CN206342932U - A kind of Multi-effect concentration equipment - Google Patents
A kind of Multi-effect concentration equipment Download PDFInfo
- Publication number
- CN206342932U CN206342932U CN201720008117.3U CN201720008117U CN206342932U CN 206342932 U CN206342932 U CN 206342932U CN 201720008117 U CN201720008117 U CN 201720008117U CN 206342932 U CN206342932 U CN 206342932U
- Authority
- CN
- China
- Prior art keywords
- heat exchanger
- concentration kettle
- concentration
- kettle
- pump
- 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
Links
- 239000000463 material Substances 0.000 claims abstract description 50
- 238000010438 heat treatment Methods 0.000 claims abstract description 11
- 229910001200 Ferrotitanium Inorganic materials 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 6
- 238000001816 cooling Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 229940023579 anhydrous betaine Drugs 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 238000010025 steaming Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 210000003298 dental enamel Anatomy 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model discloses a kind of Multi-effect concentration equipment, including concentration kettle one, concentration kettle two, concentration kettle three, condenser, heat exchanger one, heat exchanger two, heat exchanger three, heat exchanger four, material pump, vavuum pump, the concentration kettle one, concentration kettle two and concentration kettle three are sequentially connected in series one group of Multi-effect concentration device by pipeline, connect, be finally connected with vavuum pump with heat exchanger one and condenser successively again；The concentration kettle one, concentration kettle two and concentration kettle three connect heat exchanger two, heat exchanger three and heat exchanger four respectively, and the heat exchanger two, heat exchanger three and heat exchanger four are sequentially connected in series again, are finally connected with material pump two；Material pump three is connected between the concentration kettle one and concentration kettle two, between concentration kettle two and concentration kettle three；Heat exchanger one is connected with material pump one.The utility model use forcing pump circulating-heating, steam saving 60% or so, clean environment is comfortable；Virgin material is repeatedly exchanged heat before concentration kettle is entered, further increases the utilization rate of heat energy.
Description
Technical field
The utility model is related to a kind of concentrator, more particularly to a kind of Multi-effect concentration equipment.
Background technology
In the production process of anhydrous betaine, dehydration by evaporation link is exactly enrichment process.The steaming of general anhydrous betaine
Hair dehydration mostly uses single-action concentration systems, and the water vapour steamed condenses out condensation heat in water condenser and lost with regard to this
, cause great waste.
The content of the invention
Technical problem to be solved in the utility model be for prior art exist defect there is provided a kind of Multi-effect concentration
Equipment.
To solve this technical problem, the utility model provides a kind of Multi-effect concentration equipment, including concentration kettle one, concentration
Kettle two, concentration kettle three, condenser, heat exchanger one, heat exchanger two, heat exchanger three, heat exchanger four, material pump, vavuum pump, the concentration
Kettle one, concentration kettle two and concentration kettle three are sequentially connected in series one group of Multi-effect concentration device by pipeline, then successively with heat exchanger one
With condenser series connection, finally it is connected with vavuum pump；The concentration kettle one, concentration kettle two and concentration kettle three connect heat exchanger respectively
2nd, heat exchanger three and heat exchanger four, the heat exchanger two, heat exchanger three and heat exchanger four are sequentially connected in series again, finally with material pump two
Connection；Material pump three is connected between the concentration kettle one and concentration kettle two, between concentration kettle two and concentration kettle three；Heat exchanger one with
Material pump one is connected.
The internal layer and zone of heating of the concentration kettle two and concentration kettle three use titanium steel material.
The heat exchanger one, heat exchanger two, heat exchanger three and heat exchanger four use titanium steel material.
Beneficial effect：The utility model uses forcing pump circulating-heating, and material is heated efficiently, evaporation rate is fast, effectively protects
Hold material dewatering efficiency；Energy-saving effect is notable, than single effect evaporator steam saving 60% or so.Material evaporates in closed system
Concentration, clean environment is comfortable；The system equipment sets concentration kettle fluid level control devices at different levels, prevents overflow phenomenon.This practicality is new
Type employs titanium steel material compared with conventional art, so because the indirect steam of material dewatering generation is because containing the acid such as hydrogen chloride
Property medium, then ensure that the corrosion resistance of device；In addition, virgin material has carried out multiple heat exchange before concentration kettle is entered before concentration,
The utilization rate of heat energy is further increased, is more saved.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure：1 concentration kettle one, 2 concentration kettles two, 3 concentration kettles three, 4 condensers, 5 heat exchangers one, the heat exchange of 6 heat exchangers two, 7
Device three, 8 heat exchangers four, 9 material pumps one, 10 vavuum pumps, 11 material pumps two, 12 material pumps three.
Embodiment
Below in conjunction with the accompanying drawings and embodiment is specifically described to the utility model.
Fig. 1 show structural representation of the present utility model.
The utility model includes concentration kettle 1, concentration kettle 22, concentration kettle 33, condenser 4, heat exchanger 1, heat exchanger
26, heat exchanger 37, heat exchanger 48, material pump 1, vavuum pump 10, material pump 2 11 and material pump 3 12.
The concentration kettle 1, concentration kettle 22 and concentration kettle 33 are sequentially connected in series one group of Multi-effect concentration by pipeline and filled
Put, then connect successively with heat exchanger 1 and condenser 4, be finally connected with vavuum pump 10.
The concentration kettle 1, concentration kettle 22 and concentration kettle 33 connect heat exchanger 26, heat exchanger 37 and heat exchanger respectively
48, the heat exchanger 26, heat exchanger 37 and heat exchanger 48 are sequentially connected in series again, are finally connected with material pump 2 11.
Provided with material pump 3 12 between the concentration kettle 1 and concentration kettle 22, between concentration kettle 22 and concentration kettle 33, change
Hot device 1 is connected with material pump 1.
The internal layer and zone of heating of the concentration kettle 22 and concentration kettle 33 use titanium steel material, it is ensured that equipment it is corrosion-resistant
Property, other parts also use enamel equipment, cost-effective to a certain extent.
The heat exchanger 1, heat exchanger 26, heat exchanger 37 and heat exchanger 48 use titanium steel material, it is ensured that equipment is resistance to
Corrosivity.
Workflow of the present utility model：
Steam is first entered by the zone of heating of concentration kettle 1, is added thermogenetic water vapour to enter material in concentration kettle 1 and is concentrated
The zone of heating of kettle 22, is the material heating in concentration kettle 22, and the material in concentration kettle 22 seethes with excitement the water of generation under a reduced pressure
Steam enters the zone of heating of concentration kettle 33, is heated as the thermal source of concentration kettle 33 for the material in concentration kettle 33, concentration kettle 33
Interior material seethes with excitement in the state of bigger vacuum steams the water in material；The steaming that material boiling is produced in concentration kettle 33
Vapour enters after the heat exchange of heat exchanger 1, enters back into condenser 4, the concentration after cooling after cooling with concentration kettle 22 and concentration kettle 33
Water, which collects, drains；Material to be concentrated is pumped into by material pump 1, through heat exchanger 1, heat exchanger 26, heat exchanger 37, heat exchanger 48
Preheating enters the inspissator of concentration kettle 33, then is forced by concentration kettle 33 to be pumped into concentration kettle 22 through punishment in advance pump three, then by concentration kettle two
2 force to be pumped into concentration kettle 1；Material concentration in concentration kettle 1 is completed, and further after heat exchange cooling, materials pump 2 11 is delivered to
Subsequent processing.
The utility model carries out pipeline on the basis of existing single-action concentrator and is connected in series, and concentration kettle one produces concentration and steamed
Vapour does not enter back into condenser, but is reused as the heating medium of concentration kettle two, can so consume initial steam
Effectively reduction by 50%, concentration kettle two produces reduced vapor and does not also enter condenser, but enters the zone of heating of concentration kettle three, per one-level
Concentration kettle material boiling point is effectively reduced, and smoothly completes dehydration.The utility model saving heat energy, the part of acid material contact is changed to
Titanium steel material, reduces the accessory of the corrosion of acidic materials, the discontiguous part of acidic materials or common kettle, so as to save certain
Cost.
The utility model the embodiment above, is merely illustrative, be not it is only, it is all in the range of the utility model
Or the change in the range of equivalent the utility model is surrounded by the utility model.
Claims (3)
1. a kind of Multi-effect concentration equipment, including concentration kettle one (1), concentration kettle two (2), concentration kettle three (3), condenser (4), heat exchange
Device one (5), heat exchanger two (6), heat exchanger three (7), heat exchanger four (8), material pump one (9), vavuum pump (10), it is characterised in that：
The concentration kettle one (1), concentration kettle two (2) and concentration kettle three (3) are sequentially connected in series one group of Multi-effect concentration device by pipeline,
Connect, be finally connected with vavuum pump (10) with heat exchanger one (5) and condenser (4) successively again；The concentration kettle one (1), concentration
Kettle two (2) and concentration kettle three (3) connect heat exchanger two (6), heat exchanger three (7) and heat exchanger four (8), the heat exchanger two respectively
(6), heat exchanger three (7) and heat exchanger four (8) are sequentially connected in series again, are finally connected with material pump two (11)；The concentration kettle one (1) with
Material pump three (12), heat exchanger one (5) and material are connected between concentration kettle two (2), between concentration kettle two (2) and concentration kettle three (3)
Pump one (9) is respectively connected with.
2. Multi-effect concentration equipment according to claim 1, it is characterised in that：The concentration kettle two (2) and concentration kettle three (3)
Internal layer and zone of heating use titanium steel material.
3. Multi-effect concentration equipment according to claim 1 or 2, it is characterised in that：The heat exchanger one (5), heat exchanger two
(6), heat exchanger three (7) and heat exchanger four (8) use titanium steel material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720008117.3U CN206342932U (en) | 2017-01-04 | 2017-01-04 | A kind of Multi-effect concentration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720008117.3U CN206342932U (en) | 2017-01-04 | 2017-01-04 | A kind of Multi-effect concentration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206342932U true CN206342932U (en) | 2017-07-21 |
Family
ID=59323393
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720008117.3U Expired - Fee Related CN206342932U (en) | 2017-01-04 | 2017-01-04 | A kind of Multi-effect concentration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206342932U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108543320A (en) * | 2018-04-27 | 2018-09-18 | 上海成界制药设备有限公司 | A kind of method and device of high-efficiency and continuous drying |
-
2017
- 2017-01-04 CN CN201720008117.3U patent/CN206342932U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108543320A (en) * | 2018-04-27 | 2018-09-18 | 上海成界制药设备有限公司 | A kind of method and device of high-efficiency and continuous drying |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 251500 Industrial Park, Linyi Economic Development Zone, Dezhou, Shandong province (east side of Fumin Road) Patentee after: Shandong flying pharmaceutical Limited by Share Ltd. Address before: 251500 Industrial Park, Linyi Economic Development Zone, Dezhou, Shandong province (east side of Fumin Road) Patentee before: SHANDONG E.FINE PHARMACY CO.,LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170721 |