CN220071655U - Syrup floating reaction system - Google Patents
Syrup floating reaction system Download PDFInfo
- Publication number
- CN220071655U CN220071655U CN202321685674.0U CN202321685674U CN220071655U CN 220071655 U CN220071655 U CN 220071655U CN 202321685674 U CN202321685674 U CN 202321685674U CN 220071655 U CN220071655 U CN 220071655U
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- CN
- China
- Prior art keywords
- syrup
- communicated
- pipeline
- floating
- reaction
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- 239000006188 syrup Substances 0.000 title claims abstract description 68
- 235000020357 syrup Nutrition 0.000 title claims abstract description 68
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 47
- 239000006260 foam Substances 0.000 claims abstract description 17
- 238000005189 flocculation Methods 0.000 claims abstract description 6
- 230000016615 flocculation Effects 0.000 claims abstract description 5
- 239000012535 impurity Substances 0.000 abstract description 7
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 abstract description 4
- 229910000147 aluminium phosphate Inorganic materials 0.000 abstract description 2
- 238000007789 sealing Methods 0.000 abstract description 2
- 238000005187 foaming Methods 0.000 abstract 1
- 239000000654 additive Substances 0.000 description 7
- 238000007599 discharging Methods 0.000 description 6
- 230000000996 additive effect Effects 0.000 description 5
- 238000004891 communication Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 230000008569 process Effects 0.000 description 4
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 2
- 229930006000 Sucrose Natural products 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000004042 decolorization Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 240000000111 Saccharum officinarum Species 0.000 description 1
- 235000007201 Saccharum officinarum Nutrition 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 229960004793 sucrose Drugs 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Landscapes
- Jellies, Jams, And Syrups (AREA)
Abstract
The utility model discloses a syrup floating reaction system, which comprises a crude syrup storage tank, a heater, a foam maker, a flocculator, a reaction device, a foam remover, a floating separator and an overflow box, wherein the foam maker is arranged on the upper surface of the crude syrup storage tank; the foam maker is communicated with the reaction device through a pipeline; the upper end of the reaction device is communicated with the pipeline at the lower end of the flocculation device; the lower end of the bubble removing device is communicated with the lower end of the floating separator, and the upper end of the bubble removing device is communicated with the upper end of the floating separator; the floating separator is communicated with the overflow box pipeline. The utility model has the advantages that: according to the utility model, the foaming and reaction device is changed into a sealing structure, the reaction device flows out of the syrup in a way of feeding the syrup from the upper end to the lower end of the pipeline, phosphoric acid is added, the syrup enters the flocculation reaction after passing through the three-stage reaction device, finally enters the foam remover, the syrup enters the floating separator, and invalid foam is discharged into the floating pond, so that impurities of the syrup are effectively removed, and the purity of the syrup entering the next operation is ensured.
Description
Technical Field
The utility model relates to the technical field of sugar cane sugar production, in particular to a syrup floating reaction system.
Background
The syrup floating system is used as a process for purifying syrup, so that syrup impurities can be effectively removed, and the quality and yield of white sugar can be improved.
However, in the prior art, the original syrup floating system foam maker and the reaction device are of an open structure, so that the conditions of slag turning and extremely unstable quality of refined syrup are easily caused, the color value and turbidity are high, the color removal rate and turbidity reduction rate are low, the impact resistance is weak, and the effect of the equipment in the running process is not ideal.
Disclosure of Invention
The utility model aims to solve the technical problem of providing a syrup floating reaction system which can effectively improve the quality of syrup.
In order to solve the technical problems, the technical scheme of the utility model is as follows:
a syrup floating reaction system comprises a crude syrup storage tank, a heater, a foam maker, a flocculator, a reaction device, a foam remover, a floating separator and an overflow box; the foam maker is communicated with the reaction device through a pipeline; the upper end of the reaction device is communicated with the pipeline at the lower end of the flocculator; the lower end of the bubble removing device is communicated with the lower end of the floating separator, and the upper end of the bubble removing device is communicated with the upper end of the floating separator; the floating separator is communicated with the overflow box pipeline.
Further, the reaction device comprises a primary reactor, a secondary reactor and a tertiary reactor; the upper end of the primary reactor is communicated with the lower end pipeline of the secondary reactor; the upper end of the secondary reactor is communicated with the lower end of the tertiary reactor through a pipeline.
Further, the device also comprises an overflow box; the overflow box is communicated with the floating separator pipeline through a pipeline.
Further, a drain pipe is communicated with a pipeline communicated between the floating separator and the overflow box.
Further, the lower end of the overflow box is communicated with a discharging pipe.
Further, the thick syrup storage tank is communicated with a heater connecting pipeline and is provided with a pressurizing pump.
The utility model has the beneficial effects that:
according to the utility model, the bubble making device and the reaction device are changed into a sealing structure, the reaction device adopts a mode that the upper end of a pipeline is out of the way that the lower end of the pipeline is in the way of entering, phosphoric acid is added, the syrup enters the flocculation reaction after passing through the three-stage reaction device, finally enters the bubble removing device, the syrup enters the floating separator, invalid foam is discharged into the floating pond, impurities of the syrup are effectively removed, and the purity of the syrup entering the next operation is ensured.
Drawings
FIG. 1 is a schematic flow chart of a syrup floating reaction system.
In the figure, a 1-coarse syrup storage tank, a 2-heater, a 3-foam maker, a 4-reaction device, a 5-flocculation device, a 6-foam remover, a 7-overflow box, an 8-floating separator, a 9-discharge pipe, a 10-blow-down pipe, a 11-booster pump, a 12-additive inlet pipe I, a 13-additive inlet pipe II, a 41-primary reactor, a 42-secondary reactor and a 43-tertiary reactor are arranged.
Detailed Description
The following describes the embodiments of the present utility model further with reference to the drawings. The description of these embodiments is provided to assist understanding of the present utility model, but is not intended to limit the present utility model. In addition, the technical features of the embodiments of the present utility model described below may be combined with each other as long as they do not collide with each other.
Referring to FIG. 1, a syrup floating reaction system comprises a crude syrup storage tank 1, a heater 2, a foam maker 3, a flocculator 5, a reaction device 4, a foam remover 6, a floating separator 8 and an overflow box 7; the bubble maker 3 is communicated with the reaction device 4 through a pipeline; the upper end of the reaction device 4 is communicated with a pipeline at the lower end of the flocculator 5; the lower end of the bubble removing device 6 is communicated with the lower end of the floating separator 8, and the upper end is communicated with the upper end of the floating separator 8; the floating separator 8 is in pipeline communication with the overflow box 7. The coarse syrup tank 1 is provided for facilitating the storage of coarse syrup. The heater 2 is used for heating syrup flowing in from the raw syrup tank 1. The bubbler 3 is capable of bubbling the heated syrup to generate a large number of microbubbles and ultra-microbubbles, which enter the reaction apparatus 4 together with a large portion of the syrup. The reaction device 4 is used for reacting syrup. The bubble remover 6 is used for realizing bubble liquid separation. The overflow box 7 is arranged to buffer the syrup as it enters the next stage. The floating separator 8 can remove the residual impurities and ensure the purification degree of syrup.
Specifically, the reaction device 4 includes a primary reactor 41, a secondary reactor 42, and a tertiary reactor 43; the upper end of the primary reactor 41 is in pipeline communication with the lower end of the secondary reactor 42; the upper end of the secondary reactor 42 is in pipeline communication with the lower end of the tertiary reactor 43. The primary reactor 41, the secondary reactor 42 and the tertiary reactor 43 are arranged to ensure the sufficient reaction of the syrup, so that the syrup is further purified.
Specifically, an additive inlet pipe I12 is communicated with a pipeline connected between the bubble making device 3 and the primary reactor 41; an additive inlet pipe II 13 is communicated with a pipeline connected between the three-stage reactor 43 and the flocculator 5. The arrangement of the additive inlet pipe I12 and the additive inlet pipe II 13 facilitates the addition of the additive.
As another embodiment, the overflow box 7 is also included; the overflow box 7 is in pipeline communication with the floating separator 8 through a pipeline. The syrup in the floating separator 8 is introduced into the overflow box 7 for discharging through a pipeline, so that the syrup is buffered.
Specifically, a drain pipe 10 is communicated with a pipeline communicated between the floating separator 8 and the overflow box 7. The drain pipe 10 can remove impurities in the floating separator 8.
Specifically, the lower extreme intercommunication of overflow tank 7 has discharging pipe 9. The discharging pipe 9 facilitates the syrup to enter the next process.
Specifically, the connection pipeline of the crude syrup storage tank 1 and the heater 2 is communicated with a pressurizing pump 11. The pressurizing pump 11 can increase the pressure of the whole process and accelerate the reaction process of the whole device.
The working principle of the utility model is as follows:
the raw syrup stored in the raw syrup tank 1 is fed to the heater 2 by the pressurizing pump 11 to be heated, and when the syrup is heated to a predetermined temperature, the syrup is fed to the bubble maker 3 to be foamed, and under the action of the bubble maker, a large amount of microbubbles and ultra microbubbles are generated from the syrup, and the bubbles enter the reaction device 4 together with most of the syrup. The reaction device 4 is provided with 3 stages, and syrup impurities are fully reacted under the action of the three-stage reactor. The syrup after reaction of the reaction device 4 enters the flocculator 5 for flocculation, then foam reaches the upper end of the floating separator 8 through a pipeline, the syrup reaches the lower end of the floating separator 8 through a pipeline, the syrup is further separated and purified in the floating separator 8, the refined syrup meeting the detection regulation is finally obtained, the refined syrup reaches the overflow box 7 through a pipeline, and the lower end of the overflow box 7 is provided with the discharging pipe 9, so that the syrup is convenient to enter the next working flow. The arrangement of the drain pipe 10 is advantageous for discharging impurities remaining in the floating separator 8.
After the utility model is actually used, the actual obtained effects in the production are as follows: the color removal rate is about 55%; the turbidity reducing rate is about 60 percent; the syrup is purified by about 0.5 GP. The quality of the product is greatly improved through the transformation of the syrup floating system.
The embodiments of the present utility model have been described in detail above with reference to the accompanying drawings, but the present utility model is not limited to the described embodiments. It will be apparent to those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the utility model, and yet fall within the scope of the utility model.
Claims (6)
1. The utility model provides a syrup come-up reaction system, includes crude syrup storage tank (1), heater (2), bubble making ware (3), flocculation ware (5), its characterized in that: the device also comprises a reaction device (4), a bubble removing device (6), an upward floating separator (8) and an overflow box (7); the foam maker (3) is communicated with the reaction device (4) through a pipeline; the upper end of the reaction device (4) is communicated with the pipeline at the lower end of the flocculator (5); the lower end of the bubble removing device (6) is communicated with the lower end of the floating separator (8), and the upper end of the bubble removing device is communicated with the upper end of the floating separator (8); the floating separator (8) is communicated with the overflow box (7) through a pipeline.
2. The syrup floating reaction system of claim 1, wherein: the reaction device (4) comprises a primary reactor (41), a secondary reactor (42) and a tertiary reactor (43); the upper end of the primary reactor (41) is communicated with the lower end pipeline of the secondary reactor (42); the upper end of the secondary reactor (42) is communicated with the lower end of the tertiary reactor (43) through a pipeline.
3. The syrup floating reaction system of claim 1, wherein: also comprises an overflow box (7); the overflow box (7) is communicated with the floating separator (8) through a pipeline.
4. A syrup floatation reaction system according to claim 3, wherein: a drain pipe (10) is communicated with a pipeline communicated between the floating separator (8) and the overflow box (7).
5. The syrup floating reaction system of claim 1, wherein: the lower end of the overflow box (7) is communicated with a discharge pipe (9).
6. The syrup floating reaction system of claim 1, wherein: the thick syrup storage tank (1) is communicated with a connecting pipeline of the heater (2) and is provided with a pressurizing pump (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321685674.0U CN220071655U (en) | 2023-06-29 | 2023-06-29 | Syrup floating reaction system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321685674.0U CN220071655U (en) | 2023-06-29 | 2023-06-29 | Syrup floating reaction system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220071655U true CN220071655U (en) | 2023-11-24 |
Family
ID=88828872
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321685674.0U Active CN220071655U (en) | 2023-06-29 | 2023-06-29 | Syrup floating reaction system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220071655U (en) |
-
2023
- 2023-06-29 CN CN202321685674.0U patent/CN220071655U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CP02 | Change in the address of a patent holder |
Address after: 678400 North Section of Mangshi Street, Dehong Dai and Jingpo Autonomous Prefecture, Yunnan Province Patentee after: Yunnan Dehong Yingmao Sugar Industry Co.,Ltd. Address before: 678400 North Section of Mangshi Street, Xishuangbanna Dai Autonomous Prefecture, Yunnan Province Patentee before: Yunnan Dehong Yingmao Sugar Industry Co.,Ltd. |
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| CP02 | Change in the address of a patent holder |