CN203618746U - Food pulp concentrating device with status monitoring and controlling function - Google Patents
Food pulp concentrating device with status monitoring and controlling function Download PDFInfo
- Publication number
- CN203618746U CN203618746U CN201320854997.8U CN201320854997U CN203618746U CN 203618746 U CN203618746 U CN 203618746U CN 201320854997 U CN201320854997 U CN 201320854997U CN 203618746 U CN203618746 U CN 203618746U
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- Prior art keywords
- liquid level
- concentration tank
- steam
- level sensor
- tube
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- Expired - Lifetime
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- 235000013305 food Nutrition 0.000 title claims abstract description 36
- 238000012544 monitoring process Methods 0.000 title abstract description 6
- 239000007788 liquid Substances 0.000 claims abstract description 41
- 238000004519 manufacturing process Methods 0.000 claims description 8
- 238000007689 inspection Methods 0.000 claims description 5
- 238000007667 floating Methods 0.000 claims description 2
- 238000009827 uniform distribution Methods 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 abstract description 7
- 238000009835 boiling Methods 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 239000002002 slurry Substances 0.000 description 14
- 239000006260 foam Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000000284 extract Substances 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Commercial Cooking Devices (AREA)
Abstract
The utility model discloses a food pulp concentrating device with a status monitoring and controlling function. The device comprises a feeding tube, a decompressing tube, a viewing window, a concentrating tank, a discharge tube, a finished product tube and a heating device, wherein the feeding tube, the decompressing tube and the viewing window are arranged at the upper part of the concentrating tank, the discharge tube and the finished product tube are arranged at the lower part of the concentrating tank, the heating device comprises a steam manifold, a steam distributor, a safety valve and a steam branched tube, a monitoring and controlling device is arranged at the upper part of the side surface of the concentrating tank and comprises the viewing window arranged on the side wall and a liquid level sensor arranged in the concentrating tank, and the liquid level sensor is electrically connected with an external controller. The device adopts the controller to automatically control a solenoid valve to turn on and turn off, so that the boiling liquid surface of the food pulp does not exceed the preset height, the waste is reduced, and the affect on the decompressing tube and the food pulp is avoided. The food pulp concentrating device has a simple structure, is convenient to install, works reliably, and is convenient to maintain.
Description
Technical field
The utility model belongs to food size concentrator field, is specifically related to a kind of food size enrichment facility with Stateful Inspection control function.
Background technology
In food, beverage, flavouring, fruit juice, milk, refining wet goods industry, be widely used concentrator and reduce the moisture in slurry, improve slurry concentration, increase the keeping quality of goods, reduce the expense of packaging, storage and transport.In concentration process, the general distillation under vacuum that uses is removed the moisture in slurry, and slurry is in the time of extraneous pressure decreased, and its boiling temperature decreases, can at low temperatures the moisture in slurry be evaporated and not affect other compositions in slurry, reach concentrated object.The concentrator using is generally reduced pressure concentration tank, puts into after the slurries such as food in tank, extracts air in tank, reduces tank internal pressure, and then, by slurry in heat exchange method heating tank, the moisture in slurry is evaporated, and is discharged by relief pipe.But in concentration process, when slurry boiling, can form foam, in the time that firing rate is very fast, easily form at short notice a large amount of foams, while being spilled over to relief pipe place, the foam forming can be depressurized pipe and extract out, caused the waste of slurry, and foam enters relief pipe and can affect the effect of bleeding, condensed slurry from pass back in relief pipe fill with in time, can pollute to filling with interior slurry the hygienic quality of the concentrated slurry of impact.At present, be generally liquid level and the froth bed thickness relying in operating personnel's Real Time Observation tank, and result is adjusted the valve that steam is in charge of according to the observation, controls firing rate, but due to the hysteresis quality regulating, be difficult to avoid relief pipe to suck the foam of food size.Therefore, developing a kind of food size enrichment facility with Stateful Inspection control function is the key point addressing the above problem.
Utility model content
It is a kind of simple in structure that the purpose of this utility model is to provide, and is easy to implement, and working stability is reliable, has the food size enrichment facility of Stateful Inspection control function, has reduced the waste of food size, avoids the impact on depressurized system and the pollution to food size.
The purpose of this utility model is to realize like this, comprise feed pipe, relief pipe, observation window, concentration tank, blow-off pipe, production tube, heater, described feed pipe, relief pipe and observation window are arranged at the top of concentration tank, described blow-off pipe and production tube are arranged at concentration tank bottom, described heater comprises main steam range, steam distributor, safety valve and steam are in charge of, described heater is positioned at concentration tank side, be in charge of with concentration tank and be connected by steam, described top, concentration tank side arranges supervising device, described supervising device comprises the observation window being arranged on sidewall and is arranged at the liquid level sensor in concentration tank, liquid level sensor and outside controller are electrically connected.
The utility model adopts liquid level sensor to monitor the liquid level position in concentration tank, controller is by the opening and closing of the data automatic control electric magnet valve of liquid level sensor, liquid level in energy real time monitoring concentration tank, and automatically control according to liquid level the quantity of steam entering in concentration tank, make to heat while concentrating, the boiling liquid level of food size can be not too high and be overflowed in relief pipe, has reduced the waste of food size, avoids the impact on depressurized system and the pollution to food size.The utility model is simple in structure, and convenient, reliable operation is installed, easy to maintenance.
Brief description of the drawings
Fig. 1 is overall schematic of the present utility model;
In figure: 1-feed pipe, 2-relief pipe, 3-observation window, 4-concentration tank, 5-blow-off pipe, 6-production tube, 7-main steam range, 8-steam distributor, 9-safety valve, 10-steam is in charge of, 11-liquid level sensor, 12-controller, 13-magnetic valve.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is further described, but never in any form the utility model is limited, any conversion or the replacement done based on the utility model training centre, all belong to protection domain of the present utility model.
As shown in Figure 1, the utility model comprises feed pipe 1, relief pipe 2, observation window 3, concentration tank 4, blow-off pipe 5, production tube 6, heater, described feed pipe 1, relief pipe 2 and observation window 3 are arranged at the top of concentration tank 4, described blow-off pipe 5 and production tube 6 are arranged at concentration tank 4 bottoms, described heater comprises main steam range 7, steam distributor 8, safety valve 9 and steam are in charge of 10, described heater is positioned at concentration tank 4 sides, being in charge of 10 by steam is connected with concentration tank 4, described concentration tank 4 tops, side arrange supervising device, described supervising device comprises the observation window being arranged on sidewall and is arranged at the liquid level sensor 11 in concentration tank 4, liquid level sensor 11 is electrically connected with outside controller 12.Can be in real time the liquid level transfer of data in concentration tank to controller.
The magnetic valve 13 arranging on described controller 12 and steam pipework is electrically connected.Can control the unlatching of magnetic valve or close according to liquid level data.
Described liquid level sensor 11 is positioned at the inner and upper of concentration tank 4.
Described liquid level sensor 11 is along concentration tank 4 circumference uniform distributions, and quantity is 1 ~ 5.Can monitor the liquid level of diverse location.
Described liquid level sensor 11 is the one in float-type liquid level sensor or floating ball type liquid level sensor.
Described magnetic valve 13 is arranged at steam to be in charge of on 10, and the signal that magnetic valve can send according to controller is opened or closed, and controls separately the quantity of steam in being in charge of.
Described steam is in charge of 10 layerings and is arranged at the middle and lower part of concentration tank 4.
Described steam is in charge of 10 at least three layers of setting of point upper, middle and lower.Can the interior food size of homogeneous heating tank.
the utility model operation principle and the course of work:
The utility model adopts liquid level sensor to monitor the liquid level position in concentration tank, controller is by the opening and closing of the data automatic control electric magnet valve of liquid level sensor, liquid level in can real time monitoring concentration tank, and automatically control according to liquid level the quantity of steam entering in concentration tank, reduce the waste of food size, avoided the impact on depressurized system and the pollution to food size.
, by feed pipe, food size is put into concentrated tank body at the concentration process of food size, open extraction valve, reduce concentration tank internal pressure by exhaust tube, opens solenoid valve after pressure meets the requirements, steam enters in the heat-exchange tube in concentration tank, heat food size in concentration tank by heat exchange, and discharged by the other end.After liquid level boiling in concentration tank, contained humidity is evaporated, and easily forms foam, liquid level sensor Real-Time Monitoring liquid level or froth bed position, exceed after the height setting at liquid level or froth bed, and signal is transferred to controller, controller is according to signal, shut electromagnetic valve, entering of blocking-up heating steam, no longer rises liquid level or froth bed, after liquid level or froth bed reduction, opens solenoid valve again, heating steam enters the heat-exchange tube in tank, continues food size in heating tank.After moisture in food size meets the requirements, emitted by bottom production tube, complete a concentration process.The utility model is simple in structure, install convenient, working stability is reliable, has reduced the loss of food size, has avoided the impact on decompressor and the pollution to food size.
Claims (8)
1. one kind has the food size enrichment facility of Stateful Inspection control function, comprise feed pipe (1), relief pipe (2), observation window (3), concentration tank (4), blow-off pipe (5), production tube (6), heater, described feed pipe (1), relief pipe (2) and observation window (3) are arranged at the top of concentration tank (4), described blow-off pipe (5) and production tube (6) are arranged at concentration tank (4) bottom, described heater comprises main steam range (7), steam distributor (8), safety valve (9) and steam are in charge of (10), described heater is positioned at concentration tank (4) side, being in charge of (10) by steam is connected with concentration tank (4), it is characterized in that: described concentration tank (4) top, side arranges supervising device, described supervising device comprises the observation window being arranged on sidewall and is arranged at the liquid level sensor (11) in concentration tank (4), liquid level sensor (11) is electrically connected with outside controller (12).
2. food size enrichment facility according to claim 1, is characterized in that: the magnetic valve (13) arranging on described controller (1 2) and steam pipework is electrically connected.
3. food size enrichment facility according to claim 1, is characterized in that: described liquid level sensor (11) is positioned at the inner and upper of concentration tank (4).
4. food size enrichment facility according to claim 1, is characterized in that: described liquid level sensor (11) is along concentration tank (4) circumference uniform distribution, and quantity is 1 ~ 5.
5. food size enrichment facility according to claim 1, is characterized in that: described liquid level sensor (11) is the one in float-type liquid level sensor or floating ball type liquid level sensor.
6. food size enrichment facility according to claim 2, is characterized in that: described magnetic valve (13) is arranged at steam and is in charge of on (10).
7. food size enrichment facility according to claim 1, is characterized in that: described steam is in charge of (10) layering and is arranged at the middle and lower part of concentration tank (4).
8. food size enrichment facility according to claim 1, is characterized in that: described steam is in charge of (10) at least three layers of setting of point upper, middle and lower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320854997.8U CN203618746U (en) | 2013-12-24 | 2013-12-24 | Food pulp concentrating device with status monitoring and controlling function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320854997.8U CN203618746U (en) | 2013-12-24 | 2013-12-24 | Food pulp concentrating device with status monitoring and controlling function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203618746U true CN203618746U (en) | 2014-06-04 |
Family
ID=50805291
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320854997.8U Expired - Lifetime CN203618746U (en) | 2013-12-24 | 2013-12-24 | Food pulp concentrating device with status monitoring and controlling function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203618746U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022124260A1 (en) * | 2020-12-07 | 2022-06-16 | 株式会社日立ハイテク | Evaporative concentration mechanism, analysis device provided with same, and control method for evaporative concentration mechanism |
-
2013
- 2013-12-24 CN CN201320854997.8U patent/CN203618746U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022124260A1 (en) * | 2020-12-07 | 2022-06-16 | 株式会社日立ハイテク | Evaporative concentration mechanism, analysis device provided with same, and control method for evaporative concentration mechanism |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140604 |