CN206463531U - A kind of rose is produced with crystallization enrichment facility - Google Patents
A kind of rose is produced with crystallization enrichment facility Download PDFInfo
- Publication number
- CN206463531U CN206463531U CN201720086666.2U CN201720086666U CN206463531U CN 206463531 U CN206463531 U CN 206463531U CN 201720086666 U CN201720086666 U CN 201720086666U CN 206463531 U CN206463531 U CN 206463531U
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- tank body
- floater
- heat exchanger
- pipeline
- steam
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Abstract
Produced the utility model discloses a kind of rose of cosmetic material producing equipment technical field with crystallization enrichment facility, the inner cavity top of tank body is provided with vaporization chamber, the bottom of vaporization chamber is provided with floater, the bottom of floater is provided with crystallisation chamber, the bottom of tank body is provided with discharging opening, the right wall of tank body is provided with air-heater, steam (vapor) outlet is provided with the top of tank body, the left wall of tank body is provided with circulation air pump, heat exchanger is provided with the top of the bearing of left side, the left wall bottom of heat exchanger is provided with condensate outlet, material box is provided with the top of the bearing of right side, material box is connected by pipeline with floater, the bottom of hot air duct is provided with hot blast spray disk, by the way that steam zone Returning heat-exchanger is re-used, in the case where evaporative crystallization effect is improved, substantially increase heat utilization rate, and it is simple in construction, it is easy to operate, recovering effect is good, safety and sanitation, and the relatively low list of cost.
Description
Technical field
The utility model is related to cosmetic material producing equipment technical field, and specially a kind of rose is produced with crystallization
Enrichment facility.
Background technology
Rose needed for cosmetics, with anti-inflammatory, antibacterial, the activity of anti-oxidant suppression white horse with a black mane aminoacidase is being changed
Rose, which is produced, in cosmetic waste equipment needs to carry out it crystallization concentration, and Crystallization Separation technology is with wide
General application, evaporative crystallization is a kind of method commonly used in Crystallization Separation technology, and crystallizing evaporator is by dissolved with the mixing of material
Liquid evaporates a kind of container that unnecessary solvent makes material crystallization separate out and separate, and is generally divided into gas-liquid separation chamber and knot
Brilliant device, enters in gas-liquid separation chamber after the preheating of material mixed liquor, vapor and material mixed liquor is separated, in this process heat
Often lose larger, the speed that material mixed liquor reclaimed water steam raising comes out is slower, be unfavorable for crystallization, gone out from steam (vapor) outlet
Steam can also lose many heats.Chinese patent 200920025770.6 provides a kind of high-efficiency evaporating and crystallizing tower, including tower body,
The top of tower body is provided with charging aperture, and the top of tower body inner chamber is provided with feed liquid injection apparatus, and the top of tower body inner chamber is received provided with steam
Collect chamber, the cavity wall of steam collecting chamber is provided with negative pressure of vacuum steam (vapor) outlet, vapour-liquid is provided between steam collecting chamber and tower body inner chamber
Separator, the bottom of tower body is provided with crystallization bottom pond, and the bottom in crystallization bottom pond is provided with crystal discharge port, crystallizes the side wall in bottom pond
Feed liquid refluxing opening is provided with, feed liquid is ejected into evaporating space and is allowed to drench into rain shape by feed liquid injection apparatus, accelerates feed liquid
Evaporation, improve heat utilization rate, but sprinkling direction is relatively simple, and without solving the steam heat damage that evaporation is obtained
Mistake problem, the utilization rate of heat needs further raising.In view of it is mentioned above the problem of, it is pure that the utility model designs a kind of rose
Dew is produced with crystallization enrichment facility, the problem of to solve mentioned above.
Utility model content
The purpose of this utility model is that providing a kind of rose produces with crystallization enrichment facility, to solve above-mentioned background
The speed that the material mixed liquor reclaimed water steam raising proposed in technology comes out is slower, is unfavorable for crystallization, is gone out from steam (vapor) outlet
The problem of steam can also lose many heats.
To achieve the above object, the utility model provides following technical scheme：A kind of rose is produced with crystallization concentration
Device, including two groups of bearings, the bottom of the bearing, which is provided between support bar, bearing described in two groups, is provided with tank body, described
The inner cavity top of tank body is provided with vaporization chamber, and the bottom of the vaporization chamber is provided with floater, and the bottom of the floater is set
Have a crystallisation chamber, the bottom of the tank body is provided with discharging opening, the right wall of the tank body is provided with air-heater, the vaporization chamber it is interior
Top of chamber is provided with hot air duct, and the air-heater is connected with hot air duct, and steam (vapor) outlet, institute are provided with the top of the tank body
The left wall for stating tank body is provided with circulation air pump, and the steam (vapor) outlet is connected by pipeline with circulation air pump, the left side bearing
Top is provided with heat exchanger, and the circulation air pump is connected by pipeline with heat exchanger, the left wall bottom of the heat exchanger
It is provided with the top of condensate outlet, the right side bearing and is provided with material box, the material box is connected by pipeline and floater
Logical, the bottom of the hot air duct is provided with hot blast spray disk, and the heat exchanger sprays disk by pipeline and hot blast and is connected.
It is preferred that, fog-spray nozzle is provided with the top of the hot air duct, and fog-spray nozzle is provided with five groups of structure identical.
It is preferred that, the outer wall of the hot blast spray disk is provided with spray hole.
Compared with prior art, the beneficial effects of the utility model are：This kind of rose, which is produced, uses crystallization enrichment facility,
By the way that steam zone Returning heat-exchanger is re-used, in the case where evaporative crystallization effect is improved, heat energy utilization is substantially increased
Rate, and simple in construction, easy to operate, recovering effect is good, safety and sanitation, and the relatively low list of cost.
Brief description of the drawings
Fig. 1 is the utility model structural representation.
In figure：1 bearing, 2 support bars, 3 tank bodies, 4 vaporization chambers, 5 floaters, 6 crystallisation chambers, 7 discharging openings, 8 air-heaters, 9 heat
Wind pipeline, 10 steam (vapor) outlets, 11 circulation air pumps, 12 heat exchangers, 13 condensate outlets, 14 material box, 15 hot blasts spray disk.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole
Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made
The every other embodiment obtained, belongs to the scope of the utility model protection.
Referring to Fig. 1, the utility model provides a kind of technical scheme：A kind of rose, which is produced, uses crystallization enrichment facility,
Including two groups of bearings 1, the bottom of bearing 1, which is provided between support bar 2, two groups of bearings 1, is provided with tank body 3, the inner chamber top of tank body 3
Portion is provided with vaporization chamber 4, and the bottom of vaporization chamber 4 is provided with floater 5, and the bottom of floater 5 is provided with crystallisation chamber 6, tank body 3
Bottom is provided with discharging opening 7, and the right wall of tank body 3 is provided with air-heater 8, and the inner cavity top of vaporization chamber 4 is provided with hot air duct 9,
Air-heater 8 is connected with hot air duct 9, and the top of tank body 3 is provided with steam (vapor) outlet 10, and the left wall of tank body 3 is provided with circulation air pump
11, steam (vapor) outlet 10 is connected by pipeline with circulation air pump 11, and the top of left side bearing 1 is provided with heat exchanger 12, circulating air
Pump 11 is connected by pipeline with heat exchanger 12, and the left wall bottom of heat exchanger 12 is provided with condensate outlet 13, right side bearing 1
Top be provided with material box 14, material box 14 is connected by pipeline with floater 5, and the bottom of hot air duct 9 is provided with hot blast
Disk 15 is sprayed, heat exchanger 12 sprays disk 15 by pipeline and hot blast and is connected.
Wherein, the top of hot air duct 9 is provided with fog-spray nozzle, and fog-spray nozzle is provided with five groups of structure identical, passes through five
Group fog-spray nozzle causes the higher temperature of holding in vaporization chamber 4, and the outer wall of hot blast spray disk 15 is provided with spray hole, is easy to heat exchange
The hot gas that device 12 is exchanged sprays disk 15 and spray hole to being heated in vaporization chamber 4 by hot blast.
Operation principle：Tank body 3 is arranged on bearing 1, material box 14 is passed through material into floater 5 by pipeline, heat
Blower fan 8 is blown into hot blast into vaporization chamber 4 by hot air duct 9 and is easy to evaporation to material, and the liquid after evaporation passes through steam
Outlet 10 is discharged, and the steam of discharge is passed into heat exchanger 12 by circulating air pump 11, and the one side of heat exchanger 12 will
The condensate liquid of condensation is discharged by condensate outlet 13, and the hot gas of recovery on the other hand is sprayed into disk 15 to vaporization chamber 4 by hot blast
Steam is passed through, the temperature in vaporization chamber 4 can be kept, beneficial to the evaporative crystallization of solution, while making the steam of generation keep higher
Temperature, the material in floater 5 separated out by crystal after evaporation, then discharged by the discharging opening 7 of the bottom of crystallisation chamber 6.
While there has been shown and described that embodiment of the present utility model, for the ordinary skill in the art,
It is appreciated that these embodiments can be carried out in the case where not departing from principle of the present utility model and spirit a variety of changes, repaiies
Change, replace and modification, scope of the present utility model is defined by the appended claims and the equivalents thereof.
Claims (3)
1. a kind of rose is produced with crystallization enrichment facility, including two groups of bearings（1）, it is characterised in that：The bearing（1）'s
Bottom is provided with support bar（2）, bearing described in two groups（1）Between be provided with tank body（3）, the tank body（3）Inner cavity top set
It is equipped with vaporization chamber（4）, the vaporization chamber（4）Bottom be provided with floater（5）, the floater（5）Bottom be provided with knot
Brilliant room（6）, the tank body（3）Bottom be provided with discharging opening（7）, the tank body（3）Right wall be provided with air-heater（8）, institute
State vaporization chamber（4）Inner cavity top be provided with hot air duct（9）, the air-heater（8）With hot air duct（9）Connection, the tank
Body（3）Top be provided with steam (vapor) outlet（10）, the tank body（3）Left wall be provided with circulation air pump（11）, the steam goes out
Mouthful（10）Pass through pipeline and circulation air pump（11）Connection, the left side bearing（1）Top be provided with heat exchanger（12）, it is described
Circulate air pump（11）Pass through pipeline and heat exchanger（12）Connection, the heat exchanger（12）Left wall bottom be provided with condensate liquid
Outlet（13）, the right side bearing（1）Top be provided with material box（14）, the material box（14）Pass through pipeline and floater
（5）Connection, the hot air duct（9）Bottom be provided with hot blast spray disk（15）, the heat exchanger（12）Pass through pipeline and heat
Wind sprays disk（15）Connection.
2. a kind of rose according to claim 1 is produced with crystallization enrichment facility, it is characterised in that：The warm-air pipe
Road（9）Top be provided with fog-spray nozzle, and fog-spray nozzle is provided with five groups of structure identical.
3. a kind of rose according to claim 1 is produced with crystallization enrichment facility, it is characterised in that：The hot blast spray
Disk（15）Outer wall be provided with spray hole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720086666.2U CN206463531U (en) | 2017-01-23 | 2017-01-23 | A kind of rose is produced with crystallization enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720086666.2U CN206463531U (en) | 2017-01-23 | 2017-01-23 | A kind of rose is produced with crystallization enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206463531U true CN206463531U (en) | 2017-09-05 |
Family
ID=59703122
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720086666.2U Expired - Fee Related CN206463531U (en) | 2017-01-23 | 2017-01-23 | A kind of rose is produced with crystallization enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206463531U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108057258A (en) * | 2018-01-18 | 2018-05-22 | 江西金利达钾业有限责任公司 | A kind of potassium nitrate spray crystallizer |
| CN108096862A (en) * | 2018-02-11 | 2018-06-01 | 刘召柱 | A kind of two-way atomization and vaporization tank of essence production |
| CN110755875A (en) * | 2019-11-24 | 2020-02-07 | 湖南力泓新材料科技股份有限公司 | Evaporation crystallization device for preparing zinc sulfate crystals |
| CN112779095A (en) * | 2021-01-07 | 2021-05-11 | 王海峰 | Rose hydrolat system is got and is used crystallization enrichment facility |
| CN116370978A (en) * | 2022-12-21 | 2023-07-04 | 江苏德邦兴华化工科技有限公司 | Separation equipment of sodium carbonate |
-
2017
- 2017-01-23 CN CN201720086666.2U patent/CN206463531U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108057258A (en) * | 2018-01-18 | 2018-05-22 | 江西金利达钾业有限责任公司 | A kind of potassium nitrate spray crystallizer |
| CN108057258B (en) * | 2018-01-18 | 2023-08-18 | 江西金利达钾业有限责任公司 | Potassium nitrate spray crystallizer |
| CN108096862A (en) * | 2018-02-11 | 2018-06-01 | 刘召柱 | A kind of two-way atomization and vaporization tank of essence production |
| CN108096862B (en) * | 2018-02-11 | 2020-04-24 | 江西省华宝孔雀食品科技发展有限公司 | Essence production is with two-way atomizing evaporating pot |
| CN110755875A (en) * | 2019-11-24 | 2020-02-07 | 湖南力泓新材料科技股份有限公司 | Evaporation crystallization device for preparing zinc sulfate crystals |
| CN112779095A (en) * | 2021-01-07 | 2021-05-11 | 王海峰 | Rose hydrolat system is got and is used crystallization enrichment facility |
| CN112779095B (en) * | 2021-01-07 | 2024-04-19 | 深圳市璐琥实业发展有限公司 | Crystallization and concentration device for preparing rose hydrosol |
| CN116370978A (en) * | 2022-12-21 | 2023-07-04 | 江苏德邦兴华化工科技有限公司 | Separation equipment of sodium carbonate |
| CN116370978B (en) * | 2022-12-21 | 2023-09-29 | 江苏德邦兴华化工科技有限公司 | Separation equipment of sodium carbonate |
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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: 20170905 Termination date: 20220123 |
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| CF01 | Termination of patent right due to non-payment of annual fee |