CN105238886A - Brown granulated sugar redissolution proportioning system - Google Patents

Brown granulated sugar redissolution proportioning system Download PDF

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Publication number
CN105238886A
CN105238886A CN201510768625.7A CN201510768625A CN105238886A CN 105238886 A CN105238886 A CN 105238886A CN 201510768625 A CN201510768625 A CN 201510768625A CN 105238886 A CN105238886 A CN 105238886A
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CN
China
Prior art keywords
syrup
sugar
retro
redissolution
dissolved
Prior art date
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Pending
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CN201510768625.7A
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Chinese (zh)
Inventor
韦如其
肖凌
傅其军
岑跃
钟伟
李品端
李有忠
王玉军
刘绍新
农秀莲
黄飒
王宪海
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Nanning Sugar Industry Ltd Co
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Nanning Sugar Industry Ltd Co
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Publication date
Application filed by Nanning Sugar Industry Ltd Co filed Critical Nanning Sugar Industry Ltd Co
Priority to CN201510768625.7A priority Critical patent/CN105238886A/en
Publication of CN105238886A publication Critical patent/CN105238886A/en
Pending legal-status Critical Current

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  • Confectionery (AREA)

Abstract

The invention discloses a brown granulated sugar redissolution proportioning system. The system comprises a honey separator, a brown granulated sugar spiral groove, a brown granulated sugar redissolution tank, a brown granulated sugar redissolution sugar-syrup pump and an evaporating floating high-position sugar-syrup tank which are sequentially connected through liquid conveying pipelines; an automatic proportioning system is further arranged between the brown granulated sugar redissolution sugar-syrup pump and the evaporating floating high-position sugar-syrup tank, and the automatic proportioning system comprises a redissolution sugar-syrup storage tank, a redissolution sugar-syrup adjusting valve, a PLC proportioning control tank, a storage tank flow meter and a rough sugar-syrup flow meter. The redissolution sugar-syrup storage tank is arranged at the redissolution sugar-syrup output end of the brown granulated sugar redissolution sugar-syrup pump, and the redissolution sugar-syrup adjusting valve, the storage tank flow meter and the rough sugar-syrup flow meter are connected with the PLC proportioning control tank through data channels. The automatic proportioning system can control opening and closing of the redissolution sugar-syrup adjusting valve in real time according to flow rate conditions of rough sugar syrup and redissolution sugar syrup; the brown granulated sugar redissolution proportioning system has the advantages of being high in pumping efficiency and stable in proportioning.

Description

A kind of brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system
Technical field
The present invention relates to sugaring operating device field, particularly a kind of brown sugar (Saccharum Sinensis Roxb.) back dissolving Controlling System.
Background technology
Brown sugar (Saccharum Sinensis Roxb.) back dissolving is the important process processing brown sugar (Saccharum Sinensis Roxb.) at present, tradition brown sugar (Saccharum Sinensis Roxb.) back dissolving conveying flow process is: triose lamb obtains brown sugar (Saccharum Sinensis Roxb.) after sugar centrifuge sub-sieve, brown sugar (Saccharum Sinensis Roxb.) enters red sand back dissolving case by spiral slot, through adding the clear juice of high temperature or hot water and obtaining red sand retro-dissolved syrup after fully stirring, by being directly pumped into evaporation floating header box with no-clogging pump.Whole process only relies on artificial adjustment no-clogging pump outlet valve to control pump discharge, pumping efficiency is not high and regulating effect is not good, often cause raw sugar slurry flow does not mate with brown sugar (Saccharum Sinensis Roxb.) back dissolving flow, cause evaporation floating poor effect, finally affect quality product.
Domestic and international patent database also discloses some red sand back dissolving technology, as:
[title] floating method of brown granulated sugar dissolved by a-wash [applying date] the 2008.09.25[patent No.] CN200810073809.1, disclose a kind of floating method of brown granulated sugar dissolved by a-wash, take while brown sugar (Saccharum Sinensis Roxb.) back dissolving, add first and wash honey, the purity purity of mixing molasses being reached or starches close to raw sugar, by the method for Syrup Flotation, it is processed again, to reach the object reducing colour, removing reducing sugar and impurity.But facts have proved that its tone of product that the method is produced is still undesirable, basic reason is that raw sugar slurry is unstable with brown sugar (Saccharum Sinensis Roxb.) back dissolving proportioning, causes brown sugar (Saccharum Sinensis Roxb.) level of response to differ, have impact on quality product.
Therefore, existing brown sugar (Saccharum Sinensis Roxb.) back dissolving technology exists that flow velocity is uneven, raw sugar slurry and the irrational problem of brown sugar (Saccharum Sinensis Roxb.) back dissolving proportioning, requires further improvement.
Summary of the invention
Of the present inventionly be intended to solve that flow velocity in brown sugar (Saccharum Sinensis Roxb.) back dissolving process is uneven, raw sugar slurry and the irrational problem of brown sugar (Saccharum Sinensis Roxb.) back dissolving proportioning, provide the red sand back dissolving matching system that a kind of pumping efficiency is high, proportioning is stable.
Brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention, comprise sugar centrifuge, brown sugar (Saccharum Sinensis Roxb.) spiral slot, brown sugar (Saccharum Sinensis Roxb.) back dissolving case, brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump, the high-order syrup case of evaporation floating, above-mentioned parts are connected successively by liquid conducting pipes; Float between high-order syrup case at described brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump and evaporation and be also provided with automatic mixing system, described automatic mixing system comprises retro-dissolved syrup retention tank, retro-dissolved syrup variable valve, PLC burden control case, retention tank under meter, raw sugar slurry under meter; Described retro-dissolved syrup retention tank is arranged on the retro-dissolved syrup output terminal of brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump; Retro-dissolved syrup variable valve, retention tank under meter are arranged on retro-dissolved syrup retention tank and evaporate on the pipeline that floats between high-order syrup case; Raw sugar slurry under meter is arranged on the raw sugar slurry ingress of the high-order syrup case of evaporation floating; Described retro-dissolved syrup variable valve, retention tank under meter, raw sugar slurry under meter connects PLC burden control case respectively by data channel; Described automatic mixing system can be starched according to raw sugar, the traffic conditions of retro-dissolved syrup, controls the opening and closing of retro-dissolved syrup variable valve in real time.
Principle of the present invention is: floating between high-order syrup case at brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump and evaporation arranges automatic mixing system, by controlling retro-dissolved syrup variable valve, regulate and enter the raw sugar slurry of the high-order syrup case of evaporation floating and the flow of retro-dissolved syrup, raw sugar is starched and is tending towards reasonable with retro-dissolved syrup proportioning.
Further illustrate as of the present invention, described retro-dissolved syrup variable valve comprises topworks and valve two portions, and valve installation is in retro-dissolved syrup passage pipe, and topworks's part connects PLC burden control case by data channel.
Further illustrate as of the present invention, described PLC burden control case comprises flow monitoring module, valve control module.
Described flow monitoring module for receiving, distinguishing retention tank under meter and the flow information that returns of raw sugar slurry under meter, and exports result to valve control module.
The numerical value that flow monitoring module passes over by described valve control module and preset value compare, then export corresponding control signal according to comparative result to retro-dissolved syrup variable valve.
Further illustrate as of the present invention, described retention tank under meter and raw sugar slurry under meter are all intelligent electromagnetic flowmeters, and comprise sensor and transmodulator two portions, described transmodulator is connected with PLC burden control case by data channel.
Further illustrate as of the present invention, PLC burden control case is also provided with low liquid level protection module, and when retro-dissolved syrup retention tank liquid level is lower than preset value, low liquid level protection module regulates retro-dissolved syrup to enter the porthole valve of the high-order syrup case of evaporation floating.Setting like this avoids retro-dissolved syrup in retro-dissolved syrup retention tank very few, cannot reach evenly and the situation that proportioning starched by raw sugar occurs.
Brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention compared with prior art has following progress:
1, productive rate and the quality of white sugar can be improved: brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention applies in existing Closed Circulation in Sugar Production line, not only can all back dissolving process sugaring process produce brown sugar (Saccharum Sinensis Roxb.), improve white sugar output capacity, can also guarantee that the colour of white sugar controls in controlled range.
2, back dissolving process is full-automatic: automatic mixing system of the present invention can adjust the flowrate proportioning of retro-dissolved syrup, raw sugar slurry automatically, and whole process need not manual intervention, control process accurately, efficient.
3, highly versatile: the present invention floats between high-order syrup case arrange automatic mixing system at brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump and evaporation, directly can install additional on existing production line, and controling parameters can free setting, is common to most sugar refinery.
Accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the present invention is further detailed explanation:
Fig. 1 is the syndeton schematic diagram of brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention;
Fig. 2 is the schema of traditional brown sugar (Saccharum Sinensis Roxb.) back dissolving system;
Fig. 3 is the schema of brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention;
In figure, 1--sugar centrifuge; 2--brown sugar (Saccharum Sinensis Roxb.) spiral slot; 3--brown sugar (Saccharum Sinensis Roxb.) back dissolving case; 4--brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump; 5--retro-dissolved syrup retention tank; 6--retro-dissolved syrup variable valve; 7--PLC burden control case; 8--retention tank under meter; The high-order syrup case of 9--evaporation floating; 10--raw sugar slurry under meter.
Embodiment
Technical scheme of the present invention is described in detail below in conjunction with embodiment:
As shown in figures 1 and 3, brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention, comprise sugar centrifuge 1, brown sugar (Saccharum Sinensis Roxb.) spiral slot 2, brown sugar (Saccharum Sinensis Roxb.) back dissolving case 3, brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump 4, the high-order syrup case 9 of evaporation floating, above-mentioned parts are connected successively by liquid conducting pipes; Float between high-order syrup case 9 at described brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump 4 and evaporation and be also provided with automatic mixing system, described automatic mixing system comprises retro-dissolved syrup retention tank 5, retro-dissolved syrup variable valve 6, PLC burden control case 7, retention tank under meter 8, raw sugar slurry under meter 10; Described retro-dissolved syrup retention tank 5 is arranged on the retro-dissolved syrup output terminal of brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump 4; Retro-dissolved syrup variable valve 6, retention tank under meter 8 are arranged on retro-dissolved syrup retention tank 5 and evaporate on the pipeline that floats between high-order syrup case 9; Raw sugar slurry under meter 10 is arranged on the raw sugar slurry ingress of the high-order syrup case 9 of evaporation floating; Described retro-dissolved syrup variable valve 6, retention tank under meter 8, raw sugar slurry under meter 10 connects PLC burden control case 7 respectively by data channel; Described automatic mixing system can be starched according to raw sugar, the traffic conditions of retro-dissolved syrup, controls the opening and closing of retro-dissolved syrup variable valve 6 in real time.
Described retro-dissolved syrup variable valve 6 comprises topworks and valve two portions, and valve installation is in retro-dissolved syrup passage pipe, and topworks's part connects PLC burden control case 7 by data channel.
Described PLC burden control case 7 comprises flow monitoring module, valve control module.
Described flow monitoring module for receiving, distinguishing retention tank under meter 8 and the flow information that returns of raw sugar slurry under meter 10, and exports result to valve control module.
The numerical value that flow monitoring module passes over by described valve control module and preset value compare, then export corresponding control signal according to comparative result to retro-dissolved syrup variable valve 6.
Described retention tank under meter 8 and raw sugar slurry under meter 10 are all intelligent electromagnetic flowmeters, and comprise sensor and transmodulator two portions, described transmodulator is connected with PLC burden control case 7 by data channel.
PLC burden control case 7 is also provided with low liquid level protection module, and when retro-dissolved syrup retention tank 5 liquid level is lower than preset value, low liquid level protection module closes the porthole valve that retro-dissolved syrup enters the high-order syrup case 9 of evaporation floating.
The operation of brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of the present invention is as follows: as shown in Figure 3, and triose lamb obtains brown sugar (Saccharum Sinensis Roxb.) after sugar centrifuge 1 sub-sieve, and brown sugar (Saccharum Sinensis Roxb.) enters brown sugar (Saccharum Sinensis Roxb.) back dissolving case 3 by brown sugar (Saccharum Sinensis Roxb.) spiral slot 2; In brown sugar (Saccharum Sinensis Roxb.) back dissolving case 3, add the clear juice of high temperature or hot water and after fully stirring, obtain brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup; With brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump 4, retro-dissolved syrup is directly delivered to retro-dissolved syrup retention tank 5.The signal feedback of under meter 10 is starched to PLC burden control case 7 by retention tank under meter 8 and raw sugar, proportioning signal is adjusted after PLC burden control case 7 synthesise various condition, Signal transmissions to retro-dissolved syrup variable valve 6 is gone to perform, make the brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup amount flowing into evaporation floating header box 9 relatively stable, obtain metastable raw sugar slurry and the proportioning of retro-dissolved syrup, significantly reduce brown sugar (Saccharum Sinensis Roxb.) back dissolving to the impact of quality product.
Obviously, above-described embodiment is only used to example of the present invention is clearly described, and not to the restriction implemented.For the those of ordinary skill in described field, can also make other changes in different forms on the basis of the above description.Here exhaustive without the need to also giving all embodiments.And thus the apparent change of amplifying out or variation be still among protection scope of the present invention.

Claims (5)

1. a brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system, comprise sugar centrifuge (1), brown sugar (Saccharum Sinensis Roxb.) spiral slot (2), brown sugar (Saccharum Sinensis Roxb.) back dissolving case (3), brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump (4), the high-order syrup case (9) of evaporation floating, above-mentioned parts are connected successively by liquid conducting pipes; It is characterized in that: floating between high-order syrup case (9) described brown sugar (Saccharum Sinensis Roxb.) retro-dissolved syrup pump (4) and evaporation is also provided with automatic mixing system, and described automatic mixing system comprises retro-dissolved syrup retention tank (5), retro-dissolved syrup variable valve (6), PLC burden control case (7), retention tank under meter (8), raw sugar slurry under meter (10); Described retro-dissolved syrup retention tank (5) is arranged on the retro-dissolved syrup output terminal of red sand retro-dissolved syrup pump (4); Retro-dissolved syrup variable valve (6), retention tank under meter (8) are arranged on retro-dissolved syrup retention tank (5) and evaporate on the pipeline that floats between high-order syrup case (9); Raw sugar slurry under meter (10) is arranged on the raw sugar slurry ingress of the high-order syrup case (9) of evaporation floating; Described retro-dissolved syrup variable valve (6), retention tank under meter (8), raw sugar slurry under meter (10) connect PLC burden control case (7) respectively by data channel; Described automatic mixing system can be starched according to raw sugar, the traffic conditions of retro-dissolved syrup, controls retro-dissolved syrup variable valve (6) opening and closing in real time.
2. according to a claim 1 brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system, it is characterized in that: described retro-dissolved syrup variable valve (6) comprises topworks and valve two portions, valve installation is in retro-dissolved syrup passage pipe, and topworks's part connects PLC burden control case (7) by data channel.
3. brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system according to claim 2, is characterized in that: described PLC burden control case (7) comprises flow monitoring module, valve control module; Described flow monitoring module is used for receiving, distinguishing the flow information that retention tank under meter (8) and raw sugar slurry under meter (10) return, and exports result to valve control module; The numerical value that flow monitoring module passes over by described valve control module and preset value compare, then export corresponding control signal according to comparative result to retro-dissolved syrup variable valve (6).
4. according to the arbitrary described brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system of claim 1-3, it is characterized in that: described retention tank under meter (8) and raw sugar slurry under meter (10) are all intelligent electromagnetic flowmeters, comprise sensor and transmodulator two portions, described transmodulator is connected with PLC burden control case (7) by data channel.
5. brown sugar (Saccharum Sinensis Roxb.) back dissolving matching system according to claim 4; it is characterized in that: PLC burden control case (7) is also provided with low liquid level protection module; when retro-dissolved syrup retention tank (5) liquid level is lower than preset value, low liquid level protection module regulates retro-dissolved syrup to enter the porthole valve of the high-order syrup case (9) of evaporation floating.
CN201510768625.7A 2015-11-12 2015-11-12 Brown granulated sugar redissolution proportioning system Pending CN105238886A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115141899A (en) * 2022-06-21 2022-10-04 南宁糖业股份有限公司 A balanced control system for filtered juice subsides clarification fast

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115141899A (en) * 2022-06-21 2022-10-04 南宁糖业股份有限公司 A balanced control system for filtered juice subsides clarification fast

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