CN207270730U - Evaporating, concentrating and crystallizing system - Google Patents
Evaporating, concentrating and crystallizing system Download PDFInfo
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- CN207270730U CN207270730U CN201721294628.2U CN201721294628U CN207270730U CN 207270730 U CN207270730 U CN 207270730U CN 201721294628 U CN201721294628 U CN 201721294628U CN 207270730 U CN207270730 U CN 207270730U
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Abstract
The utility model discloses evaporating, concentrating and crystallizing system, wherein evaporating, concentrating and crystallizing system includes air heater, crystallizing evaporator, wind turbine, condenser and connecting pipe；Connect to form closed-cycle system by multistage connecting pipe between air heater, crystallizing evaporator, wind turbine, condenser；Air heater includes cold wind import, hot-blast outlet, Heating medium, heating agent outlet, heater body and air flow conduit；Crystallizing evaporator includes hot wind inlet, hot-blast outlet, material inlet to be evaporated, material outlet and evacuation port, material-feeding port, vaporization chamber and circulating pump；And flusher is additionally provided with the top of vaporization chamber；Condenser carries out condensation process by coolant media to the air of surrounding.Evaporating, concentrating and crystallizing system provided by the utility model, the problem of avoiding the occurrence of fouling, while it with easy to operate, system effectiveness is than higher, all many technical advantages such as stability and equipment dependability are stronger.
Description
Technical field
It the utility model is related to evaporation technique field, more particularly to evaporating, concentrating and crystallizing system.
Background technology
Existing evaporation technique mainly has multiple-effect evaporation and steam mechanical to recompress two kinds of forms.
Wherein, multiple-effect evaporation is that waste water is heated using original steam as heat source, makes moisture evaporation, its steaming produced
The heat source (i.e. heat transfer medium is water) that vapour is evaporated as next stage, carries out, so as to fulfill the cascade utilization of energy, reaches section successively
Can purpose；
Wherein, steam mechanical recompression system refers to the steam that evaporator produces being compressed by vapour compression machine,
Improve its enthalpy, then using compressed steam as heat source (i.e. heat transfer medium is vapor) treat evaporation material (such as：It is useless
Liquid) heated, make its evaporation.
It will be apparent that all there are the objective technical disadvantages of some for above-mentioned vapo(u)rization system of the prior art：Such as：(1) it is existing
The heat transfer for having two kinds of evaporation techniques is all to conduct heat to complete by dividing wall type, and inevitably there are fouling for dividing wall type heat transfer evaporation
Risk；(2) multiple-effect evaporation high energy consumption, attended operation task amount is big, and system effectiveness is than low；Steam mechanical recompression system uses
Vapour compression machine, therefore it is required that what steam caused by waste liquid evaporation should be as few as possible contains other escaping gases, in order to avoid
The reduction of compressor performance is caused, needs complicated pretreatment system could normal use into vapo(u)rization system waste liquid for this.
To sum up, how to overcome the above-mentioned technological deficiency of traditional vapo(u)rization system is that those skilled in the art are badly in need of asking for solution
Topic.
Utility model content
The purpose of this utility model is to provide a kind of evaporating, concentrating and crystallizing system, to solve the above problems.
In order to achieve the above object, the technical solution of the utility model is realized in：
The utility model provides a kind of evaporating, concentrating and crystallizing system, including air heater, crystallizing evaporator, wind turbine,
Condenser and connecting pipe；
Pass through multistage connecting pipe between the air heater, the crystallizing evaporator, the wind turbine, the condenser
Connection forms closed-cycle system；
The air heater includes cold wind import, hot-blast outlet, Heating medium, heating agent outlet, heater body and sky
Air-flow is threaded a pipe；The air flow conduit is used for ventilating air, and the both ends of the air flow conduit be respectively communicated with it is described
Cold wind import and the hot-blast outlet；The Heating medium is used to be passed through heating agent；The heating agent outlet is used to discharge heating agent；It is described
The heating agent that heater body is used to be passed through carries out heat exchange processing to the air in the air flow conduit；
The crystallizing evaporator include hot wind inlet, hot-blast outlet, material inlet to be evaporated, material outlet and evacuation port,
Material-feeding port, vaporization chamber and circulating pump；And flusher is additionally provided with the top of the vaporization chamber, the bottom of the vaporization chamber is set
There is reservoir；The flusher is connected with material inlet to be evaporated；The reservoir is connected with the material outlet；The spray
Device is spilt to be used to carry out sprinkling processing to the waste liquid entered from material inlet to be evaporated and then connect with evaporating indoor air
Touch；The reservoir is used for the waste liquid for collecting the vaporization chamber bottom；The circulating pump is arranged on the material inlet to be evaporated
On pipeline between the material outlet；The circulating pump, which is used to continuously circulate, to be discharged from the material outlet of vaporization chamber bottom
Waste liquid, the flusher being pumped at the top of vaporization chamber；The hot wind inlet passes through connecting pipe and the air heater
Hot-blast outlet connects, and the hot-blast outlet passes through connecting pipe and the inlet communication of the wind turbine；The vaporization chamber passes through heating
Air afterwards is evaporated waste liquid processing；
The wind turbine, which is used to drive, drives air to be circulated in closed-cycle system；
The condenser include condenser hot wind inlet, cold wind outlet, cooling water inlet, warm water export and condenser body,
Refrigerant delivery heat transfer device；The condenser hot wind inlet is used to be passed through damp-heat air；The cold wind outlet is used to export condensation
Air afterwards；The refrigerant delivery heat transfer device is respectively communicated with cooling water inlet and warm water outlet；The cooling water inlet is used for cold
Coolant media is passed through in condenser body；The warm water outlet is used to discharge the intrinsic coolant media of the condenser；It is described
Condenser body is used to carry out condensation process to the air of surrounding by the coolant media in the refrigerant delivery heat transfer device.
Preferably, can embodiment as one kind；The top of the vaporization chamber is rectangular shape, under the vaporization chamber
Portion is pyramidal shape.
Preferably, can embodiment as one kind；The material outlet and the evacuation port are located at lower cone body portion
On；Hot wind inlet, hot-blast outlet, the material inlet to be evaporated, material-feeding port are located on Upper cylindrical body portion.
Preferably, can embodiment as one kind；Pipeline between the material inlet to be evaporated and the material outlet
On be provided with flow control valve.
Preferably, can embodiment as one kind；The lower section for being internally located at the flusher of the vaporization chamber is set
There is one layer of filler.
Preferably, can embodiment as one kind；The evaporating, concentrating and crystallizing system further includes sludge preheating device；It is described
Sludge preheating device is used to heat the waste liquid before entering the crystallizing evaporator in advance.
Preferably, can embodiment as one kind；The sludge preheating device is heater or heat exchanger.
Preferably, can embodiment as one kind；The evaporating, concentrating and crystallizing system further includes solid-liquid separating equipment；It is described
Solid-liquid separating equipment is used to carry out solid-liquid separation treatment to the material discharged from crystallizing evaporator and then obtains crystalline particle.
Preferably, can embodiment as one kind；The air heater is finned tube exchanger or plate type heat exchanger.
Preferably, can embodiment as one kind；The wind turbine is axial fan or centrifugal fan.
Compared with prior art, it is the advantages of the utility model embodiment：
A kind of evaporating, concentrating and crystallizing system provided by the utility model, the evaporation that analysis the utility model embodiment provides are dense
The primary structure of contracting crystal system is understood：
Above-mentioned evaporating, concentrating and crystallizing system is mainly by air heater, crystallizing evaporator, wind turbine, condenser and connecting pipe
Formed etc. structure；
Wherein, the air heater includes cold wind import, hot-blast outlet, Heating medium, heating agent outlet, heater body
And air flow conduit；The heating agent that the heater body is used to be passed through carries out the air in the air flow conduit
Heat exchange processing；
The crystallizing evaporator include hot wind inlet, hot-blast outlet, material inlet to be evaporated, material outlet and evacuation port,
Material-feeding port, vaporization chamber and circulating pump；And flusher is additionally provided with the top of the vaporization chamber, the bottom of the vaporization chamber is set
There is reservoir；The flusher connects the reservoir with material inlet to be evaporated and is connected with the material outlet；The spray
Device is spilt to be used to carry out sprinkling processing to the waste liquid entered from material inlet to be evaporated and then connect with evaporating indoor air
Touch；The reservoir is used for the waste liquid for collecting the vaporization chamber bottom；The circulating pump is arranged on the material inlet to be evaporated
With on the pipeline of the material outlet；The circulating pump will discharge useless for continuously circulation from the material outlet of vaporization chamber bottom
Liquid, the flusher being pumped at the top of vaporization chamber；The hot wind inlet passes through connecting pipe and the hot wind of the air heater
Outlet, the hot-blast outlet pass through connecting pipe and the inlet communication of the wind turbine；After the vaporization chamber is by heating
Air is evaporated waste liquid processing；
The wind turbine, which is used to drive, drives air to be circulated in closed-cycle system；
The condenser is used to carry out the air of surrounding by the coolant media in the refrigerant delivery heat transfer device cold
Solidifying processing.
Wherein, mostly important structure is：Above-mentioned evaporating, concentrating and crystallizing system system architecture design and it is wherein specific
Each processing equipment connection relation and structure partial etc.；Evaporating, concentrating and crystallizing system provided by the utility model, it will
Each processing equipment carries out organically restructuring and according to certain layout designs and the supporting setting of connection mode order, composition one kind
Brand-new directly heated evaporation and crystallization system；
In general, crystallizing evaporator can be divided into two classes by mode of heating：It is with treating by heat source that direct heat source, which heats it,
The material mixing of evaporation, the method for evaporating the vapor in its material to be evaporated.Indirect heat source heating, container partition are transmitted to
The solution being evaporated.The diabatic process carried out i.e. in dividing wall type heat exchanger.It will be apparent that evaporation and concentration provided by the utility model
Crystal system, belongs to preceding one kind, it is used directly is mixed to make the water in waste liquid by heat source (i.e. heated air) with waste liquid
Evaporation of vapours is finally repeated multiple times, and when liquid waste concentration exceedes its saturated concentration, then its spontaneous nucleation forms crystalline particle.
Evaporating, concentrating and crystallizing system provided by the utility model, avoids the design using traditional dividing wall type heat transfer evaporation,
It uses clean heated air to come into full contact with mode to sprinkling waste liquid and directly by the moisture in thermal evaporation its waste liquid, avoid out
The problem of existing fouling；The evaporating, concentrating and crystallizing system at the same time, easy to operate, system effectiveness is than higher, compared to traditional evaporation equipment
With stronger stability and equipment dependability.
Brief description of the drawings
, below will be right in order to illustrate more clearly of the utility model embodiment or technical solution of the prior art
Embodiment or attached drawing needed to be used in the description of the prior art are briefly described, it should be apparent that, describe below
In attached drawing be the utility model some embodiments, for those of ordinary skill in the art, do not paying creativeness
On the premise of work, other attached drawings can also be obtained according to these attached drawings.
Fig. 1 is the configuration diagram for the evaporating, concentrating and crystallizing system that the utility model embodiment provides；
Fig. 2 is the partial enlargement knot of the air heater in the evaporating, concentrating and crystallizing system that the utility model embodiment provides
Structure schematic diagram；
Fig. 3 is the partial enlargement knot of the crystallizing evaporator in the evaporating, concentrating and crystallizing system that the utility model embodiment provides
Structure schematic diagram；
Fig. 4 is that the partial enlargement structure of the condenser in the evaporating, concentrating and crystallizing system that the utility model embodiment provides is shown
It is intended to.
Label：
1- air heaters；101- cold wind imports；103- hot-blast outlets；103- Heating mediums；104- heating agents export；
105- heater bodies；
2- crystallizing evaporators；201- hot wind inlets；202- hot-blast outlets；203- material inlets to be evaporated；204- materials go out
Mouthful；205- evacuation ports；206- material-feeding ports；207- vaporization chambers；
3- wind turbines；
4- condensers；401- condenser hot wind inlets；402- cold wind exports；403- cooling water inlets；404- warm water exports；
405- condenser bodies；406- refrigerant delivery heat transfer devices；
5- connecting pipes.
Embodiment
The technical solution of the utility model is clearly and completely described below in conjunction with attached drawing, it is clear that described
Embodiment is the utility model part of the embodiment, instead of all the embodiments.Based on the embodiment in the utility model, sheet
Field those of ordinary skill all other embodiments obtained without making creative work, belong to this practicality
Novel protected scope.
, it is necessary to explanation in the description of the utility model, term " " center ", " on ", " under ", it is "left", "right", " perpendicular
Directly ", the orientation of the instruction such as " level ", " interior ", " outer " or position relationship are based on orientation shown in the drawings or position relationship, are only
Described for the ease of description the utility model and simplifying, rather than instruction or imply signified device or element must have it is specific
Orientation, with specific azimuth configuration and operation, therefore it is not intended that limitation to the utility model.In addition, term " the
One ", " second ", " the 3rd " are only used for description purpose, and it is not intended that instruction or hint relative importance.
, it is necessary to which explanation, unless otherwise clearly defined and limited, term " are pacified in the description of the utility model
Dress ", " connected ", " connection " should be interpreted broadly, for example, it may be fixedly connected or be detachably connected, or integratedly
Connection；Can mechanically connect or be electrically connected；It can be directly connected, can also be indirectly connected by intermediary,
It can be the connection inside two elements.For the ordinary skill in the art, above-mentioned art can be understood with concrete condition
Concrete meaning of the language in the utility model.
The utility model is further described in detail below through specific implementation examples and in conjunction with the accompanying drawings.
Referring to Fig. 1, Fig. 2 and Fig. 3 and Fig. 4, a kind of evaporating, concentrating and crystallizing system of the utility model embodiment offer, bag
Include air heater 1, crystallizing evaporator 2, wind turbine 3, condenser 4 and connecting pipe 5；
Connected between the air heater 1, the crystallizing evaporator 2, the wind turbine 3, the condenser 4 by multistage
The connection of pipeline 5 forms closed-cycle system；
The air heater 1 include cold wind import 101, hot-blast outlet 103, Heating medium 103, heating agent outlet 104,
Heater body 105 and air flow conduit；The air flow conduit is used for ventilating air, and the air flow conduit
Both ends are respectively communicated with the cold wind import 101 and the hot-blast outlet 103；The Heating medium 103 is used to be passed through heating agent；It is described
Heating agent outlet 104 is used to discharge heating agent；The heating agent that the heater body 105 is used to be passed through is to the air flow conduit
Interior air carries out heat exchange processing；
The crystallizing evaporator 2 includes hot wind inlet 201, hot-blast outlet 202, material inlet to be evaporated 203, material outlet
204 and evacuation port 205, material-feeding port 206, vaporization chamber 207 and circulating pump (crystallizing evaporator 2 is tower evaporation crystallizer)；And
The top of the vaporization chamber 207 is additionally provided with flusher (not shown), and the bottom of the vaporization chamber 207 is provided with storage
Liquid bath (not shown)；The flusher is connected with material inlet 203 to be evaporated；The reservoir and the material outlet
204 connections；The flusher be used to the waste liquid that enters from material inlet 203 to be evaporated spray processing so that with evaporation
Air in room 207 is contacted；The reservoir is used for the waste liquid for collecting 207 bottom of vaporization chamber；The circulating pump is set
Put on the pipeline between the material inlet 203 to be evaporated and the material outlet 204；The circulating pump is used to continuously circulate
The waste liquid that will be discharged from the material outlet 204 of 207 bottom of vaporization chamber, is pumped to the flusher at the top of vaporization chamber 207；It is described
Hot wind inlet 201 is connected by connecting pipe with the hot-blast outlet of the air heater 1, and the hot-blast outlet 202 passes through
Connecting pipe and the inlet communication of the wind turbine 3；The vaporization chamber 207 is evaporated waste liquid at place by the air after heating
Reason；
The wind turbine 3, which is used to drive, drives air to be circulated in closed-cycle system；
The condenser 4 includes condenser hot wind inlet 401, cold wind outlet 402, cooling water inlet 403, warm water outlet 404
With condenser body 405, refrigerant delivery heat transfer device 406；The condenser hot wind inlet 401 is used to be passed through damp-heat air；Institute
Cold wind outlet 402 is stated to be used to export condensed air；The refrigerant delivery heat transfer device 406 is respectively communicated with cooling water inlet and temperature
Water out；The cooling water inlet 403 is used to be passed through coolant media into condenser body；The warm water outlet 404 is used for institute
State the intrinsic coolant media discharge of condenser；The condenser body 405 is used to pass through the refrigerant delivery heat transfer device 406
Interior coolant media carries out condensation process to the air of surrounding.
The primary structure for analyzing the evaporating, concentrating and crystallizing system that above-mentioned the utility model embodiment provides is understood：
Above-mentioned evaporating, concentrating and crystallizing system is mainly by air heater 1, crystallizing evaporator 2, wind turbine 3, condenser 4 and connection
The structures such as pipeline 5 are formed；Pass through between the air heater 1, the crystallizing evaporator 2, the wind turbine 3, the condenser 4
The connection of multistage connecting pipe 5 forms closed-cycle system；
Wherein, the air heater 1 includes cold wind import 101, hot-blast outlet 103, Heating medium 103, heating agent outlet
104th, heater body 105 and air flow conduit；The heating agent that the heater body 105 is used to be passed through is to the air
Air in circulation duct carries out heat exchange processing；
The crystallizing evaporator 2 includes hot wind inlet 201, hot-blast outlet 202, material inlet to be evaporated 203, material outlet
204 and evacuation port 205, material-feeding port 206, vaporization chamber 207 and circulating pump；And the top of the vaporization chamber 207 is additionally provided with sprinkling
Device, the bottom of the vaporization chamber 207 are provided with reservoir；The flusher is connected with material inlet 203 to be evaporated；Institute
Reservoir is stated to connect with the material outlet 204；The flusher is used for the waste liquid to entering from material inlet 203 to be evaporated
Carry out sprinkling processing and then contacted with the air in vaporization chamber 207；The reservoir is used to collect 207 bottom of vaporization chamber
The waste liquid in portion；The circulating pump is arranged on the pipeline between the material inlet to be evaporated 203 and the material outlet 204；
The circulating pump is used to continuously circulate the waste liquid that will be discharged from the material outlet 204 of 207 bottom of vaporization chamber, is pumped to vaporization chamber
The flusher at 207 tops；The hot wind inlet 201 is connected by the hot-blast outlet of connecting pipe and the air heater 1
Logical, the hot-blast outlet 202 passes through connecting pipe and the inlet communication of the wind turbine 3；After the vaporization chamber 207 is by heating
Air processing is evaporated to waste liquid；
The wind turbine 3, which is used to drive, drives air to be circulated in closed-cycle system；
The condenser 4 be used for by the coolant media in the refrigerant delivery heat transfer device 406 to the air of surrounding into
Row condensation process.
Wherein, mostly important structure is：Above-mentioned evaporating, concentrating and crystallizing system system architecture design and it is wherein specific
Each processing equipment connection relation and structure partial etc.；Evaporating, concentrating and crystallizing system provided by the utility model, it will
Each processing equipment carries out organically restructuring and according to certain layout designs and the supporting setting of connection mode order, composition one kind
Brand-new directly heated evaporation and crystallization system；It is relatively low using the opposite wetland after heating in the utility model embodiment
Air is directly contacted with waste liquid material to be evaporated, utilizes hygroscopicity (the heat vapour in moisture absorption air of dry air
Change and form water vapour) moisture in waste liquid is carried away, complete the process of evaporation.
In general, crystallizing evaporator can be divided into two classes by mode of heating：It is with treating by heat source that direct heat source, which heats it,
The material mixing of evaporation, the method for evaporating the vapor in its material to be evaporated.Indirect heat source heating, container partition are transmitted to
The solution being evaporated.The diabatic process carried out i.e. in dividing wall type heat exchanger.It will be apparent that evaporation and concentration provided by the utility model
Crystal system, belongs to preceding one kind, it is used directly is mixed to make the water in waste liquid by heat source (i.e. heated air) with waste liquid
Evaporation of vapours is finally repeated multiple times, and when liquid waste concentration exceedes its saturated concentration, then its spontaneous nucleation forms crystalline particle.
Evaporating, concentrating and crystallizing system provided by the utility model, avoids the design using traditional dividing wall type heat transfer evaporation,
It uses clean heated air to come into full contact with mode to sprinkling waste liquid and directly by the moisture in thermal evaporation its waste liquid, avoid out
The problem of existing fouling；The evaporating, concentrating and crystallizing system at the same time, easy to operate, system effectiveness is than higher, compared to traditional evaporation equipment
With stronger stability and equipment dependability.
The concrete structure and particular technique of the evaporating, concentrating and crystallizing system provided below the utility model embodiment are imitated
Fruit, which is cooked, to be described in detail：
Preferably, can embodiment as one kind；The top of the vaporization chamber 207 is rectangular shape, the vaporization chamber
207 lower part is pyramidal shape.
Preferably, can embodiment as one kind；The material outlet 204 and the evacuation port 205 are located at lower cone
On body portion；Hot wind inlet 201, hot-blast outlet 202, the material inlet 203 to be evaporated, material-feeding port 206 are located at Upper cylindrical
On body portion.
Preferably, can embodiment as one kind；Between the material inlet to be evaporated 203 and the material outlet 204
Pipeline on be provided with flow control valve.In addition, it can be filled in above-mentioned vaporization chamber 207 with some other controls of installation settings
Put, such as fluid level control device；Above-mentioned fluid level control device can coordinate the indoor waste liquid of control evaporation and only deposit situation, ensure useless
The smooth circulation cycle of liquid.
Preferably, can embodiment as one kind；Being internally located at below the flusher for the vaporization chamber 207 is set
It is equipped with one layer of filler.
It should be noted that hot-air contact with the waste liquid of concentration to be evaporated is completed in evaporator, any shape
The evaporator of formula is within the scope of the utility model.Evaporator can use no-arbitrary pricing form, and can also use has filler
Form, there is filler to increase air and the surface area of water contact.
Preferably, can embodiment as one kind；The evaporating, concentrating and crystallizing system further includes sludge preheating device；It is described
Sludge preheating device is used to heat the waste liquid before entering the crystallizing evaporator in advance.The pre- hot charging of sludge
It is set to heater.
It should be noted that whether waste liquid does not change the reality of the utility model before evaporator is entered by heating
Matter, by pre-warmed waste liquid, can wherein absorb the sensible heat obtained in warm during moisture evaporation；Without pre-
The waste liquid of heating, then the required heat of moisture evaporation mostly come from the heat in air.But in order to improve condensation recycling heat
Amount using possibility preheating then carried out to sludge be helpful.
Preferably, can embodiment as one kind；The evaporating, concentrating and crystallizing system further includes solid-liquid separating equipment；It is described
Solid-liquid separating equipment is used to carry out solid-liquid separation treatment to the material discharged from crystallizing evaporator and then obtains crystalline particle.
Preferably, can embodiment as one kind；The air heater 1 exchanges heat for finned tube exchanger or plate-sheet-type
Device.
It should be noted that air heater 1 is completed using heat exchanger, but the form with heat exchanger is unrelated, nothing
By being finned tube exchanger, or plate type heat exchanger, or other any type of exchange heat belong to the category of the utility model；
Heat air heat source can in a variety of forms, any type heat resource form all within the category of the utility model, including steam,
Waste heat flue gas, hot water or conduction oil, or other any media with heat.
The above-mentioned condenser 4 in the utility model embodiment is also not necessarily limited to specific structure type at the same time；The reality of condenser
Matter is also heat exchanger, and the heat exchanger of the either any type of heat exchanger directly contacted or any type of indirect heat exchange is all
Originally the category of utility model is being belonged to.
Preferably, can embodiment as one kind；The wind turbine 3 is axial fan or centrifugal fan.
It should be noted that the essence of condenser is also heat exchanger, the either any type of heat exchanger directly contacted
Or the heat exchanger of any type of indirect heat exchange is all originally belonging to the category of utility model.
Correspondingly, the invention also discloses a kind of evaporation process method, implemented by evaporating, concentrating and crystallizing system useless
Liquid evaporation process, including following operating procedure：
Air heater 1 carries out heating operation using heating agent to air：The Heating medium that heating agent passes through air heater 1
103 enter and are exported from heating agent outlet 104；Meanwhile heating agent to the air that is passed into from cold wind import 101 in heat exchanger body into
Row heating, and follow-up crystallizing evaporator 2 is exited into by hot-blast outlet 103；
Crystallizing evaporator 2 is to carrying out waste liquid using the air after heating heated evaporation process：Air after heating is from warm
Wind inlet 201 enters vaporization chamber 207, and is discharged from hot-blast outlet 202, and directly to the sprinkling in the vaporization chamber 207
The waste liquid that device sprays from top to bottom carries out heated evaporation process；Meanwhile waste liquid enters from material inlet 203 to be evaporated, and from
Material outlet 204 is discharged；Meanwhile circulating pump continuously circulates the waste liquid that will be discharged from the material outlet 204 of 207 bottom of vaporization chamber,
It is pumped to the flusher at the top of vaporization chamber 207；It should be noted simultaneously that in the process, flusher is used for from treating
The waste liquid that evaporation material inlet 203 enters carries out sprinkling processing and then is contacted with the air in vaporization chamber 207；The liquid storage
Groove is used for the waste liquid for collecting 207 bottom of vaporization chamber；
The driving of wind turbine drives the damp-heat air exported by crystallizing evaporator 2 to enter condenser 4；
Condenser 4 performs the condensation process to damp-heat air：Condenser hot wind inlet 401 is passed through damp-heat air；Cold wind goes out
The condensed air of the output of mouth 402；Cooling water inlet 403 is passed through coolant media into condenser body 405；Warm water outlet 404 will
Coolant media discharge in the condenser body 405；Meanwhile condenser body 405 passes through refrigerant delivery heat transfer device 406
Interior coolant media carries out condensation process to the damp-heat air of surrounding, and the air circulation after condensation process is delivered to the air
At the cold wind import 101 of heater 1.
It should be noted that in the evaporation process method that the utility model implementation is related to；First by heater by sky
Gas is heated, heater use indirect heat transfer heater, heating agent can use conduction oil, hot water or other contain heat
The medium of amount, such as waste heat flue gas.As air is heated, the relative humidity of air is gradually reduced, and the air after heating is led to
Enter vaporization chamber, air is directly contacted with the waste liquid that vaporization chamber gets off from top spray, conducted heat and realize the heat absorption of moisture
Vaporization.Entering the waste liquid of vaporization chamber can be heated in advance, after hot dry air is contacted with waste liquid, the water in waste liquid
Divide the heat vaporization absorbed in dry air, so as to escape from waste liquid and form water vapour, air is due to absorbing moisture at this time
And form the damp-heat air of certain humidity.Damp-heat air, enters condensation from evaporator out under the driving of wind turbine
Device.Condenser can use direct or indirect heat exchanger, and refrigerant can use water at low temperature or other media, damp-heat air by with
Water at low temperature exchanges heat, and with the reduction of air themperature, relative humidity gradually increases in air, when reaching 100%, then air
In vapor then condense into water droplet so that from air out, so as to complete the removing of moisture.Air after cooling is from condensation
Device come out after under the driving of wind turbine, turn again to heater, be heated again, reduce humidity, be heated after air again
Drier is admitted to, circulation successively is gone down.
As the moisture in evaporator constantly evaporates, the concentration of pollutant gradually steps up in liquid, so as to reach concentration
Purpose.When the concentration of saline pollution material therein exceedes its saturated concentration, then its spontaneous nucleation forms crystalline particle.Crystallization
Salt then deposits to the bottom of vaporization chamber, and discharges evaporator by the facility of salt discharge, then by separation of solid and liquid facility by crystal salt
It is completely separated out from liquid.Indoor waste liquid is evaporated by the exterior continuous reciprocation cycle of circulating pump, i.e. circulating pump is from steaming
Send out the water suction of room bottom reservoir, the flusher being pumped at the top of vaporization chamber, waste liquid uniformly sprayed through flusher and
Under, conducted heat and evaporated with air during falling, unevaporated waste liquid then falls and is pooled to the liquid storage of bottom again
Groove, successively constantly circulation.During circulation, a degree of heating, heat can carry out waste liquid by a heat exchanger
Source can derive from waste hot steam, waste heat flue gas, conduction oil, hot water or heat pump system water outlet etc..
Within the condenser, since coolant media absorbs the heat of air and moisture in air condensation process is discharged
The latent heat come, therefore, can be according to physical condition to being used to heat, so as to achieve the purpose that energy saving of system.
The evaporating, concentrating and crystallizing system that the utility model embodiment provides has the technical advantage of following aspect：
First, the evaporating, concentrating and crystallizing system that the utility model embodiment provides, it is mainly by air heater, evaporative crystallization
The structures such as device, wind turbine, condenser and connecting pipe are formed；At the same time, above-mentioned each device part has special structure
Design, and between concrete structure device connect, be laid out etc. all have cleverly design；Therefore, the utility model embodiment provides
Evaporating, concentrating and crystallizing system, its design is more reasonable, and system architecture is more novel, function is more perfect.The utility model carries
The evaporating, concentrating and crystallizing system of confession, each processing equipment is carried out organically restructuring and according to certain layout designs and connection by it
The supporting setting of mode order, forms a kind of brand-new directly heated evaporation and crystallization system；
2nd, the evaporating, concentrating and crystallizing system that the utility model embodiment provides, it uses brand-new design concept；It is general next
Say, crystallizing evaporator can be divided into two classes by mode of heating：It is to mix heat source with material to be evaporated that direct heat source, which heats it,
The method for evaporating the vapor in its material to be evaporated.Indirect heat source heating, container partition are transmitted to the solution being evaporated.I.e.
The diabatic process carried out in dividing wall type heat exchanger.It will be apparent that evaporating, concentrating and crystallizing system provided by the utility model, before belonging to
One kind, it uses the vapor evaporation mixed directly by heat source (i.e. heated air) with waste liquid to make in waste liquid final repeatedly
Repeatedly, when liquid waste concentration exceedes its saturated concentration, then its spontaneous nucleation forms crystalline particle.The utility model embodiment provides
Evaporating, concentrating and crystallizing system, evaporating, concentrating and crystallizing system provided by the utility model, is avoided and is conducted heat using traditional dividing wall type
The design of evaporation, it uses clean heated air to come into full contact with mode to sprinkling waste liquid and carries out directly by thermal evaporation its waste liquid
Moisture, the problem of avoiding the occurrence of fouling.
3rd, the evaporating, concentrating and crystallizing system that the utility model embodiment provides, it is provided by the utility model to be concentrated by evaporation knot
Crystallographic system is united, while the evaporating, concentrating and crystallizing system, easy to operate, and system effectiveness has more than higher compared to traditional evaporation equipment
Strong stability and equipment dependability.
Many significant technical advantages based on more than, the evaporating, concentrating and crystallizing system that the utility model embodiment provides will
Bring good market prospects and economic benefit.
Finally it should be noted that：Various embodiments above is only to illustrate the technical solution of the utility model, rather than it is limited
System；Although the utility model is described in detail with reference to foregoing embodiments, those of ordinary skill in the art should
Understand：It can still modify the technical solution described in foregoing embodiments, either to which part or whole
Technical characteristic carries out equivalent substitution；And these modifications or replacement, the essence of appropriate technical solution is departed from this practicality newly
The scope of each embodiment technical solution of type.
Claims (9)
- A kind of 1. evaporating, concentrating and crystallizing system, it is characterised in that including air heater, crystallizing evaporator, wind turbine, condenser and Connecting pipe；Connected between the air heater, the crystallizing evaporator, the wind turbine, the condenser by multistage connecting pipe Form closed-cycle system；The air heater includes cold wind import, hot-blast outlet, Heating medium, heating agent outlet, heater body and air stream Thread a pipe；The air flow conduit is used for ventilating air, and the both ends of the air flow conduit are respectively communicated with the cold wind Import and the hot-blast outlet；The Heating medium is used to be passed through heating agent；The heating agent outlet is used to discharge heating agent；The heating The heating agent that device body is used to be passed through carries out heat exchange processing to the air in the air flow conduit；The crystallizing evaporator includes hot wind inlet, hot-blast outlet, material inlet to be evaporated, material outlet and evacuation port, feed supplement Mouth, vaporization chamber and circulating pump；And flusher is additionally provided with the top of the vaporization chamber, the bottom of the vaporization chamber is provided with storage Liquid bath；The flusher is connected with material inlet to be evaporated；The reservoir is connected with the material outlet；The sprinkling dress Put for carrying out sprinkling processing to the waste liquid entered from material inlet to be evaporated and then being contacted with evaporating indoor air；Institute State the waste liquid that reservoir is used to collect the vaporization chamber bottom；The circulating pump be arranged on the material inlet to be evaporated with it is described On pipeline between material outlet；The circulating pump will discharge useless for continuously circulation from the material outlet of vaporization chamber bottom Liquid, the flusher being pumped at the top of vaporization chamber；The hot wind inlet passes through connecting pipe and the hot wind of the air heater Outlet, the hot-blast outlet pass through connecting pipe and the inlet communication of the wind turbine；After the vaporization chamber is by heating Air is evaporated waste liquid processing；The wind turbine, which is used to drive, drives air to be circulated in closed-cycle system；The condenser includes condenser hot wind inlet, cold wind outlet, cooling water inlet, warm water outlet and condenser body, refrigerant Delivery heat transfer device；The condenser hot wind inlet is used to be passed through damp-heat air；The cold wind outlet is used to export condensed Air；The refrigerant delivery heat transfer device is respectively communicated with cooling water inlet and warm water outlet；The cooling water inlet is used for condenser Coolant media is passed through in body；The warm water outlet is used to discharge the intrinsic coolant media of the condenser；The condensation Device body is used to carry out condensation process to the air of surrounding by the coolant media in the refrigerant delivery heat transfer device.
- 2. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatThe top of the vaporization chamber is rectangular shape, and the lower part of the vaporization chamber is pyramidal shape.
- 3. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatThe material outlet and the evacuation port are located on lower cone body portion；The hot wind inlet, the hot-blast outlet, institute State material inlet to be evaporated, the material-feeding port is located on Upper cylindrical body portion.
- 4. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatFlow control valve is provided with pipeline between the material inlet to be evaporated and the material outlet.
- 5. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatBeing internally located at below the flusher for the vaporization chamber is provided with one layer of filler.
- 6. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatThe evaporating, concentrating and crystallizing system further includes sludge preheating device；The sludge preheating device is used for entering the evaporation Waste liquid before crystallizer is heated in advance.
- 7. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatThe evaporating, concentrating and crystallizing system further includes solid-liquid separating equipment；The solid-liquid separating equipment is used for from crystallizing evaporator The material of discharge carries out solid-liquid separation treatment and then obtains crystalline particle.
- 8. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in thatThe air heater is finned tube exchanger or plate type heat exchanger.
- 9. evaporating, concentrating and crystallizing system as claimed in claim 1, it is characterised in that the wind turbine is axial fan or centrifugation Formula wind turbine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721294628.2U CN207270730U (en) | 2017-10-09 | 2017-10-09 | Evaporating, concentrating and crystallizing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721294628.2U CN207270730U (en) | 2017-10-09 | 2017-10-09 | Evaporating, concentrating and crystallizing system |
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| Publication Number | Publication Date |
|---|---|
| CN207270730U true CN207270730U (en) | 2018-04-27 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721294628.2U Active CN207270730U (en) | 2017-10-09 | 2017-10-09 | Evaporating, concentrating and crystallizing system |
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| CN (1) | CN207270730U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537167A (en) * | 2017-10-09 | 2018-01-05 | 利得环境科技（北京）有限公司 | Evaporating, concentrating and crystallizing system and evaporation process method |
| CN108635890A (en) * | 2018-07-05 | 2018-10-12 | 美丽国土（北京）生态环境工程技术研究院有限公司 | Evaporation and crystallization system |
| CN115068972A (en) * | 2021-03-16 | 2022-09-20 | 上海梅山钢铁股份有限公司 | Crystallization tank capable of adjusting solid-liquid ratio of ammonium sulfate mother liquor |
-
2017
- 2017-10-09 CN CN201721294628.2U patent/CN207270730U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107537167A (en) * | 2017-10-09 | 2018-01-05 | 利得环境科技（北京）有限公司 | Evaporating, concentrating and crystallizing system and evaporation process method |
| CN108635890A (en) * | 2018-07-05 | 2018-10-12 | 美丽国土（北京）生态环境工程技术研究院有限公司 | Evaporation and crystallization system |
| CN108635890B (en) * | 2018-07-05 | 2024-01-26 | 美丽国土（北京）生态环境工程技术研究院有限公司 | Evaporation crystallization system |
| CN115068972A (en) * | 2021-03-16 | 2022-09-20 | 上海梅山钢铁股份有限公司 | Crystallization tank capable of adjusting solid-liquid ratio of ammonium sulfate mother liquor |
| CN115068972B (en) * | 2021-03-16 | 2023-08-15 | 上海梅山钢铁股份有限公司 | Crystallization tank capable of adjusting solid-to-liquid ratio of ammonium sulfate mother liquor |
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