CN205329073U - High fructose syrup production is with continuous ion exchange equipment of quaternary - Google Patents
High fructose syrup production is with continuous ion exchange equipment of quaternary Download PDFInfo
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- CN205329073U CN205329073U CN201620069207.9U CN201620069207U CN205329073U CN 205329073 U CN205329073 U CN 205329073U CN 201620069207 U CN201620069207 U CN 201620069207U CN 205329073 U CN205329073 U CN 205329073U
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Abstract
The utility model discloses a high fructose syrup production is with continuous ion exchange equipment of quaternary. The mode of establishing ties with parallelly connected two sets of anion -exchange column crowds after this equipment adopts two sets of cation exchange column crowds parallelly connected, leave the liquid glucose to hand over and handle, storng -acid cation exchange resin has the effect of getting rid of protein and amino acid, consequently, can be abundant get rid of protein, can not influence the place to go effect of inorganic salts and other organic impurities, obtain high -quality liquid glucose, parallelly connected structure is formed, can avoid because of one of them interrupt from the whole production procedure of handing over the post to go wrong to lead to, and ensure the favoring production.
Description
Technical field
This utility model relates to a kind of high fructose syrup production ion-exchange unit, is specially a kind of high fructose syrup production quaternary continuous ion exchange apparatus。
Background technology
High fructose syrup production process, it is common that enter ion-exchange process after decolorization filtering, but still contain protein in the sugar liquid of decolorization filtering, if cannot remove, can affect from handing over effect, affect end product quality。It addition, in concrete production, one of them ion exchange column there is a problem, will affect the carrying out of whole technological process。
Summary of the invention
The purpose of this utility model is aiming at the defect of above-mentioned existence and provides a kind of high fructose syrup production quaternary continuous ion exchange apparatus。The pattern that this equipment is connected with two groups of anion-exchange column groups in parallel after adopting two groups of cation exchange column group's parallel connections, undertaken sugar liquid processing from friendship, storng-acid cation exchange resin has removal protein and amino acid whose effect, therefore can fully by protein removal, place to go effect without influence on inorganic salt He other organic impuritiess, obtain high-quality sugar liquid, structure composition in parallel, the interruption of the integral production flow process caused because one of them goes wrong can be avoided from friendship post, it is ensured that being smoothed out of production。
A kind of high fructose syrup production quaternary continuous ion exchange apparatus technical scheme of the present utility model is, by the first group of cation exchange column group connected and first group of anion-exchange column group, the second group cation exchange column group of series connection and second group of anion-exchange column group composition, wherein, first group of cation exchange column group's charging aperture and the second group cation exchange column group's charging aperture connect sugar liquid entrance, first group of cation exchange column group's discharging opening and the second group cation exchange column group's discharging opening are connected by material pipe, first group of anion-exchange column group's discharging opening and second group of anion-exchange column group's discharging opening connect sugar liquid outlet；First group of described cation exchange column group and the second group cation exchange column group are made up of the cation exchange column of more than 2 respectively, and first group of anion-exchange column group and second group of anion-exchange column group are made up of the anion-exchange column of more than 2 respectively。
First group of described cation exchange column group and the second group cation exchange column group are made up of 3 cation exchange columns respectively, and first group of anion-exchange column group and second group of anion-exchange column group are made up of 3 anion-exchange columns respectively。
Described cation exchange column is strong-acid type large aperture cation exchange resin column。
Described anion-exchange column is weak base type cation exchange resin column。
Described first group of cation exchange column group, the second group cation exchange column group, first group of anion-exchange column group and second group of anion-exchange column group's charging aperture place are provided with valve。
First group of cation exchange column group's discharging opening and the second group cation exchange column interconnective material pipe of group's discharging opening are provided with bidirectional sealed butterfly valve。
A kind of high fructose syrup production quaternary continuous ion exchange apparatus of the present utility model has the beneficial effect that the pattern that this equipment is connected after adopting two groups of cation exchange column group's parallel connections with two groups of anion-exchange column groups in parallel, undertaken sugar liquid processing from friendship, storng-acid cation exchange resin has removal protein and amino acid whose effect, therefore can fully by protein removal, place to go effect without influence on inorganic salt He other organic impuritiess, obtain high-quality sugar liquid, structure composition in parallel, the interruption of the integral production flow process caused because one of them goes wrong can be avoided from friendship post, ensure that what produce is smoothed out。
Accompanying drawing illustrates:
Fig. 1 show basic structure schematic diagram of the present utility model。
In figure, 1. sugar liquid entrance, 2. first group of cation exchange column group, 3. first group of anion-exchange column group, 4. the second group cation exchange column group, 5. second group of anion-exchange column group, 6. valve, 7. bidirectional sealed butterfly valve, 8. sugar liquid outlet。
Detailed description of the invention:
In order to be more fully understood that this utility model, describe the technical solution of the utility model in detail with instantiation below, but this utility model is not limited thereto。
Embodiment 1
A kind of high fructose syrup production quaternary continuous ion exchange apparatus of the present utility model, by the first group of cation exchange column group 2 connected and first group of anion-exchange column group 3, the second group cation exchange column group 4 and second group of anion-exchange column group 5 of series connection form, wherein, first group of cation exchange column group 3 charging aperture and the second group cation exchange column group 4 charging aperture connect sugar liquid entrance 1, first group of cation exchange column group 2 discharging opening and the second group cation exchange column group 4 discharging opening are connected by material pipe, first group of anion-exchange column group 3 discharging opening and second group of anion-exchange column group 5 discharging opening connect sugar liquid outlet 8；First group of described cation exchange column group 2 and the second group cation exchange column group 4 are made up of 3 cation exchange columns respectively, and first group of anion-exchange column group 3 and second group of anion-exchange column group 5 are made up of 3 anion-exchange columns respectively。
Described cation exchange column is strong-acid type large aperture cation exchange resin column。
Described anion-exchange column is weak base type cation exchange resin column。
Described first group of cation exchange column group 2,4, first group of anion-exchange column group 3 of the second group cation exchange column group and second group of anion-exchange column group 5 charging aperture place are provided with valve 6。
First group of cation exchange column group 2 discharging opening and the second group cation exchange column group 4 interconnective material pipe of discharging opening are provided with bidirectional sealed butterfly valve 7。
The pattern that this equipment is connected with two groups of anion-exchange column groups in parallel after adopting two groups of cation exchange column group's parallel connections, undertaken sugar liquid processing from friendship, storng-acid cation exchange resin has removal protein and amino acid whose effect, therefore can fully by protein removal, place to go effect without influence on inorganic salt He other organic impuritiess, obtain high-quality sugar liquid, structure composition in parallel, the interruption of the integral production flow process caused because one of them goes wrong can be avoided from friendship post, it is ensured that being smoothed out of production。
Embodiment 2
A kind of high fructose syrup production quaternary continuous ion exchange apparatus of the present utility model, by the first group of cation exchange column group 2 connected and first group of anion-exchange column group 3, the second group cation exchange column group 4 and second group of anion-exchange column group 5 of series connection form, wherein, first group of cation exchange column group 3 charging aperture and the second group cation exchange column group 4 charging aperture connect sugar liquid entrance 1, first group of cation exchange column group 2 discharging opening and the second group cation exchange column group 4 discharging opening are connected by material pipe, first group of anion-exchange column group 3 discharging opening and second group of anion-exchange column group 5 discharging opening connect sugar liquid outlet 8；First group of described cation exchange column group 2 and the second group cation exchange column group 4 are made up of 4 cation exchange columns respectively, and first group of anion-exchange column group 3 and second group of anion-exchange column group 5 are made up of 4 anion-exchange columns respectively。
Described cation exchange column is strong-acid type large aperture cation exchange resin column。
Described anion-exchange column is weak base type cation exchange resin column。
Described first group of cation exchange column group 2,4, first group of anion-exchange column group 3 of the second group cation exchange column group and second group of anion-exchange column group 5 charging aperture place are provided with valve 6。
First group of cation exchange column group 2 discharging opening and the second group cation exchange column group 4 interconnective material pipe of discharging opening are provided with bidirectional sealed butterfly valve 7。
The pattern that this equipment is connected with two groups of anion-exchange column groups in parallel after adopting two groups of cation exchange column group's parallel connections, undertaken sugar liquid processing from friendship, storng-acid cation exchange resin has removal protein and amino acid whose effect, therefore can fully by protein removal, place to go effect without influence on inorganic salt He other organic impuritiess, obtain high-quality sugar liquid, structure composition in parallel, the interruption of the integral production flow process caused because one of them goes wrong can be avoided from friendship post, it is ensured that being smoothed out of production。
Claims (6)
1. a high fructose syrup produces and uses quaternary continuous ion exchange apparatus, it is characterized in that, by the first group of cation exchange column group connected and first group of anion-exchange column group, the second group cation exchange column group of series connection and second group of anion-exchange column group composition, wherein, first group of cation exchange column group's charging aperture and the second group cation exchange column group's charging aperture connect sugar liquid entrance, first group of cation exchange column group's discharging opening and the second group cation exchange column group's discharging opening are connected by material pipe, first group of anion-exchange column group's discharging opening and second group of anion-exchange column group's discharging opening connect sugar liquid outlet；First group of described cation exchange column group and the second group cation exchange column group are made up of the cation exchange column of more than 2 respectively, and first group of anion-exchange column group and second group of anion-exchange column group are made up of the anion-exchange column of more than 2 respectively。
2. a kind of high fructose syrup production quaternary continuous ion exchange apparatus according to claim 1, it is characterized in that, first group of described cation exchange column group and the second group cation exchange column group are made up of 3 cation exchange columns respectively, and first group of anion-exchange column group and second group of anion-exchange column group are made up of 3 anion-exchange columns respectively。
3. a kind of high fructose syrup production quaternary continuous ion exchange apparatus according to claim 1, it is characterised in that described cation exchange column is strong-acid type large aperture cation exchange resin column。
4. a kind of high fructose syrup production quaternary continuous ion exchange apparatus according to claim 1, it is characterised in that described anion-exchange column is weak base type cation exchange resin column。
5. a kind of high fructose syrup production quaternary continuous ion exchange apparatus according to claim 1, it is characterized in that, described first group of cation exchange column group, the second group cation exchange column group, first group of anion-exchange column group and second group of anion-exchange column group's charging aperture place are provided with valve。
6. a kind of high fructose syrup production quaternary continuous ion exchange apparatus according to claim 1, it is characterized in that, first group of cation exchange column group's discharging opening and be provided with bidirectional sealed butterfly valve on the second group cation exchange column interconnective material pipe of group's discharging opening。
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| Application Number | Priority Date | Filing Date | Title |
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| CN201620069207.9U CN205329073U (en) | 2016-01-25 | 2016-01-25 | High fructose syrup production is with continuous ion exchange equipment of quaternary |
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| CN201620069207.9U CN205329073U (en) | 2016-01-25 | 2016-01-25 | High fructose syrup production is with continuous ion exchange equipment of quaternary |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835656A (en) * | 2019-12-04 | 2020-02-25 | 双桥（厦门）有限公司 | Sachima syrup purification process based on polysaccharide fiber carbon degumming technology |
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2016
- 2016-01-25 CN CN201620069207.9U patent/CN205329073U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110835656A (en) * | 2019-12-04 | 2020-02-25 | 双桥（厦门）有限公司 | Sachima syrup purification process based on polysaccharide fiber carbon degumming technology |
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