CN216898278U - Hickory nut dynamic circulation drying device - Google Patents

Hickory nut dynamic circulation drying device Download PDF

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Publication number
CN216898278U
CN216898278U CN202220117262.6U CN202220117262U CN216898278U CN 216898278 U CN216898278 U CN 216898278U CN 202220117262 U CN202220117262 U CN 202220117262U CN 216898278 U CN216898278 U CN 216898278U
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circulation
bin
drying device
air
ventilative
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邓杨勇
高军龙
赵美玉
田玮
刘子强
陈龙
李童
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Hangzhou Yaoshang Kee Food Co ltd
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Hangzhou Yaoshang Kee Food Co ltd
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/80Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
    • Y02P60/85Food storage or conservation, e.g. cooling or drying

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Abstract

The application discloses hickory nut dynamic circulation drying device and drying method, hickory nut dynamic circulation drying device includes ventilative feed bin, circulation inlet pipe, circulation discharging pipe and promotes the conveyer, the circulation inlet pipe sets up the circulation feed inlet department at ventilative feed bin, the circulation discharging pipe sets up the circulation discharging port department at ventilative feed bin, it sets up between circulation discharging pipe and circulation inlet pipe to promote the conveyer, ventilative feed bin one side is provided with the heat pump internal unit. The application also discloses a drying method using the dynamic circulation drying device for the hickory nuts.

Description

Hickory nut dynamic circulation drying device
Technical Field
The utility model relates to the field of food drying and dehydration, in particular to a dynamic circulation drying device for hickory nuts.
Background
At present, the drying treatment of the picked pecans is still relatively extensive, the pecans are dried naturally mainly by the traditional sun, the natural sun drying needs to be dried naturally by the sun for three days in principle, but if the pecans are continuously rainy during the picking period, the pecans cannot be dried in time, although some factories adopt an artificial drying mode, the current artificial drying is static drying in a drying pool, an oven and the like, local high temperature and untimely water volatilization are caused due to material accumulation in the drying process, the pecans germs are necrotic in the drying process, and the antioxidase loses activity, so that compared with the naturally dried pecans, the dried pecans lose the antioxidant activity of the pecans, the fat degradation speed is accelerated in the storage process, the loss of aroma and nutrition is serious after processing, and the product quality is reduced.
SUMMERY OF THE UTILITY MODEL
The utility model provides a dynamic circulation drying device for hickory nuts aiming at the problems.
The technical scheme adopted by the utility model is as follows:
the utility model provides a hickory nut dynamic cycle drying device, includes ventilative feed bin, circulation inlet pipe, circulation discharging pipe and promotes the conveyer, the circulation inlet pipe sets up the circulation feed inlet department at ventilative feed bin, the circulation discharging pipe sets up the circulation discharge outlet department at ventilative feed bin, it sets up between circulation discharging pipe and circulation inlet pipe to promote the conveyer, ventilative feed bin one side is provided with the heat pump internal unit.
In this kind of hickory nut dynamic cycle drying device, the circulation inlet pipe sets up the top at ventilative feed bin, and the exit of circulation discharging pipe setting below ventilative feed bin, the material granule (hickory nut) that needs dry dehydration gets into ventilative feed bin from the circulation inlet pipe, then the ventilative feed bin is left to the rethread circulation discharging pipe, the lift conveyer that reenters at last, it gets into ventilative feed bin again to rely on self gravity in the circulation inlet pipe to promote the feeder, continuous circulation is reciprocal in proper order, the material is in the flow state all the time like this, for the mode of static stoving, the mode of material flow stoving can not cause local high temperature at the stoving in-process, can let moisture volatilize fast.
The function of the heat pump internal machine is to form hot air flow, and the hot air flow can dry materials.
Concrete lifting conveyor one side still is provided with the step, and convenient to use person transports the material to lifting conveyor's entrance through the step like this at the beginning, and the exit that promotes the conveyer is provided with receipts material pipe equally, receives the material pipe and all is located lifting conveyor's exit with the circulation inlet pipe, and after the material accomplished dry dehydration, the material no longer got into the circulation inlet pipe, but directly got into and received the material pipe and collected.
Optionally, the air-permeable storage bin further comprises a centrifugal fan, and the centrifugal fan is arranged on one side of the air-permeable storage bin.
The centrifugal fan is arranged to blow hot air generated by the heat pump inner unit to the ventilating bin continuously, so that the dry hot air flow source can continuously dehydrate and dry materials.
Optionally, the ventilating device further comprises an air bin, and the air bin is arranged on one side of the ventilating bin.
The specific air bin is arranged at the bottom of the ventilating bin, the air bin is located outside the ventilating bin, the centrifugal fan and the heat pump inner unit are arranged on one side of the air bin, the centrifugal fan blows hot air into the air bin, then the hot air enters the ventilating bin from the air bin to dry materials, and due to the existence of the air bin, hot dry airflow generated by the centrifugal fan and the heat pump inner unit can be blown to the ventilating bin as far as possible, so that the use efficiency of the hot dry airflow is improved.
Optionally, the air-permeable bin is a funnel-shaped bin.
Optionally, the air-permeable heat pump system further comprises a shell, and the air-permeable storage bin and the heat pump inner machine are both located in the shell.
The shell is arranged to ensure that the whole ventilating bin is positioned in a small environment with relatively constant temperature, so that the ventilating bin, the heat pump inner machine and the centrifugal fan are positioned in a relatively independent environment, and the energy consumption of the heat pump inner machine during gas heating can be reduced.
Optionally, the air valve is further included, and the air valve is mounted on the shell.
The new trend blast gate is installed to the roof department of specific shell, install the hydrofuge blast gate on the lateral wall of shell, the hydrofuge blast gate on the roof is the passageway that the shell was left to the wet gas in the shell, and the new trend blast gate on the lateral wall is the passageway that gaseous entering shell, and when dry material, centrifugal fan passes through the new trend blast gate on the lateral wall and in with low temperature gas takes out the shell in with the environment, get into the wind storehouse after the heating via the heat pump internal unit, then get into ventilative feed bin from the wind storehouse again and dry the material, the hydrofuge blast gate that the last wet gas was located from the roof leaves.
Optionally, the material feeding device further comprises a material nozzle, and the material nozzle is installed on the circulating feeding pipe.
Optionally, a material distribution cone is arranged at a bin opening of the air permeable bin, and the material distribution cone is located between the air permeable bin and the material nozzle.
The branch material awl is coniform, and the effect of branch material awl is the edge with the ventilative feed bin of material direction, and the discharge gate of ventilative feed bin is located the center department of self, and the motion route of material in ventilative feed bin is for locating the motion to the center by the edge like this, and such design can effectively increase the time that the material stops in ventilative feed bin, increases the dehydration drying time of air current to the material, improves the utilization efficiency of steam. And in this way, the gravity of the pecans can be utilized to the maximum extent in the whole process to realize flowing, and the energy consumption is reduced.
Optionally, the number of the breathable bins is not less than 1.
The number of the air permeable bins can be increased according to the use requirement, and the number of the air permeable bins can be one, two or three, or even more.
A drying method using the pecan dynamic circulation drying device comprises the following steps; the material is in a falling state, the material is impacted by the airflow, the flow direction of the airflow is opposite to the falling direction of the material, the temperature of the airflow is higher than that of the material, and the humidity of the airflow is lower than that of the material.
When the method is used for drying the hickory, the hickory can be placed into the ventilating bin, the hickory particles fall down from top to bottom in the ventilating bin, the dry hot air flows upwards from bottom to top, and the water in the hickory can be taken away by the air flow blown by the hickory.
The utility model has the beneficial effects that: the material is always in a flowing state, so that local high temperature is not caused, and moisture can be quickly volatilized; the gravity of the hickory nut is utilized to the maximum extent in the whole process to realize flowing, and the energy consumption is reduced.
Description of the drawings:
FIG. 1 is a schematic view of the structure of example 1,
FIG. 2 is a schematic view showing the positional relationship between the housing and the step in embodiment 1,
fig. 3 is a schematic view of the fit relationship of the gas permeable storage bin in embodiment 2.
The figures are numbered: 1. a lifting conveyor; 2. circulating the feeding pipe; 3. a material receiving pipe; 401. a moisture exhaust air valve; 402. a fresh air valve; 5. a material nozzle; 6. a material separating cone; 7. a breathable storage bin; 8. a wind bin; 9. a support; 10. a centrifugal fan; 11. a heat pump indoor unit; 12. a step; 13. a housing; 14. circulating the discharge pipe; 15. and (4) a hopper.
The specific implementation mode is as follows:
the present invention will be described in detail below with reference to the accompanying drawings.
Example 1
Referring to attached drawings 1 and 2, a hickory nut dynamic circulation drying device comprises a ventilating bin 7, a circulation feeding pipe 2, a circulation discharging pipe 14 and a lifting conveyor 1, wherein the circulation feeding pipe 2 is arranged at the circulation feeding port of the ventilating bin 7, the circulation discharging pipe 14 is arranged at the circulation discharging port of the ventilating bin 7, the lifting conveyor 1 is arranged between the circulation discharging pipe 14 and the circulation feeding pipe 2, and a heat pump inner unit 11 is arranged on one side of the ventilating bin 7.
In this kind of hickory nut dynamic cycle drying device, circulation inlet pipe 2 sets up the top at ventilative feed bin 7, and circulation discharging pipe 14 sets up the exit in ventilative feed bin 7 below, the material granule (hickory nut) that needs dry dehydration gets into ventilative feed bin 7 from circulation inlet pipe 2, then leave ventilative feed bin 7 through circulation discharging pipe 14 again, reentrant promotion conveyer 1 at last, promote to get into ventilative feed bin 7 again in circulation inlet pipe 2 by promoting the feeder, continuous circulation is reciprocal in proper order, the material is in the flow state all the time like this, for the mode of static stoving, the mode of material flow stoving can not cause local high temperature at the stoving in-process, can let moisture volatilize fast.
The function of the heat pump inner unit 11 is to form a hot air flow, which can dry the material.
Concrete lifting conveyor one side still is provided with step 12, and convenient to use person transports the material to lifting conveyor's entrance through step 12 when beginning like this, and the exit that promotes the conveyer is provided with and receives material pipe 3 equally, receives material pipe 3 and circulation inlet pipe 2 and all is located lifting conveyor's exit, and after the material accomplished dry dehydration, the material no longer got into circulation inlet pipe 2, but directly gets into and receives material pipe 3 and collect.
The air-permeable silo 7 can be regarded as a funnel with an opening in the wall in the embodiment.
In this embodiment, the air-permeable storage bin further comprises a centrifugal fan 10, and the centrifugal fan 10 is arranged on one side of the air-permeable storage bin 7.
The centrifugal fan 10 is arranged to blow hot air generated by the heat pump inner machine 11 to the ventilating bin 7 continuously, so that the dry hot air flow source can continuously dehydrate and dry materials.
In this embodiment, still include wind storehouse 8, wind storehouse 8 sets up the one side at ventilative feed bin 7.
The specific air bin 8 is arranged at the bottom of the ventilating bin 7, the air bin is located outside the ventilating bin 7, the centrifugal fan 10 and the heat pump inner unit 11 are arranged on one side of the air bin, the centrifugal fan 10 blows hot air into the air bin, then the hot air enters the ventilating bin 7 from the air bin to dry materials, and due to the existence of the air bin, hot dry air flow generated by the centrifugal fan 10 and the heat pump inner unit 11 can blow to the ventilating bin 7 as far as possible, so that the use efficiency of the hot dry air flow is improved.
In this embodiment, the air-permeable bin 7 is a funnel-shaped bin.
In this embodiment, the air-permeable heat pump system further comprises an outer shell 13, and the air-permeable storage bin 7 and the heat pump inner machine 11 are both located in the outer shell 13.
The shell 13 is arranged to ensure that the whole ventilating bin 7 is located in a small relatively constant-temperature environment, so that the ventilating bin 7, the heat pump indoor unit 11 and the centrifugal fan 10 are located in a relatively independent environment, and the energy consumption of the heat pump indoor unit 11 during gas heating can be reduced.
In this embodiment, the air valve is further included and is installed on the housing 13.
The wet air discharging valve 401 is installed at the top of the specific shell 13, the fresh air valve 402 is installed on the side wall of the shell 13, the wet air discharging valve 4 on the top of the box is a channel through which wet air in the shell 13 leaves the shell 13, the fresh air valve 402 on the side wall is a channel through which air enters the shell 13, when materials are dried, the centrifugal fan 10 sucks low-temperature air in the environment into the shell 13 through the fresh air valve 402 on the side wall, the air enters the air bin 8 after being heated by the heat pump indoor unit 11, then the air enters the air permeable bin 7 from the air bin 8 to dry the materials, and finally the wet air leaves from the wet air discharging valve 402 on the top of the box.
In the embodiment, the device also comprises a material nozzle 5, and the material nozzle 5 is arranged on the circulating feeding pipe 2.
In this embodiment, a material distribution cone 6 is arranged at the bin opening of the air permeable bin 7, and the material distribution cone 6 is located between the air permeable bin 7 and the material nozzle 5.
Divide material awl 6 to be coniform, divide material awl 6's effect to be the edge with material direction ventilative feed bin 7, and the discharge gate of ventilative feed bin 7 is located the center department of self, and the motion route of material in ventilative feed bin 7 is for locating the motion to the center by the edge like this, and such design can effectively increase the time that the material stops in ventilative feed bin 7, increases the dehydration drying time of air current to the material, improves the utilization efficiency of steam.
The number of the air permeable bins 7 is 1 in the embodiment.
Still set up in temperature sensor and humidity transducer in ventilative feed bin 7 in this embodiment, temperature sensor is used for monitoring the temperature in the storehouse, and humidity transducer is used for monitoring the gas humidity in the storehouse.
As a variant of this embodiment, the air flap 4 at the top of the tank can also be replaced by a fan.
In the embodiment, the inclination of the material dividing cone is 5-10 degrees, and the inclination of the air permeable bin is 30-60 degrees, so that the raw materials can fall down by the gravity of the raw materials, and the energy consumption in the working process is further saved.
In this embodiment, the inside of the air-permeable storage bin 7 may be made of stainless steel, and the wall of the air-permeable storage bin 7 may be made of stainless steel, a polyurethane cold storage plate with a thickness of 100mm, and a metal plate from inside to outside, which are three layers in total.
In this embodiment, the wind box may be made of the same plate as the air permeable bin.
In this embodiment, the housing may be made of a metal plate, and may be made of a common steel material or stainless steel.
In this embodiment, in order to promote the whereabouts of material, can also set up vibrating motor in the below of branch material awl 6 for the material on the branch material awl constantly falls.
In this embodiment, a linear material distributing plate may be further disposed in the material nozzle 5, and uniform material discharge in all directions is ensured by discharging the material through the material distributing plate.
In this embodiment, in order to facilitate feeding into the lifting conveyor 1, one side of the lifting conveyor 1 is further provided with a hopper 15, and the hopper 15 is located at the feeding port of the lifting conveyor.
In this embodiment, in order to facilitate the pouring of the raw material into the hopper 15, the step 12 is provided on one side of the lifting conveyor 1, and in other equivalent embodiments, the hopper 15 and the lifting conveyor 1 may be designed to be sunk, so that the step 12 does not need to be provided aside.
In this embodiment, the support 9 is used to support the installation wind bin 8 and the ventilating bin 7.
In this embodiment, the lifting conveyor 1 is made of a soft material.
Example 2
Referring to fig. 3, this embodiment is a modified structure of embodiment 1, and in this embodiment, there are two air-permeable bins 7, and the two air-permeable bins 7 are parallel, and a material-dividing cone 6 is arranged above each air-permeable bin 7. The arrows in fig. 3 indicate the direction of the humid air during drying.
Example 3
A drying method of pecans needs to use the drying device as described in embodiment 1 or embodiment 2, the pecans are firstly put into a circulating feed pipe, then a lifting conveyor is started to enable the pecans to continuously circulate inside and outside a shell, then a centrifugal fan and a heat pump inner machine are started to continuously heat gas inside the shell, the temperature of the gas inside the shell is maintained within the range of 35-42 ℃, and the humidity of the gas inside the shell is maintained not to exceed 75% RH.
The above description is only a preferred embodiment of the present invention, and not intended to limit the scope of the present invention, which is defined by the claims and their equivalents, and can be directly or indirectly applied to other related fields of technology.

Claims (9)

1. The utility model provides a hickory nut dynamic cycle drying device, its characterized in that, is including ventilative feed bin, circulation inlet pipe, circulation discharging pipe and promotion conveyer, the circulation inlet pipe sets up in the circulation inlet port department of ventilative feed bin, the circulation discharging pipe sets up in the circulation outlet department of ventilative feed bin, it sets up between circulation discharging pipe and circulation inlet pipe to promote the conveyer, ventilative feed bin one side is provided with the heat pump internal unit, the one side that promotes the conveyer still is provided with the hopper and receives the material pipe, be provided with temperature sensor and humidity transducer in the ventilative feed bin.
2. The pecan dynamic circulation drying device of claim 1, further comprising a centrifugal fan, wherein the centrifugal fan is disposed on one side of the air permeable bin.
3. The pecan dynamic circulation drying device of claim 1, further comprising a wind bin disposed at one side of the air permeable bin.
4. The pecan dynamic circulation drying device of claim 1, wherein the air permeable bin is a funnel-shaped bin.
5. The pecan dynamic circulation drying device of claim 1, further comprising a housing, wherein the air permeable bin and the heat pump indoor unit are both located in the housing.
6. The pecan dynamic circulation drying device of claim 5, further comprising an air valve, wherein the air valve is mounted on the housing.
7. The pecan dynamic circulation drying device of claim 1, further comprising a material nozzle, wherein the material nozzle is mounted on the circulation feeding pipe.
8. The pecan dynamic circulation drying device of claim 7, wherein a material separating cone is arranged at a bin opening of the air permeable bin, and the material separating cone is positioned between the air permeable bin and the material nozzle.
9. The pecan dynamic cycle drying device of claim 1, wherein the number of the air-permeable bins is not less than 1.
CN202220117262.6U 2022-01-17 2022-01-17 Hickory nut dynamic circulation drying device Active CN216898278U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202220117262.6U CN216898278U (en) 2022-01-17 2022-01-17 Hickory nut dynamic circulation drying device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202220117262.6U CN216898278U (en) 2022-01-17 2022-01-17 Hickory nut dynamic circulation drying device

Publications (1)

Publication Number Publication Date
CN216898278U true CN216898278U (en) 2022-07-05

Family

ID=82213922

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202220117262.6U Active CN216898278U (en) 2022-01-17 2022-01-17 Hickory nut dynamic circulation drying device

Country Status (1)

Country Link
CN (1) CN216898278U (en)

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