CN212299707U - Centrifugal prickly ash drying-machine system - Google Patents
Centrifugal prickly ash drying-machine system Download PDFInfo
- Publication number
- CN212299707U CN212299707U CN202020292512.0U CN202020292512U CN212299707U CN 212299707 U CN212299707 U CN 212299707U CN 202020292512 U CN202020292512 U CN 202020292512U CN 212299707 U CN212299707 U CN 212299707U
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- centrifugal
- urceolus
- inner tube
- cylinder
- pepper dryer
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- 235000007650 Aralia spinosa Nutrition 0.000 title claims abstract description 7
- 241000949456 Zanthoxylum Species 0.000 title claims abstract description 7
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 15
- 238000010257 thawing Methods 0.000 claims abstract description 14
- 210000001503 joint Anatomy 0.000 claims abstract description 5
- 230000008676 import Effects 0.000 claims abstract description 3
- 235000002566 Capsicum Nutrition 0.000 claims description 25
- 239000006002 Pepper Substances 0.000 claims description 25
- 241000722363 Piper Species 0.000 claims description 25
- 235000016761 Piper aduncum Nutrition 0.000 claims description 25
- 235000017804 Piper guineense Nutrition 0.000 claims description 25
- 235000008184 Piper nigrum Nutrition 0.000 claims description 25
- 238000009423 ventilation Methods 0.000 claims description 2
- 239000003570 air Substances 0.000 description 29
- 238000001035 drying Methods 0.000 description 24
- 238000007791 dehumidification Methods 0.000 description 5
- 238000007599 discharging Methods 0.000 description 3
- 230000007306 turnover Effects 0.000 description 3
- 230000007547 defect Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000012080 ambient air Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
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- Drying Of Solid Materials (AREA)
Abstract
The utility model relates to a centrifugal prickly ash drying-machine system. Including feed cylinder and heat pump heating system, the feed cylinder include urceolus and inner tube, the urceolus in set up the inner tube that runs through whole urceolus height, evenly distributed gas pocket on the outer wall of inner tube and urceolus, the urceolus open and to have feed inlet and discharge gate, heating system's air outlet butt joint the hot-blast import that the inner tube lower extreme was seted up. The heating system comprises a shell, wherein a compressor, a condenser, an evaporator, a spiral electric heater and a defrosting electromagnetic valve are arranged in the shell, the spiral electric heater is connected with an axial flow fan, and an outlet of the axial flow fan is butted with an air inlet of the inner barrel. The utility model discloses rational in infrastructure, the energy saving consumes, and the heating is even, improves the quality and the efficiency that the material was dried.
Description
Technical Field
The invention relates to a centrifugal pepper dryer system.
Background
With the development of agricultural product drying technology, an energy-saving heat pump dryer gradually replaces pure electric drying and boiler drying, and becomes a new trend, pepper is used as a traditional agricultural product, the yield per year is large, the heat pump product used for drying flowers on the market at present still has great defects and shortcomings, and the problems in the aspects including a series of problems of operation cost, drying quality, transportation cost and the like need to be greatly improved, so that the popularization of the pepper dryer is further accelerated.
The prior art has the following disadvantages:
1. the drying system is not fully designed, only simple heating can be carried out, and defrosting can not be carried out in time or no defrosting function is carried out at low temperature, so that the drying effect at low temperature is poor, and the pepper is black;
2. the structural design is too complicated, the cost is too high, economic burden is caused to users, and the product is not favorable for large-scale popularization;
3. the drying material cylinder is unreasonable in design, a plastic cylinder is mostly adopted at present, capillary holes are formed in the bottom of the plastic cylinder, labor cost is high, a hot air inlet and outlet mode is adopted from bottom to top, the drying temperature is extremely uneven, and the dried materials are partially dried and partially undried;
4. most of centrifugal heat pump drying machine systems adopt centrifugal fans, and the fans are high in noise and power consumption;
5. the feeding and discharging are inconvenient, hundreds of kilograms of flowers stored in the charging barrel need to be lifted off, the manpower is consumed greatly, and the humanization is not enough.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides a centrifugal pepper dryer system which is reasonable in structure, saves energy consumption, is uniform in heating and improves the quality and efficiency of material drying.
Therefore, the invention adopts the following technical scheme: the utility model provides a centrifugal prickly ash drying-machine system, its characterized in that includes feed cylinder and heat pump heating system, the feed cylinder include urceolus and inner tube, the urceolus in set up the inner tube that runs through whole urceolus height, evenly distributed gas pocket on the outer wall of inner tube and urceolus, the urceolus open and to have feed inlet and discharge gate, heating system's air outlet butt joint the hot-blast import that the inner tube lower extreme was seted up.
The heating system comprises a shell, wherein a compressor, a condenser, an evaporator, a spiral electric heater and a defrosting electromagnetic valve are arranged in the shell, the spiral electric heater is connected with an axial flow fan, and an outlet of the axial flow fan is butted with an air inlet of the inner barrel.
The defrosting device is characterized in that a sensor is arranged on the evaporator and connected with a system controller, and the system controller controls the on-off of a defrosting electromagnetic valve.
The lower part of the shell is provided with an air inlet grid, and the shell is provided with a power switch and a controller.
A defrosting electromagnetic valve is arranged in the shell.
The lateral wall lower part of urceolus sets up the striker plate, the lower extreme of striker plate sets up down the hopper.
The lower hopper comprises a discharging plate inclined with the outer barrel, and side baffles are arranged on two sides of the discharging plate.
The material baffle is also fully distributed with air holes.
The striker plate is connected with the side wall of the outer barrel through a guide rail.
The upper end of the inner cylinder is provided with a cover plate capable of adjusting the ventilation depth of the inner cylinder
The upper end of the outer barrel is positioned on two sides of the inner barrel cover plate and is respectively provided with a hinge, the hinge is connected with a flip cover of the outer barrel, and the flip cover seals a left feeding hole and a right feeding hole which are distributed on the upper end of the outer barrel.
The centrifugal heat pump drying system has the beneficial effects that:
1. can meet different use environments, can be defrosted at low temperature, and ensures the drying quality of the pepper.
2. The simple control system is developed in a professional way, the operation is simple, the drying temperature can be checked, and the product is more intelligent.
3. The material that the feed cylinder constitutes is light, and the assembly is simple, can assemble at end user's house, only need the transportation accessory can, dozens of hundreds of platforms can be transported once, have greatly saved the cost of transportation.
4. The charging barrel discharges air from the middle part and centrifugally diffuses hot air from the inner barrel of the charging barrel, the discharged air and the temperature are uniform, the permeability is good, the drying quality of the clothes is fully guaranteed, and the drying time is shortened.
5. This centrifugal prickly ash drying system, the feeding can directly open the lid feeding, and the prickly ash dries the back well, and the unloading can directly be followed hopper feed opening and directly unloaded, need not the manual work and carries the storage bucket.
Drawings
Fig. 1 is a schematic view of the overall structure of the present invention.
Fig. 2 is a cross-sectional view of a cartridge according to the present invention.
Fig. 3 is a perspective view of the cartridge of the present invention.
Fig. 4 is a schematic structural view of the heating system of the present invention.
FIG. 5 is a schematic view of the wind direction flow of the heating system of the present invention.
Detailed Description
A centrifugal biaxial control mechanism of the present invention will be described in further detail below with reference to the accompanying drawings.
The centrifugal pepper dryer system shown in fig. 1-3 comprises a charging barrel 1 and a heat pump heating system 3, wherein an inner barrel 4 penetrating the height of the whole outer barrel is arranged in the outer barrel, air holes 5 are uniformly distributed on the outer walls of the inner barrel and the outer barrel, discharge holes are formed in the left side and the right side of the lower surface of the outer barrel, feed inlets are formed in the left side and the right side of the upper surface of the outer barrel, and an air outlet of the heating system is in butt joint with a hot air inlet formed in. The lateral wall lower part of urceolus sets up striker plate 8, the lower extreme of striker plate sets up hopper 2 down.
The blanking hopper comprises a blanking plate 10 inclined with the outer barrel, and side baffles 9 are arranged on two sides of the blanking plate. The striker plate is also fully distributed with air holes. The striker plate is fixed with the guide rail on the side wall of the outer barrel. The upper end of the inner cylinder is provided with a cover plate 7. The upper end of the outer barrel is positioned on two sides of the inner barrel cover plate and is respectively provided with a hinge 6, the hinge is connected with a flip cover of the outer barrel, and the flip cover seals a feed inlet at the upper end of the outer barrel.
As shown in fig. 4-5, the heating system includes a housing, a compressor 19, a condenser 16, an evaporator 15, a spiral electric heater and a defrosting solenoid valve 20 are disposed in the housing 11, the spiral electric heater is connected to an axial flow fan 17, and an outlet 12 of the axial flow fan is butted with an air inlet of the inner cylinder. A spiral electric heater 18 is also provided within the housing. The lower part of the shell is provided with an air inlet grid, and the shell is provided with a power switch 13 and a controller 14.
The working principle of the invention is as follows:
firstly, loading pepper into a charging barrel:
manually covering the material blocking plates on the left side and the right side of the outer barrel, opening the left turnover cover and the right turnover cover on the top of the outer barrel, pouring prepared pepper into the material barrel by using a hopper, and covering the turnover covers after the pepper is filled.
Second, drying and dehumidifying principle
After the heat pump dryer is electrified and started, the axial flow fan, the compressor and the spiral electric heater are successively started, a negative pressure area is formed in the shell along with the work of the axial flow fan, air in the surrounding environment sequentially and automatically flows into the external evaporator, the condenser and the electric heater from the shell through the grids, and finally strong hot air flow is sent to the material cylinder for drying and heating under the action of the fan, and the heat pump dryer is as follows:
when air in the environment flows through the first part evaporator, the evaporator belongs to a heat absorption part, the air is automatically condensed and dehumidified on the evaporator to become dry air, the dry air flows through the second part condenser, the condenser belongs to a heat release part, the dry air absorbs heat of the condenser after passing through the condenser, the temperature is raised to form high-temperature dry air, the dry air flows through the third part spiral electric heater for heating, the temperature of the air is further raised, after being driven by the axial flow fan, the dry hot air is sent into the charging barrel, due to the fact that the inner barrel is fully distributed with the air holes, the dry hot air is evenly diffused into the pepper in a centrifugal mode, moisture in the pepper is rapidly evaporated under the effect of the dry hot air, and after continuous dehumidification and drying, the pepper is subjected to dehumidification and drying treatment.
Thirdly, defrosting operation process:
when the ambient air temperature is lower and the air humidity is higher, the surface of the evaporator is subjected to continuous dehumidification and condensation, the evaporator frosts along with the lengthening of the dehumidification and drying time, when the system controller detects that the temperature of the evaporator is lower than a certain set value, the system automatically starts defrosting, the compressor continues to operate, the fan is turned off, the electromagnetic valve is automatically opened, the system is switched into a defrosting mode, when the system controller detects that the temperature of the surface of the evaporator is higher than the certain set value, the frost on the evaporator is completely removed, the system automatically exits defrosting, and the dehumidification and drying mode is entered again.
Fourthly, taking out the pepper from the material barrel:
the hot pump drying unit is turned off firstly, the pepper container is placed below the blanking hopper, the material baffle is taken down, the pepper flows out automatically, and when the materials cannot be discharged completely, the pepper can be taken out completely by using a material rake or other tools.
The foregoing is merely exemplary of the preferred embodiments of the present invention and is not intended to limit the invention thereto. Any modification, equivalent replacement, or improvement made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (9)
1. The utility model provides a centrifugal prickly ash drying-machine system, its characterized in that includes feed cylinder and heat pump heating system, the feed cylinder include urceolus and inner tube, the urceolus in set up the inner tube that runs through whole urceolus height, evenly distributed gas pocket on the outer wall of inner tube and urceolus, the urceolus open and to have feed inlet and discharge gate, heating system's air outlet butt joint the hot-blast import that the inner tube lower extreme was seted up, heating system include the casing, set up compressor, condenser and evaporimeter, spiral electric heater and defrosting solenoid valve in the casing, spiral electric heater connect axial fan, axial fan export butt joint the air intake of inner tube.
2. The centrifugal pepper dryer system as claimed in claim 1, wherein said evaporator is provided with a sensor, said sensor is connected to a system controller, and said system controller controls the on/off of a defrosting solenoid valve.
3. The centrifugal pepper dryer system as claimed in claim 2, wherein the lower part of the housing is provided with an air inlet grid, and the housing is provided with a power switch and a controller.
4. The centrifugal pepper dryer system as claimed in claim 1, wherein a material baffle is provided at the lower part of the sidewall of the outer cylinder, and a discharge hopper is provided at the lower end of the material baffle.
5. The centrifugal pepper dryer system as claimed in claim 4, wherein the discharge hopper comprises a discharge plate inclined with the outer cylinder, and side baffles are arranged on two sides of the discharge plate.
6. The centrifugal pepper dryer system as claimed in claim 5, wherein said baffle plate is also covered with air holes.
7. The centrifugal pepper dryer system as claimed in claim 6, wherein said striker plate is connected to the guide rail of the outer cylinder sidewall.
8. The centrifugal pepper dryer system as claimed in claim 7, wherein the upper end of the inner cylinder is provided with a cover plate for adjusting the ventilation depth of the inner cylinder.
9. The centrifugal pepper dryer system as claimed in claim 8, wherein the upper end of the outer cylinder is provided with hinges at both sides of the inner cylinder cover plate, the hinges are connected with the flip cover of the outer cylinder, and the flip cover closes the feed inlet at the upper end of the outer cylinder.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020292512.0U CN212299707U (en) | 2020-03-11 | 2020-03-11 | Centrifugal prickly ash drying-machine system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020292512.0U CN212299707U (en) | 2020-03-11 | 2020-03-11 | Centrifugal prickly ash drying-machine system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212299707U true CN212299707U (en) | 2021-01-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020292512.0U Active CN212299707U (en) | 2020-03-11 | 2020-03-11 | Centrifugal prickly ash drying-machine system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212299707U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111256445A (en) * | 2020-03-11 | 2020-06-09 | 杭州真心热能电器有限公司 | Centrifugal prickly ash drying-machine system |
-
2020
- 2020-03-11 CN CN202020292512.0U patent/CN212299707U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111256445A (en) * | 2020-03-11 | 2020-06-09 | 杭州真心热能电器有限公司 | Centrifugal prickly ash drying-machine system |
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