CN206483170U - Malleation enrichment facility - Google Patents
Malleation enrichment facility Download PDFInfo
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- CN206483170U CN206483170U CN201720104331.9U CN201720104331U CN206483170U CN 206483170 U CN206483170 U CN 206483170U CN 201720104331 U CN201720104331 U CN 201720104331U CN 206483170 U CN206483170 U CN 206483170U
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- tank body
- liquid
- malleation
- enrichment facility
- gas
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Abstract
The utility model is related to concentrator technical field; more particularly to a kind of malleation enrichment facility, malleation enrichment facility of the present utility model, heated using interlayer liquid; gas-powered pot liquid boiling type is mixed; power consumption is low, and liquid evaporation speed is fast in material, and cocnentration factor is high; liquid material is concentrated under gas shield; the extract of concentration out, with non-oxidation loss, it is pollution-free the features such as, it is and easy to clean.
Description
Technical field
The utility model is related to concentrator technical field, more particularly to a kind of malleation enrichment facility.
Background technology
Enrichment facility (concentration tank) is the conventional production equipment of the industries such as medicine, food, is mainly used in liquid material concentration
With solvent recovery, device is made up of heat exchanger, agitator, inspissator, condenser and pipeline valve etc..
Existing concentrator, evaporation rate is slower, and stirring has oxygen contact not in time, in heating process, causes material
Oxidational losses, influence concentration speed and quality.Accordingly, it is desirable to provide a kind of new technical scheme solves the above problems.
Utility model content
The technical problems to be solved in the utility model is：In order to solve existing concentrator, evaporation rate is slower, and stirring is not
In time, there is oxygen contact in heating process, cause the technical problem of material oxidational losses, influence concentration speed and quality, this reality
With a kind of malleation enrichment facility of new offer.
The utility model solves the technical scheme that its technical problem used：A kind of malleation enrichment facility, including sealing
Tank body, breather pipe and gas distributor, gas distributor is arranged on the bottom of tank inner chamber, one end of breather pipe and gas point
The gas access of orchestration is connected, and the other end of breather pipe is extend out to outside tank body from tank body upper surface, the other end of breather pipe
On be provided with dismountable sealing-plug, the upper end of the tank body is additionally provided with gas vent, and the shell of the tank body is double-deck outer
Shell, is divided into internal layer and outer layer, the cavity formation zone of heating between internal layer and outer layer, and the lower end of the tank wall is provided with liquid
Entrance, the upper end of tank wall is provided with liquid outlet, and liquid inlet is connected with liquid outlet with zone of heating.This practicality is new
The media such as water, oil can be passed through in the interlayer of type tank body ectonexine it be used for liquid material and heat with cooling down, gases at high pressure is from breather pipe
Entrance enter tank body, liquid material is entered by gas distributor, is then flowed out from gas vent, and takes away the water in material
Point.
Gas-powered pot liquid boiling type is mixed, and is consumed energy low, and liquid evaporation speed is fast in material, and cocnentration factor is high, liquid material
Concentrated under gas shield, the extract of concentration out, with non-oxidation loss, it is pollution-free the features such as, and cleaning side
Just.
For the ease of the pressure in monitoring tank body in real time, pressure sensor is additionally provided with the tank body.
The beneficial effects of the utility model are that malleation enrichment facility of the present utility model is heated, gas using interlayer liquid
The mixing of pot liquid boiling type is driven, is consumed energy low, liquid evaporation speed is fast in material, cocnentration factor is high, and liquid material is under gas shield
Concentrated, the extract of concentration out, with non-oxidation loss, it is pollution-free the features such as, it is and easy to clean.
Brief description of the drawings
The utility model is further illustrated with reference to the accompanying drawings and examples.
Fig. 1 is the structural representation of the utility model optimum embodiment.
In figure：1st, tank body, 11, internal layer, 12, outer layer, 2, breather pipe, 3, gas distributor, 4, gas vent, 5, liquid enters
Mouthful, 6, pressure sensor, 7, pressure sensor.
Embodiment
The utility model is described in further detail presently in connection with accompanying drawing.These accompanying drawings are simplified schematic diagram,
Only illustrate basic structure of the present utility model in a schematic way, therefore it only shows the composition relevant with the utility model.
As shown in figure 1, be the utility model optimum embodiment, a kind of malleation enrichment facility, including it is sealed tank body 1, logical
Tracheae 2 and gas distributor 3, gas distributor 3 are arranged on the bottom of the inner chamber of tank body 1, one end of breather pipe 2 and gas distributor
3 gas access is connected, and the other end of breather pipe 2 is extend out to outside tank body 1 from the upper surface of tank body 1, the other end of breather pipe 2
On be provided with dismountable sealing-plug, the upper end of tank body 1 be additionally provided with gas vent 4, gas vent 4 is also equipped with it is detachable
Sealing-plug, the shell of tank body 1 is double casing, is divided into internal layer 11 and outer layer 12, the cavity shape between internal layer 11 and outer layer 12
Into zone of heating, the lower end of the outer wall of tank body 1 is provided with liquid inlet 5, and the upper end of the outer wall of tank body 1 is provided with liquid outlet 6, and liquid enters
Mouth 5 is connected with liquid outlet 6 with zone of heating.Pressure sensor 7 is additionally provided with tank body 1.
Before use, first the sealing-plug on the other end of the sealing-plug on gas vent 4 and breather pipe 2 is opened, tank body 1
Built with liquid material to be concentrated, hot water is passed through at liquid inlet 5 in the zone of heating of tank body 1, is flowed out from liquid outlet 6,
High pressure nitrogen is entered in tank body 1 by gas actuating device from the other end of breather pipe 2, then distributes nitrogen by gas distributor 3,
So that nitrogen is distributed in the bottom of tank body 1 to surrounding, into liquid material, then nitrogen flows out from gas vent 4, liquid material
The moisture of middle evaporation is also taken out of by gas vent 4 in the lump, into subsequent condensation retracting device, and final liquid material is concentrated.
Using it is above-mentioned according to desirable embodiment of the present utility model as enlightenment, pass through above-mentioned description, related work people
Member can carry out various changes and amendments in the range of without departing from this utility model technological thought completely.This reality
The content on specification is not limited to new technical scope, it is necessary to its technology is determined according to right
Property scope.
Claims (2)
1. a kind of malleation enrichment facility, it is characterised in that：Including sealed tank body (1), breather pipe (2) and gas distributor (3),
Gas distributor (3) is arranged on the bottom of tank body (1) inner chamber, one end of breather pipe (2) and the gas access of gas distributor (3)
It is connected, the other end of breather pipe (2) is extend out on tank body (1) outside, the other end of breather pipe (2) from tank body (1) upper surface
Dismountable sealing-plug is provided with, the upper end of the tank body (1) is additionally provided with gas vent (4), and the shell of the tank body (1) is
Double casing, is divided into internal layer (11) and outer layer (12), the cavity formation zone of heating between internal layer (11) and outer layer (12), the tank
The lower end of body (1) outer wall is provided with liquid inlet (5), and the upper end of tank body (1) outer wall is provided with liquid outlet (6), liquid inlet
(5) it is connected with liquid outlet (6) with zone of heating.
2. malleation enrichment facility as claimed in claim 1, it is characterised in that：Pressure sensor is additionally provided with the tank body (1)
(7)。
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104331.9U CN206483170U (en) | 2017-01-24 | 2017-01-24 | Malleation enrichment facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104331.9U CN206483170U (en) | 2017-01-24 | 2017-01-24 | Malleation enrichment facility |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206483170U true CN206483170U (en) | 2017-09-12 |
Family
ID=59767207
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720104331.9U Active CN206483170U (en) | 2017-01-24 | 2017-01-24 | Malleation enrichment facility |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206483170U (en) |
-
2017
- 2017-01-24 CN CN201720104331.9U patent/CN206483170U/en active Active
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| GR01 | Patent grant | ||
| GR01 | Patent grant |