CN203744696U - Tunnel type drier with preheating warming structure - Google Patents

Tunnel type drier with preheating warming structure Download PDF

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Publication number
CN203744696U
CN203744696U CN201420052108.0U CN201420052108U CN203744696U CN 203744696 U CN203744696 U CN 203744696U CN 201420052108 U CN201420052108 U CN 201420052108U CN 203744696 U CN203744696 U CN 203744696U
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CN
China
Prior art keywords
heat exchanger
kiln body
airduct
drying
drying kiln
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201420052108.0U
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Chinese (zh)
Inventor
何晓鹏
赵玉强
刘清
师建芳
邵广
娄正
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Chinese Academy of Agricultural Engineering CAAE
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Chinese Academy of Agricultural Engineering CAAE
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Priority to CN201420052108.0U priority Critical patent/CN203744696U/en
Application granted granted Critical
Publication of CN203744696U publication Critical patent/CN203744696U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • 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
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

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  • Drying Of Solid Materials (AREA)

Abstract

A tunnel type drier with a preheating warming structure comprises a hot air stove (1) and a drying kiln body (11) which is connected with the hot air stove (1) through a hot air duct (3). A section of heat exchanger (8) is arranged in the inlet end of the drying kiln body (11), and a smoke outlet of the hot air stove (1) is communicated with the heat exchanger (8) through a smoke guide fan (4). The tunnel type drier with the preheating warming structure has the advantages that the drying characteristic requirements of large particle nut materials are met, the drying efficiency of the large particle nut materials is improved, smoke waste heat is fully utilized, and thus energy is saved.

Description

A kind of tunnel drier that heats structure with preheating
Technical field
The utility model relates to the tunnel-kiln type drying machine structure that a kind of preheating heats, and is specifically related to a kind of tunnel drier, and this machine can be widely used in the large grain of agricultural product nut dries (for example: the larger materials of the gradation of moisture such as walnut, chestnut, peanut).The utility model belongs to Drying Technology of Agriculture Products field.
Background technology
In tunnel cave drying system, current common way is one end air intake, other end air-out, or following current, or adverse current, and above way is fine to the drying effect of general vegetables, edible mushroom, but this mode is but very low to drying nut efficiency.If adopt two ends air intake mode, higher to heat source system configuration requirement, should not realize, and increase larger cost.The dry feature of large grain nut is that the preheat temperature of nut inside just starts from inner hydrofuge while rising to 45~52 DEG C, and excess Temperature will affect materials quality, and it's the end is past temperature will make prolongation drying time.The drying efficiency of drying nut if improve must be promoted to 45~52 DEG C by material internal temperature as early as possible, carries out afterwards heated-air drying again.
Summary of the invention
The utility model for overcoming the above problems adopted technical scheme is:
A kind of tunnel drier that heats structure with preheating comprises hot-blast stove 1, the drying kiln body 11 being connected with described hot-blast stove 1 by warm-air pipe 3, in the arrival end of described drying kiln body 11, be provided with one section of heat exchanger 8, the exhaust opening of described hot-blast stove 1 is connected with described heat exchanger 8 by drawing cigarette blower fan 4.
Above-mentioned heats in the tunnel drier of structure with preheating, and described heat exchanger 8 is for being located at the heat exchanger of both sides band heat exchange fin in 5~7 meters of length of drying kiln body 11 entrance.
Above-mentioned heats in the tunnel drier of structure with preheating, the described cigarette blower fan 4 that draws is connected with a sootfall case 6 by airduct I 5, the outlet of this sootfall case 6 is connected with described heat exchanger 8 by airduct II 7, connected in series or in parallel by airduct III 9 between heat exchanger 8, heat exchanger 8 is communicated with chimney 10.
Above-mentioned heats in the tunnel drier of structure with preheating, and described hot-blast stove 1 is provided with air blast 2 and warm-air pipe 3, and the other end of this warm-air pipe 3 is connected with the air intake of drying kiln body 11, and described drying kiln body 11 is provided with side door 12.
Above-mentioned heats in the tunnel drier of structure with preheating, described warm-air pipe 3, and airduct I 5, sootfall case 6 and airduct II 7 are all incubated, and they are all with lagging facility, to reduce heat loss.
The beneficial effects of the utility model are: meet bulky grain nut drying materials characteristic, improved the drying efficiency of bulky grain nut material, take full advantage of fume afterheat, saved the energy.
Brief description of the drawings
Below in conjunction with drawings and Examples, the utility model is further illustrated.
Accompanying drawing 1 is main TV structure schematic diagram of the present utility model;
Accompanying drawing 2 is plan structure schematic diagram of the present utility model;
Accompanying drawing 3 is left TV structure schematic diagram of the present utility model.
In above accompanying drawing: 1. hot-blast stove, 2. air blast, 3. warm-air pipe, 4. draw cigarette blower fan, 5. airduct I, 6. sootfall case, 7. airduct 2,8. heat exchanger, 9. airduct III, 10. chimney, 11. drying kiln bodies, 12. side doors.
Detailed description of the invention
As shown in Figure 1, this tunnel drier that heats structure with preheating by hot-blast stove 1, air blast 2, warm-air pipe 3, draw cigarette blower fan 4, airduct I 5, sootfall case 6, airduct II 7, heat exchanger 8, airduct III 9, chimney 10, drying kiln body 11, side door 12 and form.In the present embodiment, hot-blast stove 1 is indirect coal-fired hot-blast stove, and the thermal source that it is this dryer provides uniform temperature a certain amount of hot-air, and hot-air is sent into drying kiln body one end through warm-air pipe 3 under the effect of air blast 2.The flue gas of indirect coal-fired hot-blast stove blasts sootfall case 6 through the effect of drawing cigarette blower fan 4 by airduct I 5, flue gas after sootfall enters heat exchanger 8 by airduct II 7, the heat exchanger 8 of multi-group heat exchange fin is realized serial or parallel connection by airduct III 9, and flue gas goes out heat exchanger 8 and enters chimney 10 and discharge.
Heat exchanger 8 with heat exchange fin is installed entering length drying kiln body 11 interior both sides, 5~7 meters of car one end, in heat exchanger 8, pass into flue gas, through heat exchange, make the space of 5~7 meters long of feed ends form the preheating section of 50~70 DEG C of temperature environments, material, this section heated intensification rapidly, was warming up to 45~52 DEG C at 5~6 hours by material.Temperature of charge rises to 45~52 DEG C of heels and pushes the heated-air drying section of drying kiln body 11 with drying car.
Air enters from the air intake of drying kiln body 11 through the air blast 2, the burner hearth of indirect coal-fired hot-blast stove, the warm-air pipe 3 that are positioned at indirect coal-fired hot-blast stove top, the B direction from drying kiln body 11 side door 12(Fig. 2) discharge.
Dry car and enter from A mouth, go out from C mouth.Drying car normally moves according to material situation.
The utility model adopts mounting heat exchanger on 5~7 meters of inner side walls of feed end drying kiln body, passes into flue gas in heat exchanger, through heat exchange, makes the space of 5~7 meters long of feed ends form the temperature field of 50~70 DEG C, by rapid material heat temperature raising.Material was warming up to 45~52 DEG C at preheating section through 5~6 hours, and now material starts a large amount of hydrofuges.Afterwards, material is followed baking car and is continued to push ahead, and enters the ventilation drying section of drying kiln body, dries, until by drying materials under 40~60 DEG C of wind-warm syndrome states.
The above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art; do not departing under the prerequisite of the utility model know-why; can also make some improvements and modifications, these improvements and modifications also should be considered as protection domain of the present utility model.

Claims (5)

1. one kind heats the tunnel drier of structure with preheating, it is characterized in that, comprise hot-blast stove (1), the drying kiln body (11) being connected with described hot-blast stove (1) by warm-air pipe (3), in the arrival end of described drying kiln body (11), be provided with one section of heat exchanger (8), the exhaust opening of described hot-blast stove (1) is connected with described heat exchanger (8) by drawing cigarette blower fan (4); The described cigarette blower fan (4) that draws is connected with a sootfall case (6) by airduct I (5), the outlet of this sootfall case (6) is connected with described heat exchanger (8) by airduct II (7), connected in series or in parallel by airduct III (9) between heat exchanger (8), heat exchanger (8) is communicated with chimney (10).
2. the tunnel drier that heats structure with preheating according to claim 1, is characterized in that, described heat exchanger (8) is for being located at the heat exchanger of both sides band heat exchange fin in 5~7 meters of length of drying kiln body (11) entrance.
3. the tunnel drier that heats structure with preheating according to claim 1 and 2, it is characterized in that, described hot-blast stove (1) is provided with air blast (2) and warm-air pipe (3), the other end of this warm-air pipe (3) is connected with the air intake of drying kiln body (11), and described drying kiln body (11) is provided with side door (12).
4. the tunnel drier that heats structure with preheating according to claim 1 and 2, is characterized in that, described airduct I (5), and sootfall case (6) and airduct II (7) are all with lagging facility.
5. the tunnel drier that heats structure with preheating according to claim 3, is characterized in that, described warm-air pipe (3) is with lagging facility.
CN201420052108.0U 2014-01-27 2014-01-27 Tunnel type drier with preheating warming structure Expired - Fee Related CN203744696U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420052108.0U CN203744696U (en) 2014-01-27 2014-01-27 Tunnel type drier with preheating warming structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420052108.0U CN203744696U (en) 2014-01-27 2014-01-27 Tunnel type drier with preheating warming structure

Publications (1)

Publication Number Publication Date
CN203744696U true CN203744696U (en) 2014-07-30

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Application Number Title Priority Date Filing Date
CN201420052108.0U Expired - Fee Related CN203744696U (en) 2014-01-27 2014-01-27 Tunnel type drier with preheating warming structure

Country Status (1)

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CN (1) CN203744696U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105865179A (en) * 2016-05-31 2016-08-17 浙江力泰炉窑科技有限公司 Hot air drying kiln for non-dismantling heat insulation formworks
CN113983811A (en) * 2021-10-19 2022-01-28 江苏高克锈机械有限公司 Integrated intelligent curing oven
CN117870282A (en) * 2023-02-24 2024-04-12 吉林省久仙草农副产品加工有限责任公司 Low-temperature continuous drying processing method for improving quality of schisandra chinensis

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105865179A (en) * 2016-05-31 2016-08-17 浙江力泰炉窑科技有限公司 Hot air drying kiln for non-dismantling heat insulation formworks
CN113983811A (en) * 2021-10-19 2022-01-28 江苏高克锈机械有限公司 Integrated intelligent curing oven
CN117870282A (en) * 2023-02-24 2024-04-12 吉林省久仙草农副产品加工有限责任公司 Low-temperature continuous drying processing method for improving quality of schisandra chinensis

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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: 20140730

Termination date: 20150127

EXPY Termination of patent right or utility model