CN205843317U - Direct-fired dehydrator - Google Patents

Direct-fired dehydrator Download PDF

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Publication number
CN205843317U
CN205843317U CN201620627387.8U CN201620627387U CN205843317U CN 205843317 U CN205843317 U CN 205843317U CN 201620627387 U CN201620627387 U CN 201620627387U CN 205843317 U CN205843317 U CN 205843317U
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China
Prior art keywords
mixing chamber
burning
burner
burning mixing
fired
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Active
Application number
CN201620627387.8U
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Chinese (zh)
Inventor
王吉远
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Dalian Boxin Equipment Processing Factory
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Dalian Boxin Equipment Processing Factory
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Application filed by Dalian Boxin Equipment Processing Factory filed Critical Dalian Boxin Equipment Processing Factory
Priority to CN201620627387.8U priority Critical patent/CN205843317U/en
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Publication of CN205843317U publication Critical patent/CN205843317U/en
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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
    • 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

Abstract

The utility model discloses a kind of direct-fired dehydrator, including drying materials room, blower fan (1), burning mixing chamber and burner (4), described burning mixing chamber includes shutter (2), waste heat air inlet (3), inner bag (5), burning hot blast changeover bobbin (6) and heat-insulation layer (7), burning mixing chamber two ends connecting fan (1) and burner (4) respectively, inner bag (5) is arranged on inside burning mixing chamber, heat-insulation layer (7) is arranged on outside burning mixing chamber, shutter (2) is arranged on the burning mixing chamber sidewall of burner (4) lateral location, waste heat air inlet (3) is arranged on the top of burning mixing chamber, burning hot blast changeover bobbin (6) is arranged on the inside of burning mixing chamber and is connected with burner (4).This utility model instead of original steam kettle Kiln seasoned tradition drying mode, decreases pollution environment, improves production capacity 30% than the original indirect drying mode using steam boiler, save the cost of drying simultaneously.

Description

Direct-fired dehydrator
Technical field
This utility model relates to dehydrator field, is specifically related to a kind of natural gas or the direct-fired drying of liquefied gas drying Machine.
Background technology
Existing Thallus Laminariae is dried and is used Boiler Steam drying and air stove drying, the steaming that i.e. steam boiler produces Vapour, becomes steam into condensed water by radiator, blows radiator with blower fan, and cold wind is become hot blast to carry out drying.
This drying mode has been used up how many years, and this drying mode there is the problem that 1, steam is by dissipating Hot device becomes the temperature of condensed water and is up to 80 spend more, and this part high temperature water reuse is limited;2, steam boiler is used to pollute ring Border;3, for drying, steam boiler is dried is heating indirectly, and the thermal efficiency reaches 70%-80%, adds the cost of product;4, make With steam boiler costly, such as maintenance expense, the electricity charge, water rate, fireman's expense etc..
Utility model content
Burned flame is changed into hot blast by the purpose of this utility model exactly, it is provided that the thermal source of drying, prevents burning Flame enters in material and is burnt out by material.
This utility model be the technical scheme is that to include drying materials room, blower fan 1, burning for achieving the above object Mixing chamber and burner 4, burning mixing chamber includes shutter 2, waste heat air inlet 3, inner bag 5, burning hot blast changeover bobbin 6 and insulation Layer 7, burning mixing chamber two ends connecting fan 1 and burner 4 respectively, inner bag 5 is arranged on inside burning mixing chamber, and heat-insulation layer 7 sets Putting outside burning mixing chamber, play heat insulation effect, shutter 2 is arranged on the burning mixing chamber side of burner 4 lateral location On wall, constantly increasing new empty wind toward burning mixing chamber, shutter 2 size is adjustable, it is ensured that dry intake, waste heat air inlet 3 tops being arranged on burning mixing chamber, return to burning mixing from drying materials room hot blast out again through waste heat air inlet 3 Room, burning hot blast changeover bobbin 6 is arranged on the inside of burning mixing chamber and is connected with burner 4, and burning hot blast changeover bobbin 6 is used for collecting Middle heat, makes burner 4 directly heat the air in burning hot blast changeover bobbin 6 and be directly sent directly into by hot blast by blower fan 1 Drying materials room, improves the thermal efficiency of burning blender.
The distance of described burner 4 and blower fan 1 is more than 900mm, enters drying materials room with fire resistant by blower fan 1 and lights Material.
The caloric value of described burner 4 is 400,000 kilocalories, and described burner 4 also includes temperature controller, and control mode is Two-stage nitration fire.
Described shutter 2 is two, and is separately positioned on the sidewall of burning mixing chamber of 4 liang of side positions of burner.
Heat-insulation layer 7 material is the aluminum silicate insulation material of heatproof.
Direct-fired dehydrator of the present utility model instead of original steam kettle Kiln seasoned tradition drying mode, decreases Pollute environment, and because using direct-fired drying mode, improve product than the original indirect drying mode using steam boiler Energy 30%, saves the cost of drying, as without boiler electricity, water, maintenance expense etc., it is not necessary to build boiler room simultaneously, it is not necessary to artificial Control, all realize automatization and dry.
Accompanying drawing explanation
Fig. 1 is the top view of direct-fired dehydrator of the present utility model.
Fig. 2 is the front view of burning hot blast changeover bobbin of the present utility model.
Fig. 3 is the left view of burning hot blast changeover bobbin of the present utility model.
In figure: blower fan 1;Shutter 2;Waste heat air inlet 3;Burner 4;Inner bag 5;Burning hot blast changeover bobbin 6;Heat-insulation layer 7.
Detailed description of the invention
As Figure 1-3, direct-fired dehydrator of the present utility model, including drying materials room, blower fan 1, burning mixing chamber With burner 4, burning mixing chamber includes shutter 2, waste heat air inlet 3, inner bag 5, burning hot blast changeover bobbin 6 and heat-insulation layer 7, combustion Burning mixing chamber two ends connecting fan 1 and burner 4 respectively, inner bag 5 is arranged on inside burning mixing chamber, and heat-insulation layer 7 is arranged on combustion Outside burning mixing chamber, playing heat insulation effect, shutter 2 is arranged on the burning mixing chamber sidewall of burner 4 lateral location, no Disconnected increases new empty wind toward burning mixing chamber, and shutter 2 size is adjustable, it is ensured that drying intake, waste heat air inlet 3 is arranged on The top of burning mixing chamber, returns to the mixing chamber that burns, burning from drying materials room hot blast out again through waste heat air inlet 3 Hot blast changeover bobbin 6 is arranged on the inside of burning mixing chamber and is connected with burner 4, and burning hot blast changeover bobbin 6 is used for concentrating heat, Burner 4 is made to directly heat the air in burning hot blast changeover bobbin 6 and directly by blower fan 1, hot blast is sent directly into drying materials Room, improves the thermal efficiency of burning blender.
The distance of described burner 4 and blower fan 1 is more than 900mm, enters drying materials room with fire resistant by blower fan 1 and lights Material.
The caloric value of described burner 4 is 400,000 kilocalories, and described burner 4 also includes temperature controller, and control mode is Two-stage nitration fire.
Described shutter 2 is two, and is separately positioned on the sidewall of burning mixing chamber of 4 liang of side positions of burner.
Heat-insulation layer 7 material is the aluminum silicate insulation material of heatproof.
Work process:
First, burner 4 is lighted a fire, and burner 4 burned flame becomes at burning mixing chamber through burning hot blast changeover bobbin 6 Hot blast, burning mixing chamber has two shutters 2, constantly increases new empty wind toward burning mixing chamber, is become by burning mixing chamber Become hot blast, finally by blower fan 1, the high-temperature hot-air of burning mixing chamber is delivered to drying materials room, material drying.
Burner 4 also sets up temperature controller, and temperature controller automatically controls burner 4 by the hot blast temperature detected Big fire and little fire, temperature controller sets upper and lower bound as required, automatically stops when the temperature detected reaches the upper limit Big fire, changes little fire into and burns away, and homogeneous temperature declines, and when temperature reaches lower limit, burner 4 lights big fire, temperature automatically Rising, until reaching the upper limit, so circulating work, it is ensured that drying materials.
During work, the outer surface of the heat-insulation layer 7 outside burning mixing chamber has not a particle of heat.
Advantage of the present utility model is as follows:
1, instead of original steam kettle Kiln seasoned tradition drying mode, decrease pollution environment;
2, because using direct-fired drying mode, production capacity is improved than the original indirect drying mode using steam boiler 30%;
3, the cost dried is saved, as without boiler electricity, water, maintenance expense etc., it is not necessary to build boiler room, it is not necessary to artificial Control, all realize automatization and dry.

Claims (4)

  1. The most direct-fired dehydrator, including drying materials room, blower fan (1), burning mixing chamber and burner (4), it is characterised in that: institute State burning mixing chamber and include shutter (2), waste heat air inlet (3), inner bag (5), burning hot blast changeover bobbin (6) and heat-insulation layer (7), Burning mixing chamber two ends connecting fan (1) and burner (4) respectively, inner bag (5) is arranged on inside burning mixing chamber, heat-insulation layer (7) being arranged on outside burning mixing chamber, shutter (2) is arranged on the sidewall of burning mixing chamber of burner (4) lateral location, Waste heat air inlet (3) is arranged on the top of burning mixing chamber, and burning hot blast changeover bobbin (6) is arranged on the inside of burning mixing chamber also It is connected with burner (4).
  2. The most direct-fired dehydrator, it is characterised in that: the distance of described burner (4) and blower fan (1) is big In 900mm.
  3. The most direct-fired dehydrator, it is characterised in that: the caloric value of described burner (4) is 400,000 big Card, described burner (4) also includes temperature controller, and control mode is two-stage nitration fire.
  4. The most direct-fired dehydrator, it is characterised in that: described shutter (2) is two, and is respectively provided with On the sidewall of the burning mixing chamber of burner (4) two side position.
CN201620627387.8U 2016-06-23 2016-06-23 Direct-fired dehydrator Active CN205843317U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620627387.8U CN205843317U (en) 2016-06-23 2016-06-23 Direct-fired dehydrator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620627387.8U CN205843317U (en) 2016-06-23 2016-06-23 Direct-fired dehydrator

Publications (1)

Publication Number Publication Date
CN205843317U true CN205843317U (en) 2016-12-28

Family

ID=58152718

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620627387.8U Active CN205843317U (en) 2016-06-23 2016-06-23 Direct-fired dehydrator

Country Status (1)

Country Link
CN (1) CN205843317U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112097502A (en) * 2020-09-22 2020-12-18 成都市和乐门业有限公司 Accurate temperature control mode of drying equipment heating system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112097502A (en) * 2020-09-22 2020-12-18 成都市和乐门业有限公司 Accurate temperature control mode of drying equipment heating system
CN112097502B (en) * 2020-09-22 2021-11-23 成都市和乐门业有限公司 Accurate temperature control method for heating system of drying equipment

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