KR20160132624A - Down-Steream Infrared Conveyer type Dryer - Google Patents
Down-Steream Infrared Conveyer type Dryer Download PDFInfo
- Publication number
- KR20160132624A KR20160132624A KR1020150065407A KR20150065407A KR20160132624A KR 20160132624 A KR20160132624 A KR 20160132624A KR 1020150065407 A KR1020150065407 A KR 1020150065407A KR 20150065407 A KR20150065407 A KR 20150065407A KR 20160132624 A KR20160132624 A KR 20160132624A
- Authority
- KR
- South Korea
- Prior art keywords
- drying
- main body
- infrared ray
- heater
- air
- Prior art date
Links
- 238000001035 drying Methods 0.000 claims abstract description 141
- 239000000463 material Substances 0.000 claims abstract description 53
- 238000010438 heat treatment Methods 0.000 claims description 27
- 238000007664 blowing Methods 0.000 claims description 22
- 239000000919 ceramic Substances 0.000 claims description 14
- 238000005192 partition Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 9
- 238000007599 discharging Methods 0.000 claims description 3
- 239000002274 desiccant Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 238000003763 carbonization Methods 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 230000006866 deterioration Effects 0.000 description 4
- 229910052736 halogen Inorganic materials 0.000 description 4
- 150000002367 halogens Chemical class 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 240000004160 Capsicum annuum Species 0.000 description 2
- 235000008534 Capsicum annuum var annuum Nutrition 0.000 description 2
- 235000007862 Capsicum baccatum Nutrition 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 239000001728 capsicum frutescens Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 2
- 229910001092 metal group alloy Inorganic materials 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 238000002834 transmittance Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 240000008067 Cucumis sativus Species 0.000 description 1
- 235000010799 Cucumis sativus var sativus Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000000861 blow drying Methods 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 229930002875 chlorophyll Natural products 0.000 description 1
- 235000019804 chlorophyll Nutrition 0.000 description 1
- ATNHDLDRLWWWCB-AENOIHSZSA-M chlorophyll a Chemical compound C1([C@@H](C(=O)OC)C(=O)C2=C3C)=C2N2C3=CC(C(CC)=C3C)=[N+]4C3=CC3=C(C=C)C(C)=C5N3[Mg-2]42[N+]2=C1[C@@H](CCC(=O)OC\C=C(/C)CCC[C@H](C)CCC[C@H](C)CCCC(C)C)[C@H](C)C2=C5 ATNHDLDRLWWWCB-AENOIHSZSA-M 0.000 description 1
- 210000000078 claw Anatomy 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003205 fragrance Substances 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B3/00—Drying solid materials or objects by processes involving the application of heat
- F26B3/28—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun
- F26B3/30—Drying solid materials or objects by processes involving the application of heat by radiation, e.g. from the sun from infrared-emitting elements
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B17/00—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement
- F26B17/02—Machines or apparatus for drying materials in loose, plastic, or fluidised form, e.g. granules, staple fibres, with progressive movement with movement performed by belts carrying the materials; with movement performed by belts or elements attached to endless belts or chains propelling the materials over stationary surfaces
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Microbiology (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The present invention relates to an apparatus for continuously drying a downward airflow type infrared conveyor, in which an inlet (11) through which a desiccant (g) to be dried is introduced and a discharge port (12) A mesh conveyor installed inside the main body 10 for sequentially conveying the drying material g from the inlet port 11 to the outlet port 12, (10), the air sucked from the lower part of the main body (10) is supplied again from the upper side of the main body (10) so that the air flow (w) A downstream air flow circulating and drying means 40 for continuously circulating and supplying the air to pass through the mesh conveyor 20 from the upper side to the lower side, a near infrared ray and far infrared ray heat Apparatus (100); (1), characterized in that the drying apparatus (1) comprises a drying unit
Description
The present invention relates to an apparatus for continuously drying a downward airflow type infrared conveyor, in which an inlet (11) through which a desiccant (g) to be dried is introduced and a discharge port (12) A
When drying fruits, vegetables, etc. in a drying device for biological industry, a large part of the organic components (color, fragrance component, chlorophyll, etc.) of the material is lost during drying due to exposure to heat for a long time.
For this reason, a drying method capable of drying in a short time without raising the temperature of the drying material is required as one of the above solutions. As one example of conventional conveyor-type drying apparatuses currently used for this purpose, as in the "dry material dryer and method of drying a dry material using the same" in
However, in the case of this conventional embodiment, since the drying of the drying material is mostly accomplished by the blowing of the hot air, the drying material on the conveyor is increased when the supply speed of the hot air is increased in order to improve the drying speed, There is a problem that it is scattered and blown away.
Another conventional example is to improve the drying efficiency by installing a plurality of conveyors in the drying chamber and to install a far infrared ray heater on the conveyor with a dry heat source. However, But it was not enough to shorten the drying time.
On the other hand, in order to shorten the drying time in a conveyor-type dryer such as a red pepper dryer, a method of shortening the drying time by providing a separate preheater or the like at the tip of the dryer is used. However, Organic properties have been destroyed.
For this reason, there is a demand for a dryer that can dry in a short period of time without raising the temperature of the material to a certain level or more.
The present invention has been made to solve the above-mentioned problems of the prior art, and it is an object of the present invention to provide a method and apparatus for efficiently drying and drying continuously the interior of a desiccant to be dried even at a relatively low temperature at which carbonization or deterioration does not occur using a near- And to provide an apparatus for continuously drying a downflow air type infrared ray conveyor.
In the state where the drying material is stably fixed to the conveyor by the hot wind descending air stream passing from the upper side to the lower side through the drying material, the drying material is lowered by the airflow passing through the narrow space between the drying materials, And an object of the present invention is to provide a continuous drying apparatus of a descending air flow type infrared ray conveyor capable of rapidly discharging water vapor generated by heating in a drying material by pressure, thereby enabling quick and efficient drying.
A further object of the present invention is to provide a continuous drying apparatus for a downward air flow type infrared ray conveyor which is partitioned by a partition wall to provide a drying environment optimized for each stage during drying by controlling the amount of heating and the amount of air blowing I will do it.
In order to accomplish the above object, the apparatus for continuously drying a descending air flow type infrared ray conveyor according to the present invention comprises an
The
The downward airflow circulating and drying means 40 includes an
The near infrared ray and far infrared
The temperature of the hot air circulating through each of the drying chambers is measured by a temperature sensor (not shown) provided in a pipe connecting the
According to the present invention, there is an advantage that it is possible to efficiently heat the inside of a drying material to be dried and continuously dry even at a relatively low temperature at which carbonization or deterioration does not occur using a near infrared ray and far infrared ray heating apparatus.
In the state where the drying material is stably fixed to the conveyor by the hot wind descending air stream passing from the upper side to the lower side through the drying material, the drying material is lowered by the airflow passing through the narrow space between the drying materials, The steam generated by the heating in the drying material can be quickly discharged by the pressure, which makes it possible to dry more quickly and efficiently.
Meanwhile, since the inside of the main body is partitioned by the partition walls, the heating amount and the blowing amount for each drying chamber can be controlled to provide an optimal drying environment for each stage during drying.
1 is a front sectional view schematically showing the entire configuration of a continuous drying apparatus according to an embodiment of the present invention;
2 is a side sectional schematic view showing a blowing configuration of a continuous drying apparatus according to an embodiment of the present invention;
3 is a schematic diagram showing a blow drying structure of a continuous drying apparatus according to an embodiment of the present invention.
4 is a top view of a near-infrared and far-infrared heating apparatus of a continuous drying apparatus according to an embodiment of the present invention.
5 is a cross-sectional view of a near-infrared and far-infrared heat generating apparatus of a continuous drying apparatus according to an embodiment of the present invention.
Fig. 6 is a view showing a structure of a heater mounting base and a reflection plate of a near-infrared and far-infrared heating apparatus of a continuous drying apparatus according to an embodiment of the present invention.
7 is a cross-sectional view showing the operation of a near-infrared and far-infrared heating apparatus of a continuous drying apparatus according to an embodiment of the present invention;
8 is a graph showing the infrared transmission characteristics of a ceramic filter plate of a near-infrared and far-infrared heat generating apparatus of a continuous drying apparatus according to an embodiment of the present invention.
Hereinafter, a descending airflow type infrared conveyor continuous drying apparatus according to an embodiment of the present invention will be described in detail with reference to the accompanying drawings. First, it should be noted that, in the drawings, the same components or parts are denoted by the same reference numerals whenever possible. In describing the present invention, a detailed description of known functions and configurations incorporated herein will be omitted so as to avoid obscuring the subject matter of the present invention.
1, the descending airflow type infrared conveyor continuous drying apparatus of the present invention includes a
First, the
Next, the
Next, the descending airflow circulating and drying means 40 will be described. As shown in Figs. 1 and 2, the downward airflow circulating and drying means 40 supplies the air sucked from the lower portion of the
The embodiment of implementing the downward airflow circulating and drying means 40 having such a function can be applied to a wide variety of embodiments. However, the drying material g may have a property of being mounted on the
Next, the near-infrared and far-infrared
As shown in FIGS. 4 and 5, the near infrared ray and far-infrared
First, the
Next, the
Next, the heater means 130 will be described. As shown in FIGS. 5 and 6, the
Meanwhile, the
Next, the
Next, the
As shown in FIG. 8, the
In the case where the heater means 130 emits radiant heat of various wavelengths according to the characteristics thereof and the heater means 130 includes any one of a halogen lamp and a carbon heater as described above, When the supply is increased, the wavelength of the near infrared region is outputted. Therefore, in order to maintain the emission state of the far infrared ray which is advantageous for the deep penetration of the material to be dried due to the long wavelength, it is necessary to reduce the amount of current, and when the amount of current decreases, the amount of heat required for drying is insufficient.
Therefore, in order to solve this problem, in the present invention, a plurality of the heater means 130 (halogen lamp or carbon heater) is used to supply an amount of heat suitable for drying even at a low current amount, So that a large amount of heat necessary for drying can be supplied while maintaining the wavelength.
On the other hand, in accordance with the change in the absorption wavelength band depending on the color or the characteristic of the drying material (for example, in the case of red red pepper and in the case of blue cucumber, there is a difference in the wavelength of infrared rays to be absorbed) It is also possible to control the wavelength distribution of infrared rays generated by the heater means 130 when adjusting the amount of current supplied to the
In the meantime, when a normal operating current is supplied to the heater means 130, about 80% of heat is generated in the form of infrared rays, and heat of about 20% is generated in the wavelength range other than infrared rays. Heat is concentrated on the surface of the drying material, which causes the surface of the drying material to overheat, thereby deteriorating the drying quality. In this case, as shown in FIG. 8, the
Accordingly, even a heat source of a short wavelength (for example, a visible ray or an ultraviolet ray) having a low transmittance due to a temperature rise is eventually released as heat of a far infrared ray wavelength band. Therefore, most of the generated heat is converted into infrared ray (near infrared ray to far infrared ray) (Near infrared rays to far infrared ray) having a high permeability is used as a heat source, and the temperature difference between the surface and the inside of the drying material is slightly heated to rapidly activate the internal moisture, thereby improving the efficiency of the dryer .
5, the
1, the
With this configuration, it is possible to provide a compartment in which strong heat is given when the temperature of the drying material (g) is low at the beginning of drying, a compartment for supplying only the heat necessary for maintaining a moderate moisture activity when the temperature of the drying material reaches the water activation temperature, It becomes possible to constitute a compartment in which the drying material gives a weak heat for moisture balance at the time when the drying is completed. The larger the number of such compartments, the more precise and finer the drying operation can be efficiently performed. In this case, the temperature of each of the drying chambers is controlled by the
Hereinafter, a drying operation process by a descending air flow of the descending airflow type infrared ray conveyor
As shown in FIG. 2, the descending airflow type infrared conveyor
On the other hand, the airflow w prevents overheating of the upper side of the drying material g due to heat radiated from the near-infrared rays and the far-infrared
In the foregoing, optimal embodiments have been disclosed in the drawings and specification. Although specific terms have been employed herein, they are used for purposes of illustration only and are not intended to limit the scope of the invention as defined in the claims or the claims. Therefore, those skilled in the art will appreciate that various modifications and equivalent embodiments are possible without departing from the scope of the present invention. Accordingly, the true scope of the present invention should be determined by the technical idea of the appended claims.
g: Dry material w: Air flow
s: Space between dry materials v: Water vapor
1: Downflow type infrared conveyor continuous drying device
10: Body
11: inlet 12: outlet
15: first drying chamber 16: second drying chamber
17: third drying chamber 18: fourth drying chamber
20: Mesh conveyor
30: first partition 31: first passage
32: second partition wall 33: second passage hole
34: third partition wall 34: third passage hole
40: Downflow air circulation drying means
41: inlet port 42: blowing means
43: Tuyere
100: near-infrared and far-infrared heating device
110: Case 111:
120: heater mounting base 121: heater mounting plate
122: heater mounting groove 123: heater mounting portion
124:
130: heater means 131:
132: terminal portion
140: reflector 141: heater fixing portion
150: ceramic filter plate 151: filter plate bonding member
160: cover
170: cooling means
Claims (5)
A mesh conveyor 20 installed inside the main body 10 for sequentially transferring the drying material g from the inlet 11 to the outlet 12 and transferring the drying material g;
The air sucked from the lower part of the main body 10 is supplied from the upper side of the main body 10 so that the air flow w is supplied to the drying material g and the mesh conveyor (40) which continuously circulates and supplies the air to the lower portion (20) so as to pass from the upper side to the lower side;
A near infrared ray and far infrared ray heating apparatus 100 installed on the upper side of the main body 10; (1) according to claim 1 or 2, characterized in that the lowering air flow type infrared ray conveyor continuous drying apparatus (1) comprises a lower airflow type infrared ray conveyor continuous drying apparatus (1).
The main body 10 has, inside thereof,
At least one partition wall having a through hole through which the mesh conveyor 20 can pass is provided and is partitioned into a plurality of drying chambers by the partition wall,
Wherein the lower airflow circulating and drying means (40) and the near infrared ray and far infrared ray heating apparatus (100) are installed to operate independently in each of the drying chambers, respectively. .
The downward airflow circulating and drying means (40)
An inlet port 41 for sucking air from a lower side surface of the main body 10 located below the mesh conveyor 20;
A blowing means (42) for circulating and driving the air sucked from the suction port (41);
A blowing port (43) for supplying the air supplied from the blowing means (42) to the upper surface of the main body (10); (1), characterized in that it further comprises:
The near infrared ray and far-infrared ray heating apparatus (100)
A case 110 having an opening 111 formed at a lower portion thereof;
A heater mounting plate 121 formed on both sides of the case 110 and having a plurality of heater mounting grooves 122 formed on the inner lower side of the case 110,
Heater means (130) inserted between the heater mounting grooves (122) facing each other on both sides and discharging heat according to the supplied current;
A reflector 140 installed on the heater mounting base 120 and reflecting the heat radiated from the heater 130;
A ceramic filter plate 150 installed in the opening 111 to pass only far-infrared rays or near-infrared rays of heat radiated from the heater unit 130 and emit far-infrared rays according to their natural frequencies; (1) according to claim 1, characterized in that the lowering air flow type infrared ray conveyor continuous drying apparatus (1) comprises:
The temperature of the hot air circulating through each of the drying chambers is measured by a temperature sensor (not shown) provided in the piping connecting the inlet port 41 with the blowing means 42 and the blowing port 43 (1).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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KR1020150065407A KR20160132624A (en) | 2015-05-11 | 2015-05-11 | Down-Steream Infrared Conveyer type Dryer |
Applications Claiming Priority (1)
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KR1020150065407A KR20160132624A (en) | 2015-05-11 | 2015-05-11 | Down-Steream Infrared Conveyer type Dryer |
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Publication Number | Publication Date |
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KR20160132624A true KR20160132624A (en) | 2016-11-21 |
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KR1020150065407A KR20160132624A (en) | 2015-05-11 | 2015-05-11 | Down-Steream Infrared Conveyer type Dryer |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017195922A1 (en) * | 2016-05-13 | 2017-11-16 | 장태균 | Descending air current type infrared ray conveyor continuous drying apparatus |
KR102049270B1 (en) * | 2018-05-31 | 2019-12-04 | (주)그린파즈 | A pest control device |
RU196179U1 (en) * | 2019-08-19 | 2020-02-19 | Общество с ограниченной ответственностью "ГРАТОН-СК" (ООО "ГРАТОН-СК") | FURNACE FOR DRYING A COVER ON GLASS |
CN114365866A (en) * | 2022-01-25 | 2022-04-19 | 红云红河烟草(集团)有限责任公司 | Sheet type cut tobacco dryer capable of improving dewatering efficiency |
KR102402003B1 (en) * | 2021-04-06 | 2022-06-28 | 농업회사법인 주식회사 자연터 | Near-infrared type food drying device |
KR102457187B1 (en) | 2022-08-09 | 2022-10-20 | 서명수 | Forced convection type tunnel dryer |
KR20220167019A (en) * | 2021-06-11 | 2022-12-20 | 주식회사 더원리빙 | Odor exhaust device with drying function and temperature measurement function |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR960013214A (en) | 1994-10-31 | 1996-05-22 | 정태현 | Grain Dryer and Grain Drying Method |
-
2015
- 2015-05-11 KR KR1020150065407A patent/KR20160132624A/en active Search and Examination
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR960013214A (en) | 1994-10-31 | 1996-05-22 | 정태현 | Grain Dryer and Grain Drying Method |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017195922A1 (en) * | 2016-05-13 | 2017-11-16 | 장태균 | Descending air current type infrared ray conveyor continuous drying apparatus |
KR102049270B1 (en) * | 2018-05-31 | 2019-12-04 | (주)그린파즈 | A pest control device |
RU196179U1 (en) * | 2019-08-19 | 2020-02-19 | Общество с ограниченной ответственностью "ГРАТОН-СК" (ООО "ГРАТОН-СК") | FURNACE FOR DRYING A COVER ON GLASS |
KR102402003B1 (en) * | 2021-04-06 | 2022-06-28 | 농업회사법인 주식회사 자연터 | Near-infrared type food drying device |
KR20220167019A (en) * | 2021-06-11 | 2022-12-20 | 주식회사 더원리빙 | Odor exhaust device with drying function and temperature measurement function |
CN114365866A (en) * | 2022-01-25 | 2022-04-19 | 红云红河烟草(集团)有限责任公司 | Sheet type cut tobacco dryer capable of improving dewatering efficiency |
KR102457187B1 (en) | 2022-08-09 | 2022-10-20 | 서명수 | Forced convection type tunnel dryer |
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