CN216011667U - Special desiccator of fungus sediment - Google Patents
Special desiccator of fungus sediment Download PDFInfo
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- CN216011667U CN216011667U CN202122352736.3U CN202122352736U CN216011667U CN 216011667 U CN216011667 U CN 216011667U CN 202122352736 U CN202122352736 U CN 202122352736U CN 216011667 U CN216011667 U CN 216011667U
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Abstract
The utility model provides a special fungus dreg dryer, which comprises a paddle dryer, a vacuum dust removal system and a condensing system; the upper end and the lower end of the paddle dryer are respectively provided with a feeding hole and a discharging hole, and the paddle dryer comprises a drying steam control device and a drying device; the vacuum dust removal system comprises a plurality of bag-type dust removers and a vacuum pump, and the bag-type dust removers are arranged at the upper ends of the paddle dryers; the condensing system comprises a plurality of condensers and a condensate recovery tank, and the condensers are connected with the condensate recovery tank through a condensate recovery pipeline. The drying machine is suitable for the flow line production of the mushroom dregs, the production process is more efficient, and various waste materials and waste residues generated in the whole process in a sealed mode are effectively treated.
Description
Technical Field
The utility model relates to a special desiccator of fungus sediment belongs to the drying equipment field.
Background
At present, most of drying equipment for mushroom dregs on the market is simpler, the drying effect is often poorer, and a lot of pollutants can be generated in the production process. With continuous deepening of automation and environmental protection, the former drying equipment cannot adapt to flow line production, and the whole set of equipment cannot be perfected efficiently and systematically in the production process. And secondly, the waste is recycled without being treated by the system.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a special desiccator of fungus sediment to solve the relevant technical problem among the prior art.
A special desiccator of fungus sediment, including paddle desiccator, vacuum dust removal system and condensing system; the upper end and the lower end of the paddle dryer are respectively provided with a feeding hole and a discharging hole, and the paddle dryer comprises a drying steam control device and a drying device; the vacuum dust removal system comprises a plurality of bag-type dust removers and a vacuum pump, and the bag-type dust removers are arranged at the upper ends of the paddle dryers; the condensing system comprises a plurality of condensers and a condensate recovery tank, and the condensers are connected with the condensate recovery tank through a condensate recovery pipeline.
Preferably, a plurality of cleaning openings are formed in the top end of the inner part of the paddle dryer.
Preferably, the drying steam control device is provided with a steam inlet, a cooling water inlet and a condensed water outlet, and the steam inlet, the cooling water inlet and the condensed water outlet are respectively connected with the boiler, the cooling circulating water pipeline and the steam condensed water outlet pipeline.
Preferably, the drying device comprises a cooling device, a rotating blade and a power device, and the cooling device is arranged on the power device and used for cooling the power device.
Preferably, the bag-type dust collector, the condenser and the condensate recovery tank are provided with vacuum interfaces, and the vacuum pump is connected with the condensate recovery tank, the condenser and the bag-type dust collector in sequence through vacuum pipelines.
Preferably, the paddle dryer is provided at a bottom thereof with a drain pipe for discharging accumulated condensed water.
Preferably, the bag-type dust collector is provided with a steam interface, and the steam interface is connected with the boiler.
Preferably, the feed inlet, the discharge outlet, the bag-type dust collector and the condensate recovery tank are all provided with nitrogen interfaces, and the nitrogen interfaces are connected with a nitrogen pipeline.
Has the advantages that:
1. the utility model discloses can be applicable to various full-automatic production water line, automatic control can all be realized to all processes, can save a large amount of costs.
2. The utility model discloses whole airtight production to improve the pipeline of production, waste gas and the waste material that produces in process of production can directly not disperse to the air, environmental protection more.
3. The utility model discloses do not need the manual work to wash inside the equipment, can realize high-efficient continuous production.
Drawings
FIG. 1 is a schematic view of the overall structure of a special fungus dreg dryer of the present invention;
FIG. 2 is a schematic view of the overall structure of the middle paddle dryer of the present invention;
FIG. 3 is a schematic view of a part of the structure of the paddle dryer of the present invention;
in the figure: a feed inlet 1, a discharge outlet 2, a bag-type dust collector 3, a condenser 4 and a condensate recovery tank 5.
Detailed Description
The present invention is described in detail with reference to the accompanying drawings, which are not intended to limit the scope of the present invention.
As shown in fig. 1-3, a special purpose dryer for mushroom dregs comprises a paddle dryer, a vacuum dust removing system and a condensing system; the upper end and the lower end of the paddle dryer are respectively provided with a feeding port 1 and a discharging port 2, and the paddle dryer comprises a drying steam control device and a drying device; the vacuum dust removal system comprises a plurality of bag-type dust removers 3 and a vacuum pump, and the bag-type dust removers are arranged at the upper ends of the paddle dryers; the condensing system comprises a plurality of condensers 4 and a condensate recovery tank 5, and the condensers 4 and the condensate recovery tank 5 are connected through a condensate recovery pipeline.
Preferably, a plurality of cleaning openings are formed in the top end of the inner part of the paddle dryer.
Preferably, the drying steam control device is provided with a steam inlet, a cooling water inlet and a condensed water outlet, and the steam inlet, the cooling water inlet and the condensed water outlet are respectively connected with the boiler, the cooling circulating water pipeline and the steam condensed water outlet pipeline.
Preferably, the drying device comprises a cooling device, a rotating blade and a power device, and the cooling device is arranged on the power device and used for cooling the power device.
Preferably, the bag-type dust collector 3, the condenser 4 and the condensate recovery tank 5 are provided with vacuum interfaces, and the vacuum pump is sequentially connected with the condensate recovery tank 5, the condenser 4 and the bag-type dust collector 3 through vacuum pipelines.
Preferably, the paddle dryer is provided at a bottom thereof with a drain pipe for discharging accumulated condensed water.
Preferably, the bag-type dust collector 3 is provided with a steam interface, and the steam interface is connected with a boiler.
Preferably, the feed inlet 1, the discharge outlet 2, the bag-type dust collector 3 and the condensate recovery tank 5 are all provided with nitrogen interfaces, and the nitrogen interfaces are connected with a nitrogen pipeline.
The utility model discloses in the quantity of sack cleaner 3 and condenser 4 can be according to its quantity of actual production adjustment.
The utility model discloses well cooling water pressure is 0.3Mpa, and the temperature is 25-30 degrees, and the velocity of flow is 100m thin shoots/h.
The utility model discloses well nitrogen gas is 0.4-0.6Mpa, and the velocity of flow is 100 Nm/h.
The utility model discloses well boiler produces saturated steam, and pressure is 0.6Mpa, and the velocity of flow is 1500 supplyes 2000 kg/h.
The above description is only for the purpose of illustration, and it should be noted that, in the preferred embodiment of the present invention, a person skilled in the art can make several improvements and decorations on the premise of departing from the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.
Claims (8)
1. A special desiccator of fungus sediment, characterized by, including paddle desiccator, vacuum dust removal system and condensing system; the upper end and the lower end of the paddle dryer are respectively provided with a feeding port (1) and a discharging port (2), and the paddle dryer comprises a drying steam control device and a drying device; the vacuum dust removal system comprises a plurality of bag-type dust removers (3) and a vacuum pump, and the bag-type dust removers are arranged at the upper end of the paddle dryer; the condensing system comprises a plurality of condensers (4) and a condensate recovery tank (5), and the condensers (4) are connected with the condensate recovery tank (5) through a condensate recovery pipeline.
2. The special mushroom dreg dryer as claimed in claim 1, wherein the top end of the inner part of the paddle dryer is provided with a plurality of cleaning openings.
3. The special drying machine for mushroom dregs according to claim 1, wherein the drying steam control device is provided with a steam inlet, a cooling water inlet and a condensed water outlet, and the steam inlet, the cooling water inlet and the condensed water outlet are respectively connected with a boiler, a cooling circulating water pipeline and a steam condensed water outlet pipeline.
4. The special fungus dreg dryer as claimed in claim 1, wherein the drying device comprises a cooling device, a rotating blade and a power device, and the cooling device is arranged on the power device and used for cooling the power device.
5. The special fungus dreg dryer as claimed in claim 1, wherein the bag-type dust remover (3), the condenser (4) and the condensate recovery tank (5) are provided with vacuum ports, and the vacuum pump is connected with the condensate recovery tank (5), the condenser (4) and the bag-type dust remover (3) in sequence through vacuum pipes.
6. The special purpose dryer for mushroom dregs according to claim 1, wherein the bottom of the paddle dryer is provided with a drain pipe for draining accumulated condensed water.
7. The special drying machine for the mushroom dregs according to claim 1, wherein a steam interface is arranged on the bag-type dust collector (3), and the steam interface is connected with a boiler.
8. The special fungus dreg dryer as claimed in claim 1, wherein the feed inlet, the discharge outlet, the bag-type dust collector (3) and the condensate recovery tank (5) are all provided with nitrogen interfaces, and the nitrogen interfaces are connected with a nitrogen pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122352736.3U CN216011667U (en) | 2021-09-27 | 2021-09-27 | Special desiccator of fungus sediment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122352736.3U CN216011667U (en) | 2021-09-27 | 2021-09-27 | Special desiccator of fungus sediment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216011667U true CN216011667U (en) | 2022-03-11 |
Family
ID=80522805
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122352736.3U Active CN216011667U (en) | 2021-09-27 | 2021-09-27 | Special desiccator of fungus sediment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216011667U (en) |
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2021
- 2021-09-27 CN CN202122352736.3U patent/CN216011667U/en active Active
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