CN206483173U - A kind of glycine betaine salicylate, which is produced, uses evaporative filtration device - Google Patents
A kind of glycine betaine salicylate, which is produced, uses evaporative filtration device Download PDFInfo
- Publication number
- CN206483173U CN206483173U CN201720087034.8U CN201720087034U CN206483173U CN 206483173 U CN206483173 U CN 206483173U CN 201720087034 U CN201720087034 U CN 201720087034U CN 206483173 U CN206483173 U CN 206483173U
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- evaporating
- inner chamber
- column tank
- heater
- evaporating column
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Abstract
Produced the utility model discloses a kind of glycine betaine salicylate of electromechanical integration technology area and use evaporative filtration device, including evaporating column tank, the intracavity bottom of the evaporating column tank is provided with heater, evaporating dish is provided with the top of the heater, the left side wall of the evaporating column tank is provided with feed pipe, and the bottom of feed pipe is arranged on the inner chamber of evaporating dish, the outer wall of the feed pipe is provided with flow valve, the mutual cooperation that the utility model passes through heating wire in heater and temperature sensor, facilitate control of the operating personnel to evaporating temperature, make the product quality of production higher, pass through the mutual cooperation of oxidation catalyst filter device and filter, the amount of pollutant in reduction discharge gas, pass through the mutual cooperation of condenser and return duct, enable the glycine betaine salicylate contained in boil-off gas to be condensed to be back in evaporating dish again, reduce the loss of product, reduce production cost.
Description
Technical field
The utility model is related to electromechanical integration technology area, and specially a kind of glycine betaine salicylate is produced with evaporating
Filter device.
Background technology
Glycine betaine salicylate is a kind of chemical substance, mainly as bactericide, exfoliator etc., applied to personal nursing
Most of extraction of gas after articles for use field, traditional to(for) glycine betaine salicylate is vented directly in air, to air
Cause serious pollution, at the same gas be expelled directly out can take substantial amounts of glycine betaine salicylate out of, cause produce production capacity drop
It is low, increase production cost, and also evaporating temperature is not easily controlled, and the quality of product can be caused relatively low, therefore, it is proposed that a kind of
Glycine betaine salicylate, which is produced, uses evaporative filtration device.
Utility model content
The purpose of this utility model, which is to provide a kind of glycine betaine salicylate to produce, uses evaporative filtration device, with solution
State most of gas after the traditional extraction for glycine betaine salicylate proposed in background technology and be vented directly to air
In, serious pollution is caused to air, while gas be expelled directly out can take substantial amounts of glycine betaine salicylate out of, cause production
The reduction of production capacity, increases production cost, and evaporating temperature is not easily controlled, and can cause the problem of quality of product is relatively low.
To achieve the above object, the utility model provides following technical scheme：A kind of glycine betaine salicylate is produced with steaming
Filter, including evaporating column tank are sent out, the intracavity bottom of the evaporating column tank is provided with heater, the top of the heater
Portion is provided with evaporating dish, and the left side wall of the evaporating column tank is provided with feed pipe, and the bottom of feed pipe is arranged on evaporating dish
Inner chamber, the outer wall of the feed pipe is provided with flow valve, and the right side wall of the evaporating column tank is provided with blast pipe, the blast pipe
Right-hand member be connected with blower fan, the right side of the blower fan is connected with air purifier by pipeline, and the inner chamber of the evaporating column tank is horizontal
To condenser is provided with, the intracavity bottom left and right sides of the condenser is provided between draining plate, draining plate described in two groups
Vertically arranged return duct, and the bottom of return duct is arranged on the inner chamber of evaporating dish, the inner chamber of the evaporating column tank is horizontally arranged with
Oxidation catalyst filter device, and oxidation catalyst filter device is arranged on the top of condenser, at the top of the left side wall of the evaporating column tank inner chamber and
Uviol lamp is provided with the top of right side wall, the top of the evaporating column tank is vertically plugged with blast pipe, and the bottom of blast pipe is set
Put in the inner chamber of evaporating column tank, the inner chamber of the blast pipe is provided with filter.
It is preferred that, the inner chamber of the heater is evenly arranged with heating wire, and the inner cavity top of the heater is uniform
It is provided with temperature sensor.
It is preferred that, the outer wall of the oxidation catalyst filter device scribbles photocatalyst catalyst coatings.
It is preferred that, the filter includes filter screen filtration layer, and the top of the filter screen filtration layer sets active
Absorption sponge filter layer is provided with the top of charcoal filter layer, the activated carbon filter layer.
Compared with prior art, the beneficial effects of the utility model are：The utility model passes through heating wire in heater
With the mutual cooperation of temperature sensor, facilitate control of the operating personnel to evaporating temperature, make the product quality of production higher, pass through
The mutual cooperation of oxidation catalyst filter device and filter, reduction discharge gas in pollutant amount, by condenser and return
The mutual cooperation of flow tube, enables the glycine betaine salicylate contained in boil-off gas to be condensed and is back to again in evaporating dish,
The loss of product is reduced, production cost is reduced.
Brief description of the drawings
Fig. 1 is the utility model structural representation；
Fig. 2 is the utility model heater structural representation；
Fig. 3 is the utility model filter apparatus configuration schematic diagram.
In figure：1 evaporating column tank, 2 heaters, 21 heating wire, 22 temperature sensors, 3 evaporating dishes, 4 feed pipes, 5 flows
It is valve, 6 blast pipes, 7 blower fans, 8 air purifiers, 9 condensers, 10 draining plates, 11 return ducts, 12 oxidation catalyst filter devices, 13 ultraviolet
Lamp, 14 blast pipes, 15 filters, 151 filter screen filtrations layer, 152 activated carbon filter layers, 153 absorption sponge filter layers.
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.
Fig. 1-3 are referred to, the utility model provides a kind of technical scheme：A kind of glycine betaine salicylate is produced with evaporating
Device, including evaporating column tank 1 are filtered, the intracavity bottom of evaporating column tank 1 is provided with heater 2, and the top of heater 2 is provided with
Evaporating dish 3, the left side wall of evaporating column tank 1 is provided with feed pipe 4, and the bottom of feed pipe 4 is arranged on the inner chamber of evaporating dish 3, enters
The outer wall of expects pipe 4 is provided with flow valve 5, and the right side wall of evaporating column tank 1 is provided with blast pipe 6, and the right-hand member of blast pipe 6 is connected with wind
Machine 7, the right side of blower fan 7 is connected with air purifier 8 by pipeline, and the inner chamber of evaporating column tank 1 is horizontally arranged with condenser 9, cold
The intracavity bottom left and right sides of condenser 9 is provided with vertically arranged return duct 11 between draining plate 10, two groups of draining plates 10, and returns
The bottom of flow tube 11 is arranged on the inner chamber of evaporating dish 3, and the inner chamber of evaporating column tank 1 is horizontally arranged with oxidation catalyst filter device 12, and urges
Change at the top of the top that filter 12 is arranged on condenser 9, the left side wall of the inner chamber of evaporating column tank 1 and be provided with the top of right side wall
Uviol lamp 13, the top of evaporating column tank 1 is vertically plugged with blast pipe 14, and the bottom of blast pipe 14 is arranged on evaporating column tank 1
Inner chamber, the inner chamber of blast pipe 14 is provided with filter 15.
Wherein, the inner chamber of heater 2 is evenly arranged with heating wire 21, and the inner cavity top of heater 2 is evenly arranged with
Temperature sensor 22, enables the heating-up temperature in heater 2 to be monitored, and facilitates operating personnel to be evaporated the behaviour of temperature
Make, the outer wall of oxidation catalyst filter device 12 scribbles photocatalyst catalyst coatings, reduce the amount of harmful substance in discharge air, filtering
Device 15 includes filter screen filtration layer 151, and the top of filter screen filtration layer 151 is provided with activated carbon filter layer 152, activated carbon mistake
The top of filtering layer 152 is provided with the amount of pollutant in absorption sponge filter layer 153, reduction discharge gas.
Operation principle：The utility model is heated by the heating wire 21 in heater 2 to evaporating dish 3, by adding
Temperature sensor 22 in thermal 2 monitors the heating-up temperature of heating wire 21, facilitates operator to the tune of the heating-up temperature of evaporating dish 3
Section, is heated by heater 2 to evaporating dish 3, makes the raw material entered by feed pipe 4 in evaporating dish 3 by evaporative crystallization, simultaneously
Air after air purifier 8 is purified by blower fan 7 is entered in the evaporating dish 3 containing raw material liq by blast pipe 6, is passed through
The entrance of air enables the raw material liq in evaporating dish 3 to roll, and makes the evaporative crystallization of raw material liq more uniform, while plus
The evaporation of extract solution in fast liquid charging stock, the gas of evaporation first passes through difference of the condenser 9 according to set point, makes boil-off gas
In the gas condensation of glycine betaine salicylate that contains, the phase interworking that the drop after condensation passes through draining plate 10 and return duct 11
Close, being again introduced into evaporating dish 3 for concentration is evaporated again, the gas after being filtered by condenser 9 passes through oxidation catalyst filter device again
12 and uviol lamp 13 mutual cooperation carry out oxidation catalyst filter, reduce discharge air in harmful substance amount, eventually passed
Filter device 15 is discharged after filtering by blast pipe 14.
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 (4)
1. a kind of glycine betaine salicylate, which is produced, uses evaporative filtration device, including evaporating column tank（1）, it is characterised in that：It is described to steam
Send out tower tank（1）Intracavity bottom be provided with heater（2）, the heater（2）Top be provided with evaporating dish（3）, institute
State evaporating column tank（1）Left side wall be provided with feed pipe（4）, and feed pipe（4）Bottom be arranged on evaporating dish（3）Inner chamber,
The feed pipe（4）Outer wall be provided with flow valve（5）, the evaporating column tank（1）Right side wall be provided with blast pipe（6）, institute
State blast pipe（6）Right-hand member be connected with blower fan（7）, the blower fan（7）Right side air purifier is connected with by pipeline（8）,
The evaporating column tank（1）Inner chamber be horizontally arranged with condenser（9）, the condenser（9）The intracavity bottom left and right sides be all provided with
It is equipped with draining plate（10）, draining plate described in two groups（10）Between vertically arranged return duct（11）, and return duct（11）Bottom set
Put in evaporating dish（3）Inner chamber, the evaporating column tank（1）Inner chamber be horizontally arranged with oxidation catalyst filter device（12）, and be catalyzed
Filter device（12）It is arranged on condenser（9）Top, the evaporating column tank（1）At the top of the left side wall of inner chamber and right side wall top is
It is provided with uviol lamp（13）, the evaporating column tank（1）Top be vertically plugged with blast pipe（14）, and blast pipe（14）Bottom
It is arranged on evaporating column tank（1）Inner chamber, the blast pipe（14）Inner chamber be provided with filter（15）.
2. a kind of glycine betaine salicylate according to claim 1, which is produced, uses evaporative filtration device, it is characterised in that：It is described
Heater（2）Inner chamber be evenly arranged with heating wire（21）, the heater（2）Inner cavity top be evenly arranged with temperature
Sensor（22）.
3. a kind of glycine betaine salicylate according to claim 1, which is produced, uses evaporative filtration device, it is characterised in that：It is described
Oxidation catalyst filter device（12）Outer wall scribble photocatalyst catalyst coatings.
4. a kind of glycine betaine salicylate according to claim 1, which is produced, uses evaporative filtration device, it is characterised in that：It is described
Filter（15）Including filter screen filtration layer（151）, the filter screen filtration layer（151）Top be provided with activated carbon filtering
Layer（152）, the activated carbon filter layer（152）Top be provided with absorption sponge filter layer（153）.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720087034.8U CN206483173U (en) | 2017-01-23 | 2017-01-23 | A kind of glycine betaine salicylate, which is produced, uses evaporative filtration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720087034.8U CN206483173U (en) | 2017-01-23 | 2017-01-23 | A kind of glycine betaine salicylate, which is produced, uses evaporative filtration device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206483173U true CN206483173U (en) | 2017-09-12 |
Family
ID=59765881
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720087034.8U Expired - Fee Related CN206483173U (en) | 2017-01-23 | 2017-01-23 | A kind of glycine betaine salicylate, which is produced, uses evaporative filtration device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206483173U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854119A (en) * | 2018-06-25 | 2018-11-23 | 郑州仁宏医药科技有限公司 | A kind of drug vaporising device that medicine research and development safety is good |
-
2017
- 2017-01-23 CN CN201720087034.8U patent/CN206483173U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108854119A (en) * | 2018-06-25 | 2018-11-23 | 郑州仁宏医药科技有限公司 | A kind of drug vaporising device that medicine research and development safety is good |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170912 Termination date: 20220123 |