A kind of first sugar honey conveying system
By adding an upper suspension centrifuge and replacing a three-piece balanced vibration conveyor, the existing acetic sugar honey machine has been solved, and efficient material processing and improved raw sugar quality have been achieved.
Patent Information
- Application Number
- CN202421520853.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-06-28
- Publication Date
- 2025-04-01
- Estimated Expiration
- 2034-06-28
AI Technical Summary
The existing seven sugar-based honey machines have insufficient processing volume, which leads to the need to adjust the primary color value index, increase the amount of water fetching and reduce the high-speed separation time to meet production needs. At the same time, the processing capacity of the 2# vibration conveyor is also relatively small, resulting in an increase in the labor intensity of employees.
An upper suspension centrifuge was added as a sugar honey machine and replaced with a three-piece balanced vibration conveyor, which optimized the material conveying system and improved the processing capacity and sugar production rate.
It has achieved a processing capacity of 18,000t/d, reduced the labor intensity of employees, improved the quality of raw sugar and sugar production rate, stable equipment operation, low failure rate and low maintenance cost.
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Figure CN222699353U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the field of sugar making equipment, in particular to a sugar honey conveying system. Background Art
[0002] The raw sugar workshop currently has 7 Class A sugar honey extractors (C52MT5948 fully automatic intermittent centrifuges). Calculated based on a production capacity of 17,500 tons / day and a sugar yield of 13.8%, it produces approximately 2,415 tons of raw sugar per day (the maximum daily sugar yield in the 2019 / 20 crushing season was 2,263 tons, the maximum daily sugar yield in the 2020 / 21 crushing season was 2,236 tons, the maximum daily sugar yield in the 2021 / 22 crushing season was 2,403 tons, and the maximum daily sugar yield in the 2022 / 23 crushing season was 2,299 tons), and each shift produces approximately 828 tons of raw sugar. In previous years (the highest sugar production in the 2021 / 22 crushing season was 827 tons, and the highest sugar production in the 2022 / 23 crushing season was 831 tons), the highest raw sugar production in the shift was 831 tons (the raw sugar color index was adjusted to 1200IU, and the raw sugar was not screened through and there was honey), but it could only be maintained for one shift, and the screening process required increasing the amount of water pumped and reducing the high-speed separation time, which ultimately led to an increase in the moisture entering the drum dryer and increased the load of the drum dryer; after the amount of water pumped increased, the time for the sugar particles to be washed by hot water was prolonged, and the sugar was brought into the molasses, which invisibly increased the amount of material processing in the later stage and caused the high-purity material to move backward. The original A sugar system can no longer meet the actual production capacity requirements.
[0003] There are 2 vibrating conveyors in the raw sugar workshop. The 1# vibrating conveyor conveys materials from 3 A-sugar machines, and the 2# vibrating conveyor conveys materials from 4 A-sugar machines. After the A-sugar honey separator reduces the time of high-speed honey separation, the moisture, color value and viscosity of the raw sugar have increased, resulting in the 2# vibrating conveyor often requiring employees to shovel sugar on the vibrating screen surface to speed up material transportation, which invisibly increases the labor intensity of employees. The existing 2# vibrating conveyor has a small processing capacity.
[0004] Because the processing capacity of the existing 7 A-sugar machines is relatively small, it is necessary to adjust the original color value index, increase the amount of water pumped, and reduce the high-speed separation time to meet the material processing needs; the sugar transport capacity of the 2# vibrating conveyor is relatively small, which is no longer in line with the company's production capacity and cannot meet production needs. Improvements are needed to add a new A-sugar honey separator and replace a vibrating conveyor to reduce the amount of water pumped during the screening process of the A-sugar honey separator and improve the sugar yield and raw sugar quality. Utility Model Content
[0005] The utility model aims to provide a sugar honey conveying system to solve the technical problems mentioned in the background technology.
[0006] In order to achieve the above purpose, the technical solution adopted by the utility model is as follows:
[0007] A sugar honey separation and conveying system comprises a sugar paste distribution trough, a crystallizer, a sugar honey separation machine, a vibrating conveyor, a drum dryer and a raw sugar tank, wherein the bottom discharge port of the crystallizer is connected to the feed port of the sugar paste distribution trough, the top feed port of the sugar honey separation machine is connected to the discharge port of the sugar paste distribution trough, the bottom discharge port of the sugar honey separation machine is connected to the feed port of the vibrating conveyor, the discharge port of the vibrating conveyor is connected to the drum dryer via a first belt conveyor, and the discharge port of the drum dryer is connected to the raw sugar tank.
[0008] Furthermore, six crystal-making machines are provided, and the bottom outlet of each crystal-making machine is connected to the sugar paste distribution tank respectively, and the bottom outlet of the crystal-making machine is provided with a crystal-making machine valve.
[0009] Furthermore, eight first-sugar honey separators are provided, and the top inlet of each first-sugar honey separator is connected to the massecuite distribution tank respectively, and the top inlet of the first-sugar honey separator is provided with a first honey separator valve.
[0010] Furthermore, two vibrating conveyors are provided, each vibrating conveyor is connected to the bottom discharge ports of four first-sugar honey separators, and the bottom discharge ports of the first-sugar honey separators are provided with second honey separator valves.
[0011] Furthermore, the discharge ports of the two vibrating conveyors are respectively connected to the feed port of the first belt conveyor, the discharge port of the first belt conveyor is connected to the first screw conveyor, and the discharge port of the first screw conveyor is connected to the feed port of the drum dryer.
[0012] Furthermore, the discharge port of the drum dryer is connected to a second belt conveyor, and the discharge port of the second belt conveyor is connected to the feed port of the raw sugar tank.
[0013] Furthermore, the discharge port of the first screw conveyor is also connected to a raw sugar scale, a second screw conveyor is arranged below the raw sugar scale, and the discharge port of the second screw conveyor is connected to a sugar paste mixer for preparing sugar paste.
[0014] Furthermore, the sugar paste mixer is connected to an air delivery tank, an air delivery tank valve is arranged on the air delivery tank, and the discharge port of the sugar paste mixer is connected to the sugar paste tank.
[0015] The utility model has the following beneficial effects due to the adoption of the above technical solution:
[0016] 1. The newly added sugar honey separator of the utility model is a top-suspended centrifuge. The white sugar crystals separated by the top-suspended centrifuge have good gloss, low color value and moisture, good product quality, reliable operation and large processing capacity.
[0017] 2. The vibrating conveyor replaced by the utility model is a three-mass balanced vibrating conveyor, which can stably and effectively convey materials, reduce friction between materials, and reduce the formation of sugar powder during the conveying process; the damage to the material shape is very small. Since the material is in a micro-throwing continuous jumping motion in the conveying trough, the material will not be squeezed by external force during the conveying process, so the material shape is damaged very little during the conveying process. It is particularly suitable for the conveying of materials with high requirements on appearance.
[0018] 3. The processing capacity of the conveying system of the utility model can reach 18,000t / d. Employees do not need to shovel sugar onto the belt from the vibrating screen surface of the vibrating conveyor to speed up material transportation, reduce the labor intensity of employees, and reduce the amount of water pumped during the screening process of the sugar honey separator, thereby improving the sugar yield and raw sugar quality. The equipment runs stably, has a low failure rate, and has low maintenance costs. BRIEF DESCRIPTION OF THE DRAWINGS
[0019] Figure 1 It is a schematic diagram of a first sugar honey conveying system of the utility model.
[0020] In the attached drawings, 1-sugar paste dispensing trough, 2-crystallization machine, 21-crystallization machine valve, 3-first sugar honey separator, 31-first honey separator valve, 32-second honey separator valve, 4-vibrating conveyor, 5-drum dryer, 6-sugar paste mixer, 7-first belt conveyor, 8-raw sugar warehouse, 9-first screw conveyor, 10-second belt conveyor, 11-raw sugar scale, 12-second screw conveyor, 13-air delivery tank, 14-sugar paste tank, 15-air delivery tank valve. DETAILED DESCRIPTION
[0021] In order to make the purpose, technical solution and advantages of the utility model more clear, the utility model is further described in detail with reference to the accompanying drawings and preferred embodiments. However, it should be noted that many details listed in the specification are only for the purpose of enabling readers to have a thorough understanding of one or more aspects of the utility model, and these aspects of the utility model can be realized even without these specific details.
[0022] like Figure 1As shown, a type of sugar honey separation and conveying system comprises a massecuite dispensing trough 1, a crystallizer 2, a type sugar honey separation machine 3, a vibrating conveyor 4, a drum dryer 5 and a raw sugar tank 8, wherein the bottom discharge port of the crystallizer 2 is connected to the feed port of the massecuite dispensing trough 1, the top feed port of the type sugar honey separation machine 3 is connected to the discharge port of the massecuite dispensing trough 1, the bottom discharge port of the type sugar honey separation machine 3 is connected to the feed port of the vibrating conveyor 4, the discharge port of the vibrating conveyor 4 is connected to the drum dryer 5 via a first belt conveyor 7, and the discharge port of the drum dryer 5 is connected to the raw sugar tank 8. After the crystallization is completed, the sugar paste enters the sugar paste distribution tank 1 from the bottom discharge port of the crystallization machine 2, and then enters the sugar paste distribution tank 1 from the discharge port to the sugar paste distribution tank 1 for separation, and obtains raw sugar after the separation; the raw sugar enters the vibration conveyor 4 from the bottom discharge port of the sugar paste distribution tank 3 for transportation, and then enters the first belt conveyor 7 from the discharge port of the vibration conveyor 4 for transportation, and enters the drum dryer 5 from the discharge port of the first belt conveyor 7 for drying, and enters the raw sugar tank 8 from the discharge port of the drum dryer 5 after drying. The conveying system of the utility model can reduce the amount of water pumped in the screening process of the sugar paste distribution tank 1, improve the sugar yield and raw sugar quality; the equipment runs stably, has a low failure rate, and low maintenance cost.
[0023] In the embodiment of the utility model, six crystallization machines 2 are provided, and the bottom outlet of each crystallization machine 2 is respectively connected to the sugar paste distribution tank 1, and the bottom outlet of the crystallization machine 2 is provided with a crystallization machine valve 21. After the sugar paste is crystallized in the crystallization machine 2, the crystallization machine valves 21 are respectively opened, and the sugar paste enters the sugar paste distribution tank 1 from the bottom outlet of the crystallization machine 2. After the sugar paste is discharged, the crystallization machine valves 21 are closed.
[0024] In the embodiment of the utility model, eight first-sugar honey separators 3 are provided, and the top inlet of each first-sugar honey separator 3 is connected to the massecuite dispensing tank 1 respectively, and the top inlet of the first-sugar honey separator 3 is provided with a first honey separator valve 31. Among the eight first-sugar honey separators 3, seven are original first-sugar honey separators (C52MT5948 fully automatic intermittent centrifuges), and one is a newly added first-sugar honey separator (top-hanging centrifuge). The white granulated sugar crystals separated by the top-hanging centrifuge have good gloss, low color value and moisture, good product quality, reliable operation, and large processing capacity. Open the first honey separator valve 31, and the massecuite enters the first-sugar honey separator 3 from the discharge port of the massecuite dispensing tank 1 for honey separation.
[0025] In the embodiment of the utility model, two vibrating conveyors 4 are provided, each vibrating conveyor 4 is connected to the bottom discharge ports of four first sugar honey separators 3, and the bottom discharge ports of the first sugar honey separators 3 are provided with second honey separator valves 32. After the massecuite is separated in the first sugar honey separator 3, raw sugar is obtained, and the second honey separator valve 32 is opened, and the raw sugar enters the vibrating conveyor 4 from the bottom discharge port of the first sugar honey separator 3 for transportation. The vibrating conveyor 4 is a three-mass balanced vibrating conveyor, which can stably and effectively transport raw sugar, reduce friction between raw sugars, and reduce the formation of sugar powder during transportation; the damage to the appearance of raw sugar is very small, because the raw sugar is in a micro-throwing continuous jumping motion in the conveying trough, and the raw sugar will not be squeezed by external force during transportation, so the appearance of the raw sugar is very small during transportation, which is particularly suitable for the transportation of materials with high appearance requirements.
[0026] In the embodiment of the utility model, the discharge ports of the two vibrating conveyors 4 are respectively connected to the feed port of the first belt conveyor 7, the discharge port of the first belt conveyor 7 is connected to the first screw conveyor 9, and the discharge port of the first screw conveyor 9 is connected to the feed port of the drum dryer 5. The discharge port of the drum dryer 5 is connected to the second belt conveyor 10, and the discharge port of the second belt conveyor 10 is connected to the feed port of the raw sugar tank 8. The raw sugar enters the first belt conveyor 7 from the discharge port of the vibrating conveyor 4 for transportation, then enters the first screw conveyor 9 from the discharge port of the first belt conveyor 7 for transportation, and then enters the drum dryer 5 from the discharge port of the first screw conveyor 9 for drying; the dried raw sugar is transported to the raw sugar tank 8 by the second belt conveyor 10 for storage.
[0027] In the embodiment of the utility model, the discharge port of the first screw conveyor 9 is also connected to a raw sugar scale 11, a second screw conveyor 12 is arranged below the raw sugar scale 11, and a sugar paste mixer 6 for preparing sugar paste is connected to the discharge port of the second screw conveyor 12. The sugar paste mixer 6 is connected to an air delivery tank 13, an air delivery tank valve 15 is arranged on the air delivery tank 13, and a sugar paste tank 14 is connected to the discharge port of the sugar paste mixer 6. If sugar paste needs to be prepared, the raw sugar enters the raw sugar scale 11 from the discharge port of the first screw conveyor 9 for weighing, and then falls from the raw sugar scale 11 into the second screw conveyor 12, and is transported to the sugar paste mixer 6 by the second screw conveyor 12 for mixing to obtain sugar paste, and then enters the sugar paste tank 14 for storage.
[0028] How it works
[0029] After the crystallization is completed, the sugar paste enters the sugar paste distribution tank 1 from the bottom discharge port of the crystallization machine 2, and then enters the first sugar honey separator 3 from the discharge port of the sugar paste distribution tank 1 for honey separation. After the honey separation is completed, raw sugar is obtained. The raw sugar enters the vibration conveyor 4 from the bottom discharge port of the first sugar honey separator 3, and is transported to the first belt conveyor 7 by the vibration conveyor 4; it is transported from the first belt conveyor 7 to the drum dryer 5 for drying. After the drying is completed, the raw sugar enters the raw sugar tank 8 from the discharge port of the drum dryer 5 for storage; when it is necessary to prepare sugar paste, the raw sugar is transported by the first screw conveyor 9 to the raw sugar scale 11 for weighing, and then falls from the raw sugar scale 11 into the second screw conveyor 12, and is transported by the second screw conveyor 12 to the sugar paste mixer 6 for mixing to obtain sugar paste, and then enters the sugar paste tank 14 for storage.
[0030] The above is only a preferred embodiment of the present invention. It should be pointed out that for ordinary technicians in this technical field, several improvements and modifications can be made without departing from the principle of the present invention. These improvements and modifications should also be regarded as the protection scope of the present invention.
Claims
1. A first sugar honey delivery system, characterized in that: The invention comprises a sugar paste distribution trough (1), a crystallization machine (2), a first sugar honey separator (3), a vibrating conveyor (4), a drum dryer (5) and a raw sugar tank (8), wherein the bottom discharge port of the crystallization machine (2) is connected to the feed port of the sugar paste distribution trough (1), the top feed port of the first sugar honey separator (3) is connected to the discharge port of the sugar paste distribution trough (1), the bottom discharge port of the first sugar honey separator (3) is connected to the feed port of the vibrating conveyor (4), the discharge port of the vibrating conveyor (4) is connected to the drum dryer (5) via a first belt conveyor (7), and the discharge port of the drum dryer (5) is connected to the raw sugar tank (8).
2. A first sugar honey delivery system according to claim 1, characterized in that: Six crystal-assisting machines (2) are provided, and the bottom outlet of each crystal-assisting machine (2) is respectively connected to the massecuite distribution tank (1), and the bottom outlet of the crystal-assisting machine (2) is provided with a crystal-assisting machine valve (21).
3. A first sugar honey delivery system according to claim 1, characterized in that: Eight first-sugar honey separators (3) are provided, and the top inlet of each first-sugar honey separator (3) is connected to the massecuite distribution tank (1) respectively. The top inlet of the first-sugar honey separator (3) is provided with a first honey separator valve (31).
4. A system for conveying methylose molasses according to claim 1, characterized in that: Two vibrating conveyors (4) are provided, and each vibrating conveyor (4) is connected to the bottom discharge ports of four first-sugar honey extractors (3), and the bottom discharge ports of the first-sugar honey extractors (3) are provided with second honey extractor valves (32).
5. A first sugar honey delivery system according to claim 1, characterized in that: The discharge ports of the two vibrating conveyors (4) are respectively connected to the feed port of the first belt conveyor (7), the discharge port of the first belt conveyor (7) is connected to the first screw conveyor (9), and the discharge port of the first screw conveyor (9) is connected to the feed port of the drum dryer (5).
6. A system for conveying methylose molasses according to claim 1, characterized in that: The discharge port of the drum dryer (5) is connected to a second belt conveyor (10), and the discharge port of the second belt conveyor (10) is connected to the feed port of the raw sugar tank (8).
7. A system for conveying methylose molasses according to claim 5, characterized in that: The discharge port of the first screw conveyor (9) is also connected to a raw sugar scale (11), a second screw conveyor (12) is arranged below the raw sugar scale (11), and the discharge port of the second screw conveyor (12) is connected to a sugar paste mixer (6) for preparing sugar paste.
8. A system for conveying methylose molasses according to claim 7, characterized in that: The sugar paste mixer (6) is connected to an air delivery tank (13), an air delivery tank valve (15) is arranged on the air delivery tank (13), and the discharge port of the sugar paste mixer (6) is connected to a sugar paste tank (14).