CN220793572U - Wet material drying device after inositol crystallization filtration - Google Patents
Wet material drying device after inositol crystallization filtration Download PDFInfo
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- CN220793572U CN220793572U CN202322469326.6U CN202322469326U CN220793572U CN 220793572 U CN220793572 U CN 220793572U CN 202322469326 U CN202322469326 U CN 202322469326U CN 220793572 U CN220793572 U CN 220793572U
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- pipeline
- communicated
- outlet
- wet material
- absorption tower
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- 239000000463 material Substances 0.000 title claims abstract description 53
- CDAISMWEOUEBRE-UHFFFAOYSA-N scyllo-inosotol Natural products OC1C(O)C(O)C(O)C(O)C1O CDAISMWEOUEBRE-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 238000001035 drying Methods 0.000 title claims abstract description 35
- CDAISMWEOUEBRE-GPIVLXJGSA-N inositol Chemical compound O[C@H]1[C@H](O)[C@@H](O)[C@H](O)[C@H](O)[C@@H]1O CDAISMWEOUEBRE-GPIVLXJGSA-N 0.000 title claims abstract description 35
- 229960000367 inositol Drugs 0.000 title claims abstract description 35
- SQUHHTBVTRBESD-UHFFFAOYSA-N Hexa-Ac-myo-Inositol Natural products CC(=O)OC1C(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C(OC(C)=O)C1OC(C)=O SQUHHTBVTRBESD-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000002425 crystallisation Methods 0.000 title claims abstract description 17
- 230000008025 crystallization Effects 0.000 title claims abstract description 17
- 238000001914 filtration Methods 0.000 title claims abstract description 10
- 238000010521 absorption reaction Methods 0.000 claims abstract description 46
- 239000007788 liquid Substances 0.000 claims abstract description 29
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 230000001502 supplementing effect Effects 0.000 claims description 18
- 238000000034 method Methods 0.000 claims description 9
- 238000011084 recovery Methods 0.000 claims description 7
- 239000010865 sewage Substances 0.000 claims description 7
- 230000003139 buffering effect Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 8
- 238000004659 sterilization and disinfection Methods 0.000 abstract description 6
- 230000001954 sterilising effect Effects 0.000 abstract description 5
- 238000007599 discharging Methods 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000005299 abrasion Methods 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011010 flushing procedure Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- IMQLKJBTEOYOSI-GPIVLXJGSA-N Inositol-hexakisphosphate Chemical compound OP(O)(=O)O[C@H]1[C@H](OP(O)(O)=O)[C@@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@H](OP(O)(O)=O)[C@@H]1OP(O)(O)=O IMQLKJBTEOYOSI-GPIVLXJGSA-N 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- IMQLKJBTEOYOSI-UHFFFAOYSA-N Phytic acid Natural products OP(O)(=O)OC1C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C(OP(O)(O)=O)C1OP(O)(O)=O IMQLKJBTEOYOSI-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- CDAISMWEOUEBRE-NIPYSYMMSA-N epi-inositol Chemical compound O[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](O)[C@H]1O CDAISMWEOUEBRE-NIPYSYMMSA-N 0.000 description 1
- 210000003743 erythrocyte Anatomy 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- -1 hydrocarbon derivative of cyclohexane Chemical class 0.000 description 1
- 210000004185 liver Anatomy 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 210000004072 lung Anatomy 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 210000004165 myocardium Anatomy 0.000 description 1
- 238000000643 oven drying Methods 0.000 description 1
- 125000002467 phosphate group Chemical group [H]OP(=O)(O[H])O[*] 0.000 description 1
- 150000003905 phosphatidylinositols Chemical class 0.000 description 1
- 150000003904 phospholipids Chemical class 0.000 description 1
- 229940068041 phytic acid Drugs 0.000 description 1
- CDAISMWEOUEBRE-CDRYSYESSA-N scyllo-inositol Chemical compound O[C@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O CDAISMWEOUEBRE-CDRYSYESSA-N 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
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- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a wet material drying device after inositol crystallization and filtration, which relates to the technical field of post-treatment devices for inositol production, wherein the wet material enters a crusher, the crushed wet material enters a feeding bin, and falls into a chain plate conveying belt from the bottom outlet of the feeding bin and enters a tunnel type microwave dryer, drying and sterilization are realized under the action of the tunnel type microwave dryer, the air generated in the microwave drying process enters an absorption tower from bottom to top under the action of a draught fan, circulating liquid in the absorption tower enters from top to bottom through a circulating pump, firstly, water vapor generated in the microwave drying process is absorbed, secondly, the air generated in the microwave drying process is deodorized, the damage to the atmosphere during the discharge is avoided, the material feeding is not needed, the labor force is greatly saved, the drying efficiency is improved, the drying and sterilization are synchronously carried out, and the production cost is reduced.
Description
Technical Field
The utility model relates to the technical field of post-treatment devices for inositol production, in particular to a wet material drying device after inositol crystallization and filtration.
Background
Inositol can be chemically considered as a polyhydric hydrocarbon derivative of cyclohexane. There are in theory 9 possible isomers, such as myo-inositol, epi-inositol, scyllo-inositol, etc. Almost all organisms contain inositol in either the free or bound state. Inositol hexaphosphate is present as hexaphosphate in nucleated red blood cells of plants and birds. The compounds with fewer phosphate groups than the compounds are equally distributed in plants and animals, and in addition, inositol in free form is mainly present in muscles, hearts, lungs and livers and is a component of phosphatidylinositol of phospholipids.
The material after crystallization and filtration in inositol production needs to be dried, and the drying mode that adopts at present is oven drying, and the productivity is little, inefficiency, and the manual loading and unloading work is complicated, and in order to disinfect the material simultaneously, the stoving temperature that needs keeps more than 150 ℃, dries for about 1 hour, very big improvement manufacturing cost.
Disclosure of Invention
The technical problems to be solved by the utility model are as follows: aiming at the defects in the prior art, the wet material drying device after inositol crystallization and filtration is provided with high efficiency and low production cost.
In order to solve the technical problems, the technical scheme of the utility model is as follows:
the wet material drying device after inositol crystallization and filtration comprises a first vacuum feeding machine communicated with a wet material feeding pipeline, wherein an outlet of the first vacuum feeding machine is communicated with a crusher through a pipeline, an outlet of the crusher is communicated with a second vacuum feeding machine through a pipeline, a bottom outlet of the second vacuum feeding machine is communicated with a feeding bin, a chain plate conveying belt is arranged at the lower part of the outlet of the feeding bin, and a tunnel type microwave dryer is arranged at the outer side of the chain plate conveying belt;
The top gas vent of tunnel type microwave dryer has the draught fan through the pipeline intercommunication, the export of draught fan is through the lower part entry of pipeline intercommunication to the absorption tower, there is the circulating pump bottom export of absorption tower through the pipeline intercommunication, the export of circulating pump is through the pipeline intercommunication extremely the upper portion entry of absorption tower, the top export intercommunication of absorption tower has tail gas treatment pipeline.
As an improved technical scheme, the outlet of the crusher is communicated with a third vacuum feeding machine through a pipeline, the outlet of the third vacuum feeding machine is communicated with a vibrating screen through a pipeline, and an undersize buffer bin of the vibrating screen is communicated to the feeding bin through a pipeline.
As an improved technical scheme, the oversize material buffer bin of the vibrating screen is communicated to the first vacuum feeding machine through a pipeline.
As an improved technical scheme, an outlet of the feeding bin is communicated with a distributing device through a pipeline, an auger blade is arranged in the distributing device, and a chain plate conveying belt is arranged at the lower part of the outlet of the distributing device.
As an improved technical scheme, a process water supplementing pipeline is connected to an inlet at the upper part of the absorption tower, a water supplementing valve is arranged on the process water supplementing pipeline, a liquid level sensor is arranged on the absorption tower, and the water supplementing valve and the liquid level sensor are interlocked to a control system.
As an improved technical scheme, an outlet of the circulating pump is communicated with a circulating liquid recovery pipeline.
As the preferable technical scheme, the bottom outlet of the absorption tower is communicated with a sewage treatment pipeline.
As the preferable technical scheme, the crusher is a hammer crusher, and the first vacuum feeder and the bottom outlet of the crusher are both provided with conical buffer bins.
Due to the adoption of the technical scheme, the utility model has the beneficial effects that:
The utility model relates to a wet material drying device after inositol crystallization and filtration, which comprises a first vacuum feeding machine communicated with a wet material feeding pipeline, wherein an outlet of the first vacuum feeding machine is communicated with a crusher through a pipeline, an outlet of the crusher is communicated with a second vacuum feeding machine through a pipeline, a bottom outlet of the second vacuum feeding machine is communicated with a feeding bin, a chain plate conveying belt is arranged at the lower part of the outlet of the feeding bin, and a tunnel type microwave dryer is arranged at the outer side of the chain plate conveying belt; the top gas vent of tunnel type microwave dryer has the draught fan through the pipeline intercommunication, the export of draught fan is through the lower part entry of pipeline intercommunication to the absorption tower, there is the circulating pump bottom export of absorption tower through the pipeline intercommunication, the export of circulating pump is through the pipeline intercommunication extremely the upper portion entry of absorption tower, the top export intercommunication of absorption tower has tail gas treatment pipeline. The crystallized and filtered inositol wet material enters the crusher under the vacuum action of the first vacuum feeder, the crushed inositol wet material enters the feeding bin under the action of the second vacuum feeder, and falls into the chain plate conveyor belt from the bottom outlet of the feeding bin, moves forward under the action of the chain plate conveyor belt and enters the tunnel type microwave dryer, drying and sterilization are realized under the action of the tunnel type microwave dryer, the drying and sterilization are carried out, the tail end of the chain plate conveyor belt falls down and is packaged, the gas generated in the microwave drying process enters the absorption tower from bottom to top under the action of the induced draft fan, the circulating liquid in the absorption tower enters from the upper part of the absorption tower from top to bottom through the circulating pump, the absorption liquid firstly absorbs vapor generated in the microwave drying process, secondly deodorizes the gas generated in the microwave drying process, the damage to the atmosphere is avoided during the discharging, the material feeding is not needed, the labor force is greatly saved, the drying and sterilization are carried out synchronously, and the production cost is reduced.
The outlet of the crusher is communicated with a third vacuum feeding machine through a pipeline, the outlet of the third vacuum feeding machine is communicated with a vibrating screen through a pipeline, and an undersize buffer bin of the vibrating screen is communicated to the feeding bin through a pipeline. And an oversize material buffer bin of the vibrating screen is communicated to the first vacuum feeding machine through a pipeline. The crushed inositol wet material enters a vibrating screen through a third vacuum feeding machine, different-size separation is realized under the action of the vibrating screen, the small-size inositol wet material enters an undersize buffer bin and enters a feeding bin under the action of a second vacuum feeding machine, the large-size inositol wet material enters an oversize buffer bin, and enters a crusher again under the action of a first vacuum feeding machine for crushing treatment, and finally, the inositol product with uniform size is obtained.
The outlet of the feeding bin is communicated with a distributing device through a pipeline, auger blades are arranged in the distributing device, and the chain plate conveying belt is arranged at the lower part of the outlet of the distributing device. The materials in the feeding bin reach the distributor and continuously fall onto the chain plate conveying belt under the action of the auger blade, and the auger blade reduces the possibility of blocking the materials in the distributor.
The upper inlet of the absorption tower is connected with a process water supplementing pipeline, a water supplementing valve is arranged on the process water supplementing pipeline, the absorption tower is provided with a liquid level sensor, and the water supplementing valve and the liquid level sensor are interlocked to a control system. The control system controls the opening and closing of the water supplementing valve according to the numerical value of the liquid level sensor, so as to supplement water for the absorption tower.
And the outlet of the circulating pump is communicated with a circulating liquid recovery pipeline. The absorption liquid in the absorption tower is reused through the circulating liquid recovery pipeline, so that the cost is saved, and meanwhile, the waste is avoided.
The bottom outlet of the absorption tower is communicated with a sewage treatment pipeline, so that waste liquid and flushing liquid in the absorption tower can be conveniently collected through the sewage treatment pipeline, and the treatment is convenient.
The crusher is a hammer crusher, and the first vacuum feeder and the bottom outlet of the crusher are both provided with conical buffering bins. Impact resistance and abrasion resistance of the hammer crusher are high, crushing effect is good, materials are temporarily stored through the buffer bin, and meanwhile, discharging of materials in the buffer bin which is arranged in a tapered mode is smooth.
Drawings
The utility model will be further described with reference to the drawings and examples.
FIG. 1 is a schematic diagram of an embodiment of the present utility model;
Wherein: 1. a wet material feed pipe; 2. a first vacuum feeder; 3. a crusher; 4. a second vacuum feeder; 5. a feeding bin; 6. a link plate conveyor belt; 7. a tunnel microwave dryer; 8. an induced draft fan; 9. an absorption tower; 10. a circulation pump; 11. a tail gas treatment pipeline; 12. a third vacuum feeder; 13. a vibrating screen; 14. a screen lower material buffer bin; 15. a screen material buffer bin; 16. a distributing device; 17. auger blades; 18. a process water replenishing pipeline; 19. a water supplementing valve; 20. a liquid level sensor; 21. a circulating liquid recovery pipeline; 22. a sewage treatment pipeline; 23. and (5) buffering the bin.
Detailed Description
The utility model is further illustrated in the following, in conjunction with the accompanying drawings and examples.
As shown in fig. 1, the wet material drying device after inositol crystallization and filtration comprises a first vacuum feeder 2 communicated with a wet material feeding pipeline 1, wherein an outlet of the first vacuum feeder 2 is communicated with a crusher 3 through a pipeline, an outlet of the crusher 3 is communicated with a second vacuum feeder 4 through a pipeline, a bottom outlet of the second vacuum feeder 4 is communicated with a feeding bin 5, a chain plate conveying belt 6 is arranged at the lower part of an outlet of the feeding bin 5, and a tunnel type microwave dryer 7 is arranged at the outer side of the chain plate conveying belt 6; the top gas vent of tunnel microwave dryer 7 has draught fan 8 through the pipeline intercommunication, the export of draught fan 8 is through the lower part entry of pipeline intercommunication to absorption tower 9, the bottom export of absorption tower 9 has circulating pump 10 through the pipeline intercommunication, the export of circulating pump 10 is through the pipeline intercommunication to the upper portion entry of absorption tower 9, the top export intercommunication of absorption tower 9 has tail gas treatment pipeline 11. The crystallized and filtered inositol wet material enters the crusher 3 under the vacuum action of the first vacuum feeder 2, the crushed inositol wet material enters the feeding bin 5 under the action of the second vacuum feeder 4, and falls into the chain plate conveying belt 6 from the bottom outlet of the feeding bin 5, and moves forward under the action of the chain plate conveying belt 6 and enters the tunnel microwave dryer 7, drying and disinfection are realized under the action of the tunnel microwave dryer 7, and the materials fall from the tail end of the chain plate conveying belt 6 and are packaged, the gas generated in the microwave drying process enters the absorption tower 9 from bottom to top under the action of the induced draft fan 8, the circulating liquid in the absorption tower 9 enters from top to bottom to contact with the gas generated in the microwave drying process in a countercurrent manner through the circulating pump 10, the absorption liquid firstly absorbs the vapor generated in the microwave drying process, secondly deodorizes the gas generated in the microwave drying process, so that the air is prevented from being destroyed during the discharging, the materials do not need to be fed manually, the labor efficiency is improved, the drying and the production cost is reduced.
The outlet of the crusher 3 is communicated with a third vacuum feeder 12 through a pipeline, the outlet of the third vacuum feeder 12 is communicated with a vibrating screen 13 through a pipeline, and an undersize buffer bin 14 of the vibrating screen 13 is communicated to the feeding bin 5 through a pipeline. The oversize material buffer bin 15 of the vibrating screen 13 is communicated to the first vacuum feeder 2 through a pipeline. The crushed inositol wet material enters a vibrating screen 13 through a third vacuum feeder 12, different-size separation is realized under the action of the vibrating screen 13, the small-size inositol wet material enters an undersize buffer bin 14 and enters a feeding bin 5 under the action of a second vacuum feeder 4, the large-size inositol wet material enters an oversize buffer bin 15, and enters a crusher 3 again under the action of a first vacuum feeder 2 for crushing treatment, and finally, the inositol product with uniform size is obtained.
The outlet of the feeding bin 5 is communicated with a distributor 16 through a pipeline, an auger blade 17 is arranged in the distributor 16, and a chain plate conveying belt 6 is arranged at the lower part of the outlet of the distributor 16. The materials in the feeding bin 5 reach the distributor 16 and continuously fall onto the chain plate conveying belt 6 under the action of the auger blade 17, and the auger blade 17 reduces the possibility of blocking the materials in the distributor 16.
The upper inlet of the absorption tower 9 is connected with a process water supplementing pipeline 18, the process water supplementing pipeline 18 is provided with a water supplementing valve 19, the absorption tower 9 is provided with a liquid level sensor 20, and the water supplementing valve 19 and the liquid level sensor 20 are interlocked to a control system. The control system controls the opening and closing of the water replenishment valve 19 based on the numerical value of the liquid level sensor 20, thereby replenishing the water to the absorption tower 9.
The outlet of the circulating pump 10 is communicated with a circulating liquid recovery pipeline 21. The absorption liquid in the absorption tower 9 is reused through the circulating liquid recovery pipeline 21, so that the cost is saved, and the waste is avoided.
The bottom outlet of the absorption tower 9 is communicated with a sewage treatment pipeline 22, so that waste liquid and flushing liquid in the absorption tower 9 can be conveniently collected through the sewage treatment pipeline 22, and the treatment is convenient.
The crusher 3 is a hammer crusher, and the first vacuum feeder 2 and the bottom outlet of the crusher 3 are both provided with conical buffer bins 23. The hammer stone crusher 3 has strong impact resistance and abrasion resistance, good crushing effect, temporary storage of materials is realized through the buffer bin 23, and meanwhile, the discharging of the materials of the buffer bin 23 which is arranged in a tapered manner is smooth.
It is to be understood that these examples are illustrative of the present utility model and are not intended to limit the scope of the present utility model. Furthermore, it should be understood that various changes and modifications can be made by one skilled in the art after reading the teachings of the present utility model, and such equivalents are intended to fall within the scope of the utility model as defined in the appended claims.
Claims (8)
1. The utility model provides a wet material drying device after inositol crystallization filters which characterized in that: the device comprises a first vacuum feeder communicated with a wet material feeding pipeline, wherein an outlet of the first vacuum feeder is communicated with a crusher through a pipeline, an outlet of the crusher is communicated with a second vacuum feeder through a pipeline, a bottom outlet of the second vacuum feeder is communicated with a feeding bin, a chain plate conveyer belt is arranged at the lower part of the outlet of the feeding bin, and a tunnel type microwave dryer is arranged at the outer side of the chain plate conveyer belt;
The top gas vent of tunnel type microwave dryer has the draught fan through the pipeline intercommunication, the export of draught fan is through the lower part entry of pipeline intercommunication to the absorption tower, there is the circulating pump bottom export of absorption tower through the pipeline intercommunication, the export of circulating pump is through the pipeline intercommunication extremely the upper portion entry of absorption tower, the top export intercommunication of absorption tower has tail gas treatment pipeline.
2. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: the outlet of the crusher is communicated with a third vacuum feeding machine through a pipeline, the outlet of the third vacuum feeding machine is communicated with a vibrating screen through a pipeline, and an undersize buffer bin of the vibrating screen is communicated to the feeding bin through a pipeline.
3. A wet material drying device after inositol crystallization filtration as claimed in claim 2, wherein: and an oversize material buffer bin of the vibrating screen is communicated to the first vacuum feeding machine through a pipeline.
4. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: the outlet of the feeding bin is communicated with a distributing device through a pipeline, auger blades are arranged in the distributing device, and the chain plate conveying belt is arranged at the lower part of the outlet of the distributing device.
5. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: the upper inlet of the absorption tower is connected with a process water supplementing pipeline, a water supplementing valve is arranged on the process water supplementing pipeline, the absorption tower is provided with a liquid level sensor, and the water supplementing valve and the liquid level sensor are interlocked to a control system.
6. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: and the outlet of the circulating pump is communicated with a circulating liquid recovery pipeline.
7. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: the bottom outlet of the absorption tower is communicated with a sewage treatment pipeline.
8. The inositol crystallization filtered wet material drying device as claimed in claim 1, wherein: the crusher is a hammer crusher, and the first vacuum feeder and the bottom outlet of the crusher are both provided with conical buffering bins.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322469326.6U CN220793572U (en) | 2023-09-12 | 2023-09-12 | Wet material drying device after inositol crystallization filtration |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322469326.6U CN220793572U (en) | 2023-09-12 | 2023-09-12 | Wet material drying device after inositol crystallization filtration |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220793572U true CN220793572U (en) | 2024-04-16 |
Family
ID=90636010
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322469326.6U Active CN220793572U (en) | 2023-09-12 | 2023-09-12 | Wet material drying device after inositol crystallization filtration |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220793572U (en) |
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2023
- 2023-09-12 CN CN202322469326.6U patent/CN220793572U/en active Active
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