CN105148557A - Syrup decolorization system - Google Patents
Syrup decolorization system Download PDFInfo
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- CN105148557A CN105148557A CN201510563952.9A CN201510563952A CN105148557A CN 105148557 A CN105148557 A CN 105148557A CN 201510563952 A CN201510563952 A CN 201510563952A CN 105148557 A CN105148557 A CN 105148557A
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- syrup
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- storage tank
- charcoal column
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Abstract
The invention relates to the field of syrup production, particularly to a syrup decolorization system. The syrup decolorization system comprises a syrup storage tank, a feeding pump, an extraction pump, a discharging pump, an active carbon column, an active carbon storage tank, a desalting water storage tank and a water-sugar separation system, wherein a discharging opening of the syrup storage tank is connected to an inlet of the feeding pump, an outlet of the feeding pump is connected with the active carbon column, the active carbon column is connected with the discharging pump, an inlet of the extraction pump is connected with the active carbon column, an outlet of the extraction pump is connected with the syrup storage tank or the water-sugar separation system, the active carbon storage tank is connected with the active carbon column, a syrup outlet of the water-sugar separation system is connected with the syrup storage tank, and a water outlet of the water-sugar separation system is connected with the desalting water storage tank. The syrup decolorization system is simple in structure, convenient to operate and capable of effectively decoloring the syrup; meanwhile, when the de-sugar treatment on the active carbon column is carried out, the de-sugar effect is better, and less desalting water is consumed. By adopting the circulating system, the water-sugar separation system is used for effectively recycling the syrup and the desalting water, so that the waste of resources is reduced, and the environmental pollution is reduced.
Description
Technical field
The present invention relates to syrup production field, especially a kind of syrup decolorization system.
Background technology
Syrup refers to the thick liquid of Starch Hydrolysis, and sweet taste is soft, easily directly absorbs for human body, mainly maltose, also has glucose, the mixture of other monose such as compound sugar, dextrin and compound sugar.In the production process of syrup, in order to improve the quality of product, often need to carry out desolventing technology to syrup.In syrup production process in recent years, the technology of decolorizing carbon post obtains certain development at home.
The method using decolorizing carbon post to decolour to syrup, when process units stops, needs to carry out desugar process to carbon post, and traditional decolorizing carbon post desugar process is adverse current water inlet from bottom to top from carbon column bottom, is all replaced by the syrup in decolorizing carbon post.Cause the waste of a large amount of syrup like this, and along with the fluctuation of flow there will be the problem of syrup and water back mixing in adverse current desugar process, desugar process water amount is caused to increase, reduce at process units systemic concentration, increase and produce steam cost, the desugar cycle is longer, and desugar water directly discharges after using, and too increases the pressure of environment.
Summary of the invention
The present invention is directed to appeal problem and propose a kind of syrup decolorization system.The pressure effectively can strengthened the cleaning efficiency of decolorizing carbon post, reduce the waste of syrup, reduce environment.
To achieve these goals, the present invention is by the following technical solutions: a kind of syrup decolorization system comprises syrup tanks, pan feeding pump, detach pump, discharging pump, activated-charcoal column, active carbon storage tank, desalted water storage tank, molasses sugar piece-rate system, syrup tanks arranges discharging opening and connects pan feeding pump intake, pan feeding pump discharge connects activated-charcoal column, activated-charcoal column connects discharging pump, detach pump intake and connect activated-charcoal column, outlet connects syrup tanks or molasses sugar piece-rate system, active carbon storage tank connects activated-charcoal column, molasses sugar piece-rate system syrup outlet connects syrup tanks, water out connects desalted water storage tank.
Described to detach the entrance of pump on activated-charcoal column identical in the outlet of activated-charcoal column with pan feeding pump, is arranged at bottom activated-charcoal column.
Described detach pump and pan feeding pump is provided with check valve on pump inlet pipeline.
The method that described molasses sugar piece-rate system adopts pellicle to be separated is separated water, sugar.
Described activated-charcoal column, in charcoal post, the import and export of syrup are provided with screen casing.
During decolouring, the syrup in syrup tanks enters activated carbon column decoloring by pan feeding pump, is extracted out after decolouring by discharging pump; During activated-charcoal column desugar, syrup in activated-charcoal column is by detaching pump suction syrup tanks, desalted water is added again by top, below is by detaching pump by the desalted water suction molasses sugar piece-rate system of desugar in activated-charcoal column, by molasses sugar piece-rate system by desalted water and sugar from, desalted water enters desalted water storage tank, sugar enters syrup tanks.
Use the present invention have the following advantages:
1. framework is simply clear, easy to operate;
2., when carrying out desugar process to activated-charcoal column, desugar better effects if, consumption desalted water are less;
3. utilize and detach pump and detach syrup and molasses sugar piece-rate system isolates syrup, decrease the loss of the syrup when desugar process, decrease the waste of syrup;
4. adopt the circulatory system, utilize membrane separation process Separation of Water, sugar, reclaim desalted water, decrease the consumption of desalted water, reduce impact on environment, membrane separation process consumed energy is lower simultaneously;
5. use bottom to take out sugar to add and just enter wash-out salt solution mode.The eluting water consumption in decolorization can be reduced in, steam saving consumption thus reduce costs, shorten the down time of process units;
6. in charcoal post, the import and export of syrup are provided with screen casing, effectively can completely cut off active carbon, prevent active carbon from entering pipeline.
Accompanying drawing explanation
Fig. 1 is present system schematic diagram.
Specific embodiments
For setting forth the predetermined object and technological means and effect that the present invention reaches further, below in conjunction with Fig. 1 and embodiment, specific embodiment of the invention scheme is described in detail.
Embodiment 1: a kind of syrup decolorization system comprises syrup tanks, pan feeding pump, detach pump, discharging pump, activated-charcoal column, active carbon storage tank, desalted water storage tank, molasses sugar piece-rate system, syrup tanks arranges discharging opening and connects pan feeding pump intake, pan feeding pump discharge connects activated-charcoal column, activated-charcoal column connects discharging pump, detach pump intake and connect activated-charcoal column, outlet connects syrup tanks or molasses sugar piece-rate system, active carbon storage tank connects activated-charcoal column, the method that molasses sugar piece-rate system adopts pellicle to be separated is to water, sugar is separated, wherein syrup outlet connects syrup tanks, water out connects desalted water storage tank.Detach the entrance of pump on activated-charcoal column identical in the outlet of activated-charcoal column with pan feeding pump, be arranged at bottom activated-charcoal column.In activated-charcoal column, each syrup is imported and exported and is provided with screen casing.
Embodiment 2: with embodiment 1 basic simlarity, its difference is: detach pump and pan feeding pump is provided with check valve on pump inlet pipeline.
Embodiment 3: when using the system described in embodiment 1, when system is decoloured, the syrup in syrup tanks enters activated carbon column decoloring by pan feeding pump, is extracted out after decolouring by discharging pump; During activated-charcoal column desugar, syrup in activated-charcoal column is by detaching pump suction syrup tanks, desalted water is added again by top, below is by detaching pump by the desalted water suction molasses sugar piece-rate system of desugar in activated-charcoal column, by molasses sugar piece-rate system by desalted water and sugar from, desalted water enters desalted water storage tank, sugar enters syrup tanks.
As mentioned above, be only present pre-ferred embodiments, therefore appoint and allly do not depart from this programme technology contents, according to technical spirit of the present invention, any simple change, equivalent variations and modification are made to above embodiment, all still belong to the scope of technical solution of the present invention.
Claims (5)
1. a syrup decolorization system, it is characterized in that: comprise syrup tanks, pan feeding pump, detach pump, discharging pump, activated-charcoal column, active carbon storage tank, desalted water storage tank, molasses sugar piece-rate system, syrup tanks arranges discharging opening and connects pan feeding pump intake, pan feeding pump discharge connects activated-charcoal column, activated-charcoal column connects discharging pump, detach pump intake and connect activated-charcoal column, outlet connects syrup tanks or molasses sugar piece-rate system, active carbon storage tank connects activated-charcoal column, molasses sugar piece-rate system syrup outlet connects syrup tanks, and water out connects desalted water storage tank.
2. a kind of syrup decolorization system according to claim 1, is characterized in that: detach the entrance of pump on activated-charcoal column identical in the outlet of activated-charcoal column with pan feeding pump, be arranged at bottom activated-charcoal column.
3. a kind of syrup decolorization system according to claim 1, is characterized in that: detach pump and pan feeding pump is provided with check valve on pump inlet pipeline.
4. a kind of syrup decolorization system according to claim 1, is characterized in that: the method that molasses sugar piece-rate system adopts pellicle to be separated is separated water, sugar.
5. a kind of syrup decolorization system according to claim 1 or 2 or 3 or 4, is characterized in that: in activated-charcoal column, the import and export of syrup are provided with screen casing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510563952.9A CN105148557B (en) | 2015-09-08 | 2015-09-08 | A kind of syrup decolorization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510563952.9A CN105148557B (en) | 2015-09-08 | 2015-09-08 | A kind of syrup decolorization system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105148557A true CN105148557A (en) | 2015-12-16 |
| CN105148557B CN105148557B (en) | 2017-03-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510563952.9A Expired - Fee Related CN105148557B (en) | 2015-09-08 | 2015-09-08 | A kind of syrup decolorization system |
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| CN (1) | CN105148557B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109645117A (en) * | 2019-01-29 | 2019-04-19 | 淮南师范学院 | A method of Yoghourt shelf life is extended based on Flos Caryophylli extract |
| CN110898459A (en) * | 2019-12-12 | 2020-03-24 | 浙江华康药业股份有限公司 | Active carbon decoloration system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB889823A (en) * | 1959-06-22 | 1962-02-21 | American Sugar Refining Co | Improvements in purification of sugar solutions |
| CN102127122A (en) * | 2010-12-31 | 2011-07-20 | 山东西王药业有限公司 | Automatic control method and device for adding activated carbon in production of anhydrous glucose |
| CN202007232U (en) * | 2010-12-31 | 2011-10-12 | 山东西王药业有限公司 | Activated carbon addition equipment in anhydrous dextrose production |
| CN103007624A (en) * | 2012-12-16 | 2013-04-03 | 西王药业有限公司 | Decolorizing active carbon recycle device and production technique |
| CN202892973U (en) * | 2012-10-30 | 2013-04-24 | 万福生科(湖南)农业开发股份有限公司 | Continuous decoloring device for starch sugar |
-
2015
- 2015-09-08 CN CN201510563952.9A patent/CN105148557B/en not_active Expired - Fee Related
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB889823A (en) * | 1959-06-22 | 1962-02-21 | American Sugar Refining Co | Improvements in purification of sugar solutions |
| CN102127122A (en) * | 2010-12-31 | 2011-07-20 | 山东西王药业有限公司 | Automatic control method and device for adding activated carbon in production of anhydrous glucose |
| CN202007232U (en) * | 2010-12-31 | 2011-10-12 | 山东西王药业有限公司 | Activated carbon addition equipment in anhydrous dextrose production |
| CN202892973U (en) * | 2012-10-30 | 2013-04-24 | 万福生科(湖南)农业开发股份有限公司 | Continuous decoloring device for starch sugar |
| CN103007624A (en) * | 2012-12-16 | 2013-04-03 | 西王药业有限公司 | Decolorizing active carbon recycle device and production technique |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109645117A (en) * | 2019-01-29 | 2019-04-19 | 淮南师范学院 | A method of Yoghourt shelf life is extended based on Flos Caryophylli extract |
| CN110898459A (en) * | 2019-12-12 | 2020-03-24 | 浙江华康药业股份有限公司 | Active carbon decoloration system |
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| Publication number | Publication date |
|---|---|
| CN105148557B (en) | 2017-03-29 |
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