CN203382767U - System for increasing temperature of drifting water in beet sugar refinery - Google Patents
System for increasing temperature of drifting water in beet sugar refinery Download PDFInfo
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- CN203382767U CN203382767U CN201320374541.1U CN201320374541U CN203382767U CN 203382767 U CN203382767 U CN 203382767U CN 201320374541 U CN201320374541 U CN 201320374541U CN 203382767 U CN203382767 U CN 203382767U
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Abstract
The utility model relates to a technology for preparing sugar by using beets, and discloses a system for increasing the temperature of drifting water in a beet sugar refinery. The device comprises a tower plate condenser, wherein the tower plate condenser is provided with a cold water inlet, a condensed water outlet, a juice gas inlet and a noncondensable gas outlet; the cold water inlet is connected with the outlet of a drifting water box through a pipeline; the inlet of the drifting water box is connected with the outlet of a cold water pump; the inlet of the cold water pump is connected with a cold water pond arranged on the tail end of a radial flow sedimentation pond through the pipeline; the juice gas inlet is connected with a juice gas outlet through the pipeline; the condensed water outlet is connected with the inlet of a water seal tank through the pipeline; the outlet of the water seal tank is connected with the inlet of a temperature increasing water pump through the pipeline; the outlet of the temperature increasing water pump is connected to a mixed water pond through the pipeline. The device disclosed by the utility model can be used for increasing the temperature of the drifting water by carrying out heat exchange by utilizing a sugar juice gas which is discharged from a sugar preparation crystallizing tank and the drifting water and has the advantages of independence, easiness for implementation, energy conservation and high applicability.
Description
Technical field
The utility model relates to the beet sugar manufacture technology, and particularly a kind of beet-sugar factory stream send the temperature raising system of water.
Background technology
Beet is one of main sugar crop of China, and producing region mainly is distributed in 8 provinces and regions of periphery such as northeast, northwest, North China, and wherein Heilungkiang, Xinjiang and the Inner Mongol are the three advantages zones that China's beet is produced.The general cold season after October of beet processing of China, now the beet in stockyard substantially freezes.In the course of processing, beet needs one slowly to freeze process, is beneficial to the subsequent operationss such as beet slicing, and wherein beet fluming is a kind of method that domestic sugar refinery is generally used.But domestic beet-sugar factory is distributed in extremely frigid zones more, at the dirty water temp that send of open environment, descend comparatively fast.Stream send water temp too low, is unfavorable for that the slow of beet freezes, and affects the chopping operation; And too low dish slice temperature is unfavorable for oozing out of beet sugar.For this reason, a kind of way of desirable raising beet fluming water temp need to be found by manufacturing enterprise, to overcome the impact of cold snap.
Stream commonly used send following two kinds of water extraction temperature method, and the one, the water in mixing tank adds to stream and send water system, improves stream and send water temp; The 2nd, special stream is set and send water extraction temperature well heater.These two kinds of methods can improve the temperature that stream send water, but have certain defect.The shortcoming of mixing tank compensation process is: during cold snap, stream send the rate of water make-up of water much larger than the normal quantity discharged of settling tank; For keeping water balance, must cause the artificial increase of water displacement, thereby increase technique total water amount.The shortcoming of well heater temperature raising method is: steam consumption is larger, easily destroys the process steam balance, and is unfavorable for that factory is energy-conservation.
Summary of the invention
The utility model proposes the temperature raising system that a kind of beet-sugar factory stream send water, when cold season, utilize in the sugaring crystallizer syrup gas and stream out to send water to carry out thermal exchange, convection current send water to carry out temperature raising, and device independence is easy to implement, energy-conservation and suitability is strong.
For achieving the above object, the utility model is achieved by the following technical solutions.
A kind of beet-sugar factory stream send the temperature raising system of water, comprise sugaring crystallizer and flume, the top of described sugaring crystallizer is provided with the outlet of juice gas, the low side of described flume is provided with the dish water separator, the water side of described dish water separator is connected with the width flow settling pond, the tail end of described width flow settling pond is connected with and mixes pond, described mixing pond connects the entrance of first-class conveying pump by pipeline, the outlet of described stream conveying pump is connected to the high-end of described flume, it is characterized in that, described beet-sugar factory stream send the temperature raising system of water also to comprise the column plate condenser, described column plate condenser is provided with cooling water inlet, condensation-water drain, the import of juice gas and non-condensable gas outlet, described cooling water inlet connects the first-class outlet of sending water tank by pipeline, described stream send the entrance of water tank to connect a cold water pump outlet, the entrance of described water supply pump is connected with the water cooling pond of being located at described width flow settling pond tail end by pipeline, the import of described juice gas connects described juice gas outlet by pipeline, described condensation-water drain connects the entrance of a flashback tank by pipeline, the outlet of described flashback tank connects the entrance of a temperature raising water pump by pipeline, the outlet of described temperature raising water pump is connected to described mixing pond by pipeline.
Characteristics of the present utility model and further the improvement are:
Described column plate condenser is vertically placed, and described cooling water inlet is located at the upper side wall of described column plate condenser, and described condensation-water drain is located at the lower end of described column plate condenser, and the lower wall of described column plate condenser is located in the import of described juice gas.
Described column plate condenser is provided with water trap, and the sidewall of described water trap is located in described non-condensable gas outlet, and described non-condensable gas outlet is connected with vacuum pump, and the lower end of described water trap connects the entrance of described flashback tank by pipeline.
The dish delivery end of described dish water separator is connected with vegetable washing machine, and bottom is provided with water side, and described water side is connected to described width flow settling pond by pipeline.
Beet-sugar factory stream of the present utility model send the temperature raising system of water, in sugaring initial stage in season and latter stage, when envrionment temperature is higher, shuts the first control valve on water cooling pond, and without heating, the water that directly will mix in pond is extracted in flume and is circulated by the stream conveying pump; When envrionment temperature reduces, for guaranteeing that stream send the temperature of water, open the first control valve on water cooling pond, send water to inject water cooling pond cold stream, then by water supply pump, the water in water cooling pond be evacuated to stream and send water tank, and in the column plate condenser with the sugaring crystallizer in juice gas out carry out thermal exchange, make the water extraction temperature, water after temperature raising enters and mixes pond by the temperature raising water pump again, again carries out stream and send circulation, with this, reaches the purpose that circular heating and stream send.
The accompanying drawing explanation
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
Fig. 1 is the one-piece construction schematic diagram that a kind of beet-sugar factory stream of the present utility model send the temperature raising system of water.
In figure: 1, flume; 2, dish water separator; 3, vegetable washing machine; 4, sludge pump; 5, width flow settling pond; 6, the first control valve; 7, water cooling pond; 8, mix pond; 9, stream conveying pump; 10, water supply pump; 11, temperature raising water pump; 12, flashback tank; 13, column plate condenser; 14, water trap; 15, stream send water tank; 16, the second control valve; 17, sugaring crystallizer; 18, the 3rd control valve.
Embodiment
With reference to Fig. 1, it is the one-piece construction schematic diagram that a kind of beet-sugar factory stream of the present utility model send the temperature raising system of water.In figure, this beet-sugar factory stream send the temperature raising system of water to comprise sugaring crystallizer 17 and flume 1, and the top of sugaring crystallizer 17 is provided with the outlet of juice gas, the low side of flume 1 is provided with dish water separator 2, the water side of dish water separator 2 is connected with width flow settling pond 5, the water of dish water separator 2 is by pumping or flow automatically in width flow settling pond 5, the tail end of width flow settling pond 5 is connected with and mixes pond 8, mix pond 8 and connects the entrance that flows conveying pump 9 by pipeline, the stream of the high-end formation that the outlet of flowing conveying pump 9 is connected to flume 1 during without temperature raising send circulation, the tail end of width flow settling pond 5 also is provided with column plate condenser 13, column plate condenser 13 is provided with cooling water inlet, condensation-water drain, the import of juice gas and non-condensable gas outlet, cooling water inlet connects by pipeline the outlet that stream send water tank 15, stream send the entrance of water tank 15 to connect the outlet of water supply pump 10 by pipeline, the entrance of water supply pump 10 is connected with the water cooling pond 7 of the tail end of being located at width flow settling pond 5 by pipeline, the import of juice gas connects the outlet of juice gas by pipeline, condensation-water drain connects the entrance of flashback tank 12 by pipeline, the outlet of flashback tank 12 connects the entrance of temperature raising water pump 11 by pipeline, the outlet of temperature raising water pump 11 is connected to and mixes pond 8 by pipeline.Stream send water tank 15 for cold water out in temporary transient storage water cooling pond, and the entrance of water supply pump 10 also is connected with strainer, and convection current send water further to filter; Width flow settling pond 5 is connected with sludge pump 4, and sludge pump 4 is evacuated to the decontamination mud sump by the mud in width flow settling pond 5.
The dish delivery end of dish water separator 2 is connected with vegetable washing machine 3, and the top of vegetable washing machine 3 is connected with the first running water pipe, and bottom is provided with water side, and water side is connected to width sedimentation tank 5.This is that the secondary cleaning water on vegetable washing machine 3 is become to the part that stream send water.
Mix pond 8 and be connected with the second running water pipe, and be provided with the 3rd control valve 18, when stream send water to reduce in working cycle, can be supplemented by the second running water pipe mixed on pond 8.Water cooling pond 7 is provided with the first control valve 6 that send water to send into water cooling pond stream, only at cold snap, while needing convection current to send water to carry out temperature raising, just opens the first control valve 6, makes stream send water to enter water cooling pond 7 and carries out temperature raising again.While not needing temperature raising, stream send water directly to enter mixing pond 8 and is circulated.
Beet-sugar factory stream of the present utility model send the temperature raising system of water, in sugaring initial stage in season and latter stage, when envrionment temperature is higher, shut the first control valve 6 on water cooling pond 7, without heating, directly will mix water in pond 8 and be extracted into the high-end of flume 1 by stream conveying pump 9 and circulated; When envrionment temperature reduces, for guaranteeing that stream send the temperature of water, open the first control valve 6 on water cooling pond 7, send water to inject water cooling pond 7 cold stream, then by water supply pump 10, the water in water cooling pond 7 be evacuated to stream and send water tank 15, and in column plate condenser 13 with sugaring crystallizer 17 in juice gas out carry out thermal exchange, make the water extraction temperature, water after temperature raising enters and mixes pond 8 by temperature raising water pump 11 again, again carries out stream and send circulation, with this, reaches the purpose that circular heating and stream send.
Beet-sugar factory stream of the present utility model send the temperature raising system of water, utilizes the juice gas convection current in sugaring crystallizer 17 to send water to carry out temperature raising, the different control of row in the time of can be according to the varying environment temperature, and device is independent, easy to implement, energy-conservation and suitability is strong.
Although below by reference to the accompanying drawings embodiment of the present utility model is described, the utility model is not limited to above-mentioned specific embodiments, and above-mentioned specific embodiments is only schematic, guiding, rather than restrictive.Those of ordinary skill in the art, under the enlightenment of this specification sheets, in the situation that do not break away from the scope that the utility model claim is protected, can also make a variety of forms, and these all belong to the row of the utility model protection.
Claims (4)
1. a beet-sugar factory stream send the temperature raising system of water, comprise sugaring crystallizer and flume, the top of described sugaring crystallizer is provided with the outlet of juice gas, the low side of described flume is provided with the dish water separator, the water side of described dish water separator is connected with the width flow settling pond, the tail end of described width flow settling pond is connected with and mixes pond, described mixing pond connects the entrance of first-class conveying pump by pipeline, the outlet of described stream conveying pump is connected to the high-end of described flume, it is characterized in that, described beet-sugar factory stream send the temperature raising system of water also to comprise the column plate condenser, described column plate condenser is provided with cooling water inlet, condensation-water drain, the import of juice gas and non-condensable gas outlet, described cooling water inlet connects the first-class outlet of sending water tank by pipeline, described stream send the entrance of water tank to connect a cold water pump outlet, the entrance of described water supply pump is connected with the water cooling pond of being located at described width flow settling pond tail end by pipeline, the import of described juice gas connects described juice gas outlet by pipeline, described condensation-water drain connects the entrance of a flashback tank by pipeline, the outlet of described flashback tank connects the entrance of a temperature raising water pump by pipeline, the outlet of described temperature raising water pump is connected to described mixing pond by pipeline.
2. beet-sugar factory stream according to claim 1 send the temperature raising system of water, it is characterized in that, described column plate condenser is vertically placed, described cooling water inlet is located at the upper side wall of described column plate condenser, described condensation-water drain is located at the lower end of described column plate condenser, and the lower wall of described column plate condenser is located in the import of described juice gas.
3. beet-sugar factory stream according to claim 1 send the temperature raising system of water, it is characterized in that, described column plate condenser is provided with water trap, the sidewall of described water trap is located in described non-condensable gas outlet, described non-condensable gas outlet is connected with vacuum pump, and the lower end of described water trap connects the entrance of described flashback tank by pipeline.
4. beet-sugar factory stream according to claim 1 send the temperature raising system of water, it is characterized in that, the dish delivery end of described dish water separator is connected with vegetable washing machine, and bottom is provided with water side, and described water side is connected to described width flow settling pond by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320374541.1U CN203382767U (en) | 2013-06-26 | 2013-06-26 | System for increasing temperature of drifting water in beet sugar refinery |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320374541.1U CN203382767U (en) | 2013-06-26 | 2013-06-26 | System for increasing temperature of drifting water in beet sugar refinery |
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|---|---|
| CN203382767U true CN203382767U (en) | 2014-01-08 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320374541.1U Expired - Lifetime CN203382767U (en) | 2013-06-26 | 2013-06-26 | System for increasing temperature of drifting water in beet sugar refinery |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106524128A (en) * | 2016-12-16 | 2017-03-22 | 中国轻工业南宁设计工程有限公司 | Intelligent control system for efficiently using sugar factory condensate |
| CN111517500A (en) * | 2020-04-27 | 2020-08-11 | 内蒙古敕勒川糖业有限责任公司 | Water circulation system and method for beet sugar production |
-
2013
- 2013-06-26 CN CN201320374541.1U patent/CN203382767U/en not_active Expired - Lifetime
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106524128A (en) * | 2016-12-16 | 2017-03-22 | 中国轻工业南宁设计工程有限公司 | Intelligent control system for efficiently using sugar factory condensate |
| CN111517500A (en) * | 2020-04-27 | 2020-08-11 | 内蒙古敕勒川糖业有限责任公司 | Water circulation system and method for beet sugar production |
| CN111517500B (en) * | 2020-04-27 | 2021-01-29 | 内蒙古敕勒川糖业有限责任公司 | Water circulation system and method for beet sugar production |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140108 |
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| CX01 | Expiry of patent term |