CN211190084U - Powdery emulsifier granulation device and monoglyceride production line containing same - Google Patents
Powdery emulsifier granulation device and monoglyceride production line containing same Download PDFInfo
- Publication number
- CN211190084U CN211190084U CN201921854631.4U CN201921854631U CN211190084U CN 211190084 U CN211190084 U CN 211190084U CN 201921854631 U CN201921854631 U CN 201921854631U CN 211190084 U CN211190084 U CN 211190084U
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- Prior art keywords
- spray gun
- negative pressure
- vacuum
- pipe
- emulsifier
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- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 13
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 title claims abstract description 12
- 238000005469 granulation Methods 0.000 title claims description 21
- 230000003179 granulation Effects 0.000 title claims description 21
- 239000000463 material Substances 0.000 claims abstract description 83
- 238000011084 recovery Methods 0.000 claims abstract description 35
- 239000007921 spray Substances 0.000 claims abstract description 34
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 238000005507 spraying Methods 0.000 abstract description 5
- 230000001105 regulatory effect Effects 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 239000000194 fatty acid Substances 0.000 description 7
- 238000005086 pumping Methods 0.000 description 7
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 3
- 238000000199 molecular distillation Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000003921 oil Substances 0.000 description 2
- 235000019198 oils Nutrition 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002026 carminative effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 238000010410 dusting Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000004185 ester group Chemical group 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000002778 food additive Substances 0.000 description 1
- 235000013373 food additive Nutrition 0.000 description 1
- 235000015243 ice cream Nutrition 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
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Abstract
The utility model discloses a likepowder emulsifier prilling granulator and contain this likepowder emulsifier prilling granulator's monoglyceride production line, likepowder emulsifier prilling granulator include prilling tower, material conveying system and vacuum negative pressure recovery system, the interior top of prilling tower is equipped with the spray gun, material conveying system is including adjusting temperature jar and conveyer pipe, the bin outlet of adjusting temperature jar passes through the conveyer pipe with the spray gun links to each other, vacuum negative pressure recovery system with the conveyer pipe links to each other, and is used for retrieving the conveyer pipe with remaining material on the spray gun. The utility model discloses a prilling granulator is equipped with vacuum negative pressure recovery system, and this vacuum negative pressure recovery system can retrieve the residual material in spray gun and the conveyer pipe, prevents that the material from being heated for a long time and discolour in the pipeline, can not cause spray gun or delivery pump to block up yet. In addition, the vacuum negative pressure recovery system can also convey the recovered materials back to the temperature regulating tank for next spraying, so that material waste is avoided, and the vacuum negative pressure recovery system is energy-saving and environment-friendly.
Description
Technical Field
The utility model relates to a production facility of likepowder emulsifier especially relates to a likepowder emulsifier prilling granulator and contain this likepowder emulsifier prilling granulator's monoglyceride production line.
Background
The method takes natural vegetable oil as raw material to carry out ester exchange reaction with glycerol to produce fatty acid monoglyceride and diglyceride, which are also called monoglyceride for short. The effective components are purified to more than 90 percent by a molecular distillation technology, which is also called as molecular distillation monoglyceride. Monoglyceride is a surfactant, can be made into special products of various types according to the difference of monoester content, oil source composition and the like, can respectively play roles of emulsifying, foaming, defoaming, resisting starch aging, improving the meltresistance of ice cream, changing the crystallization state of oil and fat and the like, is a food additive with the widest application, is safely used in production and processing in the fields of food, medicine, plastics and the like, and accounts for more than half of the using amount of a market emulsifier.
The production process of the mono-fatty acid glyceride and the di-fatty acid glyceride comprises the following steps: esterification, decoloration and filtration, standing and layering, molecular distillation and spray granulation molding. The mono-fatty acid glyceride and the di-fatty acid glyceride are solid at normal temperature. At present, the spray granulation of the mono-fatty acid glyceride and the di-fatty acid glyceride generally adopts intermittent production, and when a spray gun stops working, materials in a pipeline need to be cleaned immediately so as to avoid the phenomenon that the materials are heated for a long time in the pipeline to cause the color to become dark. The mode that prior art generally adopted compressed air to sweep the pipeline clears away remaining material in the pipeline, however, because the height of dusting tower is about 20 meters, the back sweeps, and the interior residual material of pipeline can slowly flow to the pipeline bottom on the one hand, and then flows to the front end of delivery pump, and the material cooling solidifies the back, can cause the delivery pump to block up, and on the other hand, the residual material in the pipeline can slowly flow to the spray gun mouth, and the condensation solidifies the back, can cause the spray gun to block up. In addition, the material particles blown by the compressed air are coarse, the middle of the material particles is hollow, the color of the material particles is pale, and the production requirements of products cannot be met.
SUMMERY OF THE UTILITY MODEL
In order to solve the defects and deficiencies existing in the prior art, the utility model aims to provide a powdery emulsifier granulation device and a monoglyceride production line containing the same. When the spray gun stops working, the vacuum negative pressure recovery system of the granulating device can suck and recycle the materials remained in the pipeline or the spray gun, so that the problem of material residue is effectively solved, and a delivery pump or the spray gun cannot be blocked.
For realizing the purpose, the utility model discloses a technical scheme do:
the utility model provides a likepowder emulsifier prilling granulator, its includes prilling tower, material conveying system and vacuum negative pressure recovery system, the interior top of prilling tower is equipped with the spray gun, material conveying system is including adjusting temperature jar and conveyer pipe, the bin outlet of adjusting temperature jar passes through the conveyer pipe with the spray gun links to each other, vacuum negative pressure recovery system with the conveyer pipe links to each other, and is used for retrieving the conveyer pipe with remaining material on the spray gun.
During granulation, the temperature adjusting tank sends the materials into the spray gun through the conveying pipe, and the materials are sprayed out by the spray gun for granulation.
Preferably, the vacuum negative pressure recovery system comprises a material receiving tank, a vacuum pump and a recovery pipe, wherein the material receiving tank is connected with the vacuum pump, and the material receiving tank is further connected with the conveying pipe through the recovery pipe. When the spray gun stops spraying materials, vacuum negative pressure is formed in the material receiving tank through the vacuum pump, and then materials remained in the conveying pipe and the spray gun are sucked into the material receiving tank through the recovery pipe.
Preferably, a vacuum butterfly valve is arranged on a pipeline connecting the vacuum pump and the material receiving tank. Therefore, the opening and closing of the pipeline of the vacuum pump connected with the material receiving tank can be controlled.
Preferably, the vacuum pump is a water ring vacuum pump. The water ring vacuum pump has the advantages of uniform air suction, stable and reliable work, simple operation and convenient maintenance. Moreover, the water ring vacuum pump relies on the change of pump chamber volume to realize breathing in, compressing and carminative, and compressed gas's temperature is low, is used for the utility model discloses in, the security is high.
Preferably, the recovery pipe is provided with a material pumping valve. Thus, the opening and closing of the recovery pipe can be controlled.
Preferably, the material receiving tank is also provided with an emptying valve and a vacuum meter for displaying the vacuum degree in the tank.
Preferably, the bottom of the material receiving tank is also provided with a discharge port connected with the temperature adjusting tank. So, be sucked extremely material accessible in the receipts material jar the bin outlet of receiving the material jar is retrieved extremely in the jar adjusts the temperature, recycles, has avoided the waste of material.
Preferably, the conveying pipe is provided with a conveying pump connected with a discharge port of the temperature adjusting tank.
Preferably, the conveying pipe is provided with a first discharge valve and a second discharge valve which are positioned at two sides of the conveying pump. Therefore, the opening and closing of the pipelines at the two ends of the conveying pump can be flexibly controlled.
When the spray gun stops spraying the materials, the vacuum pump is started, and when the vacuum meter on the material receiving tank shows that the vacuum degree reaches 0.08MPa, the material pumping valve on the recovery pipe is started to pump back the residual materials in the spray gun and the conveying pipe. And after all the materials are pumped back, closing the material pumping valve and the vacuum pump, then opening the emptying valve, and when the vacuum meter displays 0, opening the discharge port of the material receiving tank and discharging the materials into the temperature adjusting tank. And after all the materials in the material receiving tank are discharged into the temperature regulating tank, closing a discharge port and an emptying valve of the material receiving tank.
The utility model also provides a monoglyceride production line, it includes likepowder emulsifier prilling granulator.
Compared with the prior art, the beneficial effects of the utility model are that: the utility model discloses a prilling granulator is equipped with vacuum negative pressure recovery system, and this vacuum negative pressure recovery system can retrieve the residual material in spray gun and the conveyer pipe, prevents that the material from being heated for a long time and discolour in the pipeline, can not cause spray gun or delivery pump to block up yet. In addition, the vacuum negative pressure recovery system can also convey the recovered materials back to the temperature regulating tank for next spraying, so that material waste is avoided, and the vacuum negative pressure recovery system is energy-saving and environment-friendly.
Drawings
Fig. 1 is a schematic structural diagram of a powdery emulsifier granulation device of the present invention.
In the figure, a granulation tower 1, a material conveying system 2, a vacuum negative pressure recovery system 3, a spray gun 4, a temperature adjusting tank 5, a conveying pipe 6, a conveying pump 7, a first discharge valve 8, a second discharge valve 9, a material receiving tank 10, a water ring vacuum pump 11, a recovery pipe 12, a vacuum butterfly valve 13, a material pumping valve 14, an emptying valve 15, a vacuum meter 16 and a discharge port 17 are arranged.
Detailed Description
For better illustration of the objects, technical solutions and advantages of the present invention, the present invention will be further described with reference to the accompanying drawings and examples. It should be understood that the embodiments of the present invention are only used for illustrating the technical effects of the present invention, and are not used for limiting the protection scope of the present invention.
Example 1
As shown in fig. 1, this embodiment 1 provides a powdery emulsifier granulation apparatus, which includes a granulation tower 1, a material conveying system 2, and a vacuum negative pressure recovery system 3. Specifically, the inner top of the prilling tower 1 is provided with a spray gun 4. The material conveying system 2 comprises a temperature adjusting tank 5 and a conveying pipe 6, a discharge port of the temperature adjusting tank 5 is connected with the spray gun 4 through the conveying pipe 6, a conveying pump 7 connected with the discharge port of the temperature adjusting tank 5 is arranged on the conveying pipe 6, and a first discharge valve 8 and a second discharge valve 9 which are located on two sides of the conveying pump 7 are arranged on the conveying pipe 6. Next, the vacuum negative pressure recovery system 3 is connected to the delivery pipe 6. The vacuum negative pressure recovery system 3 comprises a material receiving tank 10, a water ring vacuum pump 11 and a recovery pipe 12; the material receiving tank 10 is connected with a water ring vacuum pump 11, and a vacuum butterfly valve 13 is arranged on a pipeline connecting the water ring vacuum pump 11 and the material receiving tank 10; the material receiving tank 10 is connected with the delivery pipe 6 through a recovery pipe 12, and a material pumping valve 14 is arranged on the recovery pipe 12. Meanwhile, the receiving tank 10 is also provided with an emptying valve 15 and a vacuum gauge 16 for displaying the vacuum degree in the tank. In addition, the bottom of the receiving tank 10 is also provided with a discharge opening 17 connected with the temperature adjusting tank 5.
During granulation, the temperature adjusting tank 5 sends the materials into the spray gun 4 through the conveying pipe 6, and the materials are sprayed out from the spray gun 4 for granulation. When the spray gun 4 stops spraying, the water ring vacuum pump 11 is started, and when the vacuum meter 16 on the material receiving tank 10 shows that the vacuum degree reaches 0.08MPa, the material pumping valve 14 on the recovery pipe 12 is started to pump back the residual materials in the spray gun 4 and the conveying pipe 6. After all the materials are pumped back, the material pumping valve 14 and the water ring vacuum pump 11 are closed, then the emptying valve 15 is opened, and when the vacuum meter 16 shows 0, the discharge port 17 of the material receiving tank 10 is opened, and the materials are discharged into the temperature adjusting tank 5. After all the materials in the material receiving tank 10 are discharged into the temperature adjusting tank 5, the discharge port 17 and the emptying valve 15 of the material receiving tank 10 are closed.
Example 2
This example 2 provides a monoglyceride production line including the powdery emulsifier granulation apparatus of this example 1.
It should be finally noted that the above embodiments are only intended to illustrate the technical solutions of the present invention and not to limit the scope of the present invention, and although the present invention has been described in detail with reference to the preferred embodiments, those skilled in the art should understand that the technical solutions of the present invention can be modified or replaced with equivalents without departing from the spirit and scope of the technical solutions of the present invention.
Claims (10)
1. The utility model provides a likepowder emulsifier prilling granulator, its characterized in that, includes prilling tower, material conveying system and vacuum negative pressure recovery system, the interior top of prilling tower is equipped with the spray gun, material conveying system is including adjusting temperature jar and conveyer pipe, the bin outlet of adjusting temperature jar passes through the conveyer pipe with the spray gun links to each other, vacuum negative pressure recovery system with the conveyer pipe links to each other, and is used for retrieving the conveyer pipe with remaining material on the spray gun.
2. The granulation apparatus for powdery emulsifier according to claim 1, wherein the vacuum negative pressure recovery system comprises a material receiving tank, a vacuum pump and a recovery pipe, the material receiving tank is connected to the vacuum pump, and the material receiving tank is further connected to the delivery pipe through the recovery pipe.
3. The granulating apparatus for powdery emulsifier of claim 2, wherein a vacuum butterfly valve is provided on a pipe connecting the vacuum pump and the receiving tank.
4. The granulation apparatus for powdery emulsifier according to claim 2 or 3, wherein the vacuum pump is a water ring vacuum pump.
5. The granulation apparatus for powdery emulsifier according to claim 2, wherein the recovery pipe is provided with a suction valve.
6. The granulation apparatus for powdery emulsifier as claimed in claim 2, wherein the material receiving tank is further provided with an air release valve and a vacuum gauge for indicating the degree of vacuum in the tank.
7. The granulating apparatus for powdery emulsifier as claimed in claim 2, wherein the bottom of the receiving tank is further provided with a discharge port connected to the temperature-adjusting tank.
8. The granulation apparatus for powdery emulsifier as claimed in claim 1, wherein a transfer pump connected to a discharge port of the temperature-adjusting tank is provided on the transfer pipe.
9. The granulation apparatus for powdery emulsifier as claimed in claim 8, wherein said transport pipe is provided with a first discharge valve and a second discharge valve on both sides of said transport pump.
10. A monoglyceride production line characterized by comprising the powdery emulsifier granulation apparatus according to any one of claims 1 to 9.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921854631.4U CN211190084U (en) | 2019-10-30 | 2019-10-30 | Powdery emulsifier granulation device and monoglyceride production line containing same |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921854631.4U CN211190084U (en) | 2019-10-30 | 2019-10-30 | Powdery emulsifier granulation device and monoglyceride production line containing same |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211190084U true CN211190084U (en) | 2020-08-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201921854631.4U Active CN211190084U (en) | 2019-10-30 | 2019-10-30 | Powdery emulsifier granulation device and monoglyceride production line containing same |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211190084U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113491985A (en) * | 2021-09-09 | 2021-10-12 | 佳力士添加剂（海安）有限公司 | Monoglyceride prilling granulator that dusts |
| CN118437226A (en) * | 2024-05-07 | 2024-08-06 | 广东嘉美好生态科技有限公司 | Granulation mechanism of tower granulation and its application in preparation of high-tower fulvic acid compound fertilizer |
-
2019
- 2019-10-30 CN CN201921854631.4U patent/CN211190084U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113491985A (en) * | 2021-09-09 | 2021-10-12 | 佳力士添加剂（海安）有限公司 | Monoglyceride prilling granulator that dusts |
| CN113491985B (en) * | 2021-09-09 | 2021-11-19 | 佳力士添加剂（海安）有限公司 | A kind of monoglyceride powder spraying granulation device |
| CN118437226A (en) * | 2024-05-07 | 2024-08-06 | 广东嘉美好生态科技有限公司 | Granulation mechanism of tower granulation and its application in preparation of high-tower fulvic acid compound fertilizer |
| CN118437226B (en) * | 2024-05-07 | 2024-12-13 | 广东嘉美好生态科技有限公司 | Granulating mechanism for tower granulation and application of granulating mechanism in preparation of high-tower fulvic acid compound fertilizer |
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