CN110357193A - A kind of brine waste evaporated crystallization device - Google Patents
A kind of brine waste evaporated crystallization device Download PDFInfo
- Publication number
- CN110357193A CN110357193A CN201910780381.2A CN201910780381A CN110357193A CN 110357193 A CN110357193 A CN 110357193A CN 201910780381 A CN201910780381 A CN 201910780381A CN 110357193 A CN110357193 A CN 110357193A
- Authority
- CN
- China
- Prior art keywords
- water
- brine waste
- chamber
- vaporization chamber
- steam
- 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.)
- Withdrawn
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/043—Details
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
- C02F1/048—Purification of waste water by evaporation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/40—Liquid flow rate
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Life Sciences & Earth Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a kind of brine waste evaporated crystallization devices, including send waste water mechanism, send waste water mechanism to be connected with vaporization chamber, brine waste is delivered in vaporization chamber and is evaporated；Vaporization chamber side is connected with heating mechanism, and the other side is connected with the cooling chamber that cooling recycling is carried out to steam；Crystallisation chamber is laid with below the vaporization chamber.By the way that the heat-exchanger pump being vertically connected with is arranged, whole heating can be carried out to vaporization chamber, improves evaporation efficiency；By the way that flow regulator is arranged, the outle water rate of brine waste can control, and measure the volume of the brine waste passed through in water inlet pipe；By the way that crystallisation chamber is arranged, the salt component in waste water can be precipitated and crystallize and recycle；By the way that cooling chamber is arranged, the steam of evolution can be condensed, be allowed to liquefy and be recycled liquefied water；By the way that cartridge filter is arranged, the harmful substance in steam can be adsorbed, so that liquefied water is cleaner, be can be used directly.
Description
Technical field
The present invention relates to a kind of wastewater treatment equipment, specifically a kind of brine waste evaporated crystallization device.
Background technique
The waste water and waste liquid being discharged in art production process, wherein containing the industrial production materials outflowed with water, intermediate production
The pollutant generated in object, byproduct and production process is to cause environmental pollution, especially the major reason of water pollution；It is logical
Often, in industrial wastewater to contain salt, being expelled directly out can cause seriously to pollute to water quality and soil more.The prior art is to brine waste
When being evaporated crystallization, usual waste water is to flow into evaporative crystallization room with constant nonadjustable rate, and be difficult to measure the stream of waste water
Amount；In addition, the steam of evaporation evolution flows directly into air, the waste of energy is caused；Accordingly, it is desirable to provide a kind of influent waste water
Rate is adjustable, flow is statistics available and the device of steam recoverable, to improve the deficiencies in the prior art.
Summary of the invention
The purpose of the present invention is to provide a kind of brine waste evaporated crystallization devices, to solve to propose in above-mentioned background technique
The problem of.
To achieve the above object, the invention provides the following technical scheme:
A kind of brine waste evaporated crystallization device, including waste water mechanism is sent, it is described that waste water mechanism is sent to be connected with vaporization chamber, it will contain
Salt waste water, which is delivered in vaporization chamber, to be evaporated；Vaporization chamber side is connected with heating mechanism, and the other side, which is connected with, carries out steam
The cooling chamber of cooling recycling；Crystallisation chamber is laid with below the vaporization chamber；It is described to send waste water mechanism including being mounted on mounting base
Suction pump on two, suction pump are attached by water inlet pipe and vaporization chamber；It is laid on water inlet pipe to control brine waste
Outle water rate and count brine waste inflow flow regulator；As a further solution of the present invention: the flow
Adjuster includes the flowmeter to measure the brine waste volume that water inlet pipe passes through, be provided with below flowmeter to adjust into
The flow control valve of water pipe outle water rate.
As a further solution of the present invention: the heating mechanism includes the heat-exchanger pump being mounted in mounting base one, hot water
Pump by connecting tube connect with connector there are two heater, heater is connected to up and down the two of vaporization chamber by delivery pipe
End.
As a further solution of the present invention: the vaporization chamber is tank structure, and top is provided with so that heating steam stream
Enter cooling indoor steam return pipe.
As a further solution of the present invention: the crystallisation chamber includes the crystal recycling being connected with vaporization chamber, crystal
Openable partition is laid on recycling can；Crystal recycling can is internally provided with the slide unit of inclination arrangement, and lower section is laid with crystal
Discharge barrel.
As a further solution of the present invention: the cooling chamber includes condensate water pot, and condensate water pot is internally provided with steam
Recovery room, vapor recovery room top are provided with removable filter cylinder, and cartridge filter is provided with miscellaneous to adsorb the nocuousness in steam
The filler of matter；Vapor recovery room lower end is equipped with return pipe, is provided with water inlet pipe and outlet pipe on the outside of the condensate water pot, institute
It states and inlet regulating valve is installed on water inlet pipe.
As a further solution of the present invention: the filler in the cartridge filter is active carbon.
As a further solution of the present invention: the heat-exchanger pump is connected by screw bolts with mounting base one；The suction pump with
Mounting base two is connected by screw bolts.
Compared with prior art, the beneficial effects of the present invention are:
By the way that the heat-exchanger pump being vertically connected with is arranged, whole heating can be carried out to vaporization chamber, improves evaporation efficiency；It is flowed by setting
Adjuster is measured, can control the outle water rate of brine waste, and measure the volume of the brine waste passed through in water inlet pipe；By setting
Crystallisation chamber is set, the salt component in waste water can be precipitated and be crystallized and recycle；It, can be to the steaming of evolution by the way that cooling chamber is arranged
Gas is condensed, and is allowed to liquefy and be recycled liquefied water；It, can be to the nocuousness in steam by the way that cartridge filter is arranged
Substance is adsorbed, so that liquefied water is cleaner, can directly be used.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of brine waste evaporated crystallization device.
Fig. 2 is the structural schematic diagram of the flow regulator of brine waste evaporated crystallization device Zhong Song waste water mechanism.
Fig. 3 is the inlet regulating valve structural schematic diagram of cooling chamber in brine waste evaporated crystallization device.
In figure: 1- heating mechanism, 2- send waste water mechanism, 3- vaporization chamber, 4- crystallisation chamber, 5- cooling chamber, 11- mounting base one,
12- heat-exchanger pump, 13- connecting tube, 14- connector, 15- heater, 16- delivery pipe, 21- mounting base two, 22- suction pump, 23- flow
Adjuster, 24- water inlet pipe, 31- steam return pipe, 41- crystal recycling can, 42- slide unit, 43- crystal discharge barrel, 44- partition,
51- condensate water pot, 52- cartridge filter, 53- water inlet pipe, 54- inlet regulating valve, 55- outlet pipe, 56- return pipe, 57- vapor recovery
Room, 231- flowmeter, 232- flow control valve.
Specific embodiment
Technical solution of the present invention is described in more detail With reference to embodiment.
Embodiment 1
Fig. 1-3, a kind of brine waste evaporated crystallization device are please referred to, including send waste water mechanism 2, it is described to send waste water mechanism 2 and steam
Hair room 3 is connected, and brine waste is delivered in vaporization chamber 3 and is evaporated；3 side of vaporization chamber is connected with heating mechanism 1, another
Side is connected with the cooling chamber 5 that cooling recycling is carried out to steam；The lower section of the vaporization chamber 3 is laid with crystallisation chamber 4；It is described to send waste water
The specific structure of mechanism 2 is without restriction, it is preferred that in the present embodiment, the waste water mechanism 2 includes being mounted in mounting base 2 21
Suction pump 22, suction pump 22 is attached by water inlet pipe 24 with vaporization chamber 3；Flow regulator is laid on water inlet pipe 24
23, to control the outle water rate of brine waste and count the inflow of brine waste.
The specific structure of the flow regulator 23 is without limitation, it is preferred that in the present embodiment, the flow regulator 23
Flow control valve is provided with below flowmeter to measure the volume for the brine waste that water inlet pipe 24 passes through including flowmeter 231
232, to adjust the outle water rate of water inlet pipe 24.
The specific structure of the heating mechanism 1 is without restriction, it is preferred that in the present embodiment, the heating mechanism 1 includes peace
Heat-exchanger pump 12 in mounting base 1, there are two heaters 15 by connecting tube 13 and the connection of connector 14 for heat-exchanger pump 12, add
Hot device 15 is connected to the upper and lower ends of vaporization chamber 3 by delivery pipe 16, integrally to heat to the brine waste in it.
The specific structure of the vaporization chamber 3 is without limitation, it is preferred that in the present embodiment, the vaporization chamber 3 is tank body knot
Structure, top are provided with steam return pipe 31, so that the steam of heating is flowed into cooling chamber 5 by steam return pipe 31；It is described
The specific structure of crystallisation chamber 4 is without limitation, it is preferred that in the present embodiment, the crystallisation chamber 4 includes being connected with vaporization chamber 3
Crystal recycling can 41 is laid with openable partition 44 on crystal recycling can 41 to by the waste water not being fully crystallized and crystallisation chamber
4 separate；Crystal discharge barrel 43 is laid with below crystal recycling can 41, be internally provided with the slide unit 42 of inclination arrangement so that crystal more
In good slide-in crystal discharge barrel 43.
The specific structure of the cooling chamber 5 is without limitation, it is preferred that in the present embodiment, the cooling chamber 5 includes condensed water
Tank 51, condensate water pot 51 are internally provided with vapor recovery room 57, removable filter cylinder 52 are provided with above vapor recovery room 57,
Cartridge filter 52 is provided with filler, to adsorb the objectionable impurities in steam；57 lower end of vapor recovery room is equipped with return pipe 56；
It is provided with water inlet pipe 53 and outlet pipe 55 on the outside of the condensate water pot 51, inlet regulating valve 54 is installed on the water inlet pipe 53.
The specific connection type of the heat-exchanger pump 12 and mounting base 1 is without limitation, it is preferred that described in the present embodiment
Heat-exchanger pump 12 is connected by screw bolts with mounting base 1；Limit is not added in the suction pump 22 and the specific connection type of mounting base 2 21
It is fixed, it is preferred that in the present embodiment, the suction pump 22 is connected by screw bolts with mounting base 2 21.Filling in the cartridge filter 52
The concrete type of object is without limitation, it is preferred that in the present embodiment, the filler in the cartridge filter 52 is active carbon.
The working principle of the present embodiment is:
Start suction pump 22, brine waste is sent into vaporization chamber 3 by water inlet pipe 24, flow regulator 23 is adjusted, to control
The outle water rate of brine waste processed and the inflow for counting brine waste；When brine waste fills in room 3 to be evaporated, closing is drawn water
Pump 22 is opened heat-exchanger pump 12, is heated simultaneously to the upper and lower side of vaporization chamber 3, so that steam is escaped by steam return pipe 31；Wait steam
After sending out the brine waste evaporating completely in room 3, heat-exchanger pump 12 is closed, opens partition 44, so that crystal is slipped to by slide unit 42
Crystal discharge barrel 43 is recycled；Steam reaches cartridge filter 52 through steam return pipe 31, by the active carbon filled in it to steam
In harmful substance adsorbed；Meanwhile cooling water is flowed into condensate water pot 51 through water inlet pipe 53 and is cooled down to steam, through steaming
Cooling water after gas thermalization is flowed out through outlet pipe 55, realizes circulating cooling；And it is adjusted according to the adjustable water inlet of the rate of evaporation of vapours
Valve 54 is saved to control cooling water outle water rate；After steam liquefaction, flow out to realize the recycling benefit to steam by return pipe 56
With.
Embodiment 2
For steam in embodiment 1 after the suction-operated of cartridge filter 52, liquefied water is very clean, but clean cost compared with
Height needs to replace active carbon often；In order to reduce cost, and the thermal energy of steam is utilized, the present embodiment is in embodiment 1
On the basis of improve, improvements are as follows: by cooling chamber 5 cartridge filter remove, by water inlet pipe 53 and outlet pipe 55 and pot
Furnace connects to form circulation, utilizes the cold water in the heat boiler of steam, energy conservation and environmental protection；Though and liquefied water without absorption,
It still can be applied to most occasions in addition to drinking, both realized the recycling of steam, and also saved cost.
Better embodiment of the invention is explained in detail above, but the present invention is not limited to above-mentioned embodiment party
Formula within the knowledge of one of ordinary skill in the art can also be without departing from the purpose of the present invention
Various changes can be made.
Claims (8)
1. a kind of brine waste evaporated crystallization device, including send waste water mechanism (2), which is characterized in that it is described to send waste water mechanism (2)
It is connected with vaporization chamber (3)；Vaporization chamber (3) side is connected with heating mechanism (1), and the other side, which is connected with, cools back steam
The cooling chamber (5) of receipts；Crystallisation chamber (4) are laid with below the vaporization chamber (3)；It is described to send waste water mechanism (2) including being mounted on
Suction pump (22) in mounting base two (21), suction pump (22) are attached by water inlet pipe (24) with vaporization chamber (3)；Water inlet pipe
(24) it is laid with the outle water rate to control brine waste on and counts the flow regulator (23) of the inflow of brine waste.
2. brine waste evaporated crystallization device according to claim 1, which is characterized in that flow regulator (23) packet
The flowmeter (231) to measure the brine waste volume that water inlet pipe passes through is included, is provided with below flowmeter (231) to adjust
The flow control valve (232) of water inlet pipe (24) outle water rate.
3. brine waste evaporated crystallization device according to claim 2, which is characterized in that the heating mechanism (1) includes
The heat-exchanger pump (12) being mounted in mounting base one (11), heat-exchanger pump (12) pass through there are two connecting tube (13) and connector (14) connections
Heater (15), heater (15) are connected to the upper and lower ends of vaporization chamber (3) by delivery pipe (16).
4. brine waste evaporated crystallization device according to claim 3, which is characterized in that the vaporization chamber (3) is tank body
Structure, top is provided with so that steam flows into the steam return pipe (31) in cooling chamber (5).
5. brine waste evaporated crystallization device according to claim 1, which is characterized in that the crystallisation chamber (4) include with
The crystal recycling can (41) that vaporization chamber (3) is connected is laid with openable partition (44) on crystal recycling can (41)；Crystal returns
Closed cans (41) is internally provided with the slide unit (42) of inclination arrangement, and lower section is laid with crystal discharge barrel (43).
6. brine waste evaporated crystallization device according to claim 4, which is characterized in that the cooling chamber (5) includes cold
Condensate tank (51), condensate water pot (51) are internally provided with vapor recovery room (57), are provided with above vapor recovery room (57) removable
The cartridge filter (52) unloaded, cartridge filter (52) are provided with the filler to adsorb objectionable impurities in steam；Vapor recovery room (57)
Lower end is equipped with return pipe (56), is provided with water inlet pipe (53) and outlet pipe (55) on the outside of the condensate water pot (51), it is described into
Inlet regulating valve (54) are installed on water pipe (53).
7. brine waste evaporated crystallization device according to claim 6, which is characterized in that filling out in the cartridge filter (52)
Filling object is active carbon.
8. brine waste evaporated crystallization device according to claim 1, which is characterized in that the heat-exchanger pump (12) and installation
One (11) of seat are connected by screw bolts；The suction pump (22) is connected by screw bolts with mounting base two (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910780381.2A CN110357193A (en) | 2019-08-22 | 2019-08-22 | A kind of brine waste evaporated crystallization device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910780381.2A CN110357193A (en) | 2019-08-22 | 2019-08-22 | A kind of brine waste evaporated crystallization device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN110357193A true CN110357193A (en) | 2019-10-22 |
Family
ID=68225165
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910780381.2A Withdrawn CN110357193A (en) | 2019-08-22 | 2019-08-22 | A kind of brine waste evaporated crystallization device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110357193A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646624A (en) * | 2020-06-11 | 2020-09-11 | 临海市泰通医化设备有限公司 | Organic salt recovery separator |
| CN113105047A (en) * | 2021-03-01 | 2021-07-13 | 徐胡斌 | Industrial high-salinity wastewater evaporative crystallization device convenient to recycle |
| CN117819643A (en) * | 2024-02-27 | 2024-04-05 | 山东玉鑫环保科技股份有限公司 | Recovery processing system of high salt wastewater |
-
2019
- 2019-08-22 CN CN201910780381.2A patent/CN110357193A/en not_active Withdrawn
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111646624A (en) * | 2020-06-11 | 2020-09-11 | 临海市泰通医化设备有限公司 | Organic salt recovery separator |
| CN111646624B (en) * | 2020-06-11 | 2022-07-12 | 临海市泰通医化设备有限公司 | Organic salt recovery separator |
| CN113105047A (en) * | 2021-03-01 | 2021-07-13 | 徐胡斌 | Industrial high-salinity wastewater evaporative crystallization device convenient to recycle |
| CN117819643A (en) * | 2024-02-27 | 2024-04-05 | 山东玉鑫环保科技股份有限公司 | Recovery processing system of high salt wastewater |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110357193A (en) | A kind of brine waste evaporated crystallization device | |
| CN104707349A (en) | Plate evaporator type MVC heat pump evaporation system | |
| CN106766342A (en) | Ammonia still process column overhead ammonia vapour residual heat system is reclaimed using lithium bromide absorption type heat pump | |
| CN103808178B (en) | A kind of sub-control phase-change heat exchange system based on hierarchical composition heat exchange and heat-exchange method | |
| CN104922921B (en) | A kind of self-loopa MVR thermo-compression evaporation systems | |
| CN209371289U (en) | A kind of condensing combustion system | |
| CN203810940U (en) | Cooling water medium-frequency induction heating system | |
| CN108905257A (en) | A kind of waste-heat recovery device of product equipment for purifying | |
| CN109453611B (en) | Condensate recycling system for high-temperature flue gas | |
| CN107510949A (en) | A kind of MVR vapo(u)rization systems | |
| CN106931682A (en) | Air-conditioning system | |
| CN204806354U (en) | Heat pipe formula falling film evaporation low temperature waste heat utilization and water -recovery apparatus | |
| CN208959348U (en) | A kind of evaporation concentration device of feed liquid | |
| CN207532807U (en) | A kind of MVR vapo(u)rization systems | |
| CN206051600U (en) | A kind of low-temperature evaporation crystal system for processing thermal power plant's high slat-containing wastewater | |
| CN209668807U (en) | A kind of vapo(u)rization system of high siliceous oil field produced water treatment | |
| CN109798583A (en) | A kind of heat pump heat distribution system comprehensively utilizing flue gas and exhaust steam residual heat | |
| CN108662915A (en) | The indirect heat exchange vaporization type condensing system of the general vapour of concentration evaporator system end effect | |
| CN205403238U (en) | Take gas gas heater's two -period form flue gas hot water type lithium bromide absorbed refrigeration machine | |
| CN211770387U (en) | Waste water recovery device for high-temperature gas condenser | |
| CN209475918U (en) | The condensation water recovery and use system of high temperature cigarette vapour | |
| CN111333243A (en) | Small-size water purification unit of distillation formula | |
| CN209195836U (en) | A kind of novel constant-temperature formula hydraulic station fuel tank | |
| WO2022206015A1 (en) | Flue gas waste heat and condensate water recovery system for gas-fired hot water boiler | |
| CN109502868B (en) | Control method for sewage treatment with three-in-one structure |
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 | ||
| WW01 | Invention patent application withdrawn after publication |
Application publication date: 20191022 |
|
| WW01 | Invention patent application withdrawn after publication |