CN206266382U - Demineralization plant - Google Patents

Demineralization plant Download PDF

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Publication number
CN206266382U
CN206266382U CN201621348623.9U CN201621348623U CN206266382U CN 206266382 U CN206266382 U CN 206266382U CN 201621348623 U CN201621348623 U CN 201621348623U CN 206266382 U CN206266382 U CN 206266382U
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CN
China
Prior art keywords
except
salt box
reaction unit
pipeline
demineralization plant
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.)
Expired - Fee Related
Application number
CN201621348623.9U
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Chinese (zh)
Inventor
曹海燕
杨波
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chengdu Wing Tim Technology Co Ltd
Original Assignee
Chengdu Wing Tim Technology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Chengdu Wing Tim Technology Co Ltd filed Critical Chengdu Wing Tim Technology Co Ltd
Priority to CN201621348623.9U priority Critical patent/CN206266382U/en
Application granted granted Critical
Publication of CN206266382U publication Critical patent/CN206266382U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A20/00Water conservation; Efficient water supply; Efficient water use
    • Y02A20/124Water desalination
    • Y02A20/131Reverse-osmosis

Abstract

The utility model discloses a kind of demineralization plant, including heater, reaction unit and except salt box, the heater connects the reaction unit, the top of the reaction unit is provided with water inlet, the bottom of reaction unit is provided with delivery port, the bottom of reaction unit is provided with blanking port, the inside of the reaction unit is also sequentially provided with activated carbon filtering layer from top to bottom, upper strata porous plate, lower floor's porous plate and counter-infiltration film layer, the blanking port is connected by pipeline with except salt box, except the exhaust outlet on salt box is connected with vavuum pump by pipeline, the inside except salt box is provided with heating tube, except the side wall of salt box is provided with peep hole, except the bottom of salt box is provided with opening and closing except the cleaning plate of salt box.The utility model provides a kind of demineralization plant, and its desalination effect is good, improves the service life of equipment, and low cost, compact conformation, floor space is small, and water consumption and power consumption are reduced.

Description

Demineralization plant
Technical field
The utility model is related to a kind of filter plant field, and in particular to a kind of demineralization plant.
Background technology
Either hardness to water of industrial process waters or domestic water, salt content have certain requirement, at present, remove Salt processing method is divided into two classes;It is the way of distillation, freezing, hyperfiltration, hydrate and solvent extraction that the first kind is;And the Two classes then include electroosmose process and ion-exchange.
The long-term existence of salt impurity, can progressively be attached on the inner surface of reaction vessel and pipeline, form electrochemical corrosion, Can accelerate the corrosion of pipeline and reaction vessel, reduce the service life of equipment, while also being brought to production certain dangerous Hidden danger.
Existing demineralization plant is mainly based on the reverse osmosis unit equipment of the single treatment formula based on film infiltration, this kind of Mode floor space is big, high energy consumption, high cost.
Utility model content
Based on this, regarding to the issue above, it is necessary to propose a kind of demineralization plant, its desalination effect is good, improves making for equipment With life-span, low cost, compact conformation, floor space is small.
The technical solution of the utility model is:
A kind of demineralization plant, including heater, reaction unit and except salt box, the heater connect the reaction unit, The top of the reaction unit is provided with water inlet, and the bottom of reaction unit is provided with delivery port, and the bottom of reaction unit is provided with blanking Mouthful, the inside of the reaction unit is also sequentially provided with activated carbon filtering layer, upper strata porous plate, lower floor's porous plate and reverse osmosis from top to bottom Permeable membrane layer, the blanking port by pipeline with except salt box is connected, except the exhaust outlet on salt box is connected with vavuum pump by pipeline, institute State except the inside of salt box is provided with heating tube, except the side wall of salt box is provided with peep hole, except the bottom of salt box is provided with opening and closing except salt box Cleaning plate.
In the technical solution of the utility model:Current first pass around the activated carbon filtering layer in the equipment, by activated carbon Absorption, remove tiny dissolved matter in water removal, reduce the unfavorable factor to reverse osmosis membrane, finally flow into pond, wait input its His industrial processes, meanwhile, heater is to reaction unit continuous heating, the salinity in drying water, except the second method on salt box Blue mouth is connected together with vavuum pump so that except the pressure in salt box is less than the pressure in reaction unit so that in reaction unit Salt impurity smoothly fall, salt impurity is concentrated to except in salt box, except the heating tube in salt box causes that salt impurity is maintained at more dry Dry state, to reduce the loss of solvent and be easy to remove.So that desalination effect is improved, the service life of equipment is improved, and Low cost, compact conformation, floor space is small.
In a preferred embodiment, switch valve is provided with the pipeline that the blanking port is connected with except salt box.Purpose It is to control reaction unit and except the pipeline connection between salt box, being opened when desalination is needed makes reaction unit and except salt box connects It is logical, conversely, closing so that the desalting process of equipment is more flexible, in hgher efficiency.
In further preferably embodiment, multistorey strainer mesh is respectively equipped with the upper and lower surface of the activated carbon filtering layer.Mesh Be salinity in more accurate filtering and absorption water, it is ensured that water quality it is pure, while the salinity after filtering is adsorbed onto into activity On carbon filtration layer.
In further preferably embodiment, the activated carbon filtering layer is detachable.Purpose is to facilitate activated carbon filtering layer Replacing and cleaning.
In further preferably embodiment, the cleaning plate is provided with handle.Purpose is the opening and closing cleaning plate of drawer type, Easy cleaning removes the salt impurity in salt box, without excessive cumbersome operation.
In still more preferably embodiment, the counter-infiltration film layer includes multiple coiled reverse osmosis membrane elements, rolling Reverse-osmosis membrane element is connected with lower floor's porous plate for screw thread is screwed.Purpose is carbon leaching material to be rinsed the recoil with reverse osmosis membrane Wash and be combined, the effect of energy-saving and water-saving, water consumption and all relative reduction of power consumption can be reached.
The beneficial effects of the utility model are:
1st, desalination effect is lifted, efficiency, the service life of extension device is improved.
2nd, low cost, compact conformation, floor space is small.
3rd, water consumption and power consumption are reduced.
4th, the salt impurity cleaning for removing is convenient, fast.
Brief description of the drawings
Fig. 1 is the overall structure diagram of demineralization plant described in the utility model embodiment;
Fig. 2 is the structural representation except salt box;
Fig. 3 is the upward view except salt box.
Description of reference numerals:
10th, heater;20th, reaction unit;201st, water inlet;202nd, delivery port;203rd, blanking port;204th, active carbon filtration Layer;205th, upper strata porous plate;206th, lower floor's porous plate;207th, counter-infiltration film layer;30th, except salt box;301 first flanges;301a, open Close valve;302nd, second flange;302a, vavuum pump;303rd, heating tube;304th, peep hole;305th, plate is cleared up;305a, handle.
Specific embodiment
Embodiment of the present utility model is described in detail below in conjunction with the accompanying drawings.
Embodiment 1:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
Embodiment 2:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
As depicted in figs. 1 and 2, switch valve 301a is provided with the pipeline that the blanking port 203 is connected with except salt box 30.
Embodiment 3:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
As depicted in figs. 1 and 2, switch valve 301a is provided with the pipeline that the blanking port 203 is connected with except salt box 30.
Multistorey strainer mesh is respectively equipped with the upper and lower surface of the activated carbon filtering layer 204.
Embodiment 4:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
As depicted in figs. 1 and 2, switch valve 301a is provided with the pipeline that the blanking port 203 is connected with except salt box 30.
Multistorey strainer mesh is respectively equipped with the upper and lower surface of the activated carbon filtering layer 204.
The activated carbon filtering layer 204 is detachable.
Embodiment 5:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
As depicted in figs. 1 and 2, switch valve 301a is provided with the pipeline that the blanking port 203 is connected with except salt box 30.
Multistorey strainer mesh is respectively equipped with the upper and lower surface of the activated carbon filtering layer 204.
The activated carbon filtering layer 204 is detachable.
As shown in figure 3, the cleaning plate 305 is provided with the handle 305a of drawer type opening and closing cleaning plate 305.
Embodiment 6:
As depicted in figs. 1 and 2, a kind of demineralization plant, including heater 10, reaction unit 20 and except salt box 30, it is described plus Hot device 10 connects the reaction unit 20, and the top of the reaction unit 20 is provided with water inlet 201, and the bottom of reaction unit 20 sets There is a delivery port 202, the bottom of reaction unit 20 is provided with blanking port 203, the inside of the reaction unit 20 is from top to bottom also successively Activated carbon filtering layer 204, upper strata porous plate 205, lower floor's porous plate 206 and counter-infiltration film layer 207 are provided with, the blanking port 203 leads to Piping with except salt box 30 is connected, it is described except salt box 30 except the exhaust outlet on salt box 30 is connected with vavuum pump 302a by pipeline Inside be provided with heating tube 303, except the side wall of salt box 20 is provided with peep hole 304, except the bottom of salt box 30 is provided with opening and closing desalination The cleaning plate 305 of case.
As depicted in figs. 1 and 2, switch valve 301a is provided with the pipeline that the blanking port 203 is connected with except salt box 30.
Multistorey strainer mesh is respectively equipped with the upper and lower surface of the activated carbon filtering layer 204.
The activated carbon filtering layer 204 is detachable.
As shown in figure 3, the cleaning plate 305 is provided with the handle 305a of drawer type opening and closing cleaning plate 305.
As shown in figure 1, the counter-infiltration film layer 207 includes multiple coiled reverse osmosis membrane elements, coiled reverse osmosis membrane element It is connected for screw thread is screwed with lower floor porous plate 206.
Embodiment described above only expresses specific embodiment of the present utility model, and its description is more specific and detailed, But therefore can not be interpreted as the limitation to the utility model the scope of the claims.It should be pointed out that common for this area For technical staff, without departing from the concept of the premise utility, various modifications and improvements can be made, these all belong to In protection domain of the present utility model.

Claims (6)

1. a kind of demineralization plant, it is characterised in that including heater, reaction unit and except salt box, the heater connection is described Reaction unit, the top of the reaction unit is provided with water inlet, and the bottom of reaction unit is provided with delivery port, the bottom of reaction unit It is provided with blanking port, it is porous that the inside of the reaction unit is also sequentially provided with activated carbon filtering layer, upper strata porous plate, lower floor from top to bottom Plate and counter-infiltration film layer, the blanking port by pipeline with except salt box is connected, except the exhaust outlet on salt box is connected with by pipeline Vavuum pump, the inside except salt box is provided with heating tube, except the side wall of salt box is provided with peep hole, except the bottom of salt box is provided with out Close the cleaning plate except salt box.
2. demineralization plant according to claim 1, it is characterised in that setting on the pipeline that the blanking port be connected with except salt box There is switch valve.
3. demineralization plant according to claim 1, it is characterised in that be respectively equipped with the upper and lower surface of the activated carbon filtering layer Multistorey strainer mesh.
4. the demineralization plant according to claim 1 or 3, it is characterised in that the activated carbon filtering layer is detachable.
5. demineralization plant according to claim 1, it is characterised in that the cleaning plate is provided with drawer type opening and closing cleaning plate Handle.
6. demineralization plant according to claim 1, it is characterised in that the counter-infiltration film layer includes multiple coiled reverse osmosis membranes Element, coiled reverse osmosis membrane element is connected with lower floor's porous plate for screw thread is screwed.
CN201621348623.9U 2016-12-09 2016-12-09 Demineralization plant Expired - Fee Related CN206266382U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201621348623.9U CN206266382U (en) 2016-12-09 2016-12-09 Demineralization plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201621348623.9U CN206266382U (en) 2016-12-09 2016-12-09 Demineralization plant

Publications (1)

Publication Number Publication Date
CN206266382U true CN206266382U (en) 2017-06-20

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201621348623.9U Expired - Fee Related CN206266382U (en) 2016-12-09 2016-12-09 Demineralization plant

Country Status (1)

Country Link
CN (1) CN206266382U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109224548A (en) * 2018-09-13 2019-01-18 海南省博物馆(海南省文物考古研究所) A kind of ocean water outlet full-automatic desalination monitoring device of stone cultural artifact

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109224548A (en) * 2018-09-13 2019-01-18 海南省博物馆(海南省文物考古研究所) A kind of ocean water outlet full-automatic desalination monitoring device of stone cultural artifact
CN109224548B (en) * 2018-09-13 2019-07-02 海南省博物馆(海南省文物考古研究所) A kind of ocean water outlet full-automatic desalination monitoring device of stone cultural artifact

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CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170620

Termination date: 20201209