange and added
Heat and evaporate, become steam and be supplied in container body 2.
Condenser 4 is used for the steam being supplied in container body 2 being cooled down and being generated fresh water, and this condenser 4 wraps
Obtained from including multiple heat pipes 40 and each getting up with by these multiple heat pipe 40 harnesses, the two ends of heat pipe group are connected
The 1st top cover 9A and the 2nd top cover 9B.Each heat pipe 40 is configured in the way of horizontally extending, two of each heat pipe 40
End is connected to left wall face and the right wall of container body 2.
It is provided with the multiple heat pipes 50 for constituting preheater 5 above condenser 4.The plurality of heat pipe 50 is also with edge
The mode that horizontal direction extends configures, and two ends of multiple heat pipes 50 are connected to left wall face and the right wall of container body 2,
And be connected with the 1st top cover 9A and the 2nd top cover 9B.
It is provided with demarcation strip 90A in the 1st top cover 9A, in the 2nd top cover 9B, be provided with demarcation strip 90B.Separated in top cover 9A
Plate 90A is divided into the condensation top cover room 92A with top cover room 91A and lower section for the preheating of top, is drawn by demarcation strip 90B in top cover 9B
It is divided into the condensation top cover room 92B with top cover room 91B and lower section for the preheating of top.Top cover room is used in preheating top cover room 91A, preheating
91B is connected with each heat pipe 50 for constituting preheater 5, and on the other hand, top cover room is used in condensation top cover room 92A, condensation
92B is connected with each heat pipe 40 for constituting condenser 4.
As shown in figure 3, being provided with demarcation strip 93A in condensation top cover room 92A, it is provided with condensation top cover room 92B point
Dividing plate 93B.In the condensation top cover 92A of the 1st top cover 9A, the cooling water inlet room 94a in distally and near is divided into by demarcation strip 93A
The room 94b that turns back of side.Additionally, the cooling water being divided into nearside by demarcation strip 93B in the condensation top cover 92B of the 2nd top cover 9B goes out
The mouth room 94d and room 94c that turns back in distally.
It is provided with cooling water inlet 95 in the 94a of cooling water inlet room, this cooling water inlet 95 is used for importing and is used for container
The cooling sea water of the steam cooling condensation in main body 2.It is connected with cooling water supply pipeline 13 at cooling water inlet 95, should
Each sea water that cooling water supply pipeline 13 is connected in from sea water pump 11 to ship uses the sea water supply pipeline 12 at position（Reference
Fig. 1）, worked by making sea water pump 11, sea water is imported as cooling water.It is fed to the cold of cooling water inlet room 94a
But use sea water in each heat pipe 40 as shown by arrows in Figure 3 as, in carrying out in the room 94b that respectively turns back, the room 94c that turns back
Continue, towards the coolant outlet room 94d flowing of the 2nd top cover 9B of opposite side.The steam being supplied in container body 2 passes through it
And carry out heat exchange between the cooling of flowing is with sea water in each heat pipe 40 and be cooled thus being condensed, generated by condensation
Fresh water be discharged from the water outlet 96 being arranged at container body 2.
It is provided with the coolant outlet 97 for discharging cooling sea water in the 94d of coolant outlet room.Go out from cooling water
A part for the cooling sea water that mouth 97 ejects is supplied to ejector pump 8 via branch line 14, and another part is via water supply
Pipeline 15 is supplied to preheater 5, and it is outer etc. that remainder is discharged to ship（With reference to Fig. 1）.Ejector pump 8 is used for driving water to spray
Device 7, it is integrally provided with apparatus main body 6 and forms.The cooling being supplied to ejector pump 8 is boosted with seawater utilization ejector pump 8
Afterwards, it is supplied to water ejector 7, after driving water ejector 7, be discharged to outside ship.
Then, as shown in figure 4, being provided with two pieces of demarcation strip 98A in preheating top cover room 91A, in preheating top cover room 91B
Inside it is provided with two pieces of demarcation strip 98B.It is divided into the raw material seawater in distally by demarcation strip 98A in the preheating top cover 91A of the 1st top cover 9A
The room 99d that turns back of turn back room 99e and the nearside in downstream chamber 99f and central authorities.And, the preheating of the 2nd top cover 9B is with top cover 91B
The raw material seawater inlet 99a of nearside and the room 99c that turns back in turn back room 99b and the distally in central authorities are divided into by demarcation strip 98B.
It is provided with raw material seawater entrance 100 in raw material seawater inlet 99a, this raw material seawater entrance 100 is used for importing certainly
A part for the cooling sea water that condenser 4 ejects.Supply channel 15 is connected with raw material seawater entrance 100, is supplying water
Pipeline 15 is provided with donkey pump 9（With reference to Fig. 1）.A part for the cooling sea water that condenser 4 ejects is using donkey pump 9
In the state of so that it is boosted, it is fed to raw material seawater inlet 99a.Then, a part for this cooling sea water is for structure
Become in each heat pipe 50 of preheater 5 as shown in the arrow of Fig. 4, in carrying out in the room 99b that the respectively turns back～room 99e that turns back
Continue, towards the raw material seawater downstream chamber 99f flowing of the 1st top cover 9A of opposite side.Now, cooling sea water passes through respectively leading
Carry out heat exchange and the steam being supplied in container body 2 between during flowing in heat pipe 50 and be heated, be fed to
Raw material seawater downstream chamber 99f.
It is provided with the raw material seawater outlet 101 for discharging cooling sea water in raw material seawater downstream chamber 99f.From raw material
The cooling sea water that seawer outlet 101 ejects is supplied as raw material seawater via raw material seawater feeding pipe 16 and is supplied to sea water
To room 32.
So, due to there is the preheater 5 of said structure, a part of of cooling sea water that condenser 4 ejects is led to
Cross and be supplied to carry out heat exchange between the steam of the higher temperature in container body 2 and heated after, by as raw material
Sea water supply is to heater 3.Thus, it is possible to make the temperature being supplied to the raw material seawater of heater 3 higher such that it is able to improve
The thermal efficiency of heater 3.
As shown in figure 5, for constituting each heat pipe 40 of condenser 4 and being used for constituting each heat pipe 50 of preheater 5
Inner surface and outer surface carried out convex-concave processing.In the present embodiment, each heat pipe 40, each heat pipe 50 are by corrugated tube structure
Become, the tube wall 41 of heat pipe 40 alternately continuously has multiple protuberances 42 and recess 43, in the tube wall 51 of heat pipe 50
Upper alternately continuously have multiple protuberances 52 and recess 53.Protuberance 42, protuberance 52 and recess 43, recess 53 cross-sectional shape except
Be formed as Fig. 5（A）Outside chevron shape as shown, may be formed as Fig. 5（B）, Fig. 5（C）Shown
Such rectangle, waveform etc. are variously-shaped.
In addition, as each heat pipe 40, each heat pipe 50, in addition to using corrugated tube, it is possible to use following adds
Work pipe, this processing pipe is by the tube wall 41 of the smooth pipe smoothing in tube wall 41, tube wall 51, the inner surface of tube wall 51 and outer surface
On be axially integrally provided the projection of multiple ring-types circumferentially extending at a predetermined interval and concavo-convex be processed into.This
Outward, as processing pipe it is also possible to pass through to be integrally provided to projection in the shape of a spiral tube wall 41, the interior table of tube wall 51 of smooth pipe
Face and outer surface carrying out convex-concave processing, or can also by replace projection and by groove with by way of same with projection integratedly
It is arranged at tube wall 41, the inner surface of tube wall 51 and the outer surface of smooth pipe.And, can also pass through many by axially extend
Individual projection or groove are circumferentially integrally provided to smooth tube wall 41, the inner surface of tube wall 51 and the appearance of pipe at a predetermined interval
Face is carrying out convex-concave processing.So, as long as making each heat pipe 40, the surface area of heat pipe 50 becomes big, being capable of unrestricted choice
The method that convex-concave processing is carried out to tube wall 41, the inner surface of tube wall 51 and outer surface.
In the vacuum evaporation type desalter 1 of present embodiment, due to the heat pipe 40 of condenser 4 and preheater 5
The inner surface of heat pipe 50 and outer surface carried out convex-concave processing, therefore, compared with the smooth pipe that its external diameter is roughly equal, respectively led
Heat pipe 40, each heat pipe 50 surface area larger, i.e. can carry out guaranteeing bigger thermal conductive surface during heat exchange inside and outside heat pipe
Long-pending, and, to stir the cooling sea water in heat conduction Bottomhole pressure by using concavo-convex, thus improving thermal conductive surface（Tube wall 41, pipe
Wall 51）Heat transfer efficiency between the steam at place and cooling sea water, as a result, the heat exchange of each heat pipe 40, each heat pipe 50
Amount increases.Thus, by each heat pipe 40, the inner surface of each heat pipe 50 and outer surface are carried out with convex-concave processing, flat with using
The situation of slip pipe is compared, can by make each heat pipe 40, each heat pipe 50 in flow cooling sea water and steam between
Carry out heat exchange, and the cooling heating of seawater of flowing in each heat pipe 40, heat pipe 50 is become higher temperature, as a result,
The temperature being supplied to the raw material seawater of heater 3 can be made higher.Thus, it is possible to improve the thermal efficiency of heater 3 further.
On the other hand, when each heat pipe 40, the inner surface of each heat pipe 50 and outer surface are carried out with convex-concave processing, due to
Concavo-convex and lead to pipe friction coefficient to increase, thus the pressure loss in the cooling sea water of heat conduction Bottomhole pressure becomes big.Therefore, it is
Prevent the bad situation of cooling sea water flowing, need to increase the size of heat pipe or improve the capacity of sea water pump and raise
The such countermeasure of journey.For condenser 4, because using sea water pump 11, the sea water after boosted is supplied to condenser 4,
Therefore, condenser 4 is not readily susceptible to the impact of pressure loss increase, but, for preheater 5, due to condenser 4 row
Cooling sea water out is supplied to preheater 5, and, preheater 5 pressure loss of itself also increases, accordingly, as pre-
The pressure of sea water in the raw material seawater outlet 101 of the outlet of hot device 5 is greatly reduced compared with the situation using smooth pipe.
When pressure loss becomes big, from the sea water supply reduced pressure of raw material seawater outlet 101 when it is possible to cannot be sufficiently to heating
Device 3 base feed sea water.In order to solve these problems although it can be considered that improve sea water pump 11 capacity lift method,
But, in the capacity of the large-scale sea water pump 11 improving further for each sea water in sea water supply to ship being used position
Etc. aspect, there are the operating funds such as cost, amount of power consumption of pump itself and significantly raise such problem.Therefore, in this enforcement
In the vacuum evaporation type desalter 1 of mode, the supply channel 15 between condenser 4 and preheater 5 is arranged small-sized auxiliary
Help pump 9, after the cooling seawater utilization donkey pump 9 that condenser 4 is ejected boosts, supply to preheater 5.Thus, exist
It is also possible to promote the heat exchange between cooling sea water and steam in preheater 5, further, it is possible to the pressure of corresponding cooling sea water
The problem that power loss increases, therefore, it is possible to fully guarantee the output of raw material seawater for heater 3.
Using the vacuum evaporation type desalter 1 of said structure, due to the multibarrel condenser 4 in container body 2
Top arranges multibarrel preheater 5, the raw material seawater of supply to heater 3 is heated, it is therefore not necessary to be used for making preheating
The space that device 5 is provided independently from condenser 4, can seek the miniaturization of device.
And, the inner surface due to each heat pipe 50 to each heat pipe 40 of condenser 4 and preheater 5 and outer surface enter
Go convex-concave processing, therefore, it is possible to improve the heat conductivility of each heat pipe 40, each heat pipe 50.Thus, smooth pipe structure with utilizing
The existing vacuum evaporation type desalter becoming each heat pipe 40, each heat pipe 50 is compared, and can make condenser 4 via preheating
Device 5 and the temperature of raw material seawater that supplies to heater 3 is higher temperature, therefore, it is possible to improve the thermal effect of heater 3 further
Rate.It is additionally, since setting donkey pump 9 on the supply channel 15 between condenser 4 and preheater 5, condenser 4 is ejected
Cooling with seawater utilization donkey pump 9 boosting after, supply to preheater 5, therefore, it is possible to tackle each heat conduction in preheater 5
The cooling sea water of flowing in pipe 50（Raw material seawater）Pressure loss increase problem.Thus, it is possible to heater 3 sufficiently
Base feed sea water.As a result, the manufacture of the fresh water manufacturing in vacuum evaporation type desalter 1 increases, Neng Gouti
The desalting performance of high device.On the other hand, with the existing vacuum steaming constituting each heat pipe 40, each heat pipe 50 using smooth pipe
Hair style desalter is compared, and the desalting performance due to device raises, even if therefore reducing each heat conduction of condenser 4 and preheater 5
Pipe 40, the quantity of each heat pipe 50 are it is also possible to manufacture approximately equal amounts of fresh water.Thus it is also possible to seek the miniaturization of device.
And, in the existing vacuum evaporation type desalter constituting each heat pipe 40, each heat pipe 50 using smooth pipe
In, only smooth pipe is replaced with inner surface and outer surface carried out the corrugated tube of convex-concave processing, processing pipe etc. it becomes possible to improve dress
The desalting performance put, therefore, it is possible to simply and to carry out edition upgrading to existing vacuum evaporation type desalter at low cost.
More than, one embodiment of the present invention is illustrated, but, the present invention is not limited to above-mentioned embodiment party
Formula, can carry out various changes in the range of the purport without departing from the present invention.For example in the embodiment of above-mentioned Fig. 1
In, convex-concave processing is carried out to each heat pipe 40, the inner surface of each heat pipe 50 and outer surface, however, it can be only internal
One of surface or outer surface carry out convex-concave processing.
And although each heat pipe 50 of each heat pipe 40 to condenser 4 and preheater 5 implements convex-concave processing, but
It is or one of each heat pipe 50 of each heat pipe 40 only to condenser 4 or preheater 5 is implemented convex-concave and added
Work.
Furthermore, it is also possible in the same manner as each heat pipe 40 of condenser 4, each heat pipe 50 of preheater 5, to heater 3
Each heating tube 31 implement convex-concave processing.Fig. 6 represents each heat pipe of the not only each heat pipe 40 to condenser 4 and preheater 5
50 implement convex-concave processing, and also each heating tube 31 of heater 3 is implemented with the embodiment of convex-concave processing（The deformation of Fig. 2
Example）.In the same manner as each heat pipe 40 of condenser 4 and each heat pipe 50 of preheater 5, as shown in fig. 7, each heating tube 31 is at it
Tube wall 31A alternately continuously has multiple protuberance 31B and recess 31C, implements convex-concave processing on its inner surface and outer surface.
The cross-sectional shape of protuberance 31B and recess 31C is except being formed as Fig. 7's（A）As shown in chevron shape, may be formed as
As Fig. 7（B）, Fig. 7（C）Rectangle as shown, waveform etc. are variously-shaped.As the heating tube 31 of said structure, energy
Enough preferably use corrugated tube, but be in addition to outside corrugated tube, it is possible to use by by the multiple ring-types circumferentially extending
Projection is axially integrally provided to the inner surface of tube wall 31A of smooth pipe and the appearance that tube wall 31A smooths at a predetermined interval
Face and processing pipe that convex-concave is processed into.And, as processing pipe it is also possible to pass through to be integrally provided in the shape of a spiral put down by projection
The tube wall 31A inner surface of slip pipe and outer surface carrying out convex-concave processing, furthermore, it is also possible to by replace projection and by groove and projection
Similarly it is integrally provided to smooth the inner surface of tube wall 31A of pipe and outer surface to carry out convex-concave processing.And, can also lead to
Cross the tube wall 31A that the multiple projections axially extending or groove are circumferentially integrally provided at a predetermined interval smooth pipe
Inner surface and outer surface.So, as long as making the surface area of each heating tube 31 become big, can unrestricted choice to tube wall 31A
Inner surface and the outer surface method that carries out convex-concave processing.
Convex-concave processing is carried out by the inner surface and outer surface of each heating tube 31 to heater 3, with its external diameter substantially phase
Deng smooth pipe compare, the surface area of each heater 30 is larger, i.e. can carry out guaranteeing during heat exchange larger inside and outside heating tube
Heat-conducting area.And, to stir the raw material seawater in heating Bottomhole pressure by using concavo-convex, thus improving thermal conductive surface（Pipe
Wall 31A）In hot water and raw material seawater between heat transfer efficiency.As a result, the heat exchange amount of each heating tube 31 increases.Thus,
Embodiment as shown in Figure 6 is like that, by carrying out convex-concave processing to the inner surface of each heating tube 31 and outer surface, flat with using
The situation of slip pipe is compared, and efficiently carries out heat exchange, Neng Gouti in each heating tube 31 between the raw material seawater of flowing and hot water
The efficiency of heating surface of high each heating tube 31, as a result, can make raw material seawater evaporation efficiency good such that it is able to steam is sufficient
Supply to container body 2.
And, in the embodiment of above-mentioned Fig. 1, the used heat from diesel engine is used as to heat raw material in heater 3
Sea water simultaneously makes the thermal source that it evaporates, but, in addition it is also possible to utilize from for producing the used heat of the equipment of used heat,
Raw material seawater can be heated and so that it is evaporated in heater 3 using the steam from boiler.
And, in the embodiment of above-mentioned Fig. 1, a part for the cooling sea water that condenser 4 is discharged is using auxiliary
Pump 9 is helped to boost and pass through supply channel 15 and supply to preheater 5, but it is also possible to omit this donkey pump 9.Fig. 8 is the reality of Fig. 1
Apply the variation of mode, it represents the summary construction diagram of the Vacuum evaporation desalination device 1 eliminating donkey pump 9.In addition, this change
The basic structure of shape example is identical with the structure of the embodiment of above-mentioned Fig. 1, here, attached to corresponding structure mark identical
Icon is remembered, thus omitting the description.
In the embodiment of Fig. 8, a part for the cooling sea water that condenser 4 ejects passes through branch line 14 quilt
Supply to ejector pump 8, it is outer etc. that the remainder of cooling sea water is discharged to ship.It is supplied to the cooling sea of ejector pump 8
After water conservancy is boosted with ejector pump 8, the cooling sea water of a part is supplied to water ejector 7, on the other hand, remainder
Cooling sea water is supplied to preheater 5 via supply channel 19.Then, the cooling sea water being supplied to preheater 5 passes through
Carry out heat exchange and the steam being supplied in container body 2 between and heated after, as raw material seawater via raw material sea
Water supplying pipe road 16 is supplied to heater 3.So, in the embodiment of Fig. 8, by making the pipe of the ejection side of ejector pump 8
Road branch, the cooling sea water after being boosted using ejector pump 8 is supplied to preheater 5 by supply channel 19, copes with
The problem that in each heat pipe 50 of preheater 5, the pressure loss of the cooling sea water of flowing increases is such that it is able to fill to heater 3
Foot ground base feed sea water.As a result, in addition to being capable of the action effect same with the embodiment of Fig. 1, due to
Do not need donkey pump 9, thus, it is also possible to make device simplify.
And, in the embodiment of above-mentioned Fig. 1, ejector pump 8 is integrally provided with apparatus main body 6 and forms, but, such as
It is also possible to be arranged at ejector pump 8 than apparatus main body 6 position on the lower shown in Fig. 9.In the embodiment of figure 1, condenser
A part for the cooling sea water that 4 eject is supplied to ejector pump 8, but, in the embodiment of Fig. 9, ejector pump 8 is from sea
In draw sea water, and using this sea water as drive water supply to water ejector 7.
And, in the embodiment of Fig. 1, Fig. 8 and Fig. 9, it is sprayed against device and is used as decompression member 7, but, might not
It is defined in this it is also possible to vacuum pump etc. is used as decompression member 7.
And, Figure 10 represents the summary construction diagram of the Vacuum evaporation desalination device 1 of the other embodiment of the present invention.Separately
Outward, the basic structure of this embodiment is identical with the embodiment of above-mentioned Fig. 1, here, mark identical to corresponding structure
Reference, thus omitting detailed description.
In the embodiment of Figure 10, supply sea water to water ejector 7 via cooling water as driving water self-injection pump 8
Supply circuit 13 is by the cooling water supply of the desalination as Vacuum evaporation desalination device 1 to condenser 4.To be used for from marine
The small-sized pump drawing sea water and this sea water being only supplied to water ejector 7 is used as ejector pump 8.
In the embodiment of this Figure 10, make to be supplied to container body 2 in the cooling sea water being supplied to condenser 4
After interior steam cooling condenses and generates fresh water, this cooling sea water condenser 4 is discharged, but, this cooling sea
A part for water is supplied to preheater 5 processed, the part of this cooling sea water by with the steam being supplied in container body 2
Between carry out heat exchange and heated after, be supplied to sea water supply as raw material seawater via raw material seawater feeding pipe 16
Room 32.Here, by each heat pipe 50 to preheater 5（And each heat pipe 40 of condenser 4）Inner surface and outer surface in
At least one carry out convex-concave processing, so that the temperature of the raw material seawater supplying to heater 3 is higher, it is possible to increase heater
3 thermal efficiency.On the other hand, in the embodiment of Figure 10, can be by improving capacity of ejector pump 8 etc. without auxiliary
Pump 9, and, with the cost lower than the method for the capacity improving sea water pump 11 etc., to tackle each heat pipe 50 in preheater 5
（And each heat pipe 40 of condenser 4）The problem that the pressure loss of the cooling sea water of interior flowing increases, therefore, it is possible to heating
Device 3 sufficiently base feed sea water.As a result, being capable of the action effect same with the embodiment of Fig. 1.
Description of reference numerals
1st, Vacuum evaporation desalination device；2nd, container body；3rd, heater；4th, condenser；5th, preheater；7th, water injection
Device；8th, ejector pump；9th, donkey pump；11st, sea water pump；31st, heating tube；40th, 50, heat pipe.
Claims (6)
1. a kind of Vacuum evaporation desalination device, its using the heat from the thermal source being equipped on ship, from being introduced in ship
Sea water in manufacture fresh water, wherein,
This Vacuum evaporation desalination device includes：
Heater, it is heated to the raw material seawater being supplied to using the heat carrying out self-heat power and is generated steam；
The container body of hermetic type, it is imported for the steam being produced using above-mentioned heater；
Decompression member, it is used for reducing pressure in said vesse main body；
Condenser, it has multiple heat pipes, for being cooled down to the steam in said vesse main body with sea water using cooling
And generate fresh water；
Preheater, it has multiple heat pipes, for being ejected to from above-mentioned condenser using the steam in said vesse main body
Cooling heated with a part for sea water after supply to above-mentioned heater as raw material seawater；
For by cooling with sea water supply to above-mentioned condenser pump,
In above-mentioned condenser and above-mentioned preheater, the inner surface of above-mentioned each heat pipe of at least one or outer surface carry out excess convexity
Recessed processing,
It is provided with donkey pump between above-mentioned condenser and above-mentioned preheater, this donkey pump is used for making to eject from above-mentioned condenser
It is supplied to above-mentioned preheater after the part boosting of cooling sea water,
Said pump is the sea water pump for each sea water from the marine sea water supply drawing up to ship uses position,
Above-mentioned decompression member is the water ejector being driven by sea water,
For the ejector pump of driving sea water supply to above-mentioned water ejector is integrally provided with apparatus main body, this apparatus main body
It is made up of said vesse main body, above-mentioned heater, above-mentioned condenser and above-mentioned preheater,
Above-mentioned ejector pump is supplied to supreme after being used for making boosting from a part for the cooling sea water that above-mentioned condenser ejects
State water ejector.
2. Vacuum evaporation desalination device according to claim 1, wherein,
Above-mentioned heat pipe is made up of corrugated tube.
3. Vacuum evaporation desalination device according to claim 1, wherein,
Above-mentioned heat pipe is to carry out convex-concave processing by being integrally provided projection or groove on its inner surface or outer surface
's.
4. a kind of Vacuum evaporation desalination device, its using the heat from the thermal source being equipped on ship, from being introduced in ship
Sea water in manufacture fresh water, wherein,
This Vacuum evaporation desalination device includes：
Heater, it is heated to the raw material seawater being supplied to using the heat carrying out self-heat power and is generated steam；
The container body of hermetic type, it is imported for the steam being produced using above-mentioned heater；
Decompression member, it is used for reducing pressure in said vesse main body；
Condenser, it has multiple heat pipes, for being cooled down to the steam in said vesse main body with sea water using cooling
And generate fresh water；
Preheater, it has multiple heat pipes, for being ejected to from above-mentioned condenser using the steam in said vesse main body
Cooling heated with a part for sea water after supply to above-mentioned heater as raw material seawater；
For by cooling with sea water supply to above-mentioned condenser pump,
In above-mentioned condenser and above-mentioned preheater, the inner surface of above-mentioned each heat pipe of at least one or outer surface carry out excess convexity
Recessed processing,
It is provided with donkey pump between above-mentioned condenser and above-mentioned preheater, this donkey pump is used for making to eject from above-mentioned condenser
It is supplied to above-mentioned preheater after the part boosting of cooling sea water,
Said pump is the sea water pump for each sea water from the marine sea water supply drawing up to ship uses position,
Above-mentioned decompression member is the water ejector being driven by sea water,
For the ejector pump of driving sea water supply to above-mentioned water ejector is arranged at the position on the lower than apparatus main body, should
Apparatus main body is made up of said vesse main body, above-mentioned heater, above-mentioned condenser and above-mentioned preheater,
Above-mentioned ejector pump is supplied to above-mentioned water ejector after being used for making boosting from the marine sea water drawing up.
5. a kind of Vacuum evaporation desalination device, its using the heat from the thermal source being equipped on ship, from being introduced in ship
Sea water in manufacture fresh water, wherein,
This Vacuum evaporation desalination device includes：
Heater, it is heated to the raw material seawater being supplied to using the heat carrying out self-heat power and is generated steam；
The container body of hermetic type, it is imported for the steam being produced using above-mentioned heater；
Decompression member, it is used for reducing pressure in said vesse main body；
Condenser, it has multiple heat pipes, for being cooled down to the steam in said vesse main body with sea water using cooling
And generate fresh water；
Preheater, it has multiple heat pipes, for being ejected to from above-mentioned condenser using the steam in said vesse main body
Cooling heated with a part for sea water after supply to above-mentioned heater as raw material seawater,
In above-mentioned condenser and above-mentioned preheater, the inner surface of above-mentioned each heat pipe of at least one or outer surface carry out excess convexity
Recessed processing,
Above-mentioned decompression member is the water ejector being driven by sea water,
This Vacuum evaporation desalination device also include for by driving sea water supply to above-mentioned water ejector ejector pump,
Above-mentioned ejector pump is supplied to supreme after being used for making boosting from a part for the cooling sea water that above-mentioned condenser ejects
State water ejector and above-mentioned preheater.
6. Vacuum evaporation desalination device according to claim 5, wherein,
Above-mentioned heater has multiple heating tubes, and raw material seawater can import to the inside of the plurality of heating tube,
The inner surface of above-mentioned each heating tube or outer surface carried out convex-concave processing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610680720.6A CN106277116A (en) | 2012-01-16 | 2013-01-16 | Vacuum evaporation desalination device |
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2012-006182 | 2012-01-16 | ||
| JP2012006182 | 2012-01-16 | ||
| JP2012193025A JP6041584B2 (en) | 2012-01-16 | 2012-09-03 | Vacuum evaporative fresh water generator |
| JP2012-193025 | 2012-09-03 |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610680720.6A Division CN106277116A (en) | 2012-01-16 | 2013-01-16 | Vacuum evaporation desalination device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103204557A CN103204557A (en) | 2013-07-17 |
| CN103204557B true CN103204557B (en) | 2017-03-01 |
Family
ID=48752000
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310015277.7A Active CN103204557B (en) | 2012-01-16 | 2013-01-16 | Vacuum evaporation desalination device |
Country Status (2)
| Country | Link |
|---|---|
| KR (1) | KR101821660B1 (en) |
| CN (1) | CN103204557B (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101701470B1 (en) | 2015-06-26 | 2017-02-01 | 삼성중공업 주식회사 | Apparatus for making fresh water by vacuum evaporation method |
| KR101683392B1 (en) * | 2015-08-25 | 2016-12-07 | 한국과학기술원 | Ejector type refrigeration and purification system for cooling of refrigerants and purifying of fluids |
| CN105347415A (en) * | 2015-11-26 | 2016-02-24 | 河北工业大学 | External-corrugation-heat-tube falling-film low-temperature multi-effect sea water desalination evaporator |
| ES2979362T3 (en) * | 2019-09-13 | 2024-09-25 | Alfa Laval Corp Ab | Plate heat exchanger and heat exchanger for the treatment of a liquid feed |
| CN111649601B (en) * | 2020-06-29 | 2022-04-19 | 东和恩泰热能技术(江苏)有限公司 | Large-scale marine vacuum condenser |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130442A (en) * | 2006-08-25 | 2008-02-27 | 葆光（大连）节能技术研究所有限公司 | Method for desalinating sea water by using seawater source heat pump technology |
| CN201089729Y (en) * | 2007-09-05 | 2008-07-23 | 上海汉盛船舶技术有限公司 | Pipe shell-type sea water demineralizer |
| CN101274785A (en) * | 2007-03-27 | 2008-10-01 | 张建城 | Falling film evaporator with ring-shaped corrugated tube for seawater desalination |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3183986B2 (en) * | 1993-03-03 | 2001-07-09 | 株式会社ササクラ | Vacuum evaporation type fresh water generator |
| JP3879407B2 (en) * | 2001-01-29 | 2007-02-14 | 三浦工業株式会社 | Fresh water generator |
| CN1171799C (en) * | 2002-08-09 | 2004-10-20 | 周堃 | Multi-effect distilling process and equipment for desalinating seawater |
| CN200988779Y (en) * | 2006-12-25 | 2007-12-12 | 魏仕英 | Rotary jet flow flash-compression type sea water desalting system |
| JP5672450B2 (en) * | 2011-02-25 | 2015-02-18 | 株式会社ササクラ | Fresh water generator and fresh water generation method |
| CN102795693B (en) * | 2012-08-06 | 2014-04-23 | 西安交通大学 | Solar energy and wind energy jointly driven sea water desalination system based on LNG (Liquefied Natural Gas) cold energy utilization |
-
2013
- 2013-01-16 CN CN201310015277.7A patent/CN103204557B/en active Active
- 2013-01-16 KR KR1020130004816A patent/KR101821660B1/en active IP Right Grant
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101130442A (en) * | 2006-08-25 | 2008-02-27 | 葆光（大连）节能技术研究所有限公司 | Method for desalinating sea water by using seawater source heat pump technology |
| CN101274785A (en) * | 2007-03-27 | 2008-10-01 | 张建城 | Falling film evaporator with ring-shaped corrugated tube for seawater desalination |
| CN201089729Y (en) * | 2007-09-05 | 2008-07-23 | 上海汉盛船舶技术有限公司 | Pipe shell-type sea water demineralizer |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103204557A (en) | 2013-07-17 |
| KR101821660B1 (en) | 2018-01-24 |
| KR20130084264A (en) | 2013-07-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106277116A (en) | Vacuum evaporation desalination device | |
| CN103204557B (en) | Vacuum evaporation desalination device | |
| CN101636354A (en) | Desalination system | |
| TW200505801A (en) | Plate type fresh water generator | |
| CN206045444U (en) | Multi-effect evaporator based on MVR | |
| JP2017507024A (en) | Evaporator | |
| CN205035108U (en) | A light water condenser for sea water desalination device | |
| CN101745240B (en) | Method and device for pumping out incondensable gas between effects of multi-effect distillation system | |
| CN204853414U (en) | Exhaust steam heat recovery unit | |
| CN106277142B (en) | A kind of depth energy saving type desalination plant | |
| KR101323160B1 (en) | Marine vertical multistage desalinator | |
| CN105692744B (en) | A kind of medical multi-effect water distillator | |
| CN102232791A (en) | Distillation type drinking water device | |
| CN104096370B (en) | Multistage evaporating column used for carrying out evaporation process to salt-containing water through air | |
| CN206121195U (en) | Many materials multiple effect evaporation device | |
| CN101274784A (en) | Steam-water four-stage separating five-effect water distillator | |
| CN104150548B (en) | A kind of seawater desalination system | |
| CN212566627U (en) | A bipyramid desiccator toper jar body for preparing olmesartan medoxomil | |
| CN201145260Y (en) | Exhaust-heat boiler and steam drum thereof | |
| CN210728701U (en) | Take mechanical type vapor compression's triple-effect evaporator | |
| CN202576017U (en) | Water distiller | |
| CN100595484C (en) | Waste-heat boiler and steam drum thereof | |
| CN207865347U (en) | A kind of circulating and evaporating formula steam oven | |
| KR101567655B1 (en) | TVC-MED having Non-condensible Gas Venting System | |
| CN214620181U (en) | Evaporator with two ends passing in and out |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |