CN106731385B - A kind of desalting system - Google Patents
A kind of desalting system Download PDFInfo
- Publication number
- CN106731385B CN106731385B CN201611214197.4A CN201611214197A CN106731385B CN 106731385 B CN106731385 B CN 106731385B CN 201611214197 A CN201611214197 A CN 201611214197A CN 106731385 B CN106731385 B CN 106731385B
- Authority
- CN
- China
- Prior art keywords
- desalination module
- moisture trap
- inert stage
- filter
- spray head
- 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
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
- B01D50/10—Combinations of devices covered by groups B01D45/00, B01D46/00 and B01D47/00
Abstract
The present invention provides a kind of desalting systems, including the first desalination module and the second desalination module, first desalination module includes filter, at least one three-level filter and blower, three-level filter includes preceding inert stage moisture trap, silk screen knockouts and rear inert stage moisture trap, and it is arranged between each three-level filter in concatenated form, second desalination module includes baffle, strainer and spray head, under the action of blower, sea wind is successively through filter, preceding inert stage moisture trap, enter in the second desalination module after silk screen knockouts and rear inert stage moisture trap, sea wind is again successively through baffle, it is flowed out after strainer and spray head, above-mentioned desalting system, first desalination module is combined into the major diameter particle in the removable sea wind of three-level filter by inert stage and silk screen grade, second desalination module can remove as low as 1 μ m diameter particle, it can Realize 99% or more desalination rate.
Description
Technical field
The present invention relates to desalting system more particularly to a kind of desalting systems for being suitable for sea wind.
Background technique
Ocean is the important barrier, and the marine resources that are richly stored with together of national security.But saliferous in seawater
Weight percent is very high, includes certain density salt in the air on sea.Salt is present in the spray often occurred, there is also
In being suspended in air in the sea water drops of very little, separated if the aerosol of this salt takes no action to give, with air inlet
Into in mechanical device, make its performance loss.In order to extend the service life of all kinds of mechanical devices in seashore, must be strict with
Its desalination.
The silk screen knockouts of single-stage is suitable for medium flow rate (3-6m/s), and the small particles for being 2-10 μm for diameter have preferably
Capture effect, therefore experiment achieves preferable filter effect under the operating condition for having mist, but when having larger particles, filtering effect
Fruit is bad.And the characteristic of single inert stage moisture trap and silk screen agglomerate on the contrary, bulky grain (> 20 μm) is suitble to separate, this
Two kinds of separation schemes can remove most of particle under low pressure drop, however be handled even if using big pressure drop more separate small
No longer there is high efficiency.
It is big in view of marine wind speed, the particles such as the different water droplet of various sizes, dust and salinity are mingled in wind, single desalination is former
Reason is difficult that all types of particles separation in air is clean.
Summary of the invention
The purpose of the present invention is to provide a kind of desalting systems, it is intended to will be in air for solving that existing desalting system is difficult
All types of particles separate clean defect.
The present invention is implemented as follows:
A kind of desalting system, including the first desalination module and the second desalination module；
The first desalination module includes filter, at least one three-level filter and blower, the three-level filter packet
Preceding inert stage moisture trap, silk screen knockouts and rear inert stage moisture trap are included, and between each three-level filter
It is arranged in concatenated form；
The second desalination module includes baffle, strainer and spray head, and the spray head can spray fresh water and wash to air
Purification:
Under the action of the blower, sea wind is successively through the filter, preceding inert stage moisture trap, silk screen knockouts
And after rear inert stage moisture trap enter the second desalination module in, the sea wind again successively through the baffle, strainer and
It is flowed out after spray head.
In some embodiments, the filter, preceding inert stage moisture trap, silk screen knockouts and rear inert stage air water
Separator is sequentially arranged in the horizontal direction.
In some embodiments, the blower is located between the rear inert stage moisture trap and the second desalination module.
In some embodiments, the baffle, strainer and spray head are sequentially arranged along the vertical direction.
In some embodiments, the baffle is interspersed in the two sides of the second desalination module so that the sea wind exists
The baffle mid-game screws on liter.
In some embodiments, the second desalination module bottom is also provided with water outlet, the fresh water that the spray head sprays
It can be flowed out through the water outlet.
The invention has the following advantages:
Desalting system provided by the invention, including the first desalination module and the second desalination module, the first desalination module
Including filter, at least one three-level filter and blower, the three-level filter includes preceding inert stage moisture trap, silk screen
Knockouts and rear inert stage moisture trap, and arranged between each three-level filter in concatenated form, described second
Desalination module includes baffle, strainer and spray head, and under the action of the blower, sea wind is successively through the filter, preceding inert stage
Enter in the second desalination module after moisture trap, silk screen knockouts and rear inert stage moisture trap, the sea wind is again
Successively flowed out after the baffle, strainer and spray head, the application propose desalting system, in conjunction with inertial separation, silk screen cohesion with
And water washing cleaning principle, the first desalination module are combined into big straight in the removable sea wind of three-level filter by inert stage and silk screen grade
Diameter particle, the second desalination module can remove as low as 1 μ m diameter particle, by improving spray head and air flow distribution, it can be achieved that
Low pressure drop, high efficiency solid particle absorb, while also having fresh air and sterilizing function, it can be achieved that desalination using water washing cleaning
99% or more rate.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below
There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this
Some embodiments of invention for those of ordinary skill in the art without creative efforts, can be with
Other attached drawings are obtained according to these attached drawings.
Fig. 1 is the structural schematic diagram of desalting system provided in an embodiment of the present invention.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete
Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on
Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts all other
Embodiment shall fall within the protection scope of the present invention.
Embodiment 1
Referring to Fig. 1, the embodiment of the present invention 1 provides a kind of desalting system 100, including the first desalination module 110 and second removes
Salt module 120.Wherein:
The first desalination module 110 includes 1, three-level filter 111 of filter and blower 5
Wherein, the three-level filter 111 includes preceding inert stage moisture trap 2, silk screen knockouts 3, rear inert stage gas
Separator 4.
Preferably, the filter 1, preceding inert stage moisture trap 2, silk screen knockouts 3 and rear inert stage gas-water separation
Sequence is arranged device 4 in the horizontal direction.
It is appreciated that the first desalination module 100 includes preceding inert stage moisture trap 2, silk screen knockouts 3 and rear inert stage
The inert stage and silk screen grade that moisture trap 4 forms are combined into the major diameter particle in the removable sea wind of three-level filter.
The second desalination module 120 include baffle 6, strainer 7 and spray head 8, the spray head 7 can spray fresh water to air into
Row water washing cleaning.
Preferably, sequence is arranged along the vertical direction for the baffle 6, strainer 7 and spray head 8.
Further, the baffle 6 is interspersed in the two sides of the second desalination module 120 so that the sea wind is in institute
It states 6 mid-game of baffle and screws on liter.
It is appreciated that the second desalination module 120 uses rinsing type, as low as 1 μ m diameter particle can remove, by improving spray head
Water yield and air flow distribution, it can be achieved that low pressure drop, high efficiency solid particle absorb, while spray head spray fresh water also
With fresh air and sterilizing function.
Specifically, under the action of blower 5, sea wind successively through the filter 1, preceding inert stage moisture trap 2,
Enter in the second desalination module 120 after silk screen knockouts 3 and rear inert stage moisture trap 4, the sea wind successively passes through again
Outflow (outflux after A expression sea wind is purified in Fig. 1) after the baffle 6, strainer 7 and spray head 8.
Preferably, the blower 6 is located between the rear inert stage moisture trap 4 and the second desalination module 120.It can be with
Understand, by the power for changing blower 6, thus it is possible to vary air flow distribution, to better conform to various requirement.
Preferably, 120 bottom of the second desalination module is also provided with water outlet B, and the fresh water that the spray head 8 sprays can be through
The water outlet B outflow.
Embodiment 2
Difference from Example 1, the embodiment of the present invention 2 provide a kind of desalting system, and the first desalination module includes
Three-level filter there are 2 and dependent Series to arrange, other structures are identical, and which is not described herein again.
It is appreciated that the setting of the embodiment of the present application 2 can remove the major diameter in sea wind by two concatenated three-level filters
Particle, removal efficiency are more preferable.
It is appreciated that multistage three-level filter can also be designed as needed in practice, wanted with the application for adapting to different
It asks.
Desalting system provided by the present application, including the first desalination module and the second desalination module, the first desalination module is by being used to
Property grade and silk screen grade be combined into three-level filter and can remove major diameter particle in sea wind, the second desalination module can remove as low as 1 μ
M diameter particle, above-mentioned desalting system combination inertial separation, silk screen cohesion and water washing cleaning principle, by improve spray head and
Air flow distribution, it can be achieved that low pressure drop, high efficiency solid particle absorb, while using water washing cleaning also have fresh air and
Sterilizing function is, it can be achieved that 99% or more desalination rate.
Desalting system provided by the present application is applied not only to the separation of seashore salt particle, moreover it can be used to air or useless elsewhere
The separation of other particles in gas.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Within mind and principle, any modification, equivalent replacement, improvement and so on be should all be included in the protection scope of the present invention.
Claims (3)
1. a kind of desalting system, it is characterised in that: including the first desalination module and the second desalination module；
The first desalination module includes filter, at least one three-level filter and blower, before the three-level filter includes
Inert stage moisture trap, silk screen knockouts and rear inert stage moisture trap, and in string between each three-level filter
The form of connection arranges；The filter, preceding inert stage moisture trap, silk screen knockouts and rear inert stage moisture trap are along water
Square to sequence be arranged；
The second desalination module includes baffle, strainer and spray head, and the spray head can spray fresh water and carry out water washing cleaning to air,
The baffle, strainer and spray head are sequentially arranged along the vertical direction；
Under the action of the blower, sea wind successively through the filter, preceding inert stage moisture trap, silk screen knockouts and after
Enter in the second desalination module after inert stage moisture trap, the sea wind is again successively through the baffle, strainer and spray head
After flow out；
The baffle is interspersed in the two sides of the second desalination module so that the sea wind screws on liter in the baffle mid-game.
2. desalting system as described in claim 1, it is characterised in that: the blower is located at the rear inert stage moisture trap
And second between desalination module.
3. desalting system as described in claim 1, it is characterised in that: the second desalination module bottom is also provided with water outlet
Mouthful, the fresh water that the spray head sprays can be flowed out through the water outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611214197.4A CN106731385B (en) | 2016-12-26 | 2016-12-26 | A kind of desalting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201611214197.4A CN106731385B (en) | 2016-12-26 | 2016-12-26 | A kind of desalting system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106731385A CN106731385A (en) | 2017-05-31 |
| CN106731385B true CN106731385B (en) | 2019-10-29 |
Family
ID=58920777
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201611214197.4A Active CN106731385B (en) | 2016-12-26 | 2016-12-26 | A kind of desalting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106731385B (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102052715A (en) * | 2010-12-15 | 2011-05-11 | 上海交通大学 | Multi-stage M-shaped air way liquid desiccant dehumidification air-conditioning system utilizing ultrasonic atomization technology |
| CN102423597A (en) * | 2011-10-14 | 2012-04-25 | 华南理工大学 | Intelligent anti-blocking demister used for wet flue gas desulfurization |
| CN103864163A (en) * | 2014-03-27 | 2014-06-18 | 广州中国科学院先进技术研究所 | Combined type nonmetal sea water desalination demister |
| CN204073758U (en) * | 2014-09-11 | 2015-01-07 | 广东申菱空调设备有限公司 | For the filter of coastal area salt mist environment and PM2.5 particle |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20140072483A1 (en) * | 2012-09-10 | 2014-03-13 | Mitsubishi Heavy Industries, Ltd. | Desulfurization device and particulate collection system |
-
2016
- 2016-12-26 CN CN201611214197.4A patent/CN106731385B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102052715A (en) * | 2010-12-15 | 2011-05-11 | 上海交通大学 | Multi-stage M-shaped air way liquid desiccant dehumidification air-conditioning system utilizing ultrasonic atomization technology |
| CN102423597A (en) * | 2011-10-14 | 2012-04-25 | 华南理工大学 | Intelligent anti-blocking demister used for wet flue gas desulfurization |
| CN103864163A (en) * | 2014-03-27 | 2014-06-18 | 广州中国科学院先进技术研究所 | Combined type nonmetal sea water desalination demister |
| CN204073758U (en) * | 2014-09-11 | 2015-01-07 | 广东申菱空调设备有限公司 | For the filter of coastal area salt mist environment and PM2.5 particle |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106731385A (en) | 2017-05-31 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| WO2019230295A1 (en) | Device for purifying scrubber drainage water, method for same, and salinity gradient power system | |
| WO2013078164A4 (en) | Systems and methods for improved baghouse filters | |
| US20110179950A1 (en) | Tubing air purification system | |
| CN102933288B (en) | Nanoflotation | |
| CN106731385B (en) | A kind of desalting system | |
| CN1758947A (en) | Wet scrubbing apparatus and method | |
| WO2015141396A1 (en) | Water treatment device and water treatment method using same | |
| US10576425B2 (en) | Unhoused filtration device and methods of use | |
| CN202740964U (en) | Salt mist separation device and wind turbine generator system | |
| DK200501478A (en) | Separator for separating impurities, especially smaller particles, from rainwater | |
| CN101648760A (en) | Oily waste water separation treatment device for ships | |
| CN102726337A (en) | Water-pollutant separation device | |
| CN103864163B (en) | The nonmetal desalinization demister of a kind of combined type | |
| CN107754540B (en) | Inertial force pushing gas-liquid separator | |
| JP2013078747A (en) | Dust collector | |
| CN105363243A (en) | Oil-water separator | |
| CN103721480A (en) | Defogging device for double-hook waved plate | |
| KR20200060115A (en) | Bag filter dust collector | |
| SE537323C2 (en) | Air Filter System | |
| CN205164198U (en) | Oil -water separator | |
| CN206767724U (en) | A kind of conduit-type dense media powder catcher | |
| CN103100282A (en) | Ammonium nitrate technology steam demisting apparatus | |
| CN218516286U (en) | Vane type demister | |
| CN204134740U (en) | Compound concentric round shape wet type electrostatic precipitator | |
| CN202237686U (en) | Combined separating filter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |