CN208320043U - A kind of centrifugation rotation high efficient heat exchanging crystallizer - Google Patents
A kind of centrifugation rotation high efficient heat exchanging crystallizer Download PDFInfo
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- CN208320043U CN208320043U CN201820571390.1U CN201820571390U CN208320043U CN 208320043 U CN208320043 U CN 208320043U CN 201820571390 U CN201820571390 U CN 201820571390U CN 208320043 U CN208320043 U CN 208320043U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
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Abstract
A kind of centrifugation rotation high efficient heat exchanging crystallizer, comprising: central axis, motor, crystallizer and end face, the interior central axis includes cold medium circulation section and medium passing section, motor, the motor driven central axis rotation, and then drive crystallizer unitary rotation；The more crystallizers are around central axis and, the more piece crystallizers in circulation cold medium or thermal medium arranged in parallel with central axis；The both ends of the crystallizer are respectively fixed and are connected to an end face, the end face is fixed with cental axial position, the end face one at crystallizer both ends is connected to the cold medium of central axis circulation section, one is connected to the medium passing section of central axis, and cold medium or medium passing circulation are formed between crystallizer, end face and central axis.The utility model device structure is simple, and heat transfer efficiency can be improved one times or more, and equipment volume reduces 50% or more, without precious materials such as copper, will not occur to crystallize attachment phenomenon.
Description
Technical field
The utility model relates to a kind of centrifugations to rotate high efficient heat exchanging crystallizer.
Background technique
Phase-transition heat-storage is a kind of high-new energy storage technology based on phase-changing energy storage material, and improves efficiency of energy utilization
With the important technology of protection environment, it can be used for solving the contradiction of thermal energy supply and demand mismatch.Application mainly has wind-force hair at present
Electric high-temperature heat accumulation device system, solar energy power generating hold over system, wind light mutual complementing electric heat accumulator system and novel building Cooling and Heat Source
System.
Wind-power electricity generation high-temperature heat accumulation device system its using wind-driven generator issue electric energy be transformed into thermal energy, be stored directly in
In wind-power electricity generation solid heat storage device, discharged for heating and hot-water supply system；Solar energy power generating hold over system is by the sun
The luminous energy that energy photovoltaic devices absorb sunlight becomes electric energy, then converts electrical energy into thermal energy, is stored in solid crystal storage heater, shape
Thermal energy is converted at electric energy from photovoltaic power generation to the heating of solid heat storage equipment and hot-water supply system, is realized；Wind light mutual complementing electric heat storage
Wind energy and solar energy power generating are directly translated into thermal energy and are stored in heat storage by device system, are provided for user lasting, steady
Fixed heating；Novel building cold and heat source system is combined into a whole set of pipeline system using water-ice Cool Storage Technology and electric heating thermal storage equipment
System makes full use of trough-electricity, replaces central air-conditioning, solution modern city is handled official business, and power consumption is high, costly, seriously polluted to ask
Topic.
But due to because most of phase-change material crystalline solid thermal coefficient and density are small, such as in above-mentioned application
Ice crystal, paraffin, nitric hydrate salt, hydrated phosphate, the crystallization such as hydration acetate, heating conduction is excessively poor, also can not convection current
Heat exchange, how heat conduction reinforced problem becomes great problem.At present most of solution be using heat transfer method, but
Be paraffin and thermal coefficient all very littles of other chemicals crystalline solids, therefore mainly have in actual application scheme: 1. use multilayer
Spiral coil 2. plus mental-finned and takes expansion contact area to increase heat exchange area, 3. using added in paraffin copper powder,
The methods of silicon powder and stainless steel wire band strengthen the heating conduction of paraffin, and 4. are divided in small container phase-change material with certain side
Formula is arranged in storage heater, capsule, disk, ball, cylinder, circumferential direction or longitudinal fin tubular type latent heat of phase change storage heater is formed, to mention
The accumulation of heat of high storage heater and emission capacity.But there are capital intensives for above scheme, take up a large area, and equipment failure rate is high, maintenance
It is expensive, the problems such as operation difficulty, poor reliability.
Lacing film heat exchange crystallizer and other slidingtype heat exchangers are generallyd use in the paraffin deoiler of petrochemical factory, are deposited
Poor in efficiency, hardly possible operation, failure is more, high production cost.Many devices dare not be mixed with the butanone and toluene of high proportion butanone
Liquid is closed, can not be deoiled too many, quality can not improve, and dare not also use the paraffin raw material low containing oil, otherwise will lead to wax crystal
Lead to very much to be sticked to the wall surface that can be attached to equipment when wax crystal is precipitated in equipment surface fastly, conducts heat bad, operation slightly wave
It is dynamic, device parking is resulted in, hardly possible operates and shut down frequently the problem of becoming current paraffin device most headache.
Utility model content
The utility model solves above-mentioned technical problem, provides a kind of centrifugation rotation high efficient heat exchanging crystallizer.
In order to solve the above-mentioned technical problem, a kind of the technical solution of the utility model are as follows: centrifugation rotation high efficient heat exchanging crystallization
Device characterized by comprising
Central axis, the interior central axis includes cold medium circulation section and medium passing section, the cold medium circulation
Circulate cold medium in section, and circulate thermal medium in the medium passing section；
Motor, the motor driven central axis rotation, and then drive crystallizer unitary rotation；
More crystallizers, the more crystallizers are around central axis and arranged in parallel with central axis, and described more
Circulation cold medium or thermal medium in crystallizer；
End face, the both ends of the crystallizer are respectively fixed and are connected to an end face, the end face and cental axial position
Fixed, the end face at crystallizer both ends one and the cold medium of the central axis section that circulates are connected to, one with the medium passing of central axis
Duan Liantong forms cold medium or medium passing circulation between crystallizer, end face and central axis.
Further, the end face include center liquid gathering tube, top lead to medium long tube, top lead to medium short tube and
Cloth liquid communicating pipe, for the center liquid gathering tube by being connected to central axis cloth liquid communicating pipe, top leads to medium long tube and top
It holds logical medium short tube to be arranged each along the radial direction of center liquid gathering tube and surrounds the periphery of center liquid gathering tube
It is uniformly distributed, top leads to medium long tube and is alternatively arranged with the logical medium short tube in top, and the logical medium long tube of crystallizer and top, top are logical
Medium short tube was fixed and is connected to cloth liquid communicating pipe.
Further, the end face includes more fluid square tubes, and the fluid square tube surrounds and is evenly arranged on center
On axis, each fluid square tube is connected to more crystallizers.
Further, multiple broken crystalline substances that are equipped in appearance of the fluid square tube are followed closely, and the broken brilliant nail is arranged in fluid
The two sides of square tube and the position of corresponding crystallizer.
Further, the length of the broken brilliant nail of the close hollow shaft is less than the length of the broken brilliant nail far from hollow shaft.
Further, on the central axis weld flow-disturbing thin plate, the flow-disturbing thin plate around central axis place and
It is evenly arranged on the periphery of central axis.
Further, it is respectively provided with inlet and fluid-through port in cold medium circulation section and medium passing section, it is described
Fluid-through port be connected to end face.
It further, further include a cold end system and a hot end system, the central axis passes through cold end system, heat respectively
End system connects with external pipe, and the cold end system and hot end system include media flow cavity, labyrinth seal, bearing
And supportive body, the bearing holder (housing, cover) on center shaft and are fixed in supportive body, media flow cavity and central axis
Cold medium circulation section or medium passing section are connected to and pass through supportive body to connect with external pipe, is equipped in supportive body
Labyrinth seal, the central axis in cold end system are inserted into supportive body, and the central axis in the system of hot end passes through supportive body.
Further, the crystallizer reinforces the connection with central axis by small fixinig plate.
Further, the crystallizer further includes that an outside crystallizes tower body, and the crystallizer setting is crystallized in outside
The either above or below of tower body.
The utility model device structure is simple, and heat transfer efficiency can be improved one times or more, and with low investment, occupied area is small, equipment
50% or more volume-diminished will not occur to crystallize attachment phenomenon, equipment failure rate is low, maintenance cost without precious materials such as copper
Small, easy to operate, good reliability can be widely used in wind-power electricity generation high-temperature heat accumulation device system, solar energy power generating accumulation of heat system
System, wind light mutual complementing electric heat accumulator system, novel building cold and heat source system etc. generate good economic benefit and social benefit.
It especially is being used in paraffin deoiler, efficiency is higher than conventional wiper blades double-pipe chiller by 50%, failure rate low 80%, operation
It is simple and reliable, blocking will not occur and shut down.Device structure is simple, and the butanone of high proportion butanone can be used in production by with low investment
And toluene mixture liquid, sufficiently removal oil, wax crystal quality greatly improve, and can also use the paraffin raw material low containing oil, stone
Wax crystallization without being adhered to crystallizer surface, will not occurrence of equipment blocking shut down this technology of and can replace scraping formula double-pipe chiller,
It is widely used in the paraffin deoiler of the projects such as petrochemical industry and coal chemical industry, and generates good economic benefit.
Detailed description of the invention
Specific embodiment of the present utility model is described in further detail with reference to the accompanying drawing.
Fig. 1 is the utility model crystallizer normal structure schematic diagram；
Fig. 2 is end face structure first embodiment schematic diagram in the utility model crystallizer；
Fig. 3 is end face structure second embodiment schematic diagram in the utility model crystallizer；
Fig. 4 is central axis standard axle structural schematic diagram, 4(a in the utility model crystallizer) be main view, 4(b) it is to overlook
Figure；
Fig. 5 is the utility model crystallizer elongate structure schematic diagram；
Fig. 6 is central axis long axis structural schematic diagram, 6(a in the utility model crystallizer) be main view, 6(b) it is to overlook
Figure；
Fig. 7 is cold end system structural schematic diagram in the utility model crystallizer；
Fig. 8 is hot end system structure diagram in the utility model crystallizer；
Fig. 9 is that the utility model structure applies schematic diagram in paraffin de-oiling；
Figure 10 is that the utility model structure applies the stage regenerator in wind-powered electricity generation/photovoltaic hold over system paraffin medium temperature regenerator pond
Schematic diagram；
Figure 11 is that the utility model structure applies the exothermic phase in wind-powered electricity generation/photovoltaic hold over system paraffin medium temperature regenerator pond
Schematic diagram；
Figure 12 is the fuse salt stage regenerator schematic diagram that the utility model is used for photovoltaic heat accumulating power generating system；
Figure 13 is the fuse salt exothermic phase schematic diagram that the utility model is used for photovoltaic heat accumulating power generating system
Figure 14 is that the utility model is used for cold-storage stage schematic diagram when Cool Thermal Storage For The Air conditioning system；
Figure 15 is the utility model for letting cool stage schematic diagram when Cool Thermal Storage For The Air conditioning system；
Figure 16 is the utility model for letting cool stage long axis crystallizer schematic diagram when Cool Thermal Storage For The Air conditioning system.
Specific embodiment
With reference to the accompanying drawings and detailed description, the utility model is described further.
Shown in Fig. 1 to Fig. 4, a kind of centrifugation rotation high efficient heat exchanging crystallizer, comprising: central axis 10, motor 20, more root knots are brilliant
Pipe 30 and end face 40, the interior central axis 10 includes cold medium circulation section 11 and medium passing section 12, the cold medium
Circulate cold medium in the section 11 that circulates, and circulate thermal medium in the medium passing section 12；Cold medium circulation 11 He of section
Inlet 111 and fluid-through port 112 are respectively provided in medium passing section 12, the fluid-through port 112 is connected to end face 40.Described
Motor 20 drives central axis 10 to rotate, and then drives crystallizer unitary rotation；The more crystallizers 30 surround central axis 10
And, the more piece crystallizers 30 in circulation cold medium or thermal medium arranged in parallel with central axis 10；The crystallizer
30 both ends are respectively fixed with an end face 40 and are connected to, and the end face 40 is fixed with 10 position of central axis, 30 both ends of crystallizer
End face 40 1 be connected to the cold medium of central axis 10 circulation section 11, the company of medium passing section 12 of one and central axis 10
It is logical, cold medium or medium passing circulation are formed between crystallizer 30, end face 40 and central axis 10.In preferred situation, knot
The middle part of brilliant pipe 30 reinforces the connection with central axis 10 by small steel disc, in ice storage and when paraffin medium temperature regenerator, uses
Carbon steel material uses stainless steel material in high-temperature fusion salt and conduction oil.
The first structure of end face 40 include center liquid gathering tube 41, top lead to medium long tube 42, top lead to medium it is short
Pipe 43 and cloth liquid communicating pipe 44, the center liquid gathering tube 41 with central axis 10 by being connected to cloth liquid communicating pipe 44, top
Logical medium long tube 42 and top lead to during medium short tube 43 is arranged and surrounds each along the radial direction of center liquid gathering tube 41
The periphery of heart liquid gathering tube 41 is uniformly distributed, and top leads to medium long tube 42 and is alternatively arranged with the logical medium short tube 43 in top, is tied
Brilliant pipe 30 leads to medium long tube 42 with top, top leads to medium short tube 43 and cloth liquid communicating pipe 44 is fixed and is connected to, in the present embodiment,
Top, which leads to connection on medium long tube 42, to be fixed there are two crystallizer 30, and the logical medium short tube 43 in top is connected to solid with cloth liquid communicating pipe 44
Surely there is a crystallizer 30, but be not limited thereto system.It welds and disturbs between the central axis 10 and center liquid gathering tube 41
Thin plate 13 is flowed, the flow-disturbing thin plate 13 is placed around central axis 10 and is evenly arranged on the periphery of central axis 10.
Second of structure of end face includes more fluid square tubes 45, and the fluid square tube 45 surrounds and is evenly arranged on center
On axis 10, each fluid square tube 45 is connected to more crystallizers 30, and fluid square tube 45 is mutually directly hung down in the present embodiment
Straight setting, but it is not limited thereto system.The fluid square tube 45 is equipped with multiple broken brilliant nails 46, the broken brilliant nail in appearance
46 are arranged in the position of the two sides of fluid square tube 45 and corresponding crystallizer 30.The broken brilliant nail 46 of the close hollow shaft 10
Length is less than the length of the broken brilliant nail 46 far from hollow shaft 10.Flow-disturbing thin plate 13 is welded on the central axis 10, described disturbs
Stream thin plate 13 is placed around central axis 10 and is evenly arranged on the periphery of central axis 10.Since nail conducts heat, paraffin exists first
It nails on to form crystallization, the shape of nail is circle, crystallizes adhesive force, in crystallizer rotation, is easy to fall off, when crystallized mixed solution
When colliding acceleration with square tube, crystallization can not more be attached on square tube surface, and therefore, the quantity of small square tube can be reduced, and structure becomes
It obtains simply, effect is estimated more preferable.
Fig. 5, shown in 6, crystallizer elongate structure increases radical, the length of crystallizer 30, to center according to actual needs
Axis 30 be more segmented and is divided, to be suitable for wide range.
Fig. 7, shown in 8, crystallizer further includes a cold end system 50 and a hot end system 60, and the central axis 10 leads to respectively
Cross cold end system 50, hot end system 60 connects with external pipe, the cold end system 50 include cold medium flowing cavity 51, fan
Palace sealing 52, bearing 53 and cold end supportive body 54, central axis 10 are inserted into cold end supportive body 54, and described 53 sets of bearing in
It in mandrel 10 and is fixed in cold end supportive body 54, cold medium flows the cold medium circulation section 11 of cavity 51 and central axis 10
It is connected to and passes through cold end supportive body 54 and connect with external pipe, labyrinth seal 52 is equipped in cold end supportive body 54.Hot end
System 60 includes that thermal medium flowing cavity 61, labyrinth seal 52, bearing 53 and hot end supportive body 62, central axis 10 pass through hot end
Supportive body 62 is connected with motor 20.
Specifically, being equipped with small square tube or round tube, i.e. crystallizer made of a large amount of sheet metal on crystallizer；In crystallizer
Logical fluid media (medium), such as chilled water, hot water, conduction oil etc., phase-change liquid is in crystallization pipe surface and a large amount of crystallisation by cooling in periphery.
The crystallizer of these crystallizers composition is rotated by motor, positive direction and the rotation of opposite direction interval, and the crystallization crystallized in pipe surface is de-
It falls, liquid is flowed into from the both ends of crystallization tower body, and crystallization and liquid form liquid-solid mixture.When crystallizing lighter than liquid, such as ice, stone
Wax etc., crystallizer are arranged below, and liquid-solid mixture is by square tube Accelerating Removal at this time, when liquid-solid mixture rises, under encountering
One crystallizer, the crystallization on crystallizer are fallen off by hydraulic shock, are also mixed into liquid-solid mixture, liquid-solid mixture is also further
It is cooling to generate crystal, it is contemplated that when being raised to top at least by collision 2 times or more, final liquid-solid mixture rises to liquid-solid mixture
It crystallizes above tower body and is gradually gathered above liquid, crystallizer, which continues cooling liquid, makes its crystallization.Fluid in crystallizer is added
Heat flows back into one end of hollow shaft, after flowing to extraneous refrigeration system cooling, enters crystallizer from the hollow shaft other end；This circulation connects
It is continuous to carry out, then crystallization constantly production.When crystallizing heavier than liquid, such as fuse salt, crystallizer are disposed over, and liquid is solid at this time
Mixture is crystallized pipe Accelerating Removal, when liquid-solid mixture gradually declines, encounters next crystallizer, the crystallization quilt on crystallizer
Liquid-solid mixture impact falls off, and is also mixed into liquid-solid mixture, and liquid-solid mixture is also further cooling to generate crystal, it is contemplated that liquid is solid
Mixture is at least collided 2 times when dropping to top, and final liquid-solid mixture sinks to tower body lower part, and crystallization is built up,
Crystallizer, which continues cooling liquid, makes its crystallization.Fluid in crystallizer is heated to reflux one end of hollow shaft, flows to extraneous cold
After jelly system is cooling, crystallizer is entered from the hollow shaft other end, this circulation is carried out continuously, then crystallization constantly production, production are continuous
It carries out.
Shown in Fig. 9, in paraffin de-oiling, in crystallizer rotation, heated paraffin to be crystallized pipe cooling from both ends inflow
It pushes again simultaneously and rises outflow, in liquid upper crystal aggregation.
Wind-powered electricity generation/photovoltaic hold over system paraffin medium temperature regenerator pond is used for shown in Figure 10 Figure 11, the lower section installation of heat storage pool to be more
Platform crystallizer can adjust crystallizer quantity and length according to yield needs.When needing accumulation of heat, heat storage boiler heating power is provided
Hot water, hot water flow into the liquid of crystallizer, crystallizer rotation and heated periphery, and liquid is crystallized device from the entrance of crystallizer both ends and pushes away
Dynamic rise accelerates to exchange heat with solid crystal above, and solid crystal melts.Medium position is equipped with mixing pump in pond, solid when herein
When body melts, liquid pump operation is by the further up heating top solid of liquid, until all paraffin melting.When needing heat release, knot
Brilliant device leads to cooling water, and water is heated and externally exports, and the cooled crystallization of the liquid on crystallizer periphery, gradually rich product, crystallizer turn
It is dynamic, wax crystal disturbance is thrown away, solid rises to above tower.Liquid flows into crystallizer from both ends and sufficiently exchanges heat with cold water, by
It walks paraffin all solids.Stage regenerator paraffin solid melts are to the liquid pump position, and due to liquid weight, pump blade turns
Dynamic, liquid rises, enhanced heat exchange.In crystallizer rotation, cold paraffin is flowed into from both ends, after hot water heating in square tube, and is pushed away
It is dynamic to rise outflow.Exothermic phase, when wax crystal, are lighter than liquid, rise naturally, and liquid pump does not have to operation.It is rotated in crystallizer
When, heated paraffin liquid is flowed into from both ends, and after heating the cold water in square tube, wax crystal mixed liquor is crystallized device and pushes upper up-flow
Out.
It can also be used for for replacing Wiper blade type double-pipe chiller in paraffin deoiler.Structure is close with above-described embodiment
Seemingly, in production, ethylene glycol chilled water is led in crystallizer, water is heated output, and the vasoliniment on periphery is cooled to be crystallized, gradually
Wax crystal disturbance is thrown away, when mixture liquid rises, encounters next crystallizer, on crystallizer by deposition, crystallizer rotation
Crystallization fallen off by hydraulic shock, be also mixed into mixed liquor, mixed liquor is also further cooling to generate crystal, it is contemplated that mixed liquor is rising
It is at least collided 2 times when to top, final mixed liquor rises to above tower body.Crystal aggregation is discharged tower from outlet, enters
Next procedure.Upper section ketone benzene paraffin mixed liquor continues flow down and sufficiently exchanges heat with cylinder part, continuous production.
Shown in Figure 12 Figure 13, in the fuse salt high-temperature heat accumulation of photovoltaic heat accumulating power generating system, crystallizing pond top to be equipped with knot
Brilliant device, when needing accumulation of heat daytime, high temperature heat conductive oil enters crystallizer, the fuse salt on crystallizer periphery from the output of photovoltaic heat collector
Solid is heated to be high-temp liquid, and hot liquid is pushed flow down and the solid of lower part to accelerate to exchange heat, solid salt by crystallizer rotation
Melt.Medium position is equipped with mixing pump in pond, and when solid melts herein, pump operation, which further pushes liquid, goes to heating bottom
Portion's solid, until all solids melt.When needing heat release at night, low temperature conduction oil inputs crystallizer, is heated as high temperature and leads
Hot oil externally exports, and the liquid on periphery is cooled to salt crystallization, gradually rich product, and crystallizer rotation throws away crystallization disturbance, solid
Crystallization sinks to bottom.Liquid continues flowing and sufficiently exchanges heat with low-temperature oil in crystallizer, gradually crystallizes salt all solids.It stores
Pump housing position is gradually arrived in hot stage crystallization salt fusing, since liquid is light, pump blade rotation, and downward liquid flow, with bottom
Solid enhanced heat exchange.In crystallizer rotation, cold liquid is flowed into from both ends, the high temperature heat conductive oil in crystallisation by cooling pipe；Heat release rank
Than liquid weight when section salt crystallization, sink naturally, liquid pump does not have to operation.In crystallizer rotation, hot liquid is flowed into from both ends, is added
Cold conduction oil in thermal crystalline pipe.
Figure 14,15,16 are in Cool Thermal Storage For The Air conditioning system, crystallizing pond lower part to need cold-storage equipped with crystallizer at night
When, refrigerator works, and chilled water is led in crystallizer, and the mixed liquor on cooling periphery makes its icing, and crystallizer rotation disturbs ice crystal
It throws away, ice water rises to pond top.Water enters from crystallizer both ends sufficiently to exchange heat with chilled water, so constantly recycles, pond
Water gradually all freezes.Chilled water is heated into warm water and returns refrigerator cooling cycle when daytime is using cooling capacity, and normal-temperature water is into knot
Brilliant device, heated periphery water, crystallizer rotation pushes water to rise to be accelerated to exchange heat with the ice on top, ice-out Cheng Shui.In pond
In medium position mixing pump is housed, when ice-out luck herein is about to ice at the top of the further up heating of water, until all ice-out
After warm water is cooled in Crystallizer tube, output to air-conditioned room is recycled.Water in cold-storage stage cold accumulating pond is in icing rank
Section, crystallization heat exchanger rotation operation, cold water are entered, and warm water comes out, and warm water is reduced temperature by refrigerator operation, and circularly cooling stores
Until the ice of cold drop is expired in place；Tied with the cold stage, the ice in cold accumulating pond gradually melts, crystallization heat exchanger rotation operation, warm water into
It goes, cold water comes out, and refrigerator is not run or under-capacity operation.
Although specifically showing and describing the utility model in conjunction with preferred embodiment, those skilled in the art is answered
This is understood, in the spirit and scope for not departing from the utility model defined by the appended claims, in form and details
On the utility model is made a variety of changes, be the protection scope of the utility model.
Claims (10)
1. a kind of centrifugation rotates high efficient heat exchanging crystallizer characterized by comprising
Central axis, the interior central axis includes cold medium circulation section and medium passing section, and the cold medium circulates in section
Circulate cold medium, and circulate thermal medium in the medium passing section；
Motor, the motor driven central axis rotation, and then drive crystallizer unitary rotation；
More crystallizers, the more crystallizers surround central axis and more root knots crystalline substance arranged in parallel with central axis, described
Circulation cold medium or thermal medium in pipe；
End face, the both ends of the crystallizer are respectively fixed and are connected to an end face, and the end face is fixed with cental axial position,
The end face one at crystallizer both ends is connected to the cold medium of central axis circulation section, one with the medium passing Duan Lian of central axis
It is logical, cold medium or medium passing circulation are formed between crystallizer, end face and central axis.
2. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that the end face includes
Center liquid gathering tube, top lead to medium long tube, top leads to medium short tube and cloth liquid communicating pipe, the center liquid gathering tube
It is connected to by cloth liquid communicating pipe with central axis, top leads to medium long tube and top leads to medium short tube each along center liquid gathering tube
Radial direction be arranged and be uniformly distributed around the periphery of center liquid gathering tube, top leads to medium long tube and top is logical is situated between
Matter short tube is alternatively arranged, and crystallizer leads to medium long tube with top, top leads to medium short tube and fixes cloth liquid communicating pipe and is connected to.
3. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that the end face includes
More fluid square tubes, the fluid square tube are surrounded and are evenly distributed on center shaft, each fluid square tube and more root knots
Brilliant pipe connection.
4. a kind of centrifugation according to claim 3 rotates high efficient heat exchanging crystallizer, which is characterized in that the fluid square tube
Be equipped with multiple broken brilliant nails in appearance, the position of the two sides and corresponding crystallizer of fluid square tube is arranged in the broken brilliant nail.
5. a kind of centrifugation according to claim 4 rotates high efficient heat exchanging crystallizer, which is characterized in that close to the broken of hollow shaft
The length of crystalline substance nail is less than the length of the broken brilliant nail far from hollow shaft.
6. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that on the central axis
Flow-disturbing thin plate is welded, the flow-disturbing thin plate is placed around central axis and is evenly arranged on the periphery of central axis.
7. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that the cold medium stream
It is respectively provided with inlet and fluid-through port in logical section and medium passing section, the fluid-through port is connected to end face.
8. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that further include a cold end system
System and a hot end system, the central axis passes through cold end system respectively, hot end system connects with external pipe, the cold end
System and hot end system include media flow cavity, labyrinth seal, bearing and supportive body, and the bearing holder (housing, cover) is in central axis
It above and is fixed in supportive body, media flow cavity is connected to the cold medium of central axis circulation section or medium passing section
And it passes through supportive body to connect with external pipe, labyrinth seal is equipped in supportive body, the central axis insertion in cold end system
Supportive body, the central axis in the system of hot end pass through thermal medium supportive body.
9. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that the crystallizer is logical
Too small fixinig plate reinforces the connection with central axis.
10. a kind of centrifugation according to claim 1 rotates high efficient heat exchanging crystallizer, which is characterized in that the crystallizer
It further include that an outside crystallizes tower body, the either above or below of external crystallizing tower body is arranged in the crystallizer.
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479102A (en) * | 2018-04-20 | 2018-09-04 | 上海涛川能源科技有限公司 | A kind of centrifugation rotation high efficient heat exchanging crystallizer and application method |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108479102A (en) * | 2018-04-20 | 2018-09-04 | 上海涛川能源科技有限公司 | A kind of centrifugation rotation high efficient heat exchanging crystallizer and application method |
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Granted publication date: 20190104 |