CN205461062U - A energy -efficient fountain concentrator for powder production - Google Patents
A energy -efficient fountain concentrator for powder production Download PDFInfo
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- CN205461062U CN205461062U CN201521139544.2U CN201521139544U CN205461062U CN 205461062 U CN205461062 U CN 205461062U CN 201521139544 U CN201521139544 U CN 201521139544U CN 205461062 U CN205461062 U CN 205461062U
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- energy
- heating chamber
- chuck
- powder
- vaporization chamber
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Abstract
The utility model provides an energy -efficient fountain concentrator for powder production, including heating chamber and evaporating chamber, the heating chamber top is equipped with the feed inlet, and the bottom is equipped with receives cream mechanism, the heating chamber top still be equipped with with the ejection of compact pipeline of evaporating chamber intercommunication, evaporating chamber bottom be equipped with with the backflow pipeline of the receipts cream mechanism intercommunication of heating chamber, wherein, the feed inlet of heating chamber is connected with the shower head, the shower head is located the central upper portion of heating chamber, the equipartition has a plurality of mouths that spray on the shower head. The utility model discloses the creation can make the extract of raw and other materials carry out quick concentration, effectively reduces the energy consumption, improves production efficiency.
Description
Technical field
The invention belongs to powder product and produces equipment technical field, is specifically related to a kind of efficient joint produced for powder
The haplo-effect concentrator of energy fountain, is particularly well-suited to the production of the product such as food, medicine, is particularly suited for Inonqqus obliquus class
The production and processing of product powder.
Background technology
The product such as medicine, food in process of production, typically after decocting, needs to use concentrator to carry raw-material
Taking liquid and carry out heating evaporation, this process needs to carry out in concentrator.
Inonqqus obliquus formal name used at school Inonotus obliquus (Pers.:Fr.) Pil á t (=Fuscoporia obliquus (Pers.:Fr.)),
Russia is referred to as chaga, is commonly called as Phaeoporus obliquus in China, is one of food with health-care effect.As far back as 16～17 generation
That records is among the people, and Inonqqus obliquus is just taken as a kind of tea-drinking prevent and treat various difficult miscellaneous diseases, including dermatosis, the intestines and stomach
Inflammation, hepatopathy etc..The main component of Inonqqus obliquus has polysaccharide, oxidation triterpenoid compound, melanin, SOD, polyphenol
Class materials etc., have the multiple efficacies such as regulation blood glucose, blood fat, antioxidation, anticancer, enhancing immunity.Along with people are good for
The enhancing of Kang Yishi, the research to edible and medicinal fungi deepens continuously, and Inonqqus obliquus becomes the fungus of most DEVELOPMENT PROSPECT,
Abroad, its extract is developed to the product of the multiple patterns such as health promoting beverage, macaroni, cake, confection.
During Inonqqus obliquus is prepared as various food beverage, generally requires and the sclerotium of Inonqqus obliquus is ground into
After Li, carry out decocting water and carry, it is thus achieved that Inonqqus obliquus extracting solution, owing in Inonqqus obliquus extracting solution, active constituent content is relatively low,
Containing too much moisture, it is also desirable to it is carried out concentration.Existing concentrator elapsed time is long, and production efficiency is relative
Relatively low, owing to when carrying out large-scale production, energy consumption is the hugest, the energy of concentration process often can not get fully and has
The utilization of effect.
Summary of the invention
The invention is for solving the problems of the prior art, it is provided that a kind of energy-efficient fountain produced for powder
Concentrator, it is possible to raw-material extracting solution carries out rapid concentration, effectively reduces energy consumption, improves production efficiency.
The invention includes that heating chamber and vaporization chamber, described heating chamber top are provided with charging aperture, and bottom is provided with Shou Gao mechanism,
Described heating chamber top is additionally provided with the discharge pipe connected with described vaporization chamber, is provided with and described heating bottom described vaporization chamber
The reflux line receiving cream mechanism connection of room.
Wherein, the outer wall of described heating chamber is provided with the first chuck, described first chuck is respectively equipped with and is passed through inside its hollow
The first JI and the first JO, gone out by the first JI and the first chuck respectively in described first chuck
Mouth is passed through and adds vapours.
Wherein, the outer wall of described vaporization chamber is provided with the second chuck, and described second chuck passes through a jet chimney and described first
Chuck is connected, and described second chuck is additionally provided with the second JO, for circulation or the pressure release of steam.Preferably, institute
State the second JO and described jet chimney the entrance of vaporization chamber be positioned on described second chuck relative to side.
Further, described jet chimney is provided with flow control valve.
Wherein, the charging aperture of described heating chamber connects has spray head, described spray head to be positioned at the central upper of described heating chamber,
Some spray nozzles it are evenly equipped with on described spray head.
Wherein, being also arranged at intervals with some soaking plate in described heating chamber, described soaking plate central authorities are provided with and pass through for liquid
Duct.
Wherein, it is provided with additional heat coil below described vaporization chamber.
Wherein, it is protruding that the inwall of described vaporization chamber is provided with arcuation, can partly be distributed, it is possible to along inwall overall distribution.
Wherein, being additionally provided with discharging spray nozzle in described vaporization chamber, described discharging spray nozzle connects with described discharge pipe, described in go out
Some discharging arm is circumferentially distributed on material shower nozzle.
Further, the arm end of described discharging arm is near vaporization chamber inwall, and tilts downwards in a certain angle with vertical direction,
It is preferably 30 °-75 °.
The invention provides the benefit that: the setting of (1) jet chimney and the second chuck makes the steam energy of heating chamber
It is used more effectively, has simultaneously worked as preventing the effect of upflowing vapor condensation in vaporium；(2) spray in heating chamber
It is quick in heating chamber that feed liquid to be heated can be dispersed into tiny drop, beneficially drop when entering by head and spray nozzle
Ground absorbs heat；(3) soaking plate can promote that feed liquid forms turbulent flow in heating chamber, increases the probability of collision and heat exchange,
Thus improve the rate of heat addition of feed liquid further；(4) in vaporization chamber, on the one hand arcuation projection is conducive to increasing vaporization chamber inwall
Area of dissipation, on the other hand liquid film is had stretching and thinning effect, and extends liquid film on the inwall of vaporization chamber
Holdup time；(5) design that the discharging arm of discharging spray nozzle and arm end tilt so that feed liquid is easy to more effectively be formed liquid film；
(6) the invention has high evaporation efficiency generally, the most also has more preferable energy-saving effect.
Accompanying drawing explanation
Fig. 1 is a kind of structural representation of the invention；
Fig. 2 is the Fig. 1 structural representation at other direction；
Fig. 3 is the sectional structure chart of Fig. 1；
Fig. 4 is showerhead configuration schematic diagram；
Fig. 5 is soaking plate structure schematic diagram；
Fig. 6 is discharging spray nozzle structural representation.
In figure, 1-heating chamber；11-charging aperture；12-Shou Gao mechanism；13-the first chuck；131-the first JI；132-
First JO；14-spray head；141-spray nozzle；15-soaking plate；151-duct；2-vaporization chamber；21-the second chuck；
211-the second JO；The additional heat coil of 22-；23-arcuation is protruding；24-discharging spray nozzle；241-discharging arm；2411-arm
End；3-discharge pipe；4-reflux line；5-jet chimney；51-flow control valve；
Detailed description of the invention
Below by combining accompanying drawing, the invention is further described.Concrete scheme described in the following examples is only
Illustrate that the content of the invention, be not used to the restriction to the invention.
As shown in figures 1 to 6, including heating chamber 1 and vaporization chamber 2, described heating chamber 1 top is provided with the structure of the invention
Charging aperture 11, bottom is provided with Shou Gao mechanism 12, and described heating chamber 1 top is additionally provided with the discharging connected with described vaporization chamber 2
Pipeline 13, is provided with the reflux line 14 that the Shou Gao mechanism 12 with described heating chamber 1 connects bottom described vaporization chamber 2, use
In evaporation after concentrated solution flow back into Shou Gao mechanism 12 carry out receive cream.
Wherein, the outer wall of described heating chamber 1 is provided with the first chuck 13, described first chuck 13 is respectively equipped with and is passed through wherein
The first JI 131 and the first JO 132 within Kong, respectively by the first chuck in described first chuck 13
Entrance 131 and the first JO 132 are passed through and add vapours, heat the feed liquid in heating chamber 1.
Wherein, the outer wall of described vaporization chamber 2 is provided with the second chuck 21, and described second chuck 21 is by a jet chimney 5
Being connected with described first chuck 13, described second chuck 21 is additionally provided with the second JO 211, for the circulation of steam
Or pressure release.Preferably, described second JO 211 and described jet chimney 5 are positioned at described at the entrance of vaporization chamber 2
On second chuck 21 relative to side, it is simple to the steam fully flowing in the second chuck 21 and covering.Owing to being used for adding
The steam heat in hot cell 1 is the highest, after heating the feed liquid in heating chamber 1, still has the highest in its cyclic process
Heat energy, directly get rid of circulation and will make to be in and higher the steam of heat energy can not get sufficiently effective utilization；And at vaporization chamber 2
In, owing to the auxiliary heating parts in vaporization chamber 2 is often arranged on bottom so that vaporization chamber 2 upper temp reduces, material
In liquid evaporation process, the gas of evaporation rises in vaporization chamber 2, and when moving to temperature relatively low top, a part is evaporated
Gas easily condense and reflux, reduce evaporation efficiency；And by arranging the second chuck 21 at the outer wall of vaporization chamber 2,
And utilize the waste heat of steam in heating chamber 1 to make the overall heat distribution of vaporization chamber 2 be stablized, effectively prevent and steam
Get angry the condensing reflux of body, not only improve evaporation efficiency, and make the heat energy of steam obtain sufficiently effective utilization.
Further, described jet chimney 5 is provided with flow control valve 51, for the adjustment of steam flow.
Wherein, the charging aperture 11 of described heating chamber 1 connects has spray head 14, described spray head 14 to be positioned at described heating chamber
The central upper of 1, described spray head 14 is evenly equipped with some spray nozzles 141, spray nozzle 141 energy of described spray head 14
Enough feed liquid to be heated is dispersed into tiny drop, beneficially drop when entering and absorbs heat rapidly in heating chamber 1,
Thus reach the effect of heating quickly.
Wherein, being also arranged at intervals with some soaking plate 15 in described heating chamber 1, described soaking plate 15 central authorities are provided with for liquid
The duct 151 passed through；Described soaking plate 15 can promote that feed liquid forms turbulent flow in heating chamber 1, increases collision and heat is handed over
The probability changed, thus improve the rate of heat addition of feed liquid further.
Wherein, below described vaporization chamber 2, it is provided with additional heat coil 22, the auxiliary heating of feed liquid in vaporization chamber 2.
Wherein, the inwall of described vaporization chamber 2 is provided with arcuation projection 23, can partly be distributed, it is possible to along inwall overall distribution,
The area of dissipation arranging the inwall being on the one hand conducive to increase vaporization chamber 2 of described arcuation projection 23, makes the second chuck 21
The heat of transmission effectively distributes in inside, on the other hand, it is also possible to the movement locus of feed liquid in increase vaporization chamber 2,
Liquid film is had stretching and thinning effect, extends the liquid film holdup time on the inwall of vaporization chamber 2, thus greatly
Improve the evaporation efficiency of feed liquid.
Wherein, being additionally provided with discharging spray nozzle 24 in described vaporization chamber 2, described discharging spray nozzle 24 is with described discharge pipe 13 even
Logical, some discharging arm 241 is circumferentially distributed on described discharging spray nozzle 24, makes the feed liquid of heating chamber 1 in different directions
It is dispersed into vaporization chamber 2, is more beneficial for feed liquid soaking in vaporization chamber 2 and evaporation.
Further, the arm end 2411 of described discharging arm 241 is near vaporization chamber 2 inwall, and tilts downwards and vertical direction
In a certain angle, preferably 30 °-75 ° so that feed liquid is directly distributed in after arm end 2411 ejection of discharging arm 241
On vaporization chamber 2 inwall, it is simple to more effectively form liquid film, improve evaporation efficiency further.
The foregoing is only the preferred embodiment of the invention, not in order to limit the invention, all at this
Within the spirit of bright creation and principle, any modification, equivalent substitution and improvement etc. made, should be included in present invention wound
Within the protection domain made.
Claims (10)
1. the energy-efficient fountain concentrator produced for powder, including heating chamber and vaporization chamber, described heating chamber
Top is provided with charging aperture, and bottom is provided with Shou Gao mechanism, and described heating chamber top is additionally provided with the discharging connected with described vaporization chamber
Pipeline, is provided with the reflux line receiving cream mechanism connection with described heating chamber bottom described vaporization chamber；
Wherein, the charging aperture of described heating chamber connects has spray head, described spray head to be positioned at the central upper of described heating chamber,
Some spray nozzles it are evenly equipped with on described spray head.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 1, it is characterised in that
The outer wall of described heating chamber is provided with the first chuck, and described first chuck is respectively equipped with the first chuck being passed through within its hollow
Entrance and the first JO, be passed through heating by the first JI and the first JO in described first chuck respectively
Steam.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 2, it is characterised in that
The outer wall of described vaporization chamber is provided with the second chuck, and described second chuck is connected with described first chuck by a jet chimney,
Described second chuck is additionally provided with the second JO, for circulation or the pressure release of steam.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 3, it is characterised in that
Described second JO and described jet chimney the entrance of vaporization chamber be positioned on described second chuck relative to side.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 3, it is characterised in that
Described jet chimney is provided with flow control valve.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 1, it is characterised in that
Also being arranged at intervals with some soaking plate in described heating chamber, described soaking plate central authorities are provided with the duct passed through for liquid.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 1, it is characterised in that
Additional heat coil it is provided with below described vaporization chamber.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 1, it is characterised in that
It is protruding that the inwall of described vaporization chamber is provided with arcuation.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 1, it is characterised in that
Being additionally provided with discharging spray nozzle in described vaporization chamber, described discharging spray nozzle connects with described discharge pipe, on described discharging spray nozzle in
Circle distribution has some discharging arms.
A kind of energy-efficient fountain concentrator produced for powder the most according to claim 9, its feature exists
In, the arm end of described discharging arm is near vaporization chamber inwall, and tilts downwards in a certain angle with vertical direction.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521139544.2U CN205461062U (en) | 2015-12-30 | 2015-12-30 | A energy -efficient fountain concentrator for powder production |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521139544.2U CN205461062U (en) | 2015-12-30 | 2015-12-30 | A energy -efficient fountain concentrator for powder production |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205461062U true CN205461062U (en) | 2016-08-17 |
Family
ID=56663201
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521139544.2U Expired - Fee Related CN205461062U (en) | 2015-12-30 | 2015-12-30 | A energy -efficient fountain concentrator for powder production |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205461062U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105457321A (en) * | 2015-12-30 | 2016-04-06 | 天津横天生物科技有限公司 | Energy-efficient spray-type concentrator for powder production |
| CN106943761A (en) * | 2017-04-07 | 2017-07-14 | 宝鸡宝冶钛镍制造有限责任公司 | Multiinjector low-power heating type vapor seperator |
| CN112516613A (en) * | 2020-11-16 | 2021-03-19 | 吉林省金鹏制药机械成套设备有限公司 | High-efficient vacuum evaporation device |
-
2015
- 2015-12-30 CN CN201521139544.2U patent/CN205461062U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105457321A (en) * | 2015-12-30 | 2016-04-06 | 天津横天生物科技有限公司 | Energy-efficient spray-type concentrator for powder production |
| CN106943761A (en) * | 2017-04-07 | 2017-07-14 | 宝鸡宝冶钛镍制造有限责任公司 | Multiinjector low-power heating type vapor seperator |
| CN112516613A (en) * | 2020-11-16 | 2021-03-19 | 吉林省金鹏制药机械成套设备有限公司 | High-efficient vacuum evaporation device |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| 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: 20160817 Termination date: 20181230 |