CN207371136U - New Oslo crystallizer - Google Patents
New Oslo crystallizer Download PDFInfo
- Publication number
- CN207371136U CN207371136U CN201721155294.0U CN201721155294U CN207371136U CN 207371136 U CN207371136 U CN 207371136U CN 201721155294 U CN201721155294 U CN 201721155294U CN 207371136 U CN207371136 U CN 207371136U
- Authority
- CN
- China
- Prior art keywords
- heater
- crystallizing evaporator
- new
- benefits
- economic benefits
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model is related to a kind of new oslo crystallizers, including crystallizing evaporator, economic benefits and social benefits heater, feeding engine and material feeding tube, material feeding tube distinguishes the solution inlet of crystallizing evaporator bottom and economic benefits and social benefits heater by triple valve, the taphole of economic benefits and social benefits heater connects the upper side wall of crystallizing evaporator by heating feed pipe, the circulation fluid outlet of crystallizing evaporator connects the solution inlet of economic benefits and social benefits heater by circulation pipe, and the entrance of circulation pipe stretches to the lower bottom part of crystallizing evaporator.The new oslo crystallizer of the utility model solve the problems, such as in process of production due to crystalline particle is small or heating blockage caused by yield is low or even equipment parking, ensure that high-efficiency and continuous produces, and crystalline particle degree is big, particle is uniform.
Description
Technical field
The utility model is related to evaporation crystallization equipment more particularly to a kind of new oslo crystallizers.
Background technology
Technique of Heat Pump Evaporation is an energy-efficient, water-saving, green technology, which is re-use itself generation two
The indirect steam of low temperature position is carried out mechanical compression by secondary steam, is improved its temperature and pressure and is entered back into heat exchanger heat exchange, with abundant
Utilize latent heat of the steam.Application of this technology in China at present is in developing stage, uses traditional oslo crystallizer
Crystallization is evaporated to different materials, is asked there are still crystalline particle is small, heating tube easily blocks, compressor operating is abnormal etc.
Topic.
It is therefore desirable to design a kind of new oslo crystallizer, to overcome the above problem.
Utility model content
The purpose of the utility model is to overcome the defect of the prior art, provide a kind of crystalline particle degree it is big, can be efficient
The new oslo crystallizer of quantity-produced.
The utility model is realized in this way：
The utility model provides a kind of new oslo crystallizer, including crystallizing evaporator, economic benefits and social benefits heater, feeding engine and
Material feeding tube, material feeding tube distinguish the solution inlet of crystallizing evaporator bottom and economic benefits and social benefits heater, economic benefits and social benefits by triple valve
The taphole of heater connects the upper side wall of crystallizing evaporator by heating feed pipe, and the circulation fluid outlet of crystallizing evaporator is logical
The solution inlet of circulation pipe connection economic benefits and social benefits heater is crossed, the entrance of circulation pipe stretches to the lower bottom part of crystallizing evaporator.
Further, heating feed pipe enters one end of crystallizing evaporator and connects upward reducing bend, on reducing bend
Side is equipped with solar disk.
Further, economic benefits and social benefits heater includes primary heater and secondary heater, primary heater and secondary heater
Between steam control valve, steam control valve steam-out (SO) pipeline are installed.
Further, primary heater is connected with secondary heater by feeding engine.
Further, crystallizing evaporator upper end is equipped with steam (vapor) outlet.
The utility model has the advantages that：
The new oslo crystallizer of the utility model is solved in process of production since crystalline particle is small or heating tube
The problem of yield caused by blocking is low or even equipment is stopped ensure that high-efficiency and continuous produces, and crystalline particle degree is big, particle
Uniformly.
Description of the drawings
It in order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Or attached drawing needed to be used in the description of the prior art is briefly described, it should be apparent that, the accompanying drawings in the following description is only
It is some embodiments of the utility model, for those of ordinary skill in the art, in the premise not made the creative labor
Under, it can also be obtained according to these attached drawings other attached drawings.
Fig. 1 is the structure diagram of new oslo crystallizer provided by the utility model.
Specific embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out
It clearly and completely describes, it is clear that the described embodiments are only a part of the embodiments of the utility model rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are without making creative work
All other embodiments obtained shall fall within the protection scope of the present invention.
Such as Fig. 1, the new oslo crystallizer of the utility model, including crystallizing evaporator 1, economic benefits and social benefits heater 2, feeding engine
3 and material feeding tube 4,1 upper end of crystallizing evaporator is equipped with steam (vapor) outlet 11.
Material feeding tube 4 distinguishes the solution inlet of 1 bottom of crystallizing evaporator and economic benefits and social benefits heater 2 by triple valve 41, will
The setting of triple valve 41 is chain with the temperature in crystallizing evaporator 1, if 1 medium temperature of crystallizing evaporator spends height, raw material is directly entered
Crystallizing evaporator 1, to reduce its temperature；If 1 temperature of crystallizing evaporator is normal, raw material enters economic benefits and social benefits heater 2；Always steaming is made
It sends out the temperature in crystallizer 1 to keep stablizing, maintains the process for stabilizing condition of material crystallization.
The taphole of economic benefits and social benefits heater 2 connects the upper side wall of crystallizing evaporator 1, heating charging by heating feed pipe 5
Pipe 5 connects upward reducing bend 51 into one end of crystallizing evaporator 1.Material charging is changed to spray upwards by angular cut, profit
Accelerate the flowing velocity of material with reducing bend 51, prevent its fouling at elbow 51, while increase pressure.In reducing bend 51
Top is equipped with solar disk 6, and material is made on the one hand to increase material flash efficiency to scattering on four sides, material is on the other hand reduced and sprays
Shock to crystallizing evaporator 1 reduces equipment vibrations.
The circulation fluid outlet of crystallizing evaporator 1 connects the solution inlet of economic benefits and social benefits heater 2 by circulation pipe 7, circulation pipe 7
Entrance stretches to the lower bottom part of crystallizing evaporator 1, and the little particle of lower bottom part is made to be cycled in crystallizing into economic benefits and social benefits heater 2, is increased
Growing up the time for crystallization, solves the problems, such as that crystalline particle is small.
Economic benefits and social benefits heater 2 includes primary heater 21 and secondary heater 22, primary heater 21 and secondary heater 22
It is connected by feeding engine 3.Steam control valve 23, steam control valve 23 are installed between primary heater 21 and secondary heater 22
Steam-out (SO) pipeline.Steam control valve 23 and temperature and pressure interlock in shell, temperature is controlled by adjusting steam input, can
Effectively to reduce heating tube blockage problem.
Traditional oslo crystallizer 1 is subjected to equipment optimization, while after controlling the process conditions such as temperature, pressure, it can be bright
The size of aobvious increase crystalline particle, while effective the problem of delaying to heat blockage cause the device to normal continuous operation.
In conclusion the new oslo crystallizer of the utility model is solved in process of production since crystalline particle is small
Or the problem of yield is low caused by heating blockage or even equipment is stopped, it ensure that high-efficiency and continuous produces, and crystalline particle
Degree is big, and particle is uniform.
The above is only the preferred embodiment of the utility model only, is not intended to limit the utility model, all at this
Within the spirit and principle of utility model, any modifications, equivalent replacements and improvements are made should be included in the utility model
Protection domain within.
Claims (5)
1. a kind of new oslo crystallizer, which is characterized in that including crystallizing evaporator, economic benefits and social benefits heater, feeding engine and raw material
Feed pipe, by triple valve, the solution of the crystallizing evaporator bottom and the economic benefits and social benefits heater enters the material feeding tube respectively
Mouthful, the taphole of the economic benefits and social benefits heater connects the upper side wall of the crystallizing evaporator, the evaporation by heating feed pipe
The circulation fluid outlet of crystallizer connects the solution inlet of the economic benefits and social benefits heater by circulation pipe, and the entrance of the circulation pipe stretches into
To the lower bottom part of the crystallizing evaporator.
2. new oslo crystallizer as described in claim 1, it is characterised in that：The heating feed pipe enters the evaporation
One end of crystallizer connects upward reducing bend, and solar disk is equipped with above the reducing bend.
3. new oslo crystallizer as claimed in claim 2, it is characterised in that：The economic benefits and social benefits heater includes the first heating
Device and secondary heater are equipped with steam control valve, the steam tune between the primary heater and the secondary heater
Save valve steam-out (SO) pipeline.
4. new oslo crystallizer as claimed in claim 3, it is characterised in that：The primary heater and described second adds
Hot device is connected by feeding engine.
5. new oslo crystallizer as described in claim 1, it is characterised in that：The crystallizing evaporator upper end is equipped with steam
Outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721155294.0U CN207371136U (en) | 2017-09-07 | 2017-09-07 | New Oslo crystallizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201721155294.0U CN207371136U (en) | 2017-09-07 | 2017-09-07 | New Oslo crystallizer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN207371136U true CN207371136U (en) | 2018-05-18 |
Family
ID=62339670
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201721155294.0U Expired - Fee Related CN207371136U (en) | 2017-09-07 | 2017-09-07 | New Oslo crystallizer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN207371136U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109806614A (en) * | 2019-02-26 | 2019-05-28 | 湘潭埃索凯科技有限公司 | A kind of novel crystallization equipment |
-
2017
- 2017-09-07 CN CN201721155294.0U patent/CN207371136U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109806614A (en) * | 2019-02-26 | 2019-05-28 | 湘潭埃索凯科技有限公司 | A kind of novel crystallization equipment |
| CN109806614B (en) * | 2019-02-26 | 2024-01-23 | 广西埃索凯新材料科技有限公司 | Crystallization equipment |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20180518 Termination date: 20200907 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |