CN205825588U - Soak the drying and processing system after dregs pressing - Google Patents
Soak the drying and processing system after dregs pressing Download PDFInfo
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- CN205825588U CN205825588U CN201620749219.6U CN201620749219U CN205825588U CN 205825588 U CN205825588 U CN 205825588U CN 201620749219 U CN201620749219 U CN 201620749219U CN 205825588 U CN205825588 U CN 205825588U
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- rotating cylinder
- air flow
- drying
- flow bed
- boiler
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- Drying Of Solid Materials (AREA)
Abstract
A kind of soak the drying and processing system after dregs pressing, including squeezer, dry rotating cylinder, air flow bed drying plant, material collecting device and boiler.Soaking medicinal residues after the squeezing of described squeezer, through belt with dry drum feeding device and be transported to dry in rotating cylinder and dry, the gas material pipe end of this drying rotating cylinder is provided with cyclone dust extractor and air exhauster, is extracted out by the gas dried in rotating cylinder and is discharged to outdoor；The bottom drying rotating cylinder is provided with spiral discharging machine and disintegrating machine, and the port of export at disintegrating machine connects air flow bed drying plant, and the thermal source inlet end of this air flow bed drying plant is connected by pipeline heat exchanger；Discharging opening at described air flow bed drying plant has cyclone dust extractor and sack cleaner by pipeline successively connection, under the common effect of air-introduced machine and exhaustor, the dustless waste gas after air flow bed drying plant is discharged to outdoor；After the outfan of cyclone dust extractor and sack cleaner is respectively by pipeline and material collecting device and boiler feed storehouse, send into boiler burn.
Description
Technical field
This utility model relates to a kind of soaking the drying and processing system after dregs pressing, belongs to environmental technology field.
Background technology
At present, the Chinese medicine of China or and the food enterprises, have every day substantial amounts of leaching medicinal residues or food slag to produce, have at least
Several tons, have hundreds of ton at most.Therefore, these medicinal residues or food slag automobile will be shipped to exurban every day by manufacturing enterprise
Mountain region is buried, and not only to spend a large amount of manpower and financial resources, it is often more important that the foul smell rotted after burying and penetrating fluid are to surrounding air
There is serious corrosion with soil, destroy ecological environment, affect the healthy of people.The applicant on August 4th, 2015 and
Successively application on April 19th, 2016 " leaching medicinal residues boiler combustion processing system " and " a kind of squeezing extrusion process soaking material
System " two patents of invention, for Chinese medicine or the food enterprises, have found the good equipment of a kind of process for producing rubbish, not only make
With convenient, moreover it is possible to save handling every day for enterprise；And medicinal residues or food slag rubbish mountain region can be avoided to bury, both can avoid
Occupy cultivated land, be conducive to preserving the ecological environment and people healthy.During implementing the two invention, find that this is
The equipment of system is complex, and the effect processing wet medicinal residues is not felt quite pleased, and also has the necessity improved further and improve.
Summary of the invention
For overcoming existing the problems referred to above soaking medicinal residues garbage disposal, after this utility model provides one to soak dregs pressing
Drying and processing system, to reach to make, system is simpler, cost is less expensive, the more preferable purpose for the treatment of effect.
For solving its technical problem, the design people, in actual treatment soaks the work of medicinal residues, finds existing processing system
The squeezing inadequate science of post-drying processing equipment, structure is not reasonable, through experiment finally complete this utility model.Design leaching
Drying and processing system after wet dregs pressing, including: squeezer, dry drum feeding device, dry rotating cylinder, disintegrating machine machine, draw
Blower fan, water mist dust-removing exhaustor, air flow bed drying plant, material collecting device, boiler feed storehouse, and boiler, its feature is:
1, the outfan of described squeezer connects the belt having transmission, and the outfan of this belt feeds dress with drying rotating cylinder
Putting connected, in order to be transported to dry in rotating cylinder by the medicinal residues that soak after squeezing, warm-air pipe and pot are passed through in one end of this drying rotating cylinder
The heat delivery outlet of stove is connected, in order to provide drying thermal source；The other end of this drying rotating cylinder is provided with gas material pipe, described gas material pipe
End is provided with cyclone dust extractor, and the outfan of described cyclone dust extractor connects air exhauster, and drying is turned by the entrance of this air exhauster
The gas of the partially aqueous mist in Tong is extracted out, by exporting through water mist dust-removing exhaustor from the outlet of air exhauster after cyclone dust extractor
To outdoor；The bottom drying rotating cylinder is provided with spiral discharging machine and disintegrating machine, and the port of export at disintegrating machine connects has air flow bed to dry
Equipment, the thermal source inlet end of this air flow bed drying plant is connected by pipeline heat exchanger；The bottom of described heat exchanger sets
There is aerator, in order to the hot blast in heat exchanger is blown into air flow bed drying plant；Discharging at described air flow bed drying plant
Mouth is successively connected by pipeline cyclone dust extractor and sack cleaner, is provided with air-introduced machine and aerofluxus on the top of sack cleaner
Pipe, in order to be discharged to outdoor by the dustless waste gas after air flow bed drying plant；In cyclone dust extractor and the output of sack cleaner
End is connected with the entrance of material collecting device by pipeline respectively, this material collecting device after pipeline and boiler feed storehouse with the pan feeding of boiler
Mouth is connected；
2, the top at boiler is provided with supplementary fuel inlet, in order to supplement granular fuel, in order to make boiler have enough
Heat output；
3, being provided with fin in heat exchanger, this fin is connected with vapour source by turnover steam pipe.
Compared with prior art, this utility model has following features and a progress:
A, more sophisticated for Chinese medicine manufacturing enterprise process for producing garbage system, process more scientific, make rubbish material be filled
Divide and smash after drying, thus destroy the wet stock crust parcel to moisture, reach to dry fully so that it is the effect of burning
More preferably, the heat after burning is fully utilized fruit, advantageously reduces and processes the cost soaking medicinal residues；It is the most easy to use, moreover it is possible to
Handling is saved every day for enterprise；
B, the gas exported because of native system, all through water mist dust-removing, cyclone dust removal or bag-type dust, be system output
Gas without dust or harmful components, be conducive to preserving the ecological environment；
C, because this utility model is first to squeeze soaking medicinal residues, then the medicinal residues after anhydrating squeezing are dried, so
After smash, then after separate through gas, material, finally combustible material is made a gift to someone boiler combustion, therefore, the thing after this process
Material is easy to burning, and efficiency of combustion is up to more than 95%；The most this material imputrescibility goes bad, and is conducive to long-time storage, in order to
According to boiler combustion need carry out fuel supplement or interpolation, it is to avoid need to carry out accompanying burning with other fuel in the past, reach save
Energy reduction processes the purpose of rubbish cost.
Accompanying drawing explanation
Below by drawings and Examples figure, this utility model is further illustrated:
Fig. 1 is structural representation block diagram of the present utility model.
In figure: 1, boiler, 2, warm-air pipe, 3, dry rotating cylinder, 4, spiral discharging machine, 5, disintegrating machine, 6, air flow bed dries and set
Standby, 7, heat exchanger, 8, aerator, 9, cyclone dust extractor, 10, sack cleaner, 11, air-introduced machine, 12, exhaustor, 13, rewinding
Device, 14, belt conveyor, 15, boiler feed storehouse, 16, cyclone dust extractor, 17, air exhauster, 18, water mist dust-removing exhaustor,
19, squeezer, 20 belts, 21 tumble drying feed arrangements, 22 gas material pipes, 23 turnover steam pipes, 24 particulate material apparatuss for feeding.
Detailed description of the invention
Design the drying and processing system after soaking dregs pressing, including: squeezer 19, dry drum feeding device 21,
Drying rotating cylinder 3, disintegrating machine 5, air-introduced machine 11, water mist dust-removing exhaustor 18, air flow bed drying plant 6, material collecting device 13, boiler enters
Feed bin 15 and boiler 1, its feature is: 1, described squeezer 19 is to squeeze soaking medicinal residues, after squeezer squeezes
Soaking medicinal residues, be transported to dry in rotating cylinder 3 through belt 20 and drying drum feeding device 21, one end of this drying rotating cylinder is by heat
Airduct 2 is connected with the heat delivery outlet of boiler 1, dries thermal source with thinking that drying rotating cylinder 3 provides；Another of this drying rotating cylinder 3
End is provided with gas material pipe 22, and the end of described gas material pipe is provided with cyclone dust extractor 16, and the outfan of described cyclone dust extractor connects to be had
Air exhauster 17, the gas of the partially aqueous mist dried in rotating cylinder is extracted out, after cyclone dust extractor 16 by the entrance of this air exhauster
Outdoor is exported through water mist dust-removing exhaustor 18 from air exhauster outlet；The bottom drying rotating cylinder 3 is provided with spiral discharging machine 4 and smashes
Machine 5, the port of export at disintegrating machine 5 connects air flow bed drying plant 6, and the thermal source inlet end of this air flow bed drying plant is by pipe
Road connects heat exchanger 7；Being provided with fin in heat exchanger, this fin is by turnover steam pipe 23 and vapour source phase
Even；The bottom of described heat exchanger 7 is provided with aerator 8, in order to the hot blast in heat exchanger 7 is blown into air flow bed drying plant 6；
Discharging opening at described air flow bed drying plant has cyclone dust extractor 9 and sack cleaner 10, at cloth by pipeline successively connection
The top of bag dust collector 10 is provided with air-introduced machine 11 and exhaustor 12, in order to be arranged by the dustless waste gas after air flow bed drying plant 6
To outdoor；It is connected by the entrance of pipeline with material collecting device 13 respectively with the outfan of sack cleaner 10 at cyclone dust extractor 9,
This material collecting device is connected through pipeline 14 feeding mouth with boiler 1 behind boiler feed storehouse 15.2, the top at boiler 1 is provided with benefit
Fill fuel inlet 24, in order to supplement granular fuel, in order to make boiler have enough heats to export.
Claims (3)
1. soak the drying and processing system after dregs pressing, including: squeezer (19), dry drum feeding device (21),
Drying rotating cylinder (3), disintegrating machine (5), air-introduced machine (11), water mist dust-removing exhaustor (18), air flow bed drying plant (6), rewinding fills
Put (13), boiler feed storehouse (15) and boiler (1), it is characterized in that: the outfan of described squeezer (19) connects transmission
Belt (20), the outfan of this belt (20) with dry drum feeding device (21) be connected, in order to will squeeze after soak medicinal residues
Being transported to dry in rotating cylinder (3), one end of this drying rotating cylinder is connected with the heat delivery outlet of boiler (1) by warm-air pipe (2), uses
Thermal source is dried to provide；The other end of this drying rotating cylinder (3) is provided with gas material pipe (22), and the end of described gas material pipe is provided with whirlwind and removes
Dirt device (16), the outfan of described cyclone dust extractor connects air exhauster (17), and the entrance of this air exhauster will be dried in rotating cylinder
The gas of partially aqueous mist is extracted out, by after cyclone dust extractor (16) from the outlet of air exhauster (17) through water mist dust-removing exhaustor
(18) output is to outdoor；The bottom drying rotating cylinder (3) is provided with spiral discharging machine (4) and disintegrating machine (5), in going out of disintegrating machine (5)
Mouth end connects air flow bed drying plant (6), and the thermal source inlet end of this air flow bed drying plant is connected by pipeline heat exchange
Device (7)；The bottom of described heat exchanger (7) is provided with aerator (8), in order to the hot blast in heat exchanger is blown into air flow bed and dries
Equipment (6)；Discharging opening at described air flow bed drying plant has cyclone dust extractor (9) and bag-type dust by pipeline successively connection
Device (10), is provided with air-introduced machine (11) and exhaustor (12), sets in order to will dry through air flow bed on the top of sack cleaner (10)
Dustless waste gas after standby (6) is discharged to outdoor；Outfan at cyclone dust extractor (9) and sack cleaner (10) passes through pipeline respectively
Be connected with the entrance of material collecting device (13), this material collecting device after pipeline (14) and boiler feed storehouse (15) with the entering of boiler (1)
Material mouth is connected.
2., according to the drying and processing system soaked after dregs pressing described in claims 1, it is characterized in that: at boiler (1)
Top is provided with supplementary fuel inlet (24), in order to supplement granular fuel, in order to make boiler have enough heats to export.
3., according to the drying and processing system soaked after dregs pressing described in claims 1, it is characterized in that: in heat exchanger
Being provided with fin, this fin is connected with vapour source by turnover steam pipe (23).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620749219.6U CN205825588U (en) | 2016-07-18 | 2016-07-18 | Soak the drying and processing system after dregs pressing |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620749219.6U CN205825588U (en) | 2016-07-18 | 2016-07-18 | Soak the drying and processing system after dregs pressing |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205825588U true CN205825588U (en) | 2016-12-21 |
Family
ID=57562041
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620749219.6U Expired - Fee Related CN205825588U (en) | 2016-07-18 | 2016-07-18 | Soak the drying and processing system after dregs pressing |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205825588U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106016970A (en) * | 2016-07-18 | 2016-10-12 | 周伟初 | Drying treatment system used after squeezing of soaked medicine residues |
-
2016
- 2016-07-18 CN CN201620749219.6U patent/CN205825588U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106016970A (en) * | 2016-07-18 | 2016-10-12 | 周伟初 | Drying treatment system used after squeezing of soaked medicine residues |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161221 Termination date: 20200718 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |