CN207537175U - A kind of salting liquid desalter - Google Patents
A kind of salting liquid desalter Download PDFInfo
- Publication number
- CN207537175U CN207537175U CN201721397636.XU CN201721397636U CN207537175U CN 207537175 U CN207537175 U CN 207537175U CN 201721397636 U CN201721397636 U CN 201721397636U CN 207537175 U CN207537175 U CN 207537175U
- Authority
- CN
- China
- Prior art keywords
- salting liquid
- bullet
- niti
- hot
- memorial alloy
- 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
-
- 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
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
A kind of salting liquid desalter, including salting liquid heating evaporation room, its both ends entrance and exit bottom connects feed reservoir by dilute salting liquid entrance with dense saline solution outlet section respectively, outlet top in salting liquid heating evaporation room connects steam by jet chimney and condenses chamber inlet, and the outlet of steam condensation chamber passes through product water outlet product water collecting chamber；Further include the hot memorial alloy of NiTi bullet for being arranged on and being moved back and forth between salting liquid heating evaporation room and steam condensation chamber, the hot memorial alloy connection linear motor of NiTi bullet；Salting liquid heating evaporation room, steam condensation chamber and the hot memorial alloy of NiTi bullet and horizontal plane are into identical default angle；By loading and unloading of the linear motor to the hot memorial alloy of NiTi bullet, it is made, which to heat salting liquid when being contacted with vaporization chamber, makes its evaporation, and condensed steam is to realize desalination when being contacted with condensation chamber；The utility model does heat source using memorial alloy, and input energy is small, simple in structure, easily operated, good portability, the equipment that can quickly realize desalination.
Description
Technical field
The utility model is related to the technical fields to inorganic salt solution (hereinafter referred to as salting liquid) desalination, and in particular to one
Kind use and to load the method for memorial alloy to heat salting liquid and condensed steam to realize the equipment of desalination.
Background technology
There is extensive commercial Application to salting liquid desalination.Such as the essence of sea water desalination is exactly that NaCl aqueous solutions are implemented
Fresh water is obtained after desalination；In fields such as bittern water, the dirty water decontamination handles, Treated sewage reusings, mother liquor after pretreatment also can by regarding
For the aqueous solution of inorganic salts, also it is purification to its desalination, recycles the key link of water resource.In short, the desalting technology of salting liquid
It is that water is purified in production and living, improve water utilization rate and reduces the Key Common Technologies of pollutant emission.
In the industrial production, there is two class mode of embrane method and Re Fa to salting liquid desalination.Wherein embrane method mainly utilizes reverse osmosis
Saturating principle makes high pressure salting liquid pass through appropriate permeable membrane, is filtered to remove inorganic ion and realizes desalination.The main of this method lacks
Fall into is that permeable membrane has ion selectivity and need to regularly clean or replace.It is carried in addition, the operation of system also needs to power-equipment
For high pressure.Hot method is primarily referred to as detaching salt, water by evaporation.Generally use multi-effect distilling or multistage evaporation method.This method
Major defect is that enough external heat source heating salting liquids is needed to make its evaporation.In system operation, operating pressure lowers step by step, needs
Corresponding vacuum system is wanted, causes its complicated, bulky, operation and maintenance difficulty is big.
In short, embrane method and Re Fa are required to external input mass energy, system bulky complex is suitable for the life of scale
Production.And lack extra power on desert, island etc. or in occasions such as emergent, rescues, need a kind of input energy few, simple, just
It takes, the equipment that can quickly realize desalination.
Invention content
In order to solve the above-mentioned problems of the prior art, the purpose of this utility model is to provide a kind of salting liquid desalination and sets
It is standby, memorial alloy is loaded, while realize the heating of brine and the condensation of steam by a small amount of energy of external input, it is achieved thereby that
Crude salt water desalination；The equipment input energy is few, simple in structure, easy to carry, easily operated and at low cost；This novel salting liquid
Separation equipment realizes energy-saving and emission-reduction, environmental protection and the purpose increased economic efficiency.
In order to achieve the above object, technical solution is used by the utility model：
A kind of salting liquid desalter, including salting liquid heating evaporation room 2,2 liang of salting liquid heating evaporation room end entrance and
Outlet bottom connects feed reservoir 10, salting liquid heating evaporation room with dense saline solution outlet section 3 by dilute salting liquid entrance 1 respectively
2 outlets top connect 5 entrance of steam condensation chamber by jet chimney 4, and the outlet of steam condensation chamber 5 is connected by product water out 6
Product water collecting chamber 8,10 top setting charge door 9 of feed reservoir；It further includes and is arranged on salting liquid heating evaporation room 2 and steam condensation
The hot memorial alloy 7 of NiTi bullet moved back and forth between room 5, hot 7 one end of memorial alloy of NiTi bullet are brace and connecting rod framework, and the other end connects
Linear motor 11 is connect, drawing the hot memorial alloy 7 of NiTi bullet by linear motor 11 fits closely with evaporator section or condensation segment with heat release
Or heat absorption；
The salting liquid heating evaporation room 2, steam condensation chamber 5 and the hot memorial alloy 7 of NiTi bullet and horizontal plane are into identical
Default angle.
Be provided with water sealing cover on the salting liquid of the salting liquid heating evaporation room 2, avoid generate steam from salting liquid into
Outlet dissipation.
The salting liquid heating evaporation room 2, steam condensation chamber 5 and the hot memorial alloy 7 of NiTi bullet are pressed from both sides with horizontal plane into 10 °
Angle.
1 angle with horizontal plane of dilute salting liquid entrance is 75 °, and 3 angle with horizontal plane of dense saline solution outlet section is
15°。
The hot memorial alloy 7 of NiTi bullet and salting liquid heating evaporation room 2 and the binding face size one of steam condensation chamber 5
It causes.
Compared to the prior art, the utility model has the following advantages：
The utility model heating method used is the hot memorial alloy phase-change heat transfer of NiTi bullet.Ultimum Ti martensite
Bullet fuel factor in phase transition process is up to more than 20K, the corresponding latent heat more than 12J/g.Refrigerating machine is played at present can reach 14%
Thermodynamic perfect degree.When the hot memorial alloy of NiTi bullet is by compression or stretching, memorial alloy is become from austenite (Austenite)
Martensite (Martensite) generates phase transformation, releases latent heat.After unloading, martensite reverts to austenite, absorbs heat.Due to
Metal thermal resistance is small, and heat transfer is fast, and heat transfer efficiency is high.It is compared with existing salting liquid desalting technology, this system input energy is few, structure letter
It is single, it is easily operated, it is easy to carry.
Description of the drawings
Fig. 1 is the structure diagram of the utility model salting liquid desalter.
Specific embodiment
The utility model is described in further detail with reference to the accompanying drawings and detailed description.
As shown in Figure 1, the utility model is a kind of salting liquid desalter, including the dilute salting liquid entrance being sequentially communicated
1, salting liquid heating evaporation room 2, dense saline solution outlet section 3, jet chimney 4, steam condensation chamber 5, condensation segment outlet 6, NiTi bullet
Hot memorial alloy 7, product water collecting chamber 8, feed reservoir 10, charge door 9 and linear motor 11.
As shown in Figure 1, the salting liquid heating evaporation room 2, steam exothermic condensation room 5 and the hot memorial alloy 7 of NiTi bullet are all
It is to be in tilted layout, it is 10 ° to tilt the number of degrees.Vaporization chamber 2 and condensation chamber 5 are under atmospheric pressure, ignore container thickness, only consider wall surface
With the heat transfer resistance of water.
As shown in Figure 1, hot 7 mass of memorial alloy of NiTi bullet is 10-20kg, the primary thermal discharge of every gram of alloy tensile is
12J.Its left end is brace and connecting rod framework, and right end is linear motor.When motor loads alloy, on the hot memorial alloy 7 of NiTi bullet
It moves and is bonded with salting liquid heating evaporation room 2, the hot memorial alloy 7 of NiTi bullet releases heat for heating salting liquid；When motor pair
After it is unloaded, the hot memorial alloy 7 of NiTi bullet is moved down to be bonded with steam condensation chamber 5, and the hot memorial alloy 7 of NiTi bullet absorbs steam condensation
The heat of releasing.
As the preferred embodiment of the utility model, the hot memorial alloy 7 of NiTi bullet and salting liquid heating evaporation room 2 and steaming
The binding face size of vapour condensation chamber 5 is consistent.
As the preferred embodiment of the utility model, as shown in fig. 1, the water surface passes in and out its salting liquid in design level face
Mouth has carried out fluid-tight, and the steam generated is avoided to be imported and exported from salting liquid and is dissipated.
As shown in Figure 1, the operation principle of the utility model is：Dilute salting liquid enters salting liquid from dilute salting liquid entrance 1
Heating evaporation section 2, NiTi bullet hot memorial alloy 7 load heat release when being contacted with salting liquid vaporization chamber 2, salting liquid endothermic gasification generates
Vapor.Salting liquid inlet and outlet are connected with feed reservoir 10, and salting liquid outlet is high-temp liquid, and so connection can be recycled effectively useless
Heat.The water vapour of generation is spontaneous into steam condensation chamber 5 from jet chimney 4 due to expansion.When the hot memorial alloy 7 of NiTi bullet is with steaming
Vapour condensation chamber 5 unloads when contacting, and absorbs the heat that vapor condensation is released.Product water flows into product water from product water out 6 and receives
Collect room 8.
Claims (5)
1. a kind of salting liquid desalter, it is characterised in that：Including salting liquid heating evaporation room (2), salting liquid heating evaporation room
(2) entrance and exit bottom in both ends connects feed reservoir by dilute salting liquid entrance (1) with dense saline solution outlet section (3) respectively
(10), salting liquid heating evaporation room (2) outlet top connects steam condensation chamber (5) entrance, steam condensation by jet chimney (4)
Room (5) outlet connects product water collecting chamber (8) by product water out (6), and charge door (9) is set at the top of feed reservoir (10)；Also
Including being arranged on the hot memorial alloy of NiTi bullet (7) moved back and forth between salting liquid heating evaporation room (2) and steam condensation chamber (5),
The hot memorial alloy of NiTi bullet (7) one end is brace and connecting rod framework, and other end connection linear motor (11) is led by linear motor (11)
Draw the hot memorial alloy of NiTi bullet (7) to fit closely with heat release or heat absorption with evaporator section or condensation segment；
The salting liquid heating evaporation room (2), steam condensation chamber (5) and the hot memorial alloy of NiTi bullet (7) and horizontal plane are into identical
Default angle.
2. a kind of salting liquid desalter according to claim 1, it is characterised in that：The salting liquid heating evaporation room
(2) water sealing cover is provided on salting liquid, the steam generated is avoided to be imported and exported from salting liquid and is dissipated.
3. a kind of salting liquid desalter according to claim 1, it is characterised in that：The salting liquid heating evaporation room
(2), steam condensation chamber (5) and the hot memorial alloy of NiTi bullet (7) and horizontal plane are into 10 ° of angles.
4. a kind of salting liquid desalter according to claim 1, it is characterised in that：The dilute salting liquid entrance (1)
Angle with horizontal plane is 75 °, and dense saline solution outlet section (3) angle with horizontal plane is 15 °.
5. a kind of salting liquid desalter according to claim 1, it is characterised in that：The hot memorial alloy of NiTi bullet
(7) it is consistent with the binding face size of salting liquid heating evaporation room (2) and steam condensation chamber (5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721397636.XU CN207537175U (en) | 2017-10-25 | 2017-10-25 | A kind of salting liquid desalter |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721397636.XU CN207537175U (en) | 2017-10-25 | 2017-10-25 | A kind of salting liquid desalter |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207537175U true CN207537175U (en) | 2018-06-26 |
Family
ID=62611380
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721397636.XU Active CN207537175U (en) | 2017-10-25 | 2017-10-25 | A kind of salting liquid desalter |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207537175U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109970123A (en) * | 2019-02-21 | 2019-07-05 | 林明星 | A kind of processing unit of saline sewage |
| CN110925834A (en) * | 2019-11-28 | 2020-03-27 | 海信(广东)厨卫系统有限公司 | Fume exhaust fan |
| CN114132981A (en) * | 2021-12-14 | 2022-03-04 | 西安交通大学 | Desalination system and method based on solar light splitting-radiation cooling |
-
2017
- 2017-10-25 CN CN201721397636.XU patent/CN207537175U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109970123A (en) * | 2019-02-21 | 2019-07-05 | 林明星 | A kind of processing unit of saline sewage |
| CN109970123B (en) * | 2019-02-21 | 2021-07-23 | 山东格瑞水务有限公司 | Processing apparatus who contains salt sewage |
| CN110925834A (en) * | 2019-11-28 | 2020-03-27 | 海信(广东)厨卫系统有限公司 | Fume exhaust fan |
| CN114132981A (en) * | 2021-12-14 | 2022-03-04 | 西安交通大学 | Desalination system and method based on solar light splitting-radiation cooling |
| CN114132981B (en) * | 2021-12-14 | 2023-01-06 | 西安交通大学 | Desalination system and method based on solar light splitting-radiation cooling |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US8252092B2 (en) | Water separation under varied pressure | |
| CN103387308B (en) | Multi-effect membrane distillation-multistage flash evaporation seawater desalination system | |
| CN207537175U (en) | A kind of salting liquid desalter | |
| US20200198991A1 (en) | Systems and methods for recovery of purified water and concentrated brine | |
| US10752523B2 (en) | Systems and methods for recovery of purified water and concentrated brine | |
| CN201384862Y (en) | Indirect vapor recompression evaporation system | |
| JP2009539584A (en) | Multistage column distillation (MSCD) method for recovering osmotic solutes | |
| JP2009539584A6 (en) | Multistage column distillation (MSCD) method for recovering osmotic solutes | |
| WO2016041292A1 (en) | Fluid-gap multi-effect membrane distillation process and device thereof | |
| CN103663590B (en) | A kind of vacuum membrane distillation waste disposal plant that can reclaim heat | |
| WO2011085669A1 (en) | Low-temperature heat-driven distillation separation apparatus for evaporating aqueous solution under negative pressure and method for obtaining distilled water | |
| CN108246106A (en) | Vacuum type multi-effect membrane distillation system | |
| JPWO2014196610A1 (en) | Seawater desalination apparatus and seawater desalination method | |
| Si et al. | Performance analysis of treating sulfuric acid solution by the combined system of vacuum membrane distillation and mechanical vapor recompression | |
| CN103550941A (en) | Low-temperature evaporation and concentration device and high-concentration waste water concentration method | |
| CN106512450B (en) | Minimize energy-saving evaporation regenerating unit | |
| CN201834781U (en) | Single-stage vacuum distillation seawater desalination device | |
| CN203007081U (en) | Low-temperature multi-effect distillation desalination system | |
| JP2015020163A (en) | Nanofiber membrane distillation apparatus | |
| Lin et al. | Design and experimental analysis of a vapor compression heat pump combined with double‐stage forced‐circulation evaporators | |
| CN203754456U (en) | Nitrogen circulation type low-temperature evaporation concentration device | |
| CN203525336U (en) | Low-temperature evaporation and concentration device | |
| Hassan et al. | Integration of vacuum multi effect membrane distillation with adsorption/cooling system | |
| CN204778912U (en) | Concentrated processing system of evaporation formula liquid | |
| CN206631440U (en) | A kind of Tianna solution dewatering system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |