CN210340945U - Novel molasses dilution production line - Google Patents
Novel molasses dilution production line Download PDFInfo
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- CN210340945U CN210340945U CN201920804811.5U CN201920804811U CN210340945U CN 210340945 U CN210340945 U CN 210340945U CN 201920804811 U CN201920804811 U CN 201920804811U CN 210340945 U CN210340945 U CN 210340945U
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Abstract
The utility model discloses a novel molasses dilutes production line, a molasses dilutes production line, its characterized in that: including first sugar divide honey machine, second sugar divide honey machine, dissolve brilliant machine, first/first wash/second former case, delivery pump, boil sugar raw material case and boil sugar jar, first sugar divides honey machine respectively through the pipeline with dissolve the entry intercommunication of brilliant machine and first/first wash/second former case and set up the valve respectively, second sugar divides honey machine respectively through the pipeline with dissolve the brilliant machine and first/first wash/second former case the entry intercommunication and set up the valve respectively, dissolve the exit of brilliant machine and be provided with the pipeline and first/first wash/second former case the entry intercommunication, first/first wash/second former case the export with boil sugar raw material case intercommunication, boil sugar raw material case again with boil sugar jar and carry molasses to boil sugar jar and boil sugar. The utility model provides a can will avoid molasses to sink the end, avoid diluting again before boiling sugar, receive the limitation of temperature, dilution time and conventional equipment, can't dissolve crystalline completely, lead to a large amount of sand of wasting time to get into the molasses dilution technology that the system of boiling that boils sugar cake influences sugar cake absorbs and quality.
Description
Technical Field
The utility model relates to a sugaring industry technical field, in particular to novel molasses dilutes production line.
Background
Molasses is a byproduct of sugar industry, has different compositions due to different sugar-making raw materials and processing conditions, mainly contains a large amount of fermentable sugar (mainly sucrose), is a good fermentation raw material, can be used as a substrate or a base material of fermentation products such as yeast, monosodium glutamate, organic acid and the like, and can be used as a raw material of certain foods and animal feed. Due to high concentration of molasses in the production process, sugar particles in the molasses box are easy to settle, and frequent flushing is needed to keep normal use of the molasses box; moreover, the molasses has high viscosity and pumping resistance, and the particle flushing pipeline is easy to wear, so that the valve is not closed tightly; steam heating is needed for dilution before boiling, so that energy consumption is increased and caramel is locally overheated in the production process, and the product quality is influenced; the sugar is diluted before boiling, and due to the limitations of temperature, dilution time and traditional equipment, the crystal can not be completely dissolved, so that a large amount of waste sand enters a sugar boiling tank to influence the boiling absorption and quality of the sugar cake. Therefore, it is urgently required to find a process capable of solving the above problems.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide a: aiming at the problems, the molasses diluting process can avoid the bottom precipitation of the molasses, avoid the dilution before the sugar boiling, and can not completely dissolve crystals due to the limitation of temperature, diluting time and traditional equipment, so that a large amount of waste sand enters the sugar boiling tank to influence the boiling absorption and quality of the sugar cake.
In order to realize the purpose of the utility model, the utility model discloses a technical scheme as follows:
the utility model provides a molasses dilution production line, includes that first sugar divides honey machine, second sugar divides honey machine, dissolves brilliant machine, first/first wash/second former case, delivery pump, boils the former case of sugar and boils the sugar jar, first sugar divides honey machine respectively through the pipeline with dissolve the entry intercommunication of brilliant machine and first/first wash/second former case and set up the valve respectively, second sugar divides honey machine respectively through the pipeline with dissolve the entry intercommunication of brilliant machine and first/first wash/second former case and set up the valve respectively, the exit of dissolving brilliant machine is provided with the entry intercommunication of pipeline and first/first wash/second former case, the export and the former case intercommunication of boiling sugar of first/first wash/second former case, boil sugar raw material case again with boil the sugar jar and carry molasses to boil sugar jar and boil sugar.
Furthermore, dissolve brilliant machine and include that the crystalline substance case is dissolved to the one-level, the crystalline substance case is dissolved to the second grade, the crystalline substance case is dissolved to the tertiary, overflow baffle and hot water supply mouth, should dissolve brilliant machine and separate into the crystalline substance case is dissolved to the one-level, the crystalline substance case is dissolved to the second grade and the tertiary crystalline substance case is dissolved through two sets of overflow baffles, agitating unit fixes respectively in the crystalline substance case is dissolved to the one-level, the crystalline substance case is dissolved to the second grade and the tertiary crystalline substance case is dissolved to the second grade, hot water supply mouth is total three and is located the top that the crystalline substance case is dissolved to the one-level, the crystalline substance case is dissolved to the second grade and the tertiary crystalline substance case is dissolved respectively.
Furthermore, a set of overflow baffle includes last baffle and lower baffle, go up the baffle and fix in the top of dissolving brilliant machine, lower baffle is fixed in the bottom of dissolving brilliant machine, and the dislocation is separated between last baffle and the lower baffle and is made molasses pass through from the space between last baffle and the lower baffle.
Furthermore, the height of the upper partition board is greater than that of the lower partition board, and the lower edge of the upper partition board is lower than that of the upper edge of the lower partition board.
Further, agitating unit includes speed reduction agitator and agitator, the speed reduction agitator is located the top outside that brilliant case, second grade dissolved brilliant case, tertiary dissolved brilliant case were dissolved to the one-level, the agitator is fixed in speed reduction agitator below and is located and dissolves the brilliant built-in.
Furthermore, a stirring paddle blade is arranged in the stirring barrel, and the barrel wall of the stirring barrel is a perforated net.
To sum up, owing to adopted above-mentioned technical scheme, the beneficial effects of the utility model are that:
(1) the molasses diluting link is advanced to a molasses discharging outlet of the honey separator, and the molasses diluting of the sugar boiling building is eliminated, so that the molasses can be fully dissolved in the crystal inside the molasses before entering the sugar boiling building, and a stable diluting process is realized to enable the molasses to reach the desired brix;
(2) the crystal dissolving machine is arranged at the honey discharging outlet of the honey separator, so that sugar particles can be prevented from sinking, the labor intensity of flushing a box is reduced, and the service life of subsequent operation equipment is prolonged;
(3) the honey discharging brix can be reduced from 80 degrees BX to 70-72 degrees BX at the outlet of the honey separator, the viscosity of the molasses is reduced, the pumping resistance and the abrasion of a particle flushing pipeline are reduced, the valve is protected to be normal, the service life of equipment is prolonged, and the production consumption is reduced;
(4) the molasses of the medium crystal dissolver of the utility model is diluted without using steam for heating, thereby reducing energy consumption and avoiding the caramel which is locally overheated from influencing product quality, and the molasses can be diluted and heated by directly adding hot water and has the function of overflowing the molasses into the next link;
(5) the diluting process of the utility model avoids the dilution before boiling sugar, can not completely dissolve crystal due to the limitation of temperature, diluting time and traditional equipment, leads a large amount of waste sand to enter the sugar boiling pot to influence the boiling absorption and quality of the sugar cake, and can dilute and dissolve the molasses after using the diluting process of the utility model;
(6) the utility model discloses a whole processing equipment sparingly boils the diluting box of sugar building, vacates the floor space, reduces the link that artifical frequent dilution reduces workman's intensity of labour.
More comprehensive, the utility model discloses a link that technology dilutes molasses advances to honey separating machine row honey mouth, reduce molasses to boiling sugar in-process because the time length leads to the temperature to reduce the back and need steam to heat up and dilute, increase energy consumption and caramel, it is big to avoid molasses to contain the litter to lead to the head tank bottoming and transport resistance simultaneously, the pipeline wearing and tearing, utilize the different rotational speeds of brilliant machine design of dissolving to dissolve the inside litter of molasses with higher speed in addition, simultaneously through automatic control of adding technology hot water and stable dilution hammer degree, provide and boil sugar and directly use the molasses material.
Drawings
FIG. 1 is a schematic structural view of a production line of the present invention;
FIG. 2 is a schematic structural view of a medium crystal melting machine according to the present invention;
in the drawing, a first-stage crystal dissolving box 31, a second-stage crystal dissolving box 32, a third-stage crystal dissolving box 33, a stirring device 34, a speed-reducing stirrer 341, a stirring barrel 342, a stirring blade 343, an overflow partition 35, an upper partition 351, a lower partition 352, a hot water supply port 36, a molasses outlet 37, a feeding device 38, an original A/first washing/second original box 4, a conveying pump 5, a sugar boiling raw material box 6 and a sugar boiling tank 7 are arranged in the first-stage crystal dissolving box 1, the second-stage crystal dissolving box 2, the stirring device 341, the stirring barrel 342.
Detailed Description
In order to make the objects, technical solutions and advantages of the present invention more apparent, the following description will be given of preferred embodiments and further detailed description of the present invention. It should be understood, however, that the numerous specific details set forth in the specification are merely set forth to provide a thorough understanding of one or more aspects of the present invention, which may be practiced without these specific details.
Example 1
As shown in figure 1, a molasses dilution production line comprises a first molasses separator 1, a second molasses separator 2, a crystal dissolver 3, a first raw/first washing/second raw box 4, a delivery pump 5, a sugar boiling raw material box 6 and a sugar boiling tank 7, wherein the first molasses separator 1 is respectively communicated with inlets of the crystal dissolver 3 and the first raw/first washing/second raw box 4 through pipelines and is respectively provided with valves, the second molasses separator 2 is respectively communicated with inlets of the crystal dissolver 3 and the first raw/first washing/second raw box 4 through pipelines and is respectively provided with valves, an outlet of the crystal dissolver 3 is provided with a pipeline communicated with an inlet of the first raw/first washing/second raw box 4, an outlet of the first raw/first washing/second raw box 4 is communicated with the sugar boiling raw material box 6, the sugar boiling raw material box 6 is further communicated with the sugar boiling tank to deliver molasses to the sugar boiling tank 7, wherein the first molasses separator 1 is an existing device on the market, for example, an XG series full-automatic scraper discharge top-hung centrifuge, and the honey extractor 2 is also an existing device, for example, an SL series full-automatic continuous honey extractor. In the embodiment, a molasses diluting link of a sugar boiling building of the existing equipment is advanced to a honey discharging port of a honey separator, crystal dissolving dilution is designed by utilizing the principle of a sugar dissolving machine, 90 ℃ process hot water is added to enable the brix of molasses to be reduced from 80 degrees BX to 70-72 degrees BX, the temperature is controlled to be about 70 ℃, waste sand is completely dissolved by stirring at different rotating speeds, the problem that steam is needed to be heated up for dilution after the temperature is reduced due to long time in the molasses boiling process is solved, energy consumption and caramel are increased, meanwhile, the problem that the molasses contains waste sand to cause bottom sinking of a raw material box and large conveying resistance and pipeline abrasion are avoided, the waste sand in the molasses is accelerated to be dissolved by utilizing different rotating speeds of the crystal dissolving machine, and meanwhile, the brix of molasses is controlled and stabilized by automatically adding process hot water, and the molasses material is.
As shown in fig. 2, the crystal dissolving machine 3 includes a first-stage crystal dissolving tank 31, a second-stage crystal dissolving tank 32, a third-stage crystal dissolving tank 33, a stirring device 34, overflow partitions 35 and a hot water supply port 36, the crystal dissolving machine 3 is separated into the first-stage crystal dissolving tank 31, the second-stage crystal dissolving tank 32 and the third-stage crystal dissolving tank 33 by two groups of overflow partitions 35, the stirring device is respectively fixed in the first-stage crystal dissolving tank 31, the second-stage crystal dissolving tank 32 and the third-stage crystal dissolving tank 33, the hot water supply ports 36 are three in total and respectively located at the tops of the first-stage crystal dissolving tank 31, the second-stage crystal dissolving tank 32 and the third-stage crystal dissolving tank 33, the bottom of the third-stage crystal dissolving tank 33 is provided with a molasses outlet 37, and the top of the first-.
The overflow partition plates 35 comprise an upper partition plate 351 and a lower partition plate 352, the upper partition plate 351 is fixed at the top of the crystal dissolving machine 3, the lower partition plate 352 is fixed at the bottom of the crystal dissolving machine 3, and the upper partition plate 351 and the lower partition plate 352 are staggered to enable molasses to pass through the space between the upper partition plate 351 and the lower partition plate 352; the height of the upper partition 351 is greater than that of the lower partition and the lower edge of the upper partition 351 is lower than that of the lower partition.
The stirring device 34 comprises a speed-reducing stirrer 341 and a stirring barrel 342, the speed-reducing stirrer 341 is positioned at the outer side of the top of the first-stage crystal dissolving tank 31, the second-stage crystal dissolving tank 32 and the third-stage crystal dissolving tank 33, the stirring barrel 342 is fixed below the speed-reducing stirrer 341 and positioned in the crystal dissolving machine 3, a stirring blade 343 is arranged in the stirring barrel 342, and the barrel wall of the stirring barrel 342 is a leaky net.
The crystal dissolving machine 3 has the main function of achieving the process brix range of dissolving and stably diluting the crystals inside the molasses according to the flow design of the molasses, wherein the feeding device 38 on the first-stage crystal dissolving box 31 mainly meters feeding and guides automatic water addition to the stable dilution brix. The hot water supply port 36 is connected with an automatic hot water adding system above, the main functions are that the hot water flow is automatically started according to molasses metering data of the feeding device 38, the dilution brix is stabilized, the feeding device 38 and the automatic hot water adding system are controlled by a control system, the control system is an intelligent PLC control system, and the on-off of the feeding device and the on-off of a hot water injection quantity control hot water port can be controlled according to the feeding quantity.
The stirring device 34 in the crystal dissolving machine 3 is mainly used for accelerating the dissolution of the crystal in the molasses, so that the influence of the waste sand on the product quality caused by the next process is avoided, and the stirring barrel 342 is mainly used for enhancing the mixing in the design, so that the crystal dissolving process is more complete by cutting the crystal dissolving process. The overflow partition 35 has the function of diluting and dissolving crystals step by step, prolonging the crystal dissolving time and achieving the effect of complete dissolution. The overflow baffle 35 is formed to avoid the molasses dilution process part molasses short circuit to overflow, is that part sand waste can't dissolve completely, influences product quality.
Example 2
The process for diluting molasses using the production line of example 1 was: the molasses enters a crystal dissolving machine from a first molasses separating machine and a second molasses separating machine, hot water is added into the crystal dissolving machine while stirring is carried out, after multistage dilution and crystal dissolution, the molasses enters an original A/first washing/original B box for cleaning, the molasses in the original A/first washing/original B box is pumped into a sugar boiling raw material box through a delivery pump, then the molasses is sent into a sugar boiling tank for sugar boiling, the pressure in the sugar boiling tank is 0.085MPa, the vacuum degree is achieved, the sugar boiling temperature is 65 ℃, and the sugar boiling time is 3 hours.
The crystal dissolving machine comprises three-stage crystal dissolving procedures, the three-stage crystal dissolving procedures are separated by partition plates to form independent crystal dissolving spaces, molasses overflows the partition plates from the previous-stage crystal dissolving procedure and enters the next-stage crystal dissolving procedure, and hot water is added and stirred simultaneously in the third-stage crystal dissolving procedure; the temperature of hot water added into the crystal dissolving machine is 90 ℃, the stirring speed is 180rpm, and the crystal dissolving time of molasses in the crystal dissolving machine is 9 min.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of modifications and decorations can be made without departing from the principle of the present invention, and these modifications and decorations should also be regarded as the protection scope of the present invention.
Claims (6)
1. The molasses diluting production line is characterized in that: including first sugar divide honey machine, second sugar divide honey machine, dissolve brilliant machine, first/first wash/second former case, delivery pump, boil sugar raw material case and boil sugar jar, first sugar divides honey machine respectively through the pipeline with dissolve the entry intercommunication of brilliant machine and first/first wash/second former case and set up the valve respectively, second sugar divides honey machine respectively through the pipeline with dissolve the brilliant machine and first/first wash/second former case the entry intercommunication and set up the valve respectively, dissolve the exit of brilliant machine and be provided with the pipeline and first/first wash/second former case the entry intercommunication, first/first wash/second former case the export with boil sugar raw material case intercommunication, boil sugar raw material case again with boil sugar jar and carry molasses to boil sugar jar and boil sugar.
2. A molasses dilution line according to claim 1, characterized in that: dissolve brilliant machine and include that the crystalline substance case is dissolved to the primary grade, the crystalline substance case is dissolved to the secondary grade, the crystalline substance case is dissolved to the tertiary grade, agitating unit, overflow baffle and hot water supply mouth are dissolved brilliant machine and are separated into the crystalline substance case is dissolved to the primary grade, the crystalline substance case is dissolved to the secondary grade and the crystalline substance case is dissolved to the tertiary grade through two sets of overflow baffles, agitating unit fixes respectively and dissolves brilliant case, the crystalline substance case is dissolved to the secondary grade and the crystalline substance case is dissolved to the primary grade, the hot water supply mouth is total three and is located the top that the crystalline substance case is dissolved to the primary grade, the crystalline substance case is dissolved to the secondary grade and the crystalline substance case is dissolved to the tertiary grade.
3. A molasses dilution line according to claim 2, characterized in that: the overflow partition plates comprise an upper partition plate and a lower partition plate, the upper partition plate is fixed to the top of the crystal dissolving machine, the lower partition plate is fixed to the bottom of the crystal dissolving machine, and the upper partition plate and the lower partition plate are staggered to enable molasses to pass through a space between the upper partition plate and the lower partition plate.
4. A molasses dilution line according to claim 3, characterized in that: the height of the upper partition board is greater than that of the lower partition board, and the lower edge of the upper partition board is lower than that of the lower partition board.
5. A molasses dilution line according to claim 2, characterized in that: the stirring device comprises a speed reduction stirrer and a stirring barrel, wherein the speed reduction stirrer is positioned at the outer side of the tops of the first-stage crystal dissolving box, the second-stage crystal dissolving box and the third-stage crystal dissolving box, and the stirring barrel is fixed below the speed reduction stirrer and positioned in the crystal dissolving machine.
6. A molasses dilution line according to claim 5, characterized in that: stirring blades are arranged in the stirring barrel, and the wall of the stirring barrel is a perforated net.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920804811.5U CN210340945U (en) | 2019-05-31 | 2019-05-31 | Novel molasses dilution production line |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920804811.5U CN210340945U (en) | 2019-05-31 | 2019-05-31 | Novel molasses dilution production line |
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| Publication Number | Publication Date |
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| CN210340945U true CN210340945U (en) | 2020-04-17 |
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| CN201920804811.5U Active CN210340945U (en) | 2019-05-31 | 2019-05-31 | Novel molasses dilution production line |
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