CN204932936U - The decoloration device of starch liquid sugar - Google Patents
The decoloration device of starch liquid sugar Download PDFInfo
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- CN204932936U CN204932936U CN201520604999.0U CN201520604999U CN204932936U CN 204932936 U CN204932936 U CN 204932936U CN 201520604999 U CN201520604999 U CN 201520604999U CN 204932936 U CN204932936 U CN 204932936U
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- tank
- eddy flow
- tank body
- water
- flow surge
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Abstract
A kind of decoloration device of starch liquid sugar, it comprises tank body and agitator, described tank body is covered with cover, described cover is provided with feed pipe, described tank base is provided with discharge nozzle, described feed pipe is provided with an eddy flow surge tank, be provided with active carbon directly over described eddy flow surge tank and add tank, described agitator comprises drive unit and paddle, described drive unit is fixedly installed on described cover, described paddle is plugged in described tank body, the hollow interlayer of watertightness is provided with in the sidewall of described tank body, the lateral wall of described tank body is provided with for being communicated with described hollow interlayer and extraneous water inlet interface and water outlet mouthpiece, a water circulating pump and temperature-compensating cyclic water tank is connected with respectively by water receiving pipe between described water outlet mouthpiece and described water inlet interface.
Description
Technical field
The utility model relates to produces the apparatus field of starch sugar, particularly decolours to liquid glucose in a kind of starch sugar production process, the device of removal of impurities.
Background technology
Starch sugar is a kind of take starch as the sugar that raw material is produced, and is mainly used in food industry, medical industry and chemical industry.In the production process of starch sugar, the decolouring after saccharification, removal of impurities are one of whole production process important procedures heavily, directly have influence on the quality of final products.Also have some coloring matters and some impurity in liquid glucose after saccharification, impurity must be removed and coloring matter could obtain the even colourless syrupy product of clear.In Sugarcane juice decolorization, dedoping step, the general impurity used in charcoal absorption liquid glucose.Traditional Sugarcane juice decolorization removal of impurities mode is generally add in liquid glucose by activated carbon powder, stir in bleacher, and then utilize impurity in charcoal absorption liquid glucose, but this mode also exists a series of defect in the specific implementation, as, superficial attractive forces and the temperature of active carbon are inversely proportional to, but temperature its rate of adsorption high is fast, at relatively high temperatures, liquid glucose viscosity is relatively low, the absorption inner surface that liquid glucose penetrates into active carbon can be accelerated, be beneficial to adsorbing contaminant, but temperature can not be too high, otherwise the adsorption capacity reducing active carbon also can cause sugar decomposition and painted, therefore the temperature of general liquid glucose maintains 80 degrees Celsius and is advisable, traditional bleacher can not control the temperature of liquid glucose, only just as a simple reaction vessel, and when adding activated carbon powder in traditional bleacher in liquid glucose, easily form the situation that powdered carbon flies upward, be unfavorable for that activated carbon powder fully mixes with liquid glucose.
Utility model content
The purpose of this utility model is the decoloration device providing a kind of starch liquid sugar, its technical problem to be solved is: traditional bleacher just uses as a mixed reaction vessel, when adding activated carbon powder, easy powdered carbon flies upward, and the temperature of liquid glucose cannot be kept to be in optimal adsorption reaction temperature.
For solving the problems of the technologies described above, the utility model provides a kind of decoloration device of starch liquid sugar, it comprises tank body and agitator, described tank body is covered with cover, described cover is provided with feed pipe, described tank base is provided with discharge nozzle, described feed pipe is provided with an eddy flow surge tank, be provided with active carbon directly over described eddy flow surge tank and add tank, described agitator comprises drive unit and paddle, described drive unit is fixedly installed on described cover, described paddle is plugged in described tank body, the hollow interlayer of watertightness is provided with in the sidewall of described tank body, the lateral wall of described tank body is provided with for being communicated with described hollow interlayer and extraneous water inlet interface and water outlet mouthpiece, a water circulating pump and temperature-compensating cyclic water tank is connected with respectively by water receiving pipe between described water outlet mouthpiece and described water inlet interface.
Be preferable over: the bottom of described eddy flow surge tank is communicated with on described feed pipe, the sidewall of described eddy flow surge tank is coconnected is provided with an eddy flow conveying pipeline tangent with described eddy flow surge tank sidewall.
Be preferable over: described active carbon adds and is provided with one between tank and the top of described eddy flow surge tank and adds charcoal pipe, described in add charcoal pipe is provided with and add charcoal control valve.
Be preferable over: be provided with temperature sensor in described hollow interlayer, described temperature sensor is connected to a controller, and be provided with heater in described temperature-compensating cyclic water tank, described controller is connected to described water circulating pump and heater respectively.
Be preferable over: described paddle is pusher paddle.
Compared with prior art, the beneficial effects of the utility model are:
One, by the filling hot water that circulates in described hollow interlayer, temperature-compensating is carried out to the liquid glucose in described tank body, liquid glucose is made to maintain 80 degrees centigrade all the time, and then effectively can improve the mixing velocity of active carbon and liquid glucose, the rate of adsorption of active carbon can also be improved;
Two, utilize and described eddy flow surge tank is set on described feed pipe, and active carbon interpolation tank is set on described eddy flow surge tank, and then the step of adding active carbon in liquid glucose was completed before liquid glucose enters tank body, and then the situation that when can avoid adding active carbon, powdered carbon flies upward;
Three, make the liquid glucose entered in described eddy flow surge tank form eddy current by described eddy flow surge tank, and then the activated carbon powder added can be made tentatively to mix, prevent activated carbon powder from liquid glucose, tying the situation of cake, be conducive to activated carbon powder and fully mix with liquid glucose.
Accompanying drawing explanation
Fig. 1 is tank body sectional structure schematic diagram of the present utility model.
Fig. 2 is the radial sectional structure schematic diagram in eddy flow surge tank year of the present utility model.
Fig. 3 is the function of temperature compensation control module frame chart of temperature-compensating cyclic water tank of the present utility model to hollow interlayer.
Detailed description of the invention
Below with reference to accompanying drawing 1 to 3 and preferred embodiment, the decoloration device to a kind of starch liquid sugar that the utility model proposes specifically illustrates.
As shown in Figure 1, the utility model provides a kind of decoloration device of starch liquid sugar, it comprises tank body 1 and agitator 2, described tank body 1 is covered with cover 11, described cover 11 is provided with feed pipe 12, discharge nozzle 13 is provided with bottom described tank body 1, described feed pipe 12 is provided with an eddy flow surge tank 3, be provided with active carbon directly over described eddy flow surge tank 3 and add tank 4, described agitator 2 comprises drive unit 21 and paddle 22, described paddle 22 is pusher paddle, described drive unit 21 is fixedly installed on described cover 11, described paddle 22 is plugged in described tank body 1, the hollow interlayer 14 of watertightness is provided with in the sidewall of described tank body 1, the lateral wall of described tank body 1 is provided with for being communicated with described hollow interlayer 14 and extraneous water inlet interface 15 and water outlet mouthpiece 16, a water circulating pump 18 and temperature-compensating cyclic water tank 19 is connected with respectively by water receiving pipe 17 between described water outlet mouthpiece 16 and described water inlet interface 15.
The utility model in the specific implementation, under the pump of described water circulating pump 18 is dynamic, Inner eycle is realized by described water receiving pipe 17, intake interface 15 and water outlet mouthpiece 16 between described temperature-compensating cyclic water tank 19 and described hollow interlayer 14, and then temperature-compensating is carried out to the liquid glucose in described tank body 1, be conducive to the impurity in charcoal absorption liquid glucose; And the filling 3 of eddy flow buffering is set on described feed pipe 12, and adds tank 4 and in described eddy flow surge tank 3, carry out liquid glucose by being arranged on active carbon on eddy flow surge tank 3 mix with the preliminary of active carbon.
Further, the bottom of described eddy flow surge tank 3 is communicated with on described feed pipe 12, the sidewall of described eddy flow surge tank 3 is coconnected is provided with an eddy flow conveying pipeline 31 tangent with described eddy flow surge tank 3 sidewall, be provided with one between described active carbon interpolation tank 4 and the top of described eddy flow surge tank 3 and add charcoal pipe 41, described add charcoal pipe 41 is provided with add charcoal control valve 42, the activated carbon powder that described active carbon adds in tank 4 is dropped in described eddy flow surge tank 3 by the described charcoal pipe 41 that adds, described revolving to be stayed in conveying pipeline 31 liquid glucose of conveying to enter in described eddy flow surge tank 3 to form eddy current, eddy current is conducive to activated carbon powder and is tentatively blended in liquid glucose, be convenient to next step mixing entered in described tank body 1, the interpolation speed that charcoal control valve 42 controls activated carbon powder is added described in also can utilizing.
Temperature sensor 141 is provided with in described hollow interlayer 14, described temperature sensor 141 is connected to a controller 142, heater 191 is provided with in described temperature-compensating cyclic water tank 19, described controller 142 is connected to described water circulating pump 18 and heater 191 respectively, and then controls the heating power of described heater 191 and the circulation pump power of described water circulating pump 18 according to the temperature signal that described temperature sensor 141 feeds back.
Described on comprehensive, the technical solution of the utility model fully effectively can complete above-mentioned utility model object, and structural principle of the present utility model and the principle of work and power are all verified in an embodiment fully, and effect and the object of expection can be reached, and embodiment of the present utility model also can convert according to these principles, therefore, the utility model comprise all in claim mention all replacement contents in scope.Any equivalence change done in the utility model claim, within the scope of the claims of all genus this case applications.
Claims (5)
1. the decoloration device of a starch liquid sugar, it is characterized in that: comprise tank body and agitator, described tank body is covered with cover, described cover is provided with feed pipe, described tank base is provided with discharge nozzle, described feed pipe is provided with an eddy flow surge tank, be provided with active carbon directly over described eddy flow surge tank and add tank, described agitator comprises drive unit and paddle, described drive unit is fixedly installed on described cover, described paddle is plugged in described tank body, the hollow interlayer of watertightness is provided with in the sidewall of described tank body, the lateral wall of described tank body is provided with for being communicated with described hollow interlayer and extraneous water inlet interface and water outlet mouthpiece, a water circulating pump and temperature-compensating cyclic water tank is connected with respectively by water receiving pipe between described water outlet mouthpiece and described water inlet interface.
2. the decoloration device of starch liquid sugar as claimed in claim 1, it is characterized in that: the bottom of described eddy flow surge tank is communicated with on described feed pipe, the sidewall of described eddy flow surge tank is coconnected is provided with an eddy flow conveying pipeline tangent with described eddy flow surge tank sidewall.
3. the decoloration device of starch liquid sugar as claimed in claim 2, is characterized in that: described active carbon adds and is provided with one between tank and the top of described eddy flow surge tank and adds charcoal pipe, described in add charcoal pipe is provided with and add charcoal control valve.
4. the decoloration device of starch liquid sugar as claimed in claim 3, it is characterized in that: in described hollow interlayer, be provided with temperature sensor, described temperature sensor is connected to a controller, be provided with heater in described temperature-compensating cyclic water tank, described controller is connected to described water circulating pump and heater respectively.
5. the decoloration device of starch liquid sugar as claimed in claim 4, is characterized in that: described paddle is pusher paddle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201520604999.0U CN204932936U (en) | 2015-08-12 | 2015-08-12 | The decoloration device of starch liquid sugar |
Applications Claiming Priority (1)
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CN201520604999.0U CN204932936U (en) | 2015-08-12 | 2015-08-12 | The decoloration device of starch liquid sugar |
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CN204932936U true CN204932936U (en) | 2016-01-06 |
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CN201520604999.0U Expired - Fee Related CN204932936U (en) | 2015-08-12 | 2015-08-12 | The decoloration device of starch liquid sugar |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111854164A (en) * | 2020-06-17 | 2020-10-30 | 华帝股份有限公司 | Temperature control cabin with temperature compensation function and gas heat exchange equipment applying same |
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2015
- 2015-08-12 CN CN201520604999.0U patent/CN204932936U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111854164A (en) * | 2020-06-17 | 2020-10-30 | 华帝股份有限公司 | Temperature control cabin with temperature compensation function and gas heat exchange equipment applying same |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
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: 20160106 Termination date: 20180812 |