CN1583582A - Desalting apparatus and process for seawater or brackish water by moistening-drying - Google Patents
Desalting apparatus and process for seawater or brackish water by moistening-drying Download PDFInfo
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- CN1583582A CN1583582A CNA2004100194465A CN200410019446A CN1583582A CN 1583582 A CN1583582 A CN 1583582A CN A2004100194465 A CNA2004100194465 A CN A2004100194465A CN 200410019446 A CN200410019446 A CN 200410019446A CN 1583582 A CN1583582 A CN 1583582A
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- heat transfer
- seawater
- transfer tube
- tube
- brackish water
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- 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
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Abstract
A moistening-demoistening apparatus for desalinating seawater or bitter saline is composed of a main body which is a vertical heat exchanger consisting of heat eaxchanging tube and casing, an auxiliary heating connection tube on its top closure head, a boffling barrier between said heat exchanger and casing, and a lower closure head with carrier gas inlet and concentrated saline outlet. Its desalinating process features that the seawater or bitter saline flows downward while the carrier gas flows upward and is continuously moistened, and the carrier gas is then cooled and demoistened to obtain fresh water.
Description
Technical field
The present invention relates to a kind of humidifying-dehumidifying desalination apparatus and process, belong to seawater or technique of desalinating saline water.
Background technology
Common humidifying-dehumidifying desalinating process is development and come on the basis of solar still, it separates evaporation equipment with condensing equipment, control temperature separately with salt solution humidification air, makes the wet air condensation dry in condensing equipment and obtains fresh water in evaporation equipment respectively.This process can be implemented by the evaporation equipment and the condensing equipment of various different types.Adopting the evaporation equipment of a kind of paper staggered form paper honeycomb structure or porous ceramic structure as ZL98232617.3 is core component, has formed a cover humidifying-dehumidifying desalination system with another one condensing equipment and other utility appliance.
Yet in these common humidifying-dehumidifying desalination systems, evaporation humidification process and the condensation process of drying are finished in two isolating equipment respectively, and this makes whole desalination system more complicated, invests also corresponding bigger.And, because the evaporation humidification process need consume a large amount of latent heats of vaporization, in an isolating evaporation equipment, these latent heats of vaporization can only be provided by the sensible heat of charging seawater or brackish water, this just supplies with from energy and has limited the brinish evaporating capacity, and then has restricted fresh water yield; Meanwhile, in condensing equipment, a large amount of condensation latent heat then are wasted, or only use inefficient big different transfer of heat mode preheated feed make up water, and this has also restricted the raising of process thermo-efficiency.
Humidifying-dehumidifying desalination process is the process of operating below boiling point, and therefore selecting some macromolecular materials cheap and easy to get for use is one of effective way that reduces apparatus cost as heat exchange element.Form pressure strip frame heat exchange structure by human multi-layer planar polyester macromolecule film, but consider for heat exchange efficiency, polymeric membrane can only adopt very thin thickness, for avoiding its film applying that causes adjacent layers in lax distortion of when operation of being heated together, must keep enough distances between the adjacent layers, this makes the effective heat transfer area of entire equipment in unit volume reduce greatly.Another shortcoming of flat sheet membranes structural shape is the sealing difficulty of entire equipment, and is difficult to carry out effectively heat conduction reinforced.
Summary of the invention
The object of the present invention is to provide the humidifying-dehumidifying desalination apparatus of a kind of seawater or brackish water.This appliance arrangement is simple, compact construction, easy, the less investment of process operation.
The present invention is realized by following technical scheme.The humidifying-dehumidifying desalination apparatus that is used for seawater or brackish water, this device comprises interchanger and air water separator, it is characterized in that: interchanger constitutes the vertical shell-and-tube structure by heat transfer tube 1 and housing 2; The upper end of housing is provided with end socket 4, and its top and housing top are provided with communicating pipe 7, offer boosting mouth 6 on this pipe, and the heat exchange pipe end in this end socket stretches out and is higher than tube sheet, and offers aperture or pipe end is offered breach on its tube wall; The gap is provided with baffle plate 9 between heat transfer tube and housing; The lower end of housing is provided with lower cover 11, which is provided with carrier gas inlet 14 and strong brine outlet 13.
At least 2 of the intravital heat transfer tubes of above-mentioned shell, the material of heat transfer tube are polypropylene, polyethylene, polyester, polystyrene, polycarbonate, tetrafluoroethylene or polymeric amide; Or the titanium of metal, copper, aluminium, titanium alloy, copper alloy or aluminium alloy; The heat transfer tube internal diameter is 1～15mm, and wall thickness is 0.05～0.5mm, and length is 1～5m.
Adopt above-mentioned device, realize the humidifying-dehumidifying desalination process of seawater or brackish water: seawater or brackish water flow from top to bottom along the heat transfer tube inwall, air, nitrogen or carbonic acid gas gas carrier are introduced by the heat transfer tube lower end, flow from bottom to top, gas two-phase at night constantly contacts, carrier gas is constantly by humidification, enter shell side then, through cooling dehumidification, gas-liquid mixture flow to hull outside and obtain fresh water after gas-liquid separation, it is characterized in that: the temperature of charging seawater or brackish water is 50～95 ℃, and brinish falling liquid film load (quality of the feed brine that flows through in the unit time on the unit length wetted perimeter) is 0.0001～0.01kgm in the heat transfer tube
-2s
-1The operation vapour-liquid ratio ratio of the mass rate of feed water (dry air in the carrier gas with) is 0.1～2, steam-to-gas ratio (adding the ratio of the pure steam mass flow of heat reduced and the mass rate of dry air) is 0～0.2, and the output of the condensation fresh water on the unit heat transfer area is 0.05～3.0kgm
-2h
-1
Carrier gas desalinating process provided by the present invention, compared with prior art, its major advantage is device thermo-efficiency height, the output of unit heat transfer area is big, atmospheric operation, unit scale is flexible, invests for a short time, simple to operate, utilizes Lowlevel thermal energy such as sun power convenient etc.
Description of drawings
Fig. 1 is the synoptic diagram of apparatus of the present invention structure.
Among the figure:
The 1-heat transfer tube; The 2-housing; The import of 3-hot salt brine; The 4-upper cover; The outlet of 5-humid gas; 6-boosting mouth; 7-communicating pipe; The import of 8-condensed gas; The 9-baffle plate; 10-condensed gas and water outlet; The 11-air water separator; The 12-lower cover; The outlet of 13-strong brine; The 14-carrier gas inlet.
Embodiment
Adopt the desalting equipment of tube shell type structure as shown in Figure 1, this device is vertically placed during operation.Wherein evaporate humidification process and finish at the tube side of interchanger, the condensation process of drying is finished at the shell side of interchanger.Charging seawater or brackish water through preheating are introduced in the upper cover 4 from hot salt brine import 3, by overflow, perhaps by the liquid distribution device of particular design, seawater or brackish water uniform distribution are entered in the pipe, and flow along the inside pipe wall falling liquid film by action of gravity.Generally between 50～95 ℃, flow is then looked the different and different of equipment heat transfer tube number and diameter to the temperature of feed water, and the falling liquid film load is at 0.0001～0.01kgm usually
-2s
-1Between, with 0.0008～0.008kgm
-2s
-1For good.Carrier gas is introduced tube side by the carrier gas inlet 14 of blower fan on lower cover 12, and its suitable flow is operated vapour-liquid ratio between 0.1～2 usually with the feed water fluctuations in discharge.Carrier gas is flowed in pipe from bottom to top, with the salt solution counter current contact that covers tube wall, makes that the water vapor of salt solution near surface is constantly taken away, the water vapor that a part of salt solution is also constantly vaporized and taken away to replenish in liquid-vaqor interface.And also constantly absorbed by salt solution from the heat that shell side passes over, to replenish the latent heat that evaporation consumes.The process of the continuous vaporization of salt solution here also is that carrier gas is constantly by the process of humidification.Strong brine after the part evaporation flows out from the pipe lower end, compiles the back by directly discharging or recycle of strong brine outlet 13 at lower cover.Carrier gas in pipe by humidification after, the mixed gas that obtains leaves from pipe upper end, upper cover compile the back by humid gas outlet 5 by communicating pipe 7 introducing shell side.Enter the mixed gas constantly cooling from top to bottom of shell side, the most of water vapour that wherein carries then is condensed into fresh water, and condensation latent heat then is delivered to the process that is evaporated in the pipe by tube wall and utilizes.At last, carrier gas and condensation fresh water leave from exporting 10, collect condensation fresh water via air water separator 11 backs, and carrier gas is then directly discharged or recycle.
In order to set up the heat transfer temperature difference between shell side and the tube side, can enter at the mixed gas that the tube side humidification obtains before the shell side condensation, its temperature is improved a little.This can a certain amount ofly add pure steam and realize by being introduced by boosting mouth 6, also an intermediate receptacle can be set on communicating pipe 7, and the form by heat exchange realizes.The increase rate of this temperature is generally below 5 ℃, and the operation steam-to-gas ratio is 0～0.2.
This humidifying-dehumidifying desalination apparatus provided by the present invention and gas-liquid operator scheme, by heat passage condensation process and evaporative process are coupled together, effectively the shell side condensation latent heat is delivered to tube side, for evaporation salt solution provides the latent heat of vaporization, both strengthened humidification process, improve fresh water yield, also made the more common humidifying-dehumidifying technology of efficiency of utilization of process improve greatly.
Below be one embodiment of the present of invention.The heat-exchanging tube bundle of interchanger is made up of 73 copper tubes, and the pipe specification is: external diameter 6mm, wall thickness 0.25mm, long 2400mm.Copper tube is arranged by the equilateral triangle mode, and effective heat exchange area is 2.75m
2Housing internal diameter 78mm, external diameter 90mm, material is a polypropylene.Shell side evenly is provided with 40 baffles.Fresh water yield data under the different operating condition are as shown in the table:
Table one, different operating condition are downloaded the water of condensation output of qi exhaustion salt process
| Carrier gas flux brine flow salt solution inlet temperature add steam flow water of condensation output (kg/h) (kg/h) (℃) (kg/h) (kg/h) |
| ????3.56???????7.82??????87.0????????????0.10?????????1.188 ????7.12???????11.73?????80.7????????????0.15?????????1.358 ????9.49???????11.73?????81.5????????????0.15?????????1.789 |
As seen, use less heat transfer area and very a spot of steam that adds, the output of small-sized desalting plant can reach 0.6kg/m
2More than the h, and this index majority of prior art is at 0.2kg/m
2Below the h.
Claims (3)
1. the humidifying-dehumidifying desalination apparatus of seawater or brackish water, this device comprises interchanger and air water separator, it is characterized in that: interchanger constitutes the vertical shell-and-tube structure by heat transfer tube (1) and housing (2); The upper end of housing is provided with end socket (4), and its top and housing top are provided with communicating pipe (7), and this pipe is offered the boosting mouth
(6), the heat exchange pipe end in this end socket stretches out and is higher than tube sheet, and offers aperture or pipe end is offered breach on its tube wall; The gap is provided with baffle plate (9) between heat transfer tube and housing; The lower end of housing is provided with lower cover
(12), which is provided with carrier gas inlet (14) and strong brine outlet (13).
2. the humidifying-dehumidifying desalination apparatus of seawater according to claim 1 or brackish water, it is characterized in that: at least 2 of the intravital heat transfer tubes of shell, the material of heat transfer tube are polypropylene, polyethylene, polyester, polystyrene, polycarbonate, tetrafluoroethylene or polymeric amide; Or the titanium of metal, copper, aluminium, titanium alloy, copper alloy or aluminium alloy; The heat transfer tube internal diameter is 1～15mm, and wall thickness is 0.05～0.Smm, and length is 1～5m.
3. one kind is adopted the described device of claim 1, realize the humidifying-dehumidifying desalination process of seawater or brackish water: seawater or brackish water flow from top to bottom along the heat transfer tube inwall, carrier gas is introduced by the heat transfer tube lower end, flow also from bottom to top constantly by humidification, enter shell side afterwards and obtain fresh water through cooling dehumidification, be characterised in that: the temperature of charging seawater or brackish water is 50～95 ℃, and brinish falling liquid film load is 0.0001～0.01kg m in the heat transfer tube
-2s
-1, the operation vapour-liquid ratio is 0.1～2, and steam-to-gas ratio is 0～0.2, and the condensation fresh water yield on the unit heat transfer area is 0.05～3.0kg m
-2h
-1
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100194465A CN1255325C (en) | 2004-05-28 | 2004-05-28 | Desalting apparatus and process for seawater or brackish water by moistening-drying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2004100194465A CN1255325C (en) | 2004-05-28 | 2004-05-28 | Desalting apparatus and process for seawater or brackish water by moistening-drying |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1583582A true CN1583582A (en) | 2005-02-23 |
| CN1255325C CN1255325C (en) | 2006-05-10 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2004100194465A Expired - Fee Related CN1255325C (en) | 2004-05-28 | 2004-05-28 | Desalting apparatus and process for seawater or brackish water by moistening-drying |
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| CN (1) | CN1255325C (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100341792C (en) * | 2006-05-17 | 2007-10-10 | 天津大学 | Polymer material small-sized humidifying-dehumidifying desalination apparatus and manufacturing method |
| CN102422111A (en) * | 2009-04-29 | 2012-04-18 | 巴斯夫欧洲公司 | Shell and tube heat exchanger and method for removing volatile substances from a polymer solution |
| CN102757102A (en) * | 2011-04-28 | 2012-10-31 | 中国科学院理化技术研究所 | Method and device for desalting seawater or brackish water |
| CN103332758A (en) * | 2013-06-13 | 2013-10-02 | 山东开元电子有限公司 | Solar seawater desalination heating device |
| CN104114250A (en) * | 2012-04-25 | 2014-10-22 | 盐场科技有限公司 | Modular humidification-dehumidification apparatus for concentrating solutions |
| CN104495966A (en) * | 2014-12-17 | 2015-04-08 | 西北工业大学 | Bubble humidification and heat pump cycle coupled sea water desalination system and process method |
-
2004
- 2004-05-28 CN CNB2004100194465A patent/CN1255325C/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100341792C (en) * | 2006-05-17 | 2007-10-10 | 天津大学 | Polymer material small-sized humidifying-dehumidifying desalination apparatus and manufacturing method |
| CN102422111A (en) * | 2009-04-29 | 2012-04-18 | 巴斯夫欧洲公司 | Shell and tube heat exchanger and method for removing volatile substances from a polymer solution |
| CN102422111B (en) * | 2009-04-29 | 2013-07-10 | 斯蒂罗卢辛有限公司 | Shell and tube heat exchanger and method for removing volatile substances from a polymer solution |
| CN102757102A (en) * | 2011-04-28 | 2012-10-31 | 中国科学院理化技术研究所 | Method and device for desalting seawater or brackish water |
| CN104114250A (en) * | 2012-04-25 | 2014-10-22 | 盐场科技有限公司 | Modular humidification-dehumidification apparatus for concentrating solutions |
| US9259667B2 (en) | 2012-04-25 | 2016-02-16 | Saltworks Technologies Inc. | Modular humidification-dehumidification apparatus for concentrating solutions |
| CN104114250B (en) * | 2012-04-25 | 2016-08-24 | 苏特沃克技术有限公司 | For concentrating the modularization humidifying-dehumidifying device of solution |
| CN103332758A (en) * | 2013-06-13 | 2013-10-02 | 山东开元电子有限公司 | Solar seawater desalination heating device |
| CN103332758B (en) * | 2013-06-13 | 2014-06-11 | 山东开元电子有限公司 | Solar seawater desalination heating device |
| CN104495966A (en) * | 2014-12-17 | 2015-04-08 | 西北工业大学 | Bubble humidification and heat pump cycle coupled sea water desalination system and process method |
| CN104495966B (en) * | 2014-12-17 | 2016-04-13 | 西北工业大学 | The seawater desalination system that a kind of bubbling humidification is coupled with heat pump cycle and processing method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1255325C (en) | 2006-05-10 |
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