CN208049437U - A kind of crystallizing tank syrup capture automatic control device - Google Patents
A kind of crystallizing tank syrup capture automatic control device Download PDFInfo
- Publication number
- CN208049437U CN208049437U CN201720910645.8U CN201720910645U CN208049437U CN 208049437 U CN208049437 U CN 208049437U CN 201720910645 U CN201720910645 U CN 201720910645U CN 208049437 U CN208049437 U CN 208049437U
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- China
- Prior art keywords
- syrup
- liquid glucose
- collector
- collecting box
- pipe
- 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.)
- Expired - Fee Related
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Abstract
The utility model is related to a kind of crystallizing tank syrups to capture automatic control device, including crystallizing tank, syrup collector, vacuum condenser, liquid glucose collecting box and PLC controller；The juice gas that crystallization generates is transported in syrup collector by the crystallizing tank, and juice gas passes through the syrup carried secretly after the spraying in the syrup collector to become the drop of larger particles and condense into liquid glucose, and the liquid glucose collecting box collects the liquid glucose to be formed；Juice vapour non-condensing in collector is extracted into vacuum condenser by the vacuum condenser；The concentration meter for measuring its internal sugar concentration is equipped in the collecting box, the concentration meter simultaneously sends measured data to PLC controller, and the PLC controller controls the liquid glucose in the collecting box and be recycled in the syrup collector and condenses once or be discharged to the outside again according to measurement data.The device is up to the liquid glucose recycling of concentration, is reached and increase sugar recovery, and the purpose to reduce environmental pollution by ringing.
Description
Technical field
The utility model is related to the fields of refining sugar, and in particular to a kind of crystallizing tank syrup capture automatic control device.
Background technology
In Closed Circulation in Sugar Production, syrup concentrates in crystallizing tank, needs to heat syrup, it is made to evaporate a large amount of water
Point, reach enrichment stage or hypersaturated state.In the process, a large amount of steam is will produce, is unavoidably entrained in steam
Syrup, these syrups are run into steam in vacuum condenser, and circulating water pool is flowed into cooling water, cause cooling water COD dense
Degree, which increases, leads to aqueous metamorphism, meanwhile, sugar waste is also resulted in, a squeezing is got off in season, and prodigious economic loss can be caused.It ties in sugar refinery
The brilliant existing juice catching device of tank, design is all very simple, and capturing efficiency is relatively low, it is difficult to the sugar in clean juice vapour is captured, it is also more
Short grained syrup can follow high speed steam flow to flow away, and cause sugar loss.
Utility model content
In conclusion in order to overcome the deficiencies of the prior art, the technical problem to be solved by the utility model is to provide one kind
Crystallizing tank syrup captures automatic control device.
The technical solution that the utility model solves above-mentioned technical problem is as follows：A kind of capture of crystallizing tank syrup automatically controls dress
It sets, including crystallizing tank, syrup collector, vacuum condenser, liquid glucose collecting box and PLC controller；The crystallizing tank passes through juice vapour
Pipe connects the feed inlet of syrup collector side and the juice gas that crystallization generates is transported in syrup collector, and juice gas
The syrup carried secretly after the spraying in the syrup collector becomes the drop of larger particles and condenses into liquid glucose, described
Liquid glucose collecting box connects the discharge port of syrup collector bottom by drain pipe and collects the liquid glucose of formation；The vacuum is cold
Condenser is connected at the top of the syrup collector by vacuum connection tube and juice vapour non-condensing in collector is extracted into vacuum condensation
In device；
The concentration meter for measuring its internal sugar concentration is equipped in the collecting box, the PLC controller is in the collection
The outside of case, the concentration meter connect the PLC controller by data line and send measured data to PLC controller, and
And the PLC controller controls the liquid glucose in the collecting box and is recycled in the syrup collector and condenses again according to measurement data
Once or it is discharged to the outside.
The utility model has the beneficial effects that：The device is up to the liquid glucose recycling of concentration, reaches increasing by ringing
Sugaring divides recovery, and the purpose to reduce environmental pollution.
Based on the above technical solution, the utility model can also do following improvement：
Further, further include liquid glucose circulation pipe and ring pipe；Multilayer is sleeved on the syrup collector above and below the endless tube
On, and multiple nozzles are uniformly provided on the inside of the endless tube, the ejiction opening of the nozzle passes through the side of the syrup collector
Wall extends to the inside of syrup collector and forms spraying；One end of the liquid glucose circulation pipe connects the outlet of the collecting box,
Its other end connects the endless tube, and the bypass pipe of discharge liquid glucose is also associated in the liquid glucose circulation pipe；
The liquid glucose circulation pipe, which is equipped with, controls its circulating regulation valve whether be connected to the endless tube, on the bypass pipe
Equipped with the bypass regulator valve for being turned on or closing, and the PLC controller is separately connected the cycle by control line
Regulating valve and the bypass regulator valve and being turned on or off according to both the measurement data of concentration meter control.
Advantageous effect using above-mentioned further scheme is：Realize ringing, i.e., by nozzle by liquid glucose with spraying square
Formula contacts droplet with the syrup in juice vapour, and short grained syrup, which is become bulky grain, to be captured.
Further, the collecting box is equipped with the water inlet pipe to supplement cold water inside it, and the water inlet pipe is equipped with water inlet
Regulating valve, and the PLC controller by control line connects the inlet regulating valve and according to the measurement number of the concentration meter
According to being turned on or off for control inlet regulating valve.
Advantageous effect using above-mentioned further scheme is：In time to the consumed cold water of supplement spraying inside collecting box.
Further, syrup collector top is cylinder, and its underpart is taper, and in the syrup collector
Top be equipped with inner cylinder, the vacuum condenser connects the inside of the inner cylinder by the vacuum connection tube.
Advantageous effect using above-mentioned further scheme is：Syrup collector lower part is that taper liquid glucose is easier to flow down；?
Inner cylinder is set in syrup collector so that juice gas enters elder generation and plume contact in the chuck between syrup collector and inner cylinder,
Finally vacuumized by vacuum condenser so that crystallizing tank crystallizes under condition of negative pressure.
Further, the liquid glucose circulation pipe, which is equipped with, is transported to the liquid glucose in the collecting box in the endless tube or other
Liquid glucose circulating pump in siphunculus.
Description of the drawings
Fig. 1 is the structural schematic diagram of the utility model.
In attached drawing, parts list represented by the reference numerals are as follows：
1, crystallizing tank, 2, juice steam pipe, 3, syrup collector, 4, vacuum connection tube, 5, vacuum condenser, 6, inner cylinder, 7, row
Liquid pipe, 8, water inlet pipe, 9, inlet regulating valve, 10, liquid glucose collecting box, 11, liquid glucose circulating pump, 12, liquid glucose circulation pipe, 13, cycle
Regulating valve, 14, bypass pipe, 15, bypass regulator valve, 16, ring pipe, 17, nozzle, 18, concentration meter, 19, PLC controller.
Specific implementation mode
The principles of the present invention and feature are described below in conjunction with attached drawing, example is served only for explaining this practicality
It is novel, it is not intended to limit the scope of the utility model.
As shown in Figure 1, a kind of crystallizing tank syrup captures automatic control device, which is characterized in that including crystallizing tank 1, syrup
Collector 3, vacuum condenser 5, liquid glucose collecting box 10 and PLC controller 19；The crystallizing tank 1 is connected described by juice steam pipe 2
The juice gas that crystallization generates simultaneously is transported in syrup collector 3 by the feed inlet of 3 side of syrup collector, and juice gas is across described
The syrup carried secretly after spraying in syrup collector 3 becomes the drop of larger particles and condenses into liquid glucose, and the liquid glucose is received
Header 10 connects the discharge port of 3 bottom of syrup collector by drain pipe 7 and collects the liquid glucose of formation；The vacuum condensation
Device 5 connects the top of the syrup collector 3 by vacuum connection tube 4 and that juice vapour non-condensing in collector 3 is extracted into vacuum is cold
In condenser 5.3 top of syrup collector is cylinder, and its underpart is taper, and upper in the syrup collector 3
Portion is equipped with inner cylinder 6, and the vacuum condenser 5 connects the inside of the inner cylinder 6 by the vacuum connection tube 4.Syrup collector 3
Lower part is that taper liquid glucose is easier to flow down.Inner cylinder 6 is set in syrup collector 3 so that juice gas enters 3 He of syrup collector
Elder generation and plume contact in chuck between inner cylinder 6 are finally vacuumized by vacuum condenser 9 so that crystallizing tank 1 is under condition of negative pressure
Crystallization.
The concentration meter 18 for measuring its internal sugar concentration is equipped in the collecting box 10, the PLC controller 19 is in institute
The outside of collecting box 10 is stated, the concentration meter 18 connects the PLC controller 19 by data line and sends measured data to
PLC controller 19, and the PLC controller 19 according to measurement data control the liquid glucose in the collecting box 10 be recycled to it is described
It condenses primary in syrup collector 3 or is discharged to the outside again, realized especially by such as under type：
The device further includes liquid glucose circulation pipe 12 and ring pipe 16；The syrup that is sleeved on of about 16 multilayer of the endless tube is received
On storage 3, and the inside of the endless tube 16 is uniformly provided with multiple nozzles 17, and the ejiction opening of the nozzle 17 passes through the syrup
The side wall of collector 3 extends to the inside of syrup collector 3 and forms spraying；Described in one end connection of the liquid glucose circulation pipe 12
The outlet of collecting box 10, the other end connect the endless tube 16, and the side of discharge liquid glucose is also associated in the liquid glucose circulation pipe 12
Siphunculus 14.The liquid glucose circulation pipe 12, which is equipped with, to be transported to the liquid glucose in the collecting box 10 in the endless tube 16 or bypasses
Liquid glucose circulating pump 11 in pipe 14.The liquid glucose circulation pipe 12 is equipped with the cycle tune controlled whether it is connected to the endless tube 16
Valve 13 is saved, the bypass pipe 14 is equipped with the bypass regulator valve 15 for being turned on or closing, and the PLC controller 19 is logical
It crosses control line and is separately connected the circulating regulation valve 13 and the bypass regulator valve 15 and the measurement number according to the concentration meter 18
According to being turned on or off for both control.
PLC controller 19 obtains the concentration of the liquid glucose in collecting box 10 by concentration meter 18, if the sugar in collecting box 10
When the concentration of liquid meets the requirements, it is discharged to outside collecting box 10；If the concentration of the liquid glucose in collecting box 10 is undesirable, receive
Liquid glucose in header 10 contacts after the spraying of liquid glucose circulation pipe 12 with juice vapour in collector 3, and condensation is i.e. short grained sugar again
Juice becomes bulky grain and captures, and eventually becomes the liquid glucose after concentration increases and enters in collecting box 10, by this cycle, until sugar
The concentration of liquid reaches that be then exhausted from collecting box 10 after the concentration of requirement outer.
The collecting box 10 is equipped with the water inlet pipe 8 to supplement cold water inside it, and the water inlet pipe 8 is equipped with water inlet and adjusts
Valve 9, and the PLC controller 19 by control line connects the inlet regulating valve 9 and according to the measurement of the concentration meter 18
Data control inlet regulating valve 9 is turned on or off.PLC controller 19 is by controlling inlet regulating valve 9 in time to collecting box
The consumed cold water of 10 inside supplement sprayings, ensures that nozzle 17 can normally spray.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all in this practicality
Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model
Within the scope of shield.
Claims (5)
1. a kind of crystallizing tank syrup captures automatic control device, which is characterized in that including crystallizing tank (1), syrup collector (3),
Vacuum condenser (5), liquid glucose collecting box (10) and PLC controller (19)；The crystallizing tank (1) connects institute by juice steam pipe (2)
It states the feed inlet of syrup collector (3) side and the juice gas that crystallization generates is transported in syrup collector (3), and juice gas is worn
The syrup carried secretly after the spraying crossed in the syrup collector (3) becomes the drop of larger particles and condenses into liquid glucose, institute
Liquid glucose collecting box (10) is stated to connect the discharge port of syrup collector (3) bottom by drain pipe (7) and collect the sugar of formation
Liquid；The vacuum condenser (5) is connected at the top of the syrup collector (3) by vacuum connection tube (4) and will be in collector (3)
Non-condensing juice vapour is extracted into vacuum condenser (5)；
The concentration meter (18) for measuring its internal sugar concentration is equipped in the collecting box (10), the PLC controller (19) is in
The outside of the collecting box (10), the concentration meter (18) connect the PLC controller (19) by data line and will measure number
According to being sent to PLC controller (19), and the PLC controller (19) is controlled according to measurement data in the collecting box (10)
Liquid glucose is recycled in the syrup collector (3) to be condensed primary or is discharged to the outside again.
2. crystallizing tank syrup according to claim 1 captures automatic control device, which is characterized in that further include liquid glucose cycle
Manage (12) and ring pipe (16)；Multilayer is sleeved on the syrup collector (3) ring pipe (16) up and down, and the ring
Multiple nozzles (17) are uniformly provided on the inside of shape pipe (16), the ejiction opening of the nozzle (17) passes through the syrup collector (3)
Side wall extend to the inside of syrup collector (3) and form spraying；One end of the liquid glucose circulation pipe (12) connects the receipts
The outlet of header (10), the other end connect the ring pipe (16), and discharge sugar is also associated in the liquid glucose circulation pipe (12)
The bypass pipe (14) of liquid；
The liquid glucose circulation pipe (12) is equipped with the circulating regulation valve (13) controlled whether it is connected to the ring pipe (16), institute
It states bypass pipe (14) and is equipped with the bypass regulator valve (15) for being turned on or closing, and the PLC controller (19) passes through
Control line is separately connected the circulating regulation valve (13) and the bypass regulator valve (15) and according to the survey of the concentration meter (18)
Both amount data control is turned on or off.
3. crystallizing tank syrup according to claim 1 captures automatic control device, which is characterized in that the collecting box (10)
It is equipped with the water inlet pipe (8) to supplement cold water inside it, the water inlet pipe (8) is equipped with inlet regulating valve (9), and described
PLC controller (19) by control line connects the inlet regulating valve (9) and according to the measurement data control of the concentration meter (18)
Inlet regulating valve (9) processed are turned on or off.
4. crystallizing tank syrup according to any one of claims 1 to 3 captures automatic control device, which is characterized in that described
Syrup collector (3) top is cylinder, during its underpart is taper, and the top in the syrup collector (3) is equipped with
The inner cylinder (6) of hollow structure, the vacuum condenser (5) connect the inside of the inner cylinder (6) by the vacuum connection tube (4).
5. crystallizing tank syrup according to claim 2 captures automatic control device, which is characterized in that the liquid glucose circulation pipe
(12) be equipped with the sugar liquid glucose in the collecting box (10) being transported in the ring pipe (16) or in bypass pipe (14)
Liquid circulating pump (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720910645.8U CN208049437U (en) | 2017-07-25 | 2017-07-25 | A kind of crystallizing tank syrup capture automatic control device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720910645.8U CN208049437U (en) | 2017-07-25 | 2017-07-25 | A kind of crystallizing tank syrup capture automatic control device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208049437U true CN208049437U (en) | 2018-11-06 |
Family
ID=63997267
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720910645.8U Expired - Fee Related CN208049437U (en) | 2017-07-25 | 2017-07-25 | A kind of crystallizing tank syrup capture automatic control device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN208049437U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261543A (en) * | 2017-07-25 | 2017-10-20 | 广西农垦糖业集团红河制糖有限公司 | A kind of crystallizing tank syrup catches automaton |
| CN109601921A (en) * | 2019-01-28 | 2019-04-12 | 溜溜果园集团股份有限公司 | A kind of continuous cooking machine |
-
2017
- 2017-07-25 CN CN201720910645.8U patent/CN208049437U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107261543A (en) * | 2017-07-25 | 2017-10-20 | 广西农垦糖业集团红河制糖有限公司 | A kind of crystallizing tank syrup catches automaton |
| CN109601921A (en) * | 2019-01-28 | 2019-04-12 | 溜溜果园集团股份有限公司 | A kind of continuous cooking machine |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20181106 Termination date: 20190725 |
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| CF01 | Termination of patent right due to non-payment of annual fee |