CN206318730U - Portable Membrane Materials method seawater desalination system - Google Patents
Portable Membrane Materials method seawater desalination system Download PDFInfo
- Publication number
- CN206318730U CN206318730U CN201621401538.4U CN201621401538U CN206318730U CN 206318730 U CN206318730 U CN 206318730U CN 201621401538 U CN201621401538 U CN 201621401538U CN 206318730 U CN206318730 U CN 206318730U
- Authority
- CN
- China
- Prior art keywords
- seawater desalination
- desalination system
- materials method
- membrane module
- membrane materials
- 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
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses a kind of portable Membrane Materials method seawater desalination system, belong to field of sea water desalting technology.The system includes the equipment outer container being arranged on lorry, constant temperature water bath apparatus is provided with equipment outer container, constant temperature water bath apparatus connects fluid flowmeter by magnetic drive pump, fluid flowmeter connects membrane module, supply channel between the fluid flowmeter and membrane module is provided with pressure gauge and thermometer, membrane module connects water return pipeline and steam pipework, the water return pipeline is provided with pressure gauge, the steam pipework is provided with condenser pipe, condenser pipe connects vavuum pump, passes through condensate line connection production tank between the condenser pipe and vavuum pump.This seawater desalination system is equipped on lorry, mobility strong, simple to operate, easy to use, and fading effect is good, efficiency high.
Description
Technical field
The utility model is related to a kind of portable sea water desalting equipment, belongs to field of sea water desalting technology.
Background technology
In recent years, being continuously increased with population, fresh water demand increases year by year, and tellurian freshwater resources account for total Water
Less than 3%, account for total Water the 2.53% of land fresh water, water resource is seriously in short supply；And tellurian seawater resources are abundant, utilize
Seawater carries out desalt processing, and a new way of solution water scarcity is turned into for people to use.Current desalinization is set
Standby bulky, complex structure, it is strongly professional, it is necessary to carry out desalt processing in special desalt processing region in professional,
Cost is higher, and can not meet the requirement of the progress desalinization processing of maneuverability.
Utility model content
To solve the defect that prior art is present, the purpose of this utility model is to provide a kind of simple in construction, treatment effect
It is good, the portable Membrane Materials method seawater desalination system of maneuverability.
The technical solution of the utility model is：Portable Membrane Materials method seawater desalination system, including be arranged on lorry
Constant temperature water bath apparatus is provided with equipment outer container, equipment outer container, constant temperature water bath apparatus connects fluid flowmeter, liquid by magnetic drive pump
Flowmeter connects membrane module, and the supply channel between the fluid flowmeter and membrane module is provided with pressure gauge and thermometer, film
Component connects water return pipeline and steam pipework, and the water return pipeline is provided with pressure gauge, and the steam pipework is provided with condenser pipe,
Condenser pipe connects vavuum pump, passes through condensate line connection production tank between the condenser pipe and vavuum pump.
The water return pipeline is provided with thermometer.
The water return pipeline outlet connects constant temperature water bath apparatus and floss hole by valve respectively.
The membrane module is hollow fiber film assembly.
The hollow fiber film assembly includes dewatering microporous film.
The membrane module is provided with least two steam (vapor) outlets, and the steam (vapor) outlet connects steam pipework.
The beneficial effects of the utility model are：This seawater desalination system is equipped on lorry, mobility strong, simple to operate,
Easy to use, fading effect is good, efficiency high.
Brief description of the drawings
The utility model has the width of accompanying drawing 1.
Fig. 1 is the utility model schematic diagram.
Reference is as follows in figure：1st, constant temperature water bath apparatus, 2, magnetic drive pump, 3, fluid flowmeter, 4.1, pressure gauge, 4.2,
Pressure gauge, 5.1, thermometer, 5.2, thermometer, 6, membrane module, 7, condenser pipe, 8, production tank, 9, vavuum pump, 10, floss hole,
11st, equipment outer container.
Embodiment
1 pair of the utility model is described further below in conjunction with the accompanying drawings：
In portable Membrane Materials method seawater desalination system, including the equipment outer container 11 being arranged on lorry, equipment outer container 11
Provided with constant temperature water bath apparatus 1, constant temperature water bath apparatus 1 connects fluid flowmeter 3, the junctional membrane group of fluid flowmeter 3 by magnetic drive pump 2
Part 6, the supply channel between the fluid flowmeter 3 and membrane module 6 is provided with pressure gauge 4.1 and thermometer 5.1, membrane module 6
Water return pipeline and steam pipework are connected, the water return pipeline is provided with pressure gauge 4.2, and the steam pipework is provided with condenser pipe 7,
Condenser pipe 7 connects vavuum pump 9, passes through condensate line connection production tank 8 between the condenser pipe 7 and vavuum pump 9.
The water return pipeline is provided with thermometer 5.2.
The water return pipeline outlet connects constant temperature water bath apparatus 1 and floss hole 10 by valve respectively.
The membrane module 6 is hollow fiber film assembly.
The hollow fiber film assembly includes dewatering microporous film.
The membrane module 6 is provided with least two steam (vapor) outlets, and the steam (vapor) outlet connects steam pipework.
The vavuum pump 9 is circulating water type vavuum pump.
Vehicular Membrane Materials method seawater desalination system is integrally placed on motor van, is broadly divided into membrane module part and distillation
Part.Membrane Materials are the membrane separating process that membrane technology is combined with still-process, and it is using dewatering microporous film as medium, in film both sides
In the presence of steam pressure difference, volatile component passes through the fenestra of hollow fiber film assembly in vapour form in feed liquid (seawater), from
And realize the purpose of separation.Membrane Materials subtraction unit is divided into two loops of hot side and cold side.Hot side loop is by constant temperature water bath apparatus
1st, magnetic drive pump 2, fluid flowmeter 3, pressure gauge, thermometer composition；Cold-side loop is then provided in circulating water type vavuum pump
Under vacuum, the fenestra of vapour transmission hollow-fibre membrane enters production tank after condensed pipework condensation.
Feed liquid (seawater) is heated to after predetermined temperature in water bath with thermostatic control, is opened hot and cold side circulating pump, vavuum pump, is passed through
Flowmeter regulation fluid flow (flow velocity) arrives predetermined value.After the temperature of the import and export of membrane module both sides is all stablized, just it can beat
Production water valve is driven to start to collect production water.Whole device is fixed on mobile motor van, is used with that need to move.
The above is only preferred embodiment of the present utility model, it is noted that for the common skill of the art
For art personnel, on the premise of the utility model know-why is not departed from, some improvement and modification can also be made, these change
Enter and protection domain of the present utility model is also should be regarded as with modification.
Claims (7)
1. a kind of portable Membrane Materials method seawater desalination system, it is characterised in that including the equipment outer container being arranged on lorry
(11) constant temperature water bath apparatus (1), is provided with equipment outer container (11), constant temperature water bath apparatus (1) connects liquid flow by magnetic drive pump (2)
Gauge (3), fluid flowmeter (3) connection membrane module (6), the supply channel between the fluid flowmeter (3) and membrane module (6)
It is provided with pressure gauge (4.1) and thermometer (5.1), membrane module (6) connection water return pipeline and steam pipework, the water return pipeline
Provided with pressure gauge (4.2), the steam pipework is provided with condenser pipe (7), condenser pipe (7) connection vavuum pump (9), the condenser pipe
(7) production tank (8) is connected by condensate line between vavuum pump (9).
2. portable Membrane Materials method seawater desalination system according to claim 1, it is characterised in that on the water return pipeline
Provided with thermometer (5.2).
3. portable Membrane Materials method seawater desalination system according to claim 1, it is characterised in that the water return pipeline goes out
Mouth connects constant temperature water bath apparatus (1) and floss hole (10) by valve respectively.
4. portable Membrane Materials method seawater desalination system according to claim 1, it is characterised in that the membrane module (6)
For hollow fiber film assembly.
5. portable Membrane Materials method seawater desalination system according to claim 4, it is characterised in that the hollow-fibre membrane
Component includes dewatering microporous film.
6. portable Membrane Materials method seawater desalination system according to claim 1, it is characterised in that the membrane module (6)
Provided with least two steam (vapor) outlets, the steam (vapor) outlet connects steam pipework.
7. portable Membrane Materials method seawater desalination system according to claim 1, it is characterised in that the vavuum pump (9)
For circulating water type vavuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621401538.4U CN206318730U (en) | 2016-12-20 | 2016-12-20 | Portable Membrane Materials method seawater desalination system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621401538.4U CN206318730U (en) | 2016-12-20 | 2016-12-20 | Portable Membrane Materials method seawater desalination system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206318730U true CN206318730U (en) | 2017-07-11 |
Family
ID=59259468
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621401538.4U Active CN206318730U (en) | 2016-12-20 | 2016-12-20 | Portable Membrane Materials method seawater desalination system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206318730U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352624A (en) * | 2017-08-31 | 2017-11-17 | 江苏大学 | A kind of high flux double flat plate pressure reducing film distillation experimental provision |
-
2016
- 2016-12-20 CN CN201621401538.4U patent/CN206318730U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107352624A (en) * | 2017-08-31 | 2017-11-17 | 江苏大学 | A kind of high flux double flat plate pressure reducing film distillation experimental provision |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101659451B (en) | Method for treating high-salt water by air stripping type membrane distillation | |
| CN105709601A (en) | Heat pump-double-effect membrane distillation apparatus and distillation method | |
| CN104803532B (en) | A kind of membrane type humidifies dehumidification sea water desalinating unit and method for desalting seawater | |
| CN104291406B (en) | A kind of step coupling utilizes solar energy and the vacuum membrane distillation seawater desalination system of diesel cylinder sleeve cooling water heat | |
| CN107032543A (en) | A kind of marine desalination equipment | |
| CN103848463A (en) | Treatment device of low-temperature evaporation high-concentration sewage | |
| CN104190260A (en) | Decompression combination airgap membrane distillation method and device thereof | |
| CN206318730U (en) | Portable Membrane Materials method seawater desalination system | |
| CN108128831A (en) | Solar heat pump desalination plant | |
| CN106995228B (en) | Membrane distillation method and distillation device for high-concentration brine | |
| CN109867401A (en) | It is a kind of to produce water resource system device and method using deep sea low temperature water condensation | |
| CN201517039U (en) | Heat pump type sea water desalination device | |
| CN206861916U (en) | A kind of HEAT PUMP BASED ON EJECTING PRINCIPLE residual heat resources retracting device of vegetable protein flash-off steam | |
| CN203820489U (en) | Low-temperature evaporation treatment device for high-concentration wastewater | |
| CN106966462A (en) | A kind of multistage seawater desalting coupled system | |
| CN108597636A (en) | A kind of method and system of film distillation technology processing radioactive wastewater | |
| CN205061622U (en) | Efficient membrane distillation plant | |
| CN104261497B (en) | A kind of bubbling negative pressure evaporation sea water desalinating plant and production method | |
| CN107970628A (en) | Triple effect falling liquid film low-temperature vacuum thickener | |
| CN107758777A (en) | A kind of marine seawater desalination system of high waste heat utilization | |
| CN101844821B (en) | Equipment and technology for improving reverse osmosis efficiency by waste heat recovery | |
| CN204384909U (en) | Sea water desalinating plant | |
| CN203425540U (en) | Filtrate concentration device used in pectin production | |
| CN207006115U (en) | A kind of residual heat of condensed water retracting device | |
| CN206720952U (en) | A kind of marine desalination equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |