CN109091897A - A kind of low temperature concentration basin - Google Patents
A kind of low temperature concentration basin Download PDFInfo
- Publication number
- CN109091897A CN109091897A CN201811061519.5A CN201811061519A CN109091897A CN 109091897 A CN109091897 A CN 109091897A CN 201811061519 A CN201811061519 A CN 201811061519A CN 109091897 A CN109091897 A CN 109091897A
- Authority
- CN
- China
- Prior art keywords
- porous plate
- hollow porous
- concentration basin
- low temperature
- boiling pool
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0082—Regulation; Control
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L21/00—Marmalades, jams, jellies or the like; Products from apiculture; Preparation or treatment thereof
- A23L21/20—Products from apiculture, e.g. royal jelly or pollen; Substitutes therefor
- A23L21/25—Honey; Honey substitutes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01B—BOILING; BOILING APPARATUS ; EVAPORATION; EVAPORATION APPARATUS
- B01B1/00—Boiling; Boiling apparatus for physical or chemical purposes ; Evaporation in general
- B01B1/005—Evaporation for physical or chemical purposes; Evaporation apparatus therefor, e.g. evaporation of liquids for gas phase reactions
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/0011—Heating features
- B01D1/0041—Use of fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/14—Evaporating with heated gases or vapours or liquids in contact with the liquid
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
Abstract
A kind of low temperature concentration basin, including boiling pool, air blower, hollow porous plate, heater, cover board and negative-pressure air fan, cover plate lid is in boiling pool, ventilation duct is connected on cover board, ventilation duct one end is equipped with negative-pressure air fan, and air blower is connected by pipeline with hollow porous plate, and heater is mounted on the pipeline between air blower and hollow porous plate, hollow porous plate is fixed on the bottom of boiling pool, and hollow porous plate upper surface only a fraction has stomata.Low temperature concentration basin of the invention, stomata is distributed in its hollow porous plate upper surface only a fraction, the liquid material for corresponding to Bubble Region is set to generate upward flowing during bubble rises, it is rolled again to bubble-free area, to make the liquid material of concentration basin internal upper part and lower part mix, the uneven problem of existing cold concentration basin concentration is overcome.Negative-pressure air fan quickly detaches the humid air above concentration basin, and makes to have further speeded up the evaporation rate of moisture in certain negative pressure state inside concentration basin.
Description
Technical field
The present invention relates to the liquid material concentrators more particularly to a kind of low temperature concentration basin in food industry.
Background technique
Honey cannot be concentrated using high temperature evaporation, because high temperature can destroy the active constituent in honey, reduce honey itself
Nutritive value.Though problems, its high requirements on the equipment are not present in freeze concentration and vacuum concentration, process equipment structure is answered
Miscellaneous and equipment cost and O&M cost are all very high.Patent CN201310428173 discloses a kind of imitating natural honey thickener, leads to
Cross air blower the honey on flow plate is carried out it is air-dried, but since in the thickener, honey leaves at stock, and inclined
Flowing velocity is slow on plate, and the contact area of air and honey is limited, and thickening efficiency is not high, and concentration amount is small, is not suitable for batch production
Large-scale use.Patent CN2018101895214 discloses one kind and blows the cold concentration basin of boiling, is caused air flow through using air blower
Empty porous plate generates a large amount of bubbles, and a large amount of bubbles take away the moisture in honey in uphill process.This method is relative to previous
The imitative nature thickener of kind has biggish progress, but finds in actual use, after the completion of cold concentration operation, the honey in pond
Concentration is simultaneously unbalanced, and the concentration of concentration bottom of pond portion honey is greater than the honey on pond body top, this is because a large amount of bubble simultaneously from
Pool bottom rises, and bubble has preferentially taken away the moisture in pool bottom honey, this is in the process again since the honey of bottom of pond is close
Degree is greater than pond body top, because due to the honey that has been concentrated can be deposited on bottom, lead to concentration unevenly.In water content detection,
If being taken at pond body top, will lead to concentration, and influenced mouthfeel and also increase processing cost, and if pond body sample, can lead
Cause concentration insufficient, moisture content honey not up to standard is easy to fermentation blistering after filling, influences quality, or even cannot eat.
So requiring to be stirred the honey in pond with stirring every time after concentration, detection is then carried out again and is concentrated again, very
It is time-consuming and laborious.In addition, it has also been found that, the honey through supercooling concentration is when temperature is lower in winter, the sugarcane in honey in Quality Detection
Sugared content is easy to exceeded, and after-ripening is incomplete, and when winter low temperature, and concentration time is much higher than summer, and power consumption is also more.Reason
It is, temperature is higher when summer, and moisture additional issue is fast, and the sucrase active in honey is higher, and the sucrose in honey is cold concentrated
More thoroughly, and winter temperature is lower for the ratio decomposed in journey, causes to evaporate slack-off, and sucrase active is low, leads to sucrose decomposition not
Completely.
Summary of the invention
The purpose of the present invention is to provide a kind of can to make the cold concentration basin of liquid material convection current in concentration process, so that liquid
Body material is concentrated more uniform.
For achieving the above object, the technical solution of the present invention is as follows:
A kind of low temperature concentration basin, including boiling pool, air blower, hollow porous plate, heater, cover board and negative-pressure air fan, lid
Plate covers in boiling pool, and ventilation duct is connected on cover board, and ventilation duct one end is equipped with negative-pressure air fan, and air blower is by pipeline in
Empty porous plate is connected, and air blower is located on the liquid level in boiling pool, heater be mounted on air blower and hollow porous plate it
Between pipeline on, and heater is located on the liquid level in boiling pool, and hollow porous plate is fixed on the bottom of boiling pool, hollow more
Orifice plate upper surface only a fraction has stomata.
Technical solution as a further improvement of that present invention, the gas cell distribution is in the hollow porous plate upper surface
Portion or periphery.
Technical solution as a further improvement of that present invention, the leachy part of tool are located in hollow porous plate
Portion, the leachy part of tool is polygon.
Technical solution as a further improvement of that present invention, the polygon be triangle, it is rectangular, pentalpha or just
Octagon.
Technical solution as a further improvement of that present invention, further includes discharge nozzle, the first control valve, and discharge nozzle passes through described
The side wall of boiling pool is simultaneously connected with the hollow porous plate, and the first control valve is on discharge nozzle.
Technical solution as a further improvement of that present invention further includes charge pipe, the second control valve and storage tank.Charge pipe
One end be connected with the boiling pool, the other end is connected with storage tank, and the second control valve is on the charge pipe.
Compared with prior art, beneficial effects of the present invention:
1. one kind provided by the invention blows the cold concentration basin of boiling, generate hollow porous plate upper surface by air blower a large amount of
Bubble, a large amount of bubbles pass through liquid material in uphill process and take away the moisture in liquid material；
2. stomata is distributed in hollow porous plate upper surface only a fraction, make to correspond to bubble during bubble rises
The liquid material in area generates upward flowing, then rolls to bubble-free area, to make the liquids of concentration basin internal upper part and lower part
Material mixes, and overcomes the uneven problem of existing cold concentration basin concentration；
3. by the dry air for the air-flow certain temperature that heater and deduster make to enter in porous plate, accelerating liquid object
The evaporation rate of moisture in material；When liquid material is honey, the After-ripening of honey may additionally facilitate；
4. quickly detaching the humid air above concentration basin by negative-pressure air fan, and make to bear inside concentration basin in certain
Pressure condition has further speeded up the evaporation rate of moisture.
Detailed description of the invention
Fig. 1 is a kind of structural schematic diagram of low temperature concentration basin of the embodiment of the present invention；
Fig. 2 is hollow porous plate of gas cell distribution when middle part in the embodiment of the present invention；
Fig. 3 is hollow porous plate of gas cell distribution when periphery in the embodiment of the present invention；
In Fig. 1-3,1- boiling pool；2- air blower；3- hollow porous plate；4- heater；5- deduster；6- discharge nozzle, 7-
First control valve；8- charge pipe；The second control valve of 9-；10- storage tank；11- cover board；12- negative-pressure air fan.
Specific embodiment:
The present invention is described further with reference to the accompanying drawings.
Embodiment 1
As shown in Figure 1, a kind of low temperature concentration basin, including boiling pool 1, air blower 2, hollow porous plate 3, heater 4, dedusting
Device 5, cover board 11 and negative-pressure air fan 12.Cover board 11 covers in boiling pool 1, and ventilation duct, ventilation duct one end peace are connected on cover board 11
Equipped with negative-pressure air fan 12.Air blower 2 is connected by pipeline with hollow porous plate 3, and air blower 2 is located on the liquid level of boiling pool 1,
Heater 4 is mounted on the pipeline between air blower 2 and hollow porous plate 3, and heater 4 is located on the liquid level of boiling pool 1,
Hollow porous plate 3 is fixed on the bottom of boiling pool 1.
Its working principle is that air blower 2 will be done when opening air blower 2, deduster 5, heater 4 and negative-pressure air fan 12
Air blasts hollow porous plate 3, makes a large amount of bubbles of Surface Creation thereon, and a large amount of bubbles pass through in concentration basin 1 in uphill process
Liquid material, to take away the moisture in liquid material, meanwhile, negative-pressure air fan 12 is quick by the humid air of 1 top of concentration basin
It detaches, and makes to have further speeded up the evaporation rate of moisture in liquid material in certain negative pressure state inside concentration basin 1.
As shown in Figures 2 and 3, only part has stomata on the upper surface of hollow porous plate 3, and gas cell distribution is in hollow porous
The middle part or periphery of plate 3 make the liquid material for the Bubble Region for corresponding to stomata generate upward stream during bubble rises
It is dynamic, then roll to the bubble-free area of stomata is not corresponded to, to make in concentration process, the liquids of concentration basin 1 internal upper part and lower part
Material can be mutually mixed.
Embodiment 2
The cold concentration operation of honey is carried out using the low temperature concentration basin in embodiment 1, it is to be concentrated by being added in boiling pool 1
Honey opens air blower 2, deduster 5, heater 4 and negative-pressure air fan 12, and the air in pipeline is through 5 dedusting of deduster and heating
Device 4 becomes dry air after heating and enters hollow porous plate 3, and 3 upper surface of hollow porous plate is made to generate a large amount of bubbles.Bubble is in honey
Middle rapid increase takes away moisture therein, and negative-pressure air fan 12 quickly detaches the humid air of 1 top of concentration basin.Heating is adjusted simultaneously
The output power of device 4 makes the temperature of the honey raw material in concentration basin 1 reach 37 DEG C or so, and the invertase in honey is made to be in most suitable
Temperature reaches while low temperature concentration so that the sucrose in honey sufficiently decomposes, promotes the after-ripening of honey raw material.
During bubble rises, the honey for corresponding to stomata flows up under the drive for rising bubble, to concentration
1 top of pond is rolled again to the bubble-free area for not corresponding to stomata, meanwhile, the honey for not corresponding to the bubble-free area of stomata flows to correspondence
The Bubble Region of stomata, to make in concentration process, the honey of 1 internal upper part of concentration basin and lower part can be mutually mixed, and be overcome
Uneven problem is concentrated.
In addition, for the ease of feed and be concentrated honey discharge, increase discharge nozzle 6, the first control valve 7, charge pipe 8,
Storage tank 10 and the second control valve 9.The side wall that discharge nozzle 6 passes through boiling pool 1 is connected with hollow porous plate 3, the first control valve 7
On discharge nozzle 6.One end of charge pipe 8 is connected with boiling pool 1, and the other end is connected with storage tank 10, and the second control valve 9 is mounted in
On charge pipe 8.Charge pipe 8 and the connector of boiling pool 1 are located in boiling pool 1 on honey liquid level.The concentration for carrying out honey is made
Before industry, first honey to be concentrated can be stored in storage tank 10.After the honey in boiling pool 1 has been concentrated, first is opened
The honey being concentrated is discharged in control valve 7, at this point, air blower 2 does not shut down, the row that the honey being concentrated can be made more efficient
Out, honey will not accumulate in hollow porous plate 3.After good honey discharge to be concentrated, the first control valve 7 is closed, opens the
Honey to be concentrated in storage tank 10 is added boiling pool 1 by charge pipe 8 by two control valves 9 again.After charging, close
Second control valve 9 continues the concentration operation of honey.
Claims (6)
1. a kind of low temperature concentration basin, which is characterized in that including boiling pool, air blower, hollow porous plate, heater, cover board and bear
Pressure fan, cover plate lid are connected with ventilation duct in boiling pool on cover board, ventilation duct one end is equipped with negative-pressure air fan, and air blower is logical
It crosses pipeline to be connected with hollow porous plate, heater is mounted on the pipeline between air blower and hollow porous plate, hollow porous plate
It is fixed on the bottom of boiling pool, hollow porous plate upper surface only a fraction has stomata.
2. a kind of low temperature concentration basin according to claim 1, which is characterized in that the gas cell distribution is in described hollow porous
The middle part or periphery of plate upper surface.
3. a kind of low temperature concentration basin according to claim 1, which is characterized in that the leachy part of tool is located at hollow
The middle part of porous plate, the leachy part of tool is polygon.
4. a kind of low temperature concentration basin according to claim 3, which is characterized in that the polygon be triangle, it is rectangular,
Pentalpha or octagon.
5. a kind of low temperature concentration basin according to claim 1, which is characterized in that further include discharge nozzle, the first control valve, out
Expects pipe passes through the side wall of the boiling pool and is connected with the hollow porous plate, and the first control valve is on discharge nozzle.
6. a kind of low temperature concentration basin according to claim 1, which is characterized in that further include charge pipe, the second control valve and
Storage tank, one end of charge pipe are connected with the boiling pool, and the other end is connected with storage tank, and the second control valve is mounted in charge pipe
On.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811061519.5A CN109091897A (en) | 2018-09-12 | 2018-09-12 | A kind of low temperature concentration basin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811061519.5A CN109091897A (en) | 2018-09-12 | 2018-09-12 | A kind of low temperature concentration basin |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN109091897A true CN109091897A (en) | 2018-12-28 |
Family
ID=64866182
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811061519.5A Pending CN109091897A (en) | 2018-09-12 | 2018-09-12 | A kind of low temperature concentration basin |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN109091897A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114470830A (en) * | 2021-12-07 | 2022-05-13 | 安徽世华化工有限公司 | Ethanol recovery and purification device |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463823A (en) * | 2013-09-18 | 2013-12-25 | 翟自景 | Thickener capable of imitating natural honey |
| CN205313204U (en) * | 2015-12-11 | 2016-06-15 | 广西南宁绿泽环保科技有限公司 | Multistage compound moving bed biofilm reactor MC -MBBR's aeration systems |
| CN206444210U (en) * | 2016-12-18 | 2017-08-29 | 曲靖市沾益区红联养蜂专业合作社 | A kind of vacuum concentration purifying plant of honey |
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN108434765A (en) * | 2018-03-08 | 2018-08-24 | 江苏师范大学 | One kind blowing the cold concentration basin of boiling |
-
2018
- 2018-09-12 CN CN201811061519.5A patent/CN109091897A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103463823A (en) * | 2013-09-18 | 2013-12-25 | 翟自景 | Thickener capable of imitating natural honey |
| CN205313204U (en) * | 2015-12-11 | 2016-06-15 | 广西南宁绿泽环保科技有限公司 | Multistage compound moving bed biofilm reactor MC -MBBR's aeration systems |
| CN206444210U (en) * | 2016-12-18 | 2017-08-29 | 曲靖市沾益区红联养蜂专业合作社 | A kind of vacuum concentration purifying plant of honey |
| CN108404435A (en) * | 2018-03-08 | 2018-08-17 | 江苏师范大学 | A kind of cold concentration tower |
| CN108434765A (en) * | 2018-03-08 | 2018-08-24 | 江苏师范大学 | One kind blowing the cold concentration basin of boiling |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114470830A (en) * | 2021-12-07 | 2022-05-13 | 安徽世华化工有限公司 | Ethanol recovery and purification device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107012073B (en) | Aerobic fermentation system | |
| CN209558832U (en) | A kind of drying device dry for pannage | |
| CN206483378U (en) | A kind of agitator for being easy to control temperature and humidity | |
| CN108404435A (en) | A kind of cold concentration tower | |
| CN204499328U (en) | A kind of grain drying device | |
| CN206347826U (en) | A kind of raw material of industry removal moisture drying tank for being easy to control inlet amount | |
| CN109091897A (en) | A kind of low temperature concentration basin | |
| CN208700917U (en) | A kind of automation fertilizer installation for fermenting | |
| CN109091896A (en) | A kind of low temperature method for concentration of liquid material | |
| CN104757364B (en) | A kind of honey concentrating device | |
| CN109107205A (en) | A kind of convection type low-temp concentration basin | |
| CN108434765A (en) | One kind blowing the cold concentration basin of boiling | |
| CN204973737U (en) | Viscidity powder material disperses dissolving device fast | |
| CN210313950U (en) | A municipal sludge fermentation vat for preparing afforestation soil | |
| CN206980126U (en) | A kind of small-sized honey thickener | |
| CN220450069U (en) | Straw fermentation treatment device | |
| CN208711622U (en) | Flocculant automatic dilution and transportation system | |
| CN206420285U (en) | A kind of hot-air drying device of Dual-energy source heat supply | |
| CN206121181U (en) | Tomato is with heating enrichment facility | |
| CN207854701U (en) | A kind of plant protection fertilizer apparatus | |
| CN218846737U (en) | Lopinavir intermediate storage equipment | |
| CN206502811U (en) | A kind of hydraulic methane pool device for exempting from crust | |
| CN209092738U (en) | A kind of enrichment facility in liquid fertilizer production | |
| CN209573079U (en) | A kind of full-automatic pile fermentation device of Dark Green Tea | |
| CN206809804U (en) | A kind of triple effect evaporation equipment |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20181228 |
|
| WD01 | Invention patent application deemed withdrawn after publication |