CN202808813U - Refine sugar production system capable of improving crystallization assisting efficiency of full-sealed crystallization assisting tank - Google Patents
Refine sugar production system capable of improving crystallization assisting efficiency of full-sealed crystallization assisting tank Download PDFInfo
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- CN202808813U CN202808813U CN 201220230444 CN201220230444U CN202808813U CN 202808813 U CN202808813 U CN 202808813U CN 201220230444 CN201220230444 CN 201220230444 CN 201220230444 U CN201220230444 U CN 201220230444U CN 202808813 U CN202808813 U CN 202808813U
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Abstract
The utility model discloses a refine sugar production system capable of improving the crystallization assisting efficiency of a full-sealed crystallization assisting tank. The system is characterized by comprising a raw sugar dissolving tank, sugar water cleaning equipment, an evaporation pot, a sugar boiling pot, a crystallization assisting tank, a honey extractor and drying equipment sequentially connected through a pipeline, wherein a pot washing water outlet is formed on the sugar boiling pot. The production system also comprises a buffer tank with a water inlet, a water outlet and a steam emptying pipe, wherein the pot washing water outlet of the sugar boiling pot is communicated with the water inlet of the buffer tank through a pot washing water valve and a corresponding pipeline; and the water outlet of the buffer tank is communicated with the raw sugar dissolving tank through a corresponding pipeline. The refine sugar production system disclosed by the utility model can avoid decline in the product quality caused by directly discharging the pot washing water of the sugar boiling pot into the crystallization assisting tank at present, and is favorable for improving the crystallization assisting efficiency of the full-sealed crystallization assisting tank, stabilizing the automatic operation of the honey extractor, improving the effect of the honey extractor and stabilizing the product quality.
Description
Technical field
The utility model relates to the production system of sugar enterprise, more particularly relates to a kind of Closed Circulation in Sugar Production system that improves hermetically sealed crystallization in motion case crystallization in motion efficient.
Background technology
During cane sugar manufacture was produced, massecuite was discharged into the crystallization in motion case from boiling pan, and the process through lowering the temperature gradually helps crystal to continue to grow up, and makes the sucrose in the mother liquor separate out more complete.Fig. 1 is the production equipment system synoptic diagram that this Production Flow Chart is usually used at present in the cane sugar manufacture enterprise.As shown in the figure, this part producing system includes boiling pan and crystallization in motion case, and the two is connected by valve with sugar and respective line; For fully reclaiming the sugar in the boiling pan cleaning of evaporator water, the cleaning of evaporator water of boiling pan directly enters corresponding crystallization in motion case by cleaning of evaporator water water valve.But, adopt the production equipment system of this structure to produce, produce easily following problem:
(1) because cleaning of evaporator steam is high, and the cleaning of evaporator water temp of generation still reaches about 96 ℃ usually, behind the massecuite in contact crystallization in motion case, makes massecuite sand grains local dissolution;
(2) because boiling pan is totally-enclosed the connection with the crystallization in motion case, cleaning of evaporator steam is to discharge through crystallization in motion case blow-down pipe from valve with sugar, in cleaning of evaporator parameter (the 15 minutes cleaning of evaporator time of usually adopting, 125 ℃ of vapor temperatures) under, cleaning of evaporator steam also can cause at high temperature local dissolution of the interior massecuite sand grains of crystallization in motion case;
(3) consider that from the angle that improves process efficiency and quality product the refined sugar production process is usually all shorter, the residence time of massecuite in the crystallization in motion case is often less than 1 hour; If adopting production equipment system shown in Figure 1 produces, when entering the crystallization in motion case, cleaning of evaporator water in case, forms easily one deck water layer above the massecuite, because syrup and massecuite are difficult to mix in the short period of time, suddenly the situation that thinning, flow velocity is accelerated can appear in Automatic sieve when sugar massecuite, thereby cause the sugar centrifuge vibration or the phenomenon that massecuite is scraped sieve occurs, and then affect quality product.
The utility model content
The purpose of this utility model namely is to provide a kind of simple in structure, Closed Circulation in Sugar Production system that can improve hermetically sealed crystallization in motion case crystallization in motion efficient.
The utility model can improve the Closed Circulation in Sugar Production system of hermetically sealed crystallization in motion case crystallization in motion efficient, includes the raw sugar dissolving case, syrup cleaning device, evaporating pot, boiling pan, crystallization in motion case, sugar centrifuge and the drying plant that link to each other by the pipeline order; Described boiling pan is provided with the cleaning of evaporator water out; This production system also includes a baffle-box that is provided with water-in, water outlet and steam evacuation pipe; The cleaning of evaporator water out of described boiling pan is connected with the water-in of described baffle-box by cleaning of evaporator water valve and respective line, and the water outlet of described baffle-box is connected with described raw sugar dissolving case by respective line.
When production system was provided with a plurality of described boiling pan, the cleaning of evaporator water out of each boiling pan can be connected to by cleaning of evaporator water valve and respective line the water-in of same baffle-box.
The utility model can improve in the Closed Circulation in Sugar Production system of hermetically sealed crystallization in motion case crystallization in motion efficient, and the cleaning of evaporator water of boiling pan is to be discharged into the raw sugar dissolving case that is in technological process of production front end by a baffle-box, and cleaning of evaporator steam is discharged from baffle-box steam evacuation pipe.Adopt the technical program, because cleaning of evaporator water enters baffle-box (but not entering the crystallization in motion case), raw sugar dilute juice after the raw sugar dissolving send clarify process equipment again to boil sugar behind clarify process again, thereby cause the generation of deterioration in quality situation in the time of can avoiding boiling pan cleaning of evaporator water directly to enter the crystallization in motion case, help to improve the crystallization in motion efficient of hermetically sealed crystallization in motion case, the automatic operation of stablizing sugar centrifuge, raising sugar centrifuge effect and stabilized product quality.
Description of drawings
Fig. 1 boils the usual production equipment system synoptic diagram that uses in the sugared crystallization in motion Production Flow Chart in the cane sugar manufacture enterprise.
Fig. 2 is the schematic block diagram of an embodiment of the utility model Closed Circulation in Sugar Production system that can improve hermetically sealed crystallization in motion case crystallization in motion efficient.
Fig. 3 is the production unit connection diagram (boiling sugared crystallization in motion part) of an embodiment of the utility model Closed Circulation in Sugar Production system that can improve hermetically sealed crystallization in motion case crystallization in motion efficient.
1-boiling pan 2-valve 3-with sugar crystallization in motion case 4-cleaning of evaporator water valve
5-baffle-box 6-steam evacuation pipe
Embodiment
Below in conjunction with accompanying drawing the Closed Circulation in Sugar Production system that the utility model can improve hermetically sealed crystallization in motion case crystallization in motion efficient is further described.
Fig. 1 boils the usual production equipment system synoptic diagram that uses in the sugared crystallization in motion Production Flow Chart in the cane sugar manufacture enterprise.This part producing system has as shown in the figure illustrated 5 covers and has boiled sugared crystallization in motion equipment, and every cover includes a boiling pan 1 and a crystallization in motion case 3, and the two is connected by valve 2 with sugar and respective line; For fully reclaiming the sugar in the boiling pan cleaning of evaporator water, the cleaning of evaporator water of each boiling pan 1 directly enters corresponding crystallization in motion case 3 by cleaning of evaporator water valve 4.
Fig. 2 is the schematic block diagram of an embodiment of the utility model Closed Circulation in Sugar Production system that can improve hermetically sealed crystallization in motion case crystallization in motion efficient.Fig. 3 is the production unit connection diagram (boiling sugared crystallization in motion part) of an embodiment of the utility model Closed Circulation in Sugar Production system that can improve hermetically sealed crystallization in motion case crystallization in motion efficient.Such as figure, the Closed Circulation in Sugar Production system that the utility model can improve hermetically sealed crystallization in motion case crystallization in motion efficient includes raw sugar dissolving case, syrup cleaning device, evaporating pot, boiling pan, crystallization in motion case, sugar centrifuge and the drying plant that links to each other by the pipeline order, also is provided with a baffle-box between the cleaning of evaporator water out of boiling pan and the raw sugar dissolving case.Such as Fig. 3, baffle-box 5 is provided with water-in, water outlet and steam evacuation pipe 6, the cleaning of evaporator water of each boiling pan 1 drains into same baffle-box 5 altogether: the cleaning of evaporator water out of each boiling pan 1 is connected with the water-in of baffle-box 5 by cleaning of evaporator water valve 4 and respective line, and the water outlet of baffle-box 5 is connected with described raw sugar dissolving case by respective line.
In the production process, send raw sugar dissolving case behind clarify process, again to boil again sugar from the cleaning of evaporator water of each boiling pan 1 cleaning of evaporator water out with raw sugar, sugar water; The cleaning of evaporator steam of boiling pan 1 is discharged from the steam evacuation pipe 6 of baffle-box 5.
In the utility model Closed Circulation in Sugar Production system, because the cleaning of evaporator water of boiling pan is to be discharged into the raw sugar dissolving case that is in technological process of production front end by baffle-box to recycle, thereby cause the generation of deterioration in quality situation in the time of can avoiding boiling pan cleaning of evaporator water directly to enter the crystallization in motion case.Inventor place enterprise once boiled sugared crystallization in motion production system and made simultaneous test Fig. 1 and two covers shown in Figure 3: production system 40m3R1 massecuite shown in Figure 1 sieves to get 28.5 tons of refined sugar, and sugar producing rate is 53.3%; The 40m3R1 massecuite of production system shown in Figure 3 sieves to get 32 tons of refined sugar, sugar producing rate is 59.8%, improved 6.5%, the employing of evidence the utility model Closed Circulation in Sugar Production system really helps to improve the crystallization in motion efficient of hermetically sealed crystallization in motion case, stablizes the automatic operation of sugar centrifuge, improves sugar centrifuge effect and stabilized product quality.
Claims (2)
1. can improve the Closed Circulation in Sugar Production system of hermetically sealed crystallization in motion case crystallization in motion efficient, it is characterized in that: include the raw sugar dissolving case, syrup cleaning device, evaporating pot, boiling pan, crystallization in motion case, sugar centrifuge and the drying plant that link to each other by the pipeline order; Described boiling pan is provided with the cleaning of evaporator water out;
This production system also includes a baffle-box that is provided with water-in, water outlet and steam evacuation pipe;
The cleaning of evaporator water out of described boiling pan is connected with the water-in of described baffle-box by cleaning of evaporator water valve and respective line, and the water outlet of described baffle-box is connected with described raw sugar dissolving case by respective line.
2. the Closed Circulation in Sugar Production system that improves hermetically sealed crystallization in motion case crystallization in motion efficient according to claim 1, it is characterized in that: described boiling pan has a plurality of, and the cleaning of evaporator water out of each boiling pan is connected to the water-in of same baffle-box by cleaning of evaporator water valve and respective line.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220230444 CN202808813U (en) | 2012-05-22 | 2012-05-22 | Refine sugar production system capable of improving crystallization assisting efficiency of full-sealed crystallization assisting tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220230444 CN202808813U (en) | 2012-05-22 | 2012-05-22 | Refine sugar production system capable of improving crystallization assisting efficiency of full-sealed crystallization assisting tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202808813U true CN202808813U (en) | 2013-03-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220230444 Expired - Fee Related CN202808813U (en) | 2012-05-22 | 2012-05-22 | Refine sugar production system capable of improving crystallization assisting efficiency of full-sealed crystallization assisting tank |
Country Status (1)
| Country | Link |
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| CN (1) | CN202808813U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103409564A (en) * | 2013-08-16 | 2013-11-27 | 开远华丰机电机械工贸有限公司 | Thermal system and technology for evaporation, heating and sugar boiling in sugar preparation |
| CN106011320A (en) * | 2016-06-27 | 2016-10-12 | 广西农垦糖业集团红河制糖有限公司 | Sugar boiling tank with tank washer |
-
2012
- 2012-05-22 CN CN 201220230444 patent/CN202808813U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103409564A (en) * | 2013-08-16 | 2013-11-27 | 开远华丰机电机械工贸有限公司 | Thermal system and technology for evaporation, heating and sugar boiling in sugar preparation |
| CN103409564B (en) * | 2013-08-16 | 2015-05-13 | 开远华丰机电机械工贸有限公司 | Thermal system and technology for evaporation, heating and sugar boiling in sugar preparation |
| CN106011320A (en) * | 2016-06-27 | 2016-10-12 | 广西农垦糖业集团红河制糖有限公司 | Sugar boiling tank with tank washer |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20130320 Termination date: 20140522 |