CN201733819U - Main structure of thickener - Google Patents
Main structure of thickener Download PDFInfo
- Publication number
- CN201733819U CN201733819U CN2010202579872U CN201020257987U CN201733819U CN 201733819 U CN201733819 U CN 201733819U CN 2010202579872 U CN2010202579872 U CN 2010202579872U CN 201020257987 U CN201020257987 U CN 201020257987U CN 201733819 U CN201733819 U CN 201733819U
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- Prior art keywords
- separator
- grades
- links
- separators
- pipe
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Abstract
The utility model relates to a main structure of a thickener, which comprises separators, wherein an inlet pipe and a vapor output pipe are arranged at the upper end of each separator, and a material outlet is formed at the lower end of each separator. The main structure of the thickener is characterized in that each separator includes a primary separator, a secondary separator and a tertiary separator, wherein the vapor output pipe of the primary separator is connected with the inlet pipe of the secondary separator through a pipe, the vapor output pipe of the secondary separator is connected with the inlet pipe of the tertiary separator through a pipe, a feeding/discharging cylinder is connected with the inlet pipe of the primary separator through a primary pipe, the material outlet of the primary separator is connected with the inlet pipe of the tertiary separator through a pipe, the material outlet of the tertiary separator is connected with the inlet pipe of the secondary separator through a pipe, and the material outlet of the secondary separator is connected with the feeding/discharging cylinder.
Description
Technical field
The utility model relates to a kind of inspissated juice agent structure.
Background technology
China is one of fruit the biggest in the world, vegetables producing country, and fruits and vegetables production is generally by the branch in busy season and dull season, because the fruit and vegetable food moisture content is very high, the busy season results untimely processing in back descends at microbial action and very easily to rot, and causes tremendous loss; In the dull season, Bei Fang winter and spring especially, fruit and vegetable food market supply difficulty, therefore the deep processing to Juice has proposed requirement.At present, existing inspissated juice production equipment exists production efficiency low, and heat energy loss rate height, problem such as waste energy.
Summary of the invention
The purpose of this utility model is to provide a kind of inspissated juice production equipment, and this equipment can effectively utilize the thermal efficiency of steam, reduces heat energy loss.
The technical solution of the utility model is: a kind of thickener agent structure, comprise separator, the separator upper end is provided with and feeds pipeline and steam output pipe, its lower end is provided with material outlet, it is characterized in that: described separator is provided with three grades, the steam output pipe of primary separator links to each other with the access tube of second-stage separator by the road, the steam output pipe of second-stage separator links to each other with the access tube of three grades of separators by the road, advance/discharge barrel links to each other with the access tube of primary separator through the one-level pipeline, the material outlet of primary separator links to each other with the access tube of three grades of separators by the road, the material outlet of three grades of separators links to each other with the access tube of second-stage separator by the road, the material outlet of second-stage separator with advance/discharge barrel links to each other.
Advantage of the present utility model is: rational in infrastructure, low cost of manufacture, and compare and can improve the thermal efficiency greatly with traditional inspissated juice equipment, make full use of heat energy; Concentrated effect is good, can effectively improve thickening efficiency; Improve the utilization rate of material, prevent in the link of precooking that tradition concentrates waste the liquid of precooking.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
The specific embodiment
A kind of thickener agent structure, comprise separator, the separator upper end is provided with and feeds pipeline and steam output pipe, its lower end is provided with material outlet, it is characterized in that: described separator is provided with three grades, the steam output pipe 2 of primary separator 1 links to each other with the access tube 4 of second-stage separator 3 by the road, the steam output pipe 5 of second-stage separator links to each other with the access tube 7 of three grades of separators 6 by the road, advance/discharge barrel 8 links to each other with the access tube 10 of primary separator through one-level pipeline 9, the material outlet 11 of primary separator links to each other with the access tube of three grades of separators by the road, the material outlet 12 of three grades of separators links to each other with the access tube of second-stage separator by the road, the material outlet 13 of second-stage separator with advance/discharge barrel links to each other.
In order to give off the vapours in last one separation circuit in the concentration process, the steam output pipe of three grades of separators links to each other with outlet through condenser 14.
Be equipped with pump 15,16,17,18 on the discharging pipeline of the material output pipe of described separator and advancing/discharge barrel.
The material intake line of described primary separator and steam input pipe are provided with valve 19,20.
In order to make whole system reach airtight and to make the vacuum of system reach requirement, described condenser bottom is provided with a drainpipe 21, one sides and is provided with a charging pump 22, and opposite side is provided with a pump 23, and described three grades of separators are provided with vavuum pump 24.
Production process of the present utility model is as follows: 1, at first start the charging pump on the condenser, the drainpipe of condenser is come in and gone out under the liquid level in pond, be full of water in the pipeline of charging pump, thereby make whole system become closed system; Open vavuum pump, make the vacuum of separators at different levels reach requirement.
2, will precook liquid from advancing/being delivered in the primary separator the discharge barrel, while delivering vapor in primary separator, the steam of input mixes with concentrate, the concentrate temperature is raise, moisture in the liquid of precooking of heating is separated under vacuum state simultaneously, the once concentration that forms is precooked, and liquid enters separator and the discharging opening by the bottom enters three grades of separators, and the steam output pipe of the vapours that produces in first separator by first separator enters second separator.
3, once concentration the is precooked top of three grades of separators of liquid input, second separator provides steam to three grades of separators, this once concentration liquid of precooking enters before three grades of separators, when being heated by vapours under the effect of vacuum, moisture further evaporates, simultaneously secondary concentration is precooked, and liquid enters three grades of separators and the discharging opening by the bottom enters second-stage separator, and the steam in three grades of separators leads to condenser by steam output pipe simultaneously.
4, the secondary concentration liquid of precooking is delivered to the top of second-stage separator, primary separator provides vapours to second-stage separator, precooking through the secondary concentration of heating, liquid forms steam under vacuum action and the steam output pipe by second-stage separator leads to three grades of separators, and concentrate falls into bottom the second-stage separator and by pipeline and is delivered to into/discharge barrel.
5, detect/discharge barrel in the concentration of concentrate, then concentrate is taken out if reach requirement, if do not reach requirement, then this enters circulation and concentrates until concentration and reach standard again.
The above only is preferred embodiment of the present utility model, and all equalizations of being done according to the utility model claim change and modify, and all should belong to covering scope of the present utility model.
Claims (6)
1. thickener agent structure, comprise separator, the separator upper end is provided with and feeds pipeline and steam output pipe, its lower end is provided with material outlet, it is characterized in that: described separator is provided with three grades, the steam output pipe of primary separator links to each other with the access tube of second-stage separator by the road, the steam output pipe of second-stage separator links to each other with the access tube of three grades of separators by the road, advance/discharge barrel links to each other with the access tube of primary separator through the one-level pipeline, the material outlet of primary separator links to each other with the access tube of three grades of separators by the road, the material outlet of three grades of separators links to each other with the access tube of second-stage separator by the road, the material outlet of second-stage separator with advance/discharge barrel links to each other.
2. thickener agent structure according to claim 1 is characterized in that: the steam output pipe of three grades of separators links to each other with outlet through condenser.
3. thickener agent structure according to claim 1 is characterized in that: be equipped with pump on the discharging pipeline of the material output pipe of described separator and advancing/discharge barrel.
4. thickener agent structure according to claim 1 is characterized in that: the material intake line and the steam input pipe of described primary separator are provided with valve.
5. thickener agent structure according to claim 2 is characterized in that: described condenser bottom is provided with a drainpipe, and a side is provided with a charging pump, and opposite side is provided with a pump.
6. thickener agent structure according to claim 1 is characterized in that: described three grades of separators are provided with vavuum pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202579872U CN201733819U (en) | 2010-07-14 | 2010-07-14 | Main structure of thickener |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202579872U CN201733819U (en) | 2010-07-14 | 2010-07-14 | Main structure of thickener |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201733819U true CN201733819U (en) | 2011-02-09 |
Family
ID=43549093
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202579872U Expired - Fee Related CN201733819U (en) | 2010-07-14 | 2010-07-14 | Main structure of thickener |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201733819U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430381A (en) * | 2016-12-12 | 2017-02-22 | 十堰市绿田生物科技有限公司 | Pueraria starch processing wastewater concentrating unit |
| CN106477659A (en) * | 2016-12-12 | 2017-03-08 | 十堰市绿田生物科技有限公司 | Waste water Retreatment method after Radix Puerariae starch processing |
-
2010
- 2010-07-14 CN CN2010202579872U patent/CN201733819U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106430381A (en) * | 2016-12-12 | 2017-02-22 | 十堰市绿田生物科技有限公司 | Pueraria starch processing wastewater concentrating unit |
| CN106477659A (en) * | 2016-12-12 | 2017-03-08 | 十堰市绿田生物科技有限公司 | Waste water Retreatment method after Radix Puerariae starch processing |
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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 |
Granted publication date: 20110209 Termination date: 20170714 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |