CN104432442A - Food freeze-concentration device - Google Patents
Food freeze-concentration device Download PDFInfo
- Publication number
- CN104432442A CN104432442A CN201410733045.XA CN201410733045A CN104432442A CN 104432442 A CN104432442 A CN 104432442A CN 201410733045 A CN201410733045 A CN 201410733045A CN 104432442 A CN104432442 A CN 104432442A
- Authority
- CN
- China
- Prior art keywords
- chamber
- crystallizer
- separation chamber
- crystallization
- food
- 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
Landscapes
- Freezing, Cooling And Drying Of Foods (AREA)
- Fats And Perfumes (AREA)
Abstract
The invention discloses a food freeze-concentration device. The food freeze-concentration device comprises a freeze-insulation chamber, a crystallization chamber and a separation chamber which are sequentially arranged from top to bottom, wherein a charge tube is arranged at the top end of the freeze-insulation chamber; a group of crystallization tubes are arranged in the crystallization chamber and communicated with the freeze-insulation chamber; the top end of the separation chamber is connected with the bottom end of the crystallization chamber, the separation chamber is communicated with the crystallization tubes, a discharge tube is arranged on the sidewall of the separation chamber, a suction filtration tube and a circulation tube are arranged on the discharge tube, the end part of the circulation tube extends into the freeze-insulation chamber, a liquid suction pump is arranged on the circulation tube, a valve is arranged on the discharge tube, the end part of the discharge tube is connected with a material collection tank, and vertical filter cloth is further arranged between the discharge tube and the group of crystallization tubes in the separation chamber. The food freeze-concentration device disclosed by the invention overcomes the technical effects of slow crystallization speed, non-uniform crystallized crystal sizes and low separation efficiency of the existing food freeze-concentration device, and provides a food freeze-concentration device which is fast in crystallization speed, uniform in crystallized crystal sizes and high in separation efficiency.
Description
Technical field
The invention belongs to Food Freeze Concentration field, be specifically related to a kind of Food Freeze Concentration device.
Background technology
The freeze concentration of food is a kind of food-processing method making the solvent crystallization in food by sub-cooled thus improve food concentration, freeze concentration is generally used for some to the more sensitive food liquid of ratio of specific heat, can also keep the natural aromatic material in product.Because freeze concentration energy consumption is low and concentrated product quality is high, therefore it has huge development potentiality.
Freeze concentration mainly comprises the following steps: the cooling of food liquid, the crystallization of food liquid, crystal are separated with concentrate.Current Food Freeze Concentration is normally carried out in freezing concentrating device, existing freezing concentrating device generally includes crystallisation chamber and separation chamber, the crystallisation by cooling of crystallisation chamber charge liquid food, separation chamber is responsible for being separated of crystal and concentrate, and crystallisation chamber and separation chamber normally separate, first food liquid is inputted during operation in the crystallisation chamber of low temperature and carry out automatic crystallisation by cooling, again concentrate and crystal are delivered to separation chamber together by pipeline after crystallization a period of time to be cooled to filter, the filtrate after filtration is required concentrate.
But, because food liquid is actionless during crystallisation by cooling in crystallisation chamber, and cooling medium is usually located at that crystallisation chamber is outer, itself and food liquid generation heat exchange time normally from outside to inside, therefore inner food liquid temperature can be made higher than the food liquid temperature of outside, namely food liquid is caught a cold inequality, thus in food liquid, the crystalline particle granularity of solvent is uneven, is not easy to filter, and the crystallization rate of food liquid can be made slow, thus cause whole concentration process efficiency low.In addition, the filter cloth in existing separation chamber is all laterally place, after filtration usually, crystal is blocked in filter cloth upper surface, and when the crystal accumulation thickness on filter cloth is larger, the follow-up rate of filtration can be more and more lower, thus affect separative efficiency, and then affect whole condensing crystallizing efficiency.
Summary of the invention
The technical problem to be solved in the present invention is the uneven and technological deficiency that separative efficiency is low of crystal size that is slow for existing Food Freeze Concentration device crystallization rate, crystallization, provide that a kind of crystallization rate is fast, the crystal size of crystallization evenly and the high Food Freeze Concentration device of separative efficiency.
In order to solve the problems of the technologies described above, the invention provides following technical scheme: Food Freeze Concentration device, comprise freezing moist closet, crystallisation chamber and separation chamber, described freezing moist closet top is provided with feed pipe, the top of described crystallisation chamber is connected with the bottom of freezing moist closet, crystallization chamber is provided with one group of crystallizer, crystallizer two ends are each passed through crystallisation chamber top and crystallisation chamber bottom, and crystallizer communicates with freezing moist closet, on the left of crystallisation chamber, the bottom of sidewall is provided with feed tube, and the top of crystallisation chamber right sidewall is provided with escape pipe, the top of described separation chamber is connected with the bottom of crystallisation chamber, and separation chamber communicates with crystallizer, the sidewall of separation chamber is provided with discharge nozzle, discharge nozzle is provided with suction filtering tube and circulation pipe, the end of suction filtering tube extends to the top of freezing moist closet, the end of circulation pipe extends in freezing moist closet, circulation pipe is provided with drawing liquid pump, discharge nozzle is positioned at the outside of suction filtering tube, and the outside being positioned at circulation pipe is provided with valve, the end of discharge nozzle is connected with aggregate tank, between discharge nozzle and one group of crystallizer, vertical filter cloth discharge nozzle and one group of crystallizer separated also is provided with in separation chamber, the bottom of separation chamber is provided with crystal outlet.
Adopt the Food Freeze Concentration device of technical solution of the present invention, comprise freezing moist closet, freezing moist closet is used for liquid towards food and carries out pre-cooled, thus efficiency when accelerating food liquid crystallization, the top of freezing moist closet is provided with feed pipe, for inputting food liquid, also comprise crystallisation chamber, crystallisation chamber is used for the crystallisation by cooling of food liquid, crystallization chamber is provided with feed tube, escape pipe and one group of crystallizer, feed tube is used for the input of liquid cooling medium, escape pipe is used for the output of cooling medium steam, crystallizer is used for the crystallisation by cooling of liquid food, is spaced apart from each other between one group of crystallizer, also comprise separation chamber, separation chamber is used for being separated of crystalline solid and concentrate, the sidewall of separation chamber is provided with discharge nozzle, discharge nozzle is for exporting concentrate, discharge nozzle is provided with suction filtering tube, circulation pipe, valve and the end of discharge nozzle is connected with aggregate tank, suction filtering tube is for accelerating the filtration of concentrate and crystalline solid, during enforcement, the end of suction filtering tube is connected with suction filter pump, suction filtering tube extends to the top of freezing moist closet, thus suction filter pump can be avoided to contact with concentrate, circulation pipe is used for the circulation crystallization of concentrate, concentrate is avoided to enter in aggregate tank when valve is used for circulation crystallization, aggregate tank is for collecting qualified concentrate, also filter cloth is provided with in separation chamber, filter cloth is used for the filtration of concentrate and crystalline solid, the bottom of separation chamber is also provided with crystal outlet, crystal outlet is used for the discharge of crystalline solid.
Know-why of the present invention and technique effect are: food liquid carries out pre-cooled in freezing moist closet, during enforcement, the temperature of freezing moist closet is adjusted to the crystallization temperature near solvent, thus when food liquid enters in crystallizer can crystallization rapidly, thus make the granule size of crystalline solid even, be convenient to isolated by filtration; Crystallizer is in the separate setting of crystallization chamber, cooling medium is still can be used for pass through between crystallizer and crystallizer, thus cooling medium promptly can cool the food liquid of inside, namely food liquid is caught a cold evenly, make the crystalline solid granule size of solvent in food liquid even, be convenient to isolated by filtration; Because discharge nozzle is positioned on the sidewall of separation chamber, filter cloth is vertical setting, therefore when crystalline solid moves to filter cloth surface because the Action of Gravity Field of himself can downward landing, thus avoid crystalline solid and be piled up in filter cloth surface and then avoid crystalline solid and hinder the subsequent filter of food liquid, make the isolated by filtration efficiency of concentrate and crystalline solid high.
Further, described filter cloth is obliquely installed, and the incline direction of filter cloth is towards one group of crystallizer.Thus more easily there is downward landing when moving to filter cloth surface in crystalline solid.
Further, described crystallizer is flat.Thus heat transfer area between food liquid and cooling medium is larger.
Further, the tapered shape in the bottom of described separation chamber.Thus it is easier to make crystalline solid derive.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, technical solution of the present invention is further illustrated:
Fig. 1 is the schematic diagram of Food Freeze Concentration device embodiment of the present invention.
Detailed description of the invention
Wherein: circulation pipe 1, freezing moist closet 2, feed pipe 3, crystallisation chamber 4, crystallizer 5, separation chamber 6, filter cloth 7, suction filtering tube 8, discharge nozzle 9, aggregate tank 10, valve 11.
As shown in Figure 1, Food Freeze Concentration device of the present invention, comprise from top to bottom set gradually freezing moist closet 2, crystallisation chamber 4 and separation chamber 6, freezing moist closet 2 top is provided with feed pipe 3, the tapered shape in upper end of feed pipe 3, the top of crystallisation chamber 4 is connected with the bottom of freezing moist closet 2, one group of vertical crystallizer 5 is provided with in crystallisation chamber 4, crystallizer 5 is in flat, crystallizer 5 two ends are each passed through the top of crystallisation chamber 4 and the bottom of crystallisation chamber 4, and one group of crystallizer 5 all communicates with freezing moist closet 2, on the left of crystallisation chamber 4, the bottom of sidewall is provided with feed tube, and the top of crystallisation chamber 4 right sidewall is provided with escape pipe, the bottom of crystallisation chamber 4 right sidewall is provided with discharging tube, and discharging tube is normally closed, the top of separation chamber 6 is connected with the bottom of crystallisation chamber 4, and separation chamber 6 all communicates with one group of crystallizer 5, the sidewall of separation chamber 6 is provided with discharge nozzle 9, the upper end of discharge nozzle 9 is respectively equipped with suction filtering tube 8 and circulation pipe 1, the end of suction filtering tube 8 extends to the top of freezing moist closet 2, and the end of suction filtering tube 8 is connected with suction filter pump, the end of circulation pipe 1 is passed the sidewall of freezing moist closet 2 and extends in freezing moist closet 2, circulation pipe 1 is provided with drawing liquid pump, discharge nozzle 9 is positioned at the outside of suction filtering tube 8, and the outside being positioned at circulation pipe 1 is provided with valve 11, valve 11 can tackle the concentrate in discharge nozzle 9, concentrate is avoided to continue to discharging opening endwall flow, the end of discharge nozzle 9 is connected with aggregate tank 10, between discharge nozzle 9 and one group of crystallizer 5, vertical filter cloth 7 is also provided with in separation chamber 6, filter cloth 7 is skewed, its direction tilted is towards one group of crystallizer 5, the end of the end of discharge nozzle 9 and one group of crystallizer 5 can separate by filter cloth 7, the tapered shape in bottom of separation chamber 6, and the center of the bottom, separation chamber 6 of cone-shaped is also provided with crystal outlet, crystalline solid is discharged.
In specific implementation process, concentrated food liquid to be frozen from feed pipe 3 drop into carry out in freezing moist closet 2 pre-cooled, fall in crystallizer 5 under the Action of Gravity Field of himself after food liquid is pre-cooled and carry out crystallisation by cooling, fall to 6 li, separation chamber after food liquid crystallisation by cooling again and carry out isolated by filtration; Suction filter pump and valve 11 is opened when starting to feed intake, make concentrate enter discharge nozzle 9 and flow in aggregate tank 10, if sampling Detection is lower to the concentration of concentrate, can valve-off 11, open drawing liquid pump, concentrate after filtering is re-entered in freezing moist closet 2 by circulation pipe 1, carries out further freezing and crystallizing.In implementation process, note the food liquid dropping into crystallization to be frozen continuously in feed pipe 3, ensure that the food liquid volume in freezing moist closet 2 is greater than the half of freezing moist closet 2 volume.
For a person skilled in the art, under the prerequisite not departing from structure of the present invention, can also make some distortion and improvement, these also should be considered as protection scope of the present invention, and these all can not affect effect of the invention process and practical applicability.
Claims (4)
1. Food Freeze Concentration device, is characterized in that: comprise freezing moist closet, crystallisation chamber and separation chamber, and described freezing moist closet top is provided with feed pipe, the top of described crystallisation chamber is connected with the bottom of freezing moist closet, crystallization chamber is provided with one group of crystallizer, crystallizer two ends are each passed through crystallisation chamber top and crystallisation chamber bottom, and crystallizer communicates with freezing moist closet, on the left of crystallisation chamber, the bottom of sidewall is provided with feed tube, and the top of crystallisation chamber right sidewall is provided with escape pipe, the top of described separation chamber is connected with the bottom of crystallisation chamber, and separation chamber communicates with crystallizer, the sidewall of separation chamber is provided with discharge nozzle, discharge nozzle is provided with suction filtering tube and circulation pipe, the end of suction filtering tube extends to the top of freezing moist closet, the end of circulation pipe extends in freezing moist closet, circulation pipe is provided with drawing liquid pump, discharge nozzle is positioned at the outside of suction filtering tube, and the outside being positioned at circulation pipe is provided with valve, the end of discharge nozzle is connected with aggregate tank, between discharge nozzle and one group of crystallizer, vertical filter cloth discharge nozzle and one group of crystallizer separated also is provided with in separation chamber, the bottom of separation chamber is provided with crystal outlet.
2. Food Freeze Concentration device as claimed in claim 1, it is characterized in that: described filter cloth is obliquely installed, and the incline direction of filter cloth is towards one group of crystallizer.
3. Food Freeze Concentration device as claimed in claim 2, is characterized in that: described crystallizer is flat.
4. Food Freeze Concentration device as claimed in claim 3, is characterized in that: the tapered shape in bottom of described separation chamber.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410733045.XA CN104432442A (en) | 2014-12-07 | 2014-12-07 | Food freeze-concentration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410733045.XA CN104432442A (en) | 2014-12-07 | 2014-12-07 | Food freeze-concentration device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN104432442A true CN104432442A (en) | 2015-03-25 |
Family
ID=52879788
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201410733045.XA Pending CN104432442A (en) | 2014-12-07 | 2014-12-07 | Food freeze-concentration device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN104432442A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104801058A (en) * | 2015-04-17 | 2015-07-29 | 安徽扬子化工有限公司 | Pymetrozine crystallization kettle |
CN109198706A (en) * | 2018-08-28 | 2019-01-15 | 河南本象科技服务有限公司 | The freezing concentrating device of food liquid |
CN111418690A (en) * | 2020-05-19 | 2020-07-17 | 昆明凯澜创意科技有限公司 | Coffee stock solution concentrating device and production method of flash-dissolved reduced coffee |
CN112715715A (en) * | 2020-12-24 | 2021-04-30 | 昆明弘承食品科技有限公司 | Coffee feed liquid freezing and concentrating method and device |
-
2014
- 2014-12-07 CN CN201410733045.XA patent/CN104432442A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104801058A (en) * | 2015-04-17 | 2015-07-29 | 安徽扬子化工有限公司 | Pymetrozine crystallization kettle |
CN109198706A (en) * | 2018-08-28 | 2019-01-15 | 河南本象科技服务有限公司 | The freezing concentrating device of food liquid |
CN109198706B (en) * | 2018-08-28 | 2024-01-30 | 河南本象科技服务有限公司 | Freezing and concentrating device for liquid food |
CN111418690A (en) * | 2020-05-19 | 2020-07-17 | 昆明凯澜创意科技有限公司 | Coffee stock solution concentrating device and production method of flash-dissolved reduced coffee |
CN112715715A (en) * | 2020-12-24 | 2021-04-30 | 昆明弘承食品科技有限公司 | Coffee feed liquid freezing and concentrating method and device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN104432442A (en) | Food freeze-concentration device | |
CN107032429A (en) | A kind of reverse osmosis thick water treatment system and handling process | |
CN204417272U (en) | A kind of crystallization treatment device of high slat-containing wastewater | |
CN108726578B (en) | Ferrous sulfate continuous crystallization process in sulfuric acid method titanium dioxide production | |
CN204601675U (en) | A kind of freeze concentration equipment | |
CN105664521A (en) | Dynamic crystallization equipment and dynamic crystallization method | |
CN204351045U (en) | Food Freeze Concentration device | |
CN204275560U (en) | A kind of tea juice freezing concentrating device | |
CN102895796A (en) | Low-temperature concentration device | |
CN101239730B (en) | Method and device for producing crystal anhydrous lithium chloride | |
CN103432756A (en) | All-in-one evaporation and crystallization device | |
CN202638034U (en) | Lysine hydrochloride evaporation crystallization tank | |
CN204034314U (en) | A kind of gluconic acid sodium salt crystallization apparatus | |
CN110860105A (en) | Equipment and method for producing inorganic salt with solubility changing along with temperature by using cooling crystallization | |
CN208617377U (en) | Crystal separator in potassium chloride magma | |
CN103405942A (en) | Novel suspension type freeze concentration equipment | |
CN208049437U (en) | A kind of crystallizing tank syrup capture automatic control device | |
CN213221025U (en) | Control system for improving potassium chloride particle size in potassium-sodium separation | |
CN201124063Y (en) | Cyclone filter solid-liquid separator | |
CN212282946U (en) | Equipment for producing inorganic salt with solubility changing along with temperature by utilizing cooling crystallization | |
CN201906482U (en) | Vacuum crystallizing device | |
CN214458078U (en) | Sugar boiling crystallizing tank | |
CN205235452U (en) | Crystallization kettle | |
CN204034313U (en) | A kind of gluconic acid sodium salt crystallization apparatus of efficient, energy-conservation, continuous discharge | |
CN203736933U (en) | Granule cutting water filter device of underwater granule cutting machine for polyamide polymerization device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150325 |
|
WD01 | Invention patent application deemed withdrawn after publication |