CN208362090U - A kind of crystallization of strong brine divides salt captation - Google Patents

A kind of crystallization of strong brine divides salt captation Download PDF

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Publication number
CN208362090U
CN208362090U CN201820561960.9U CN201820561960U CN208362090U CN 208362090 U CN208362090 U CN 208362090U CN 201820561960 U CN201820561960 U CN 201820561960U CN 208362090 U CN208362090 U CN 208362090U
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CN
China
Prior art keywords
strong brine
evaporator
holding vessel
processor
captation
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Expired - Fee Related
Application number
CN201820561960.9U
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Chinese (zh)
Inventor
王倩
于海琴
孙明明
王梓欣
邓恒涛
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Beijing Jiaotong University
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Beijing Jiaotong University
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Priority to CN201820561960.9U priority Critical patent/CN208362090U/en
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Publication of CN208362090U publication Critical patent/CN208362090U/en
Expired - Fee Related legal-status Critical Current
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Abstract

The utility model discloses a kind of crystallizations of strong brine to divide salt captation, a kind of strong brine crystallization divides salt captation, including support, strong brine holding vessel, evaporator, suction pump, dust-collecting bucket, holding vessel inlet and holding vessel liquid outlet are provided on the strong brine holding vessel, solenoid valve is provided on the holding vessel outlet tube of the strong brine holding vessel, filter cloth is provided on the evaporator water inlet pipe, hydraulic press is provided at the top of the evaporator, hydraulic stem is connected on the axis of the hydraulic press, bracket is connected on the hydraulic stem, annular scraper is connected on the bracket, the annular scraper is adapted to evaporator, flexible heater piece is provided on the evaporation top tank structure, the evaporation pot bottom is provided with heating wire, Baume hydrometer is provided on the support, solidifying water plate is provided on the dust-collecting bucket.The features such as a kind of the utility model strong brine crystallization divides salt captation to have to divide salt effect good, and structure is simple, easy to operate.

Description

A kind of crystallization of strong brine divides salt captation
Technical field
The utility model relates to strong brine processing technology fields, more specifically, are related to a kind of crystallization of strong brine and divide salt collection Water installations.
Background technique
Sea water desalination is to solve the problems, such as the important measures of shortage of fresh water, there is more than 100 of more than ten country in the world There is the sea water desalination facility of hundreds of different structures and different capabilities in scientific research institution in work in the research for carrying out sea water desalination Make.The large-scale seawater desalting plant of one modernization, can produce thousands of, tens of thousands of or even nearly million tons of fresh water daily.The cost of water It is reduced constantly, some countries have already decreased to similar with the price of tap water.The coastal sea water desalination work of China in Recent Years Journey scale expands increasingly.The desalination water of certain areas has reached the water supply scale of countries and cities, has been greatly facilitated Chinese edge The fast development of extra large regional economy.But sea water desalination production process can generate a large amount of strong brines, wherein containing highly concentrated in strong brine The chemical substance being added in the metal ions such as sodium, magnesium, calcium, the potassium of degree, various acid ions and preprocessing process, direct emission Both threat can be generated to the fragile marine eco-environment, and to the huge waste of resource.
Strong brine is directly evaporated to obtain the mixture of salinity, product composition is complicated, and utility value is extremely low.
Summary of the invention
The utility model is intended to solve at least some of the technical problems in related technologies.For this purpose, this reality It is to propose that a kind of strong brine crystallization divides salt captation with a novel purpose, which divides salt to catchment dress The features such as setting to have divides salt effect good, and structure is simple, easy to operate.
The technical solution that the utility model solves above-mentioned technical problem is as follows: a kind of crystallization of strong brine divides salt captation, Including support, strong brine holding vessel, evaporator, suction pump, dust-collecting bucket, the strong brine holding vessel is arranged on the support, described Evaporator is arranged on the support, and the dust-collecting bucket setting on the support, is provided with holding vessel feed liquor on the strong brine holding vessel Mouthful and holding vessel liquid outlet, be provided with evaporator water inlet pipe and evaporator steam (vapor) outlet, the suction pump two on the evaporator End is connect with holding vessel liquid outlet and evaporator water inlet pipe respectively, is provided on the holding vessel outlet tube of the strong brine holding vessel Solenoid valve is provided with filter cloth on the evaporator water inlet pipe, is provided with hydraulic press, the axis of the hydraulic press at the top of the evaporator On be connected with hydraulic stem, bracket is connected on the hydraulic stem, is connected with annular scraper on the bracket, the annular scraper with Evaporator is adapted to, and is provided with flexible heater piece on the evaporation top tank structure, the evaporation pot bottom is provided with heating wire, the branch Baume hydrometer is provided on seat, the densimeter probe setting of the Baume hydrometer is on evaporation tank skin, on the dust-collecting bucket It is provided with solidifying water plate, the dust-collecting bucket bottom is provided with water outlet, and flowing water Valve, the processor are provided on the water outlet It is electrically connected with the solenoid valve, the processor and hydraulic mechatronics, the processor are electrically connected with Baume hydrometer, the processing Device is electrically connected with suction pump, and the processor is electrically connected with flexible heater piece, and the processor is electrically connected with heating wire, the steaming Hair pot bottom is provided with Outlet cover plate.
Further, power interface and switch are provided on the processor.
Further, semi-conductor condensation piece is provided in the solidifying water plate, the semi-conductor condensation piece is electrically connected with processor It connects.
Further, bionical protrusion is provided in the solidifying water plate.
Further, elbow is connected on the evaporator steam (vapor) outlet.
Above the beneficial effects of the utility model are: a kind of crystallization of strong brine divides salt captation, mentioned by the utility model For a kind of combination Baume hydrometer real time monitoring strong brine crystallization divide salt captation, using Baume degrees as evaporate node, The principles such as bionical condensate, have sufficiently held three inversion of phases of strong brine, and overall process does not generate any adverse effect, and energy to environment Synchronous recycling salinity and fresh water, salinity removal rate is high and purity is high, and apparatus structure is simple, can environmental protection, efficiently realize it is with high salt The rational utilization of water.
2. structure is independently simple, energy conservation and environmental protection, divide salt effect good.
3. reducing the generation of solid waste, while creating economic value.
4. the crystal salt of evaporator can be prevented to be sucked pump sucking strong brine holding vessel by the way that filter cloth is arranged, protect simultaneously Suction pump.
Detailed description of the invention
Fig. 1 is the structural schematic diagram that a kind of strong brine crystallization of the utility model divides salt captation;
Fig. 2 is the electrical block diagram that a kind of strong brine crystallization of the utility model divides salt captation;
In attached drawing, parts list represented by the reference numerals are as follows:
1, support;2, strong brine holding vessel;20, holding vessel inlet;21, holding vessel liquid outlet;22, solenoid valve;3, it takes out Sucking pump;4, processor;5, evaporator;50, evaporator water inlet pipe;51, evaporator steam (vapor) outlet;52, elbow;53, hydraulic press; 54, hydraulic stem;55, bracket;56, annular scraper;57, flexible heater piece;58, heater strip;59, Outlet cover plate;6, gravity Baume Meter;60, densimeter is popped one's head in;7, dust-collecting bucket;70, solidifying water plate;71, bionical protrusion;72, water outlet;73, flowing water Valve;8, it partly leads Body condensate film;9, filter cloth.
Specific embodiment
The embodiments of the present invention are described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning Same or similar element or element with the same or similar functions are indicated to same or similar label eventually.Below by The embodiment being described with reference to the drawings is exemplary, it is intended to for explaining the utility model, and should not be understood as practical new to this The limitation of type.
In the description of the present invention, it should be understood that term " center ", " longitudinal direction ", " transverse direction ", " length ", " width Degree ", " thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom", "inner", "outside", The orientation or positional relationship of the instructions such as " clockwise ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " is based on the figure Orientation or positional relationship is merely for convenience of describing the present invention and simplifying the description, rather than the dress of indication or suggestion meaning It sets or element must have a particular orientation, be constructed and operated in a specific orientation, therefore should not be understood as to the utility model Limitation.
In addition, term " first ", " second " are used for descriptive purposes only and cannot be understood as indicating or suggesting relative importance Or implicitly indicate the quantity of indicated technical characteristic.Define " first " as a result, the feature of " second " can be expressed or Implicitly include at least one this feature.The meaning of " plurality " is at least two, such as two in the description of the present invention, It is a, three etc., unless otherwise specifically defined.
In the present invention unless specifically defined or limited otherwise, term " installation ", " connected ", " connection ", " Gu It is fixed " etc. terms shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or integral;It can be Mechanical connection, is also possible to be electrically connected;It can be directly connected, two can also be can be indirectly connected through an intermediary The interaction relationship of connection or two elements inside element, unless otherwise restricted clearly.For the common skill of this field For art personnel, the concrete meaning of above-mentioned term in the present invention can be understood as the case may be.
In the present invention unless specifically defined or limited otherwise, fisrt feature is in the second feature " on " or " down " It can be that the first and second features directly contact or the first and second features are by intermediary mediate contact.Moreover, first Feature can be fisrt feature above the second feature " above ", " above " and " above " and be directly above or diagonally above the second feature, or only Only indicate that first feature horizontal height is higher than second feature.Fisrt feature under the second feature " below ", " below " and " below " may be used To be that fisrt feature is directly under or diagonally below the second feature, or is merely representative of first feature horizontal height less than second feature.
As shown in Figs. 1-2, a kind of strong brine crystallization of the present embodiment divides salt captation, including support 1, strong brine storage Tank 2, evaporator 5, suction pump 3, dust-collecting bucket 7, strong brine holding vessel 2 are arranged on support 1, and evaporator 5 is arranged on support 1, Dust-collecting bucket 7 is arranged on support 1, and holding vessel inlet 20 and holding vessel liquid outlet 21 are provided on strong brine holding vessel 2, evaporates Be provided with evaporator water inlet pipe 50 and evaporator steam (vapor) outlet 51 on tank 5,3 both ends of suction pump respectively with holding vessel liquid outlet 21 and Evaporator water inlet pipe 50 connects, and is provided with solenoid valve 22, evaporator water inlet pipe on the holding vessel outlet tube 21 of strong brine holding vessel 2 It is provided with filter cloth 9 on 50, hydraulic press 53 is provided at the top of evaporator 5, hydraulic stem 54, hydraulic stem are connected on the axis of hydraulic press 53 It is connected with bracket 55 on 54, annular scraper 56 is connected on bracket 55, annular scraper 56 is adapted to evaporator 5,5 inner wall of evaporator On be provided with flexible heater piece 57,5 bottom of evaporator is provided with heating wire 58, Baume hydrometer 6, Baume is provided on support 1 The densimeter probe 60 of densimeter 6 is arranged on 5 wall of evaporator, solidifying water plate 70 is provided on dust-collecting bucket 7,7 bottom of dust-collecting bucket is set Be equipped with water outlet 72, flowing water Valve 73 be provided on water outlet 72, processor 4 is electrically connected with solenoid valve 22, processor 4 with it is hydraulic Machine 53 is electrically connected, and processor 4 is electrically connected with Baume hydrometer 6, and processor 4 is electrically connected with suction pump 3, and processor 4 and flexibility add Backing 57 is electrically connected, and processor 4 is electrically connected with heating wire 58, and 5 bottom of evaporator is provided with Outlet cover plate 59.
A kind of strong brine crystallization of the present embodiment, which divides in salt captation, is provided with power interface and switch on processor 4.
A kind of strong brine crystallization of the present embodiment, which divides, is provided with semi-conductor condensation piece in solidifying water plate 70 in salt captation, described Semi-conductor condensation piece is electrically connected with processor 4.
A kind of strong brine crystallization of the present embodiment, which divides, is provided with bionical raised 71 in solidifying water plate 70 in salt captation.
A kind of strong brine crystallization of the present embodiment, which divides, is connected with elbow 52 on evaporator steam (vapor) outlet 51 in salt captation.
The present embodiment specific operation process is as follows:
1, the water inlet of strong brine holding vessel 2 is injected into strong brine;
2. starting processor 4,4 opens solenoid valve 22 of processor, processor 4 is opened and suction pump 3, and strong brine is taken out at this time Enter into evaporator 5, water inlet finishes preprocessor 4 and closes solenoid valve 223, closes suction pump;
3. processor 4 opens flexible heater piece 57 and heating wire 58 and Baume hydrometer 6, heated, in evaporator 5 Start to evaporate, the vapor of evaporation enters dust-collecting bucket 7 by evaporator steam (vapor) outlet 51, due to 7 top of dust-collecting bucket be provided with it is solidifying Water plate 70 condenses into water afterwards to the cold and is collected into ponding bucket 7, when being evaporated to the Baume degrees of setting: calcium sulfate when such as 13.46 ° of B é Start to be precipitated in the inner wall and bottom mass crystallization of evaporator, processor 4 closes flexible heater piece 57 and heating wire 58 stops adding Heat, and solenoid valve 22 is opened, suction pump 3 is opened, remaining all strong brines are pumped into strong brine holding vessel 2 through filter cloth 9 In, close solenoid valve 22;
4. processor 4 opens hydraulic press 53, the hydraulic stem 54 of hydraulic press 53 is acted on annular scraper 56 by bracket 55, Annular scraper 56 scrapes the salinity being adhered on barrel to 5 lower part of evaporator from top to bottom, passes through the outlet of 559 lower part of evaporator Cover board collects salinity;
5. after salinity has been collected, starting processor 4,4 opens solenoid valve 22 of processor, processor 4 is opened and suction pump 3, Strong brine is pumped into evaporator 5 from strong brine holding vessel 2 again at this time, and water inlet finishes preprocessor and closes solenoid valve 22, Close suction pump 3;
6. reopening solenoid valve 22, start suction pump 3, the strong brine in strong brine holding vessel 2 is sucked into evaporator;
7. repeating evaporation process on last stage, chlorination when reaching another Baume degrees of setting such as 24.30 ° of B é Sodium crystal starts to be precipitated in the inner wall and bottom mass crystallization of evaporator 5, and power-off stops heating.Solenoid valve 22 is opened, opens and takes out Remaining all strong brines are pumped into strong brine holding vessel 2 through filter cloth 9 by sucking pump 3;
8. above procedure is repeated, until all salinities are precipitated.
Case one
Certain Seawater Desalination Project carries out sea water desalination using reverse osmosis unit, and the strong brine Baume degrees of generation is 7.52 ° of B é, wherein the concentration of various ions be Na+22.226g/L, Mg2+3.007g/L, Ca 2+0.934g/L, Cl-41.855g/L, SO42-g/L enters strong brine holding vessel by the road.After entering evaporator by suction pump, start to evaporate, when Baume degrees rises to When 13.46 ° of B é, calcium sulfate starts to be precipitated in the inner wall and bottom mass crystallization of evaporator, stops heating at this time, starts suction pump Water is transferred to strong brine holding vessel, then carries out the evaporation of next stage, when being evaporated to 24.30 ° of B é, salinity is collected in power-off, Sodium chloride crystal can be obtained.Distilled water is obtained from dust-collecting bucket simultaneously.
For the device while realizing sea water desalination resource utilization, the discharge for avoiding strong brine causes marine ecology Threat.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " example ", " specifically show The description of example " or " some examples " etc. means specific features, structure, material or spy described in conjunction with this embodiment or example Point is contained at least one embodiment or example of the utility model.In the present specification, to the schematic table of above-mentioned term It states and is necessarily directed to identical embodiment or example.Moreover, particular features, structures, materials, or characteristics described can be with It can be combined in any suitable manner in any one or more of the embodiments or examples.In addition, without conflicting with each other, ability The technical staff in domain can be by different embodiments or examples described in this specification and the feature of different embodiments or examples It is combined.
Although the embodiments of the present invention have been shown and described above, it is to be understood that above-described embodiment is Illustratively, it should not be understood as limiting the present invention, those skilled in the art are in the scope of the utility model Inside can make changes, modifications, alterations, and variations to the above described embodiments should be included in the protection scope of the utility model it It is interior.

Claims (5)

1. a kind of crystallization of strong brine divides salt captation, which is characterized in that a kind of strong brine crystallization divides salt captation, wraps Include support, strong brine holding vessel, evaporator, suction pump, dust-collecting bucket, the strong brine holding vessel setting on the support, the steaming Send out tank setting on the support, the dust-collecting bucket setting on the support, is provided with holding vessel inlet on the strong brine holding vessel With holding vessel liquid outlet, evaporator water inlet pipe and evaporator steam (vapor) outlet, the suction pump both ends are provided on the evaporator It is connect respectively with holding vessel liquid outlet and evaporator water inlet pipe, is provided with electricity on the holding vessel outlet tube of the strong brine holding vessel Magnet valve is provided with filter cloth on the evaporator water inlet pipe, is provided with hydraulic press at the top of the evaporator, on the axis of the hydraulic press It is connected with hydraulic stem, bracket is connected on the hydraulic stem, annular scraper, the annular scraper and steaming are connected on the bracket Tank adaptation is sent out, is provided with flexible heater piece on the evaporation top tank structure, the evaporation pot bottom is provided with heating wire, the support On be provided with Baume hydrometer, the densimeter probe setting of the Baume hydrometer is set on the dust-collecting bucket on evaporation tank skin Be equipped with solidifying water plate, the dust-collecting bucket bottom is provided with water outlet, be provided with flowing water Valve on the water outlet, the processor with Solenoid valve electrical connection, the processor and hydraulic mechatronics, the processor are electrically connected with Baume hydrometer, the processor It is electrically connected with suction pump, the processor is electrically connected with flexible heater piece, and the processor is electrically connected with heating wire, the evaporation Pot bottom is provided with Outlet cover plate.
2. a kind of strong brine crystallization divides salt captation according to claim 1, which is characterized in that be arranged on the processor There are power interface and switch.
3. a kind of strong brine crystallization divides salt captation according to claim 1, which is characterized in that be arranged in the solidifying water plate There is semi-conductor condensation piece, the semi-conductor condensation piece is electrically connected with processor.
4. a kind of strong brine crystallization divides salt captation according to claim 1, which is characterized in that be arranged in the solidifying water plate There is bionical protrusion.
5. a kind of strong brine crystallization divides salt captation according to claim 1, which is characterized in that the evaporator steam goes out Elbow is connected on mouthful.
CN201820561960.9U 2018-04-19 2018-04-19 A kind of crystallization of strong brine divides salt captation Expired - Fee Related CN208362090U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
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
CN117509792A (en) * 2024-01-05 2024-02-06 河北绿鸿环保科技有限公司 Salt separating and water collecting device for crystallization of strong brine

Cited By (4)

* Cited by examiner, † Cited by third party
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
CN117509792A (en) * 2024-01-05 2024-02-06 河北绿鸿环保科技有限公司 Salt separating and water collecting device for crystallization of strong brine
CN117509792B (en) * 2024-01-05 2024-03-19 河北绿鸿环保科技有限公司 Salt separating and water collecting device for crystallization of strong brine

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

Granted publication date: 20190111

Termination date: 20200419

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