CN203212344U - Preliming liquid separation device in carbonic acid method production process - Google Patents
Preliming liquid separation device in carbonic acid method production process Download PDFInfo
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- CN203212344U CN203212344U CN 201320165993 CN201320165993U CN203212344U CN 203212344 U CN203212344 U CN 203212344U CN 201320165993 CN201320165993 CN 201320165993 CN 201320165993 U CN201320165993 U CN 201320165993U CN 203212344 U CN203212344 U CN 203212344U
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- liquid separation
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Abstract
The utility model discloses a preliming liquid separation device in a carbonic acid method production process. The preliming liquid separation device comprises a preliming tank (1) which is connected with an input pipeline of an air floating separation device (3); two output pipelines of the air floating separation device (3) are connected with a clear liquid storage tank (5) and a muddy dreg storage tank (4) respectively; the clear liquid storage tank (5) is connected with a main ash bucket (2) through a pump; the muddy dreg storage tank (4) discharges impurities through a pump. According to the preliming liquid separation device disclosed by the utility model, a lot of impurities, which are flocculated in a preliming procedure, are separated and removed in advance by the air floating separation device so as to realize solid-liquid separation and effectively improve the purity of materials, obtained high-purity clear liquid enters following procedures, and thus the quality of a product is obviously improved. The viscosity of material liquid is reduced, the filtering performance is greatly improved and the ash adding amount is obviously reduced. According to the device disclosed by the utility model, the technical difficulty of traditional processing equipment that flocculated impurities are dissolved again is successfully solved.
Description
Technical field:
The utility model relates to a kind of in the process of carbonatation process production inulin or beet sugar manufacture, predefecation juice is carried out the device of filtering separation.
Background technology:
The carbonatation process cleaning technique is one of main purification method of producing inulin or beet sugar manufacture, and its main traditional process is: the raw material diffusion juice, and---------main ash bucket---carbonation---once filters etc. well heater preliming tank.This traditional process can be removed about 40% impurity, only does flocculation because of the predefecation juice of this traditional process, does not do separation, all dirt flocculation back enters main ash bucket together with material through heating, the impurity that causes having flocculated is dissolved in the material again, causes feed purity to reduce, and influences quality product; The material filtering difficulty, in order to improve the strainability of material, often this traditional process needs the very high ash amount that adds, and generally speaking, always adding the ash amount is 2.5% pair of raw material weight, and lime consumption is very big.
Summary of the invention:
The utility model provides a kind of and improves the quality of products at the above-mentioned deficiency of prior art, and the carbonatation process that significantly reduces lime consumption is produced the predefecation juice tripping device of inulin.
Technical solution of the present utility model is: predefecation juice tripping device in a kind of carbonatation process production technique, be provided with preliming tank, preliming tank is connected with the input channel of gas floatation separation device, the two-way output channel of gas floatation separation device is connected with clear liquid storage tank, turbid slag storage tank respectively, the clear liquid storage tank is connected with main ash bucket by pump, and turbid slag storage tank effluxes by pump.
The utility model adopts gas floatation separation device to separate in advance at most of impurity that pre-ash process has flocculated and removes, and realizes solid-liquid separation, has improved the purity of material effectively, and the clear juice of the high purity that obtains enters the back operation, and quality product obviously improves.The bad raw material of quality is had better adaptability, even when raw materials quality is inferior, quality product also can be more stable.Viscosity of sludge descends, and strainability improves significantly, adds the ash amount and obviously reduces.The solution that this device is successful the technical barrier that dissolves again of the impurity that has flocculated that exists of traditional process equipment.Because the impurity in the predefecation juice of carbonatation process production inulin, flocculation together under certain basicity condition, dehydration property is very poor, other filter types except membrane filtration separate, almost be irrealizable, and membrane filtration investment is bigger, and therefore adopting gas floatation separation device is separation scheme the most cost-effectively.
Description of drawings:
Fig. 1 is structural representation of the present utility model.
Embodiment:
As shown in Figure 1, predefecation juice tripping device in a kind of carbonatation process production technique, be provided with preliming tank 1, preliming tank 1 is connected with the input channel of gas floatation separation device 3, the two-way output channel of gas floatation separation device 3 is connected with clear liquid storage tank 5, turbid slag storage tank 4 respectively, clear liquid storage tank 5 is connected with main ash bucket 2 by pump, and turbid slag storage tank 4 effluxes by pump.
Preliming tank produces the qualified predefecation juice of index, and gas floatation separation device is realized the solid-liquid separation of predefecation juice, removes partial impurities, and clear liquid enters the clear liquid storage tank, enters traditional peace and quiet system master's ash bucket, and turbid slag enters turbid slag storage tank, is discharged to the appointed place outside after desugar is handled.
Claims (1)
1. predefecation juice tripping device in the carbonatation process production technique, be provided with preliming tank (1), it is characterized in that: preliming tank (1) is connected with the input channel of gas floatation separation device (3), the two-way output channel of gas floatation separation device (3) is connected with clear liquid storage tank (5), turbid slag storage tank (4) respectively, clear liquid storage tank (5) is connected with main ash bucket (2) by pump, and turbid slag storage tank (4) effluxes by pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320165993 CN203212344U (en) | 2013-04-07 | 2013-04-07 | Preliming liquid separation device in carbonic acid method production process |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320165993 CN203212344U (en) | 2013-04-07 | 2013-04-07 | Preliming liquid separation device in carbonic acid method production process |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203212344U true CN203212344U (en) | 2013-09-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320165993 Expired - Fee Related CN203212344U (en) | 2013-04-07 | 2013-04-07 | Preliming liquid separation device in carbonic acid method production process |
Country Status (1)
| Country | Link |
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| CN (1) | CN203212344U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104805223A (en) * | 2015-04-16 | 2015-07-29 | 南宁易速德机械设备有限公司 | Automatic solid-liquid separation prelimer |
-
2013
- 2013-04-07 CN CN 201320165993 patent/CN203212344U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104805223A (en) * | 2015-04-16 | 2015-07-29 | 南宁易速德机械设备有限公司 | Automatic solid-liquid separation prelimer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: YIAN HENGXIN BIOLOGY ENGINEERING TECHNOLOGY CO., L Free format text: FORMER OWNER: ZUOYUAN GROUP CO., LTD. Effective date: 20150430 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 116000 DALIAN, LIAONING PROVINCE TO: 161500 QIQIHAR, HEILONGJIANG PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20150430 Address after: Qigihar City, Heilongjiang province Yi'an town 161500 Yi'an County outside the West Patentee after: Ian constant new biological engineering technology Co. Ltd. Address before: 116000 Dalian City, Liaoning province high tech Industrial Park, No. 596 Huangpu Road, layer 3, No. 17, No. 4 Patentee before: Joy Yuen Group Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130925 Termination date: 20210407 |