CN115301142A - Online dilution system is washed to first nail - Google Patents
Online dilution system is washed to first nail Download PDFInfo
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- CN115301142A CN115301142A CN202210902887.8A CN202210902887A CN115301142A CN 115301142 A CN115301142 A CN 115301142A CN 202210902887 A CN202210902887 A CN 202210902887A CN 115301142 A CN115301142 A CN 115301142A
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- Prior art keywords
- sugar
- machine
- confluence channel
- passageway
- converges
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- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Links
- 238000010790 dilution Methods 0.000 title claims abstract description 18
- 239000012895 dilution Substances 0.000 title claims abstract description 18
- 235000012907 honey Nutrition 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims abstract description 23
- 239000013078 crystal Substances 0.000 claims abstract description 16
- 238000005406 washing Methods 0.000 claims abstract description 12
- 239000002994 raw material Substances 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims description 21
- 238000009835 boiling Methods 0.000 abstract description 14
- 239000004576 sand Substances 0.000 abstract description 14
- 239000002699 waste material Substances 0.000 abstract description 8
- 239000002245 particle Substances 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000000034 method Methods 0.000 description 16
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 14
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 14
- 235000013379 molasses Nutrition 0.000 description 13
- 230000008569 process Effects 0.000 description 13
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 8
- 239000008103 glucose Substances 0.000 description 8
- 230000009471 action Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000000855 fermentation Methods 0.000 description 2
- 230000004151 fermentation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- MIDXCONKKJTLDX-UHFFFAOYSA-N 3,5-dimethylcyclopentane-1,2-dione Chemical compound CC1CC(C)C(=O)C1=O MIDXCONKKJTLDX-UHFFFAOYSA-N 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000003321 amplification Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 235000013736 caramel Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 238000003113 dilution method Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 125000002791 glucosyl group Chemical group C1([C@H](O)[C@@H](O)[C@H](O)[C@H](O1)CO)* 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- LPUQAYUQRXPFSQ-DFWYDOINSA-M monosodium L-glutamate Chemical compound [Na+].[O-]C(=O)[C@@H](N)CCC(O)=O LPUQAYUQRXPFSQ-DFWYDOINSA-M 0.000 description 1
- 235000013923 monosodium glutamate Nutrition 0.000 description 1
- 239000004223 monosodium glutamate Substances 0.000 description 1
- 238000003199 nucleic acid amplification method Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/83—Mixing plants specially adapted for mixing in combination with disintegrating operations
- B01F33/831—Devices with consecutive working receptacles, e.g. with two intermeshing tools in one of the receptacles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
- B01F33/836—Mixing plants; Combinations of mixers combining mixing with other treatments
- B01F33/8361—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating
- B01F33/83612—Mixing plants; Combinations of mixers combining mixing with other treatments with disintegrating by crushing or breaking
Abstract
The invention discloses an online dilution system for first washing, which belongs to the technical field of sugar manufacturing industry and comprises a first sugar honey separator, a second sugar honey separator and a crystal dissolving machine, wherein the crystal dissolving machine is sequentially communicated with a raw box, a sugar boiling raw material box and a sugar boiling tank along a material supply direction, a confluence device is arranged at the junction of the first sugar honey separator, the second sugar honey separator and the crystal dissolving machine, the confluence device comprises an aggregate funnel, a first sugar confluence channel and a second sugar confluence channel are arranged on the surface of the aggregate funnel, the first sugar confluence channel is communicated with the first sugar honey separator, the second sugar confluence channel is communicated with the second sugar honey separator, the first sugar confluence channel and the second sugar confluence channel are intersected in the crystal dissolving machine, and the diameters of the first sugar confluence channel and the second sugar confluence channel are different. The macromolecular particles in the aggregate funnel are screened to remove partial waste sand.
Description
Technical Field
The invention belongs to the technical field of sugar industry, and particularly relates to an online first-washing dilution system.
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 sugar boiling, so that energy consumption and local overheating caramel of molasses are increased 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 cannot 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.
In order to overcome the defects, the prior art CN110205410A discloses a novel molasses diluting process, which comprises the following steps: 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 multi-stage dilution and crystal dissolving, the molasses enters an original A/first washing/original B box and is cleaned, the molasses in the original A/first washing/original B box is pumped into a sugar boiling raw material box through a conveying pump, and then the molasses is sent into a sugar boiling tank for sugar boiling.
Although the scheme has partial removing effect on the waste sand, the manual operation of the first-washing dilution process in the sugar making link has high randomness, the dilution basically does not meet the requirements of the brix and the temperature, the effect is poor, sand grains are carried in partial materials, and the sand grains greatly influence the boiling quality of the sugar mass. Because the dilution of the washing honey does not reach the standard, too much sand is carried, the boiling time is prolonged, the steam consumption is increased, and the requirements of energy conservation and consumption reduction can not be met.
Disclosure of Invention
In order to solve the problems, the invention aims to provide a first-washing online dilution system to reduce the granularity of waste sand and remove part of the waste sand.
In order to achieve the purpose, the technical scheme of the invention is as follows: the utility model provides an online dilution system is washed to first, includes that the first sugar divides honey machine, the second sugar divides honey machine and dissolves brilliant machine, dissolves brilliant machine and has communicate in proper order along material supply direction and have former case, boil the former case of sugar and boil the sugar jar, the first sugar divides honey machine, the second sugar divides honey machine and dissolves the intersection of brilliant machine and be equipped with the device that converges, the device that converges includes the funnel that gathers materials, and the surface of funnel that gathers materials has first sugar to converge passageway and second sugar to converge the passageway, and wherein first sugar converges the passageway and communicates in first sugar divides honey machine, and second sugar converges the passageway and communicates in second sugar divides honey machine, and first sugar converges passageway and second sugar to converge the passageway and intersect in dissolving brilliant machine, and first sugar converges passageway and second sugar and converge the diameter of passageway and is different.
Has the advantages that: 1. compared with the prior art, the technical scheme includes that the methyl sugar honey separator and the ethyl sugar honey separator are mixed into the crystal dissolving machine, the methyl sugar and the ethyl sugar are respectively and gradually collected into the collecting funnel along the methyl sugar collecting channel and the ethyl sugar collecting channel in the mixing process, the diameters of the channels through which the methyl sugar and the ethyl sugar pass are different in the collecting process, so that the flowing rotating speeds of the methyl sugar and the ethyl sugar are different, the treating space is formed among substances flowing at different heights, when the substances are located in the treating space, the directions are the same in the steering process and have the rotating speed difference, the airflow in the treating space is in an instantaneous weightlessness state, the macromolecular particulate matters in the collecting funnel are screened at the moment, and part of waste sand is removed.
2. Compared with the prior art of zero-gravity treatment of waste sand, in the technical scheme, because two fluids with different rotating speeds exist, sand particles in the treatment space slide on the surface of the liquid to form a shear surface, and the molecules in the shapes of clusters or particles slide and collide with each other and are worn and consumed mutually.
Furthermore, the methyl sugar confluence channel and the ethyl sugar confluence channel are arranged along the inner wall of the collecting funnel in a spiral curve mode, the methyl sugar confluence channel and the ethyl sugar confluence channel are independent of each other, the superposition positions of the middle positions of the methyl sugar confluence channel and the ethyl sugar confluence channel and the collecting funnel are provided with a space, and the length of the space is equal to twice of the interval between the methyl sugar confluence channel and the ethyl sugar confluence channel.
Has the advantages that: the technical scheme is provided with the space, and when materials located in the space upper flow channel and the space lower flow channel flow mutually, the space between the upper flow channel and the lower flow channel forms a blank space under the air flow pressure, and due to the effect of inertia, particles in the materials are scattered in the space, so that the materials at the space are convenient to sink.
Further, a stirring assembly is arranged in the crystal dissolving machine, the stirring assembly comprises a stirring shaft and a differential motor, the stirring shaft comprises an upper hammer part and a lower carrier, a connecting rod shaped like a Chinese character '\21274' is connected between the upper hammer part and the lower carrier, the differential motor drives the stirring shaft to reciprocate along the vertical distance, and the differential motor drives the stirring shaft to rotate circumferentially.
Further, the connecting rod includes first horizontal pole, vertical pole and second horizontal pole, and first horizontal pole is connected in last hammer block, and the second horizontal pole is connected in the microscope unloading platform, goes up and is connected vertical pole between hammer block and the download platform, and is articulated between vertical pole and the second horizontal pole.
Furthermore, the lower carrying platform and the upper hammer part are oppositely arranged, and a groove is formed in the surface of the lower carrying platform.
Further, go up fixed connection between hammer portion and the connecting rod, and the top dead center of second horizontal pole motion is hammer portion in the contact of second horizontal pole, and the lower dead center of second horizontal pole motion is perpendicular between second horizontal pole and the vertical pole.
After the scheme is adopted, the following beneficial effects are realized: utilize the lower microscope stage to hold back the partial material of stirring in-process, the material of lower microscope stage is hammered to descending last hammer portion this moment, utilizes the pin joint of second horizontal pole to realize the enlargeing of moment in the hammering process.
Drawings
FIG. 1 is a schematic view of the structure of the production line of the present invention.
Fig. 2 is a block diagram of the collection hopper of fig. 1.
FIG. 3 is a schematic diagram of the stirring apparatus.
Detailed Description
The following is further detailed by way of specific embodiments:
reference numerals in the drawings of the specification include: the sugar boiling device comprises a first sugar honey separator 1, a second sugar honey separator 2, a crystal dissolving machine 3, a raw box 4, a sugar boiling raw material box 5, a sugar boiling tank 6, an aggregate funnel 7, a first sugar confluence channel 8, a second sugar confluence channel 9, a space 10, a stirring shaft 11, a differential motor 12, an upper hammer part 13, a lower carrier 14 and a connecting rod 15.
The embodiment is basically as shown in the attached figure 1: the utility model provides an online dilution system is washed to first, includes that the first sugar divides honey machine 1, the second sugar divides honey machine 2 and dissolves brilliant machine 3, dissolves brilliant machine 3 and communicates in proper order along material supply direction has former case 4, boils sugar raw material case 5 and boils sugar jar 6, the first sugar divides honey machine 1, the second sugar divides honey machine 2 and dissolves the intersection of brilliant machine 3 to be equipped with the device that converges, the device that converges includes collection funnel 7, and collection funnel 7's surface has first sugar and converges passageway 8 and second sugar and converge passageway 9, and wherein first sugar converges passageway 8 and communicates in first sugar divide honey machine 1, and second sugar converges passageway 9 and communicates in second sugar honey machine 2, and first sugar converges passageway 8 and second sugar and converge passageway 9 and intersect in dissolving brilliant machine 3, and first sugar converges passageway 8 and second sugar and converge the diameter of passageway 9 and differ.
Referring to fig. 2, the glucose collecting channel 8 and the glucose collecting channel 9 are arranged along the inner wall of the collecting funnel 7 in a spiral curve, the glucose collecting channel 8 and the glucose collecting channel 9 are independent of each other, the overlapping position of the glucose collecting channel 8 and the glucose collecting channel 9 with the collecting funnel 7 at the middle position has a space 10, and the length of the space 10 is equal to twice the interval between the glucose collecting channel 8 and the glucose collecting channel 9
Referring to fig. 3, a stirring assembly is provided in the crystal dissolving machine 3, the stirring assembly includes a stirring shaft 11 and a differential motor 12, the stirring shaft 11 includes an upper hammer portion 13 and a lower table 14, a connecting rod 15 shaped like '21274' is connected between the upper hammer portion 13 and the lower table 14, the connecting rod 15 includes a first cross rod, a vertical rod and a second cross rod, the first cross rod is connected to the upper hammer portion 13, the second cross rod is connected to the lower table 14, the vertical rod is connected between the upper hammer portion 13 and the lower table 14, and the vertical rod is hinged to the second cross rod.
The specific implementation process is as follows: according to the technical scheme, the methyl sugar honey separator 1 and the ethyl sugar honey separator 2 are mixed into the crystal dissolving machine 3, the methyl sugar and the ethyl sugar are respectively converged into the collecting hopper 7 along the methyl sugar converging channel 8 and the ethyl sugar converging channel 9 in the mixing process, the flowing rotating speeds of the methyl sugar and the ethyl sugar are different due to the fact that the diameters of the channels through which the methyl sugar and the ethyl sugar pass are different in the converging process, sand grains in the processing space slide on the liquid surface to form a shearing surface due to the fact that two fluids with different rotating speeds exist, and the molecules in the shapes of lumps or grains slide and collide with each other and are worn and consumed by each other.
Meanwhile, treatment spaces are formed among substances flowing at different heights, when the substances are positioned in the treatment spaces, the airflow in the treatment spaces is in an instantaneous weightless state due to the fact that the directions are the same and the rotation speed difference exists in the steering process, and at the moment, macromolecular particles in the aggregate funnel 7 are screened to remove part of waste sand.
When the material passes through the clearance 10 between the upper runner and the lower runner, and the material in the upper runner and the lower runner at the clearance 10 flows mutually, the middle clearance 10 forms a blank space under the airflow pressure, and the particulate matters in the material are scattered in the clearance 10 under the action of inertia, so that the material at the clearance 10 is settled, and then the material enters the crystal dissolving machine 3.
The materials in the crystal dissolving machine 3 are stirred by the stirring shaft 11, the stirring group utilizes the lower platform 14 to intercept partial materials in the stirring process, the downward upper hammer part 13 hammers the materials of the lower platform 14, the hinge point of the second cross rod is utilized to realize the amplification of the moment in the hammering process, and the brix and the sand discharging degree of the sugar are increased.
It should be noted that, in this document, relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Also, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
The foregoing are embodiments of the present invention and are not intended to limit the scope of the invention to the particular forms set forth in the specification, which are set forth in the claims below, but rather are to be construed as the full breadth and scope of the claims, as defined by the appended claims, as defined in the appended claims, in order to provide a thorough understanding of the present invention. It should be noted that, for those skilled in the art, without departing from the structure of the present invention, several changes and modifications can be made, which should also be regarded as the protection scope of the present invention, and these will not affect the effect of the implementation of the present invention and the practicability of the patent. The scope of the claims of the present application shall be determined by the contents of the claims, and the description of the embodiments and the like in the specification shall be used to explain the contents of the claims.
Claims (6)
1. The utility model provides an online dilution system is washed to first, includes that the first sugar divides honey machine, the second sugar divides honey machine and dissolves brilliant machine, its characterized in that: dissolve brilliant machine and feed through in proper order along the material direction of supply and have former case, boil sugar raw material tank and boil the sugar jar, the intersection that first sugar divides honey machine, second sugar to divide honey machine and dissolve brilliant machine is equipped with the device that converges, the device that converges includes the funnel that gathers materials, and the surface of funnel that gathers materials has first sugar to converge passageway and second sugar and converges the passageway, and wherein first sugar converges the passageway and communicates in first sugar divides honey machine, and second sugar converges the passageway and communicates in second sugar divides honey machine, and first sugar converges passageway and second sugar and converges the passageway and intersect in dissolving the brilliant machine, and first sugar converges the passageway and the diameter that second sugar converged the passageway is different.
2. The on-line nail-washing dilution system according to claim 1, wherein: the first sugar confluence channel and the second sugar confluence channel are arranged along the inner wall of the collecting funnel in a spiral curve mode, the first sugar confluence channel and the second sugar confluence channel are independent of each other, the coincidence positions of the first sugar confluence channel, the second sugar confluence channel and the collecting funnel at the middle positions are provided with space distances, and the length of the space distances is equal to twice of the interval between the first sugar confluence channel and the second sugar confluence channel.
3. An online nail-washing dilution system according to claim 2, characterized in that: the crystal dissolving machine is internally provided with a stirring assembly, the stirring assembly comprises a stirring shaft and a differential motor, the stirring shaft comprises an upper hammer part and a lower carrying platform, and a '21274' -shaped connecting rod is connected between the upper hammer part and the lower carrying platform.
4. An online nail-washing dilution system according to claim 3, characterized in that: the connecting rod comprises a first cross rod, a vertical rod and a second cross rod, the first cross rod is connected to the upper hammer portion, the second cross rod is connected to the lower platform, the vertical rod is connected between the upper hammer portion and the lower platform, and the vertical rod is hinged to the second cross rod.
5. The on-line nail-washing dilution system according to claim 4, wherein: the lower carrying platform and the upper hammer part are oppositely arranged, and a groove is formed in the surface of the lower carrying platform.
6. A nail washing online dilution system according to claim 5, wherein: go up fixed connection between hammer portion and the connecting rod, and the top dead center of second horizontal pole motion is that the second horizontal pole contacts hammer portion on, and the lower dead center of second horizontal pole motion is perpendicular between second horizontal pole and the vertical pole.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210902887.8A CN115301142A (en) | 2022-07-29 | 2022-07-29 | Online dilution system is washed to first nail |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210902887.8A CN115301142A (en) | 2022-07-29 | 2022-07-29 | Online dilution system is washed to first nail |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115301142A true CN115301142A (en) | 2022-11-08 |
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ID=83859493
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210902887.8A Pending CN115301142A (en) | 2022-07-29 | 2022-07-29 | Online dilution system is washed to first nail |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115301142A (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102186570A (en) * | 2008-10-20 | 2011-09-14 | 旭有机材工业株式会社 | Helical fluid mixer and device using helical fluid mixer |
| CN110205410A (en) * | 2019-05-31 | 2019-09-06 | 广西吉然科技有限公司 | A kind of novel molasses dilution technique |
-
2022
- 2022-07-29 CN CN202210902887.8A patent/CN115301142A/en active Pending
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102186570A (en) * | 2008-10-20 | 2011-09-14 | 旭有机材工业株式会社 | Helical fluid mixer and device using helical fluid mixer |
| CN110205410A (en) * | 2019-05-31 | 2019-09-06 | 广西吉然科技有限公司 | A kind of novel molasses dilution technique |
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