CN2522808Y - Grain-drying machine - Google Patents

Grain-drying machine Download PDF

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Publication number
CN2522808Y
CN2522808Y CN 01273765 CN01273765U CN2522808Y CN 2522808 Y CN2522808 Y CN 2522808Y CN 01273765 CN01273765 CN 01273765 CN 01273765 U CN01273765 U CN 01273765U CN 2522808 Y CN2522808 Y CN 2522808Y
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CN
China
Prior art keywords
fluid bed
materials
elevator
fluidized bed
cooling tower
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
CN 01273765
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Chinese (zh)
Inventor
刘鹏立
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Individual
Original Assignee
Individual
Priority date (The priority date 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 date listed.)
Filing date
Publication date
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Priority to CN 01273765 priority Critical patent/CN2522808Y/en
Application granted granted Critical
Publication of CN2522808Y publication Critical patent/CN2522808Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

A grain-drying machine consists of a mill furnace (8) which generates hot air, a blower (13) which blows the hot air into a fluidized bed, a fluidized bed (10) in which the materials are heated to dry, a hoisting machine (11) which lifts the materials, a cooling tower (12) in which the materials are cooled, a waste material hoisting machine (9) which treats waste materials and a dustbin (7). The front end of the fluidized bed is provided with an adjustable baffle (1) which controls the material fluidization thickness during the material fluidization process and the bottom of the fluidized bed is provided with a fluidization supporting frame (2) which can adjust height. When the utility model is in use and the materials have different moistures, the material adjustable baffle can adjust the thickness of the materials on the fluidized bed to ensure the drying effect of the materials; meanwhile, the adjustment of a lifting device of the fluidized bed can change the flow speed of the materials on the fluidized bed so as to improve the drying effect.

Description

Foodstuff drying device
Technical field
The utility model relates to a kind of grain-drying equipment, particularly to flow-control and the current velocity controller of granular material in the fluidisation drying course, and the elevator charging, the improvement of the control device of the flow size of discharging.
Background technology
Present domestic cereal fluid bed since front end not baffled, the fluid bed punch-through takes place in material more easily, material more for a long time, drying materials is inhomogeneous.The fluid bed inclination angle is unadjustable in addition, has limited the raising of the production efficiency of fluid bed.Simultaneously, the control of fluidised bed material flow size is in the fluid bed internal regulation at present, is easy to generate the material clogging.
Summary of the invention
The utility model is not done change to the basic module formation of existing foodstuff drying device, just the structure of part assembly is improved.Specifically, a kind of foodstuff drying device, by the heating furnace (8) that produces hot blast, hot blast is blasted the blower fan (13) of fluid bed, material is subjected to the fluid bed (10) of heated drying therein, elevator (11) with the material lifting, the cooling tower that material cools off therein (12), waste material elevator (9) and the dustbin (7) of handling waste material constitute, the air outlet of heating furnace (8) is communicated with blower fan (13) and inserts fluid bed (10) air inlet, fluid bed (10) discharging opening links to each other with grain elevator (11), cooling tower (12) is positioned at grain elevator bottom, dustbin (7) is connected by refuse elevator (9) and fluid bed (10) air inlet top, it is provided with the adjustable baffle plate (1) that the goods fluid thickness of material in fluid mapper process is controlled at the fluid bed front end, in the fluid bed bottom fluid bed bracing frame (2) that can regulate height is set.
Import department at grain elevator (11) is provided with the control valve (4) of controlling the flow size, and the adjustable hyoplastron (3) of control material outlet flow velocity is set at discharge end.
The setting of fluidised bed material control device has realized flow (time of staying) and control fluid bed mounting inclination angle and the outlet ratio of control material on fluid bed, thereby increases the purpose of (or minimizing) material outlet flow velocity.The setting of the volume control device of elevator charging, discharging can be controlled the feed rate size, control material outlet flow velocity.Realized that respectively the elevator mass flow can be in harmonious proportion the fluidised bed material flow and can regulate, thereby made the use of two distinct devices reach coupling, reduced unnecessary energy resource consumption.
The wind wing (5) of blower fan (13) is short type.Adapted to blower fan and worked under 200 degree high temperature, its wind wing is designed to short type, guarantees that long-term work is indeformable, and mechanical transmission mechanism separates with volute of blower is heat insulation.
Radiating tube (6) on the cooling tower (12) is five jiaos of types, and heat exchange area is bigger, has increased the area that cold wind contacts with material, has improved radiating efficiency, has reduced cold and hot swap time.
The utility model when work, when the humidity of material not simultaneously, the material controllable register can be regulated the thickness of material on fluid bed, guarantees the drying effect of material; Simultaneously, the adjusting of fluid bed lowering or hoisting gear can change the flowing velocity of material on fluid bed, improves drying efficiency.The setting of elevator charging control valve can realize regulating arbitrarily feed rate, can guarantee reliably that the mass flow of fluid bed matches; The setting of hyoplastron is regulated in discharging, can improve discharging speed, has avoided the generation of elevator clogging, and the blower fan wind wing is designed to short type, can guarantee that it at high temperature works for a long time, and is indeformable.The pentagon radiating tube can increase cold and hot exchange area, reduces cold and hot swap time.
Description of drawings
Fig. 1 is the utility model structural representation.
Fig. 2 is the schematic diagram of fluid bed in the utility model.
Fig. 3 is the schematic diagram of controllable register in the utility model.
Fig. 4 is a fluid bed bracing frame schematic diagram in the utility model.
Fig. 5 is a grain elevator schematic diagram in the utility model.
Fig. 6 is the control valve schematic diagram on the grain elevator in the utility model.
Fig. 7 is the adjustable hyoplastron schematic diagram on the grain elevator in the utility model.
Fig. 8 is the wind wing schematic diagram on the blower fan in the utility model.
Fig. 9 is the side view of Fig. 8.
Figure 10 is the radiating tube sectional view on the cooling tower in the utility model.
Figure 11 is the schematic diagram of the radiating tube on the cooling tower in the utility model.
The specific embodiment
A kind of foodstuff drying device, its each assembly constitutes identical with existing fluidized bed type foodstuff drying device.Specifically, by the heating furnace 8 that produces hot blast, hot blast is blasted the blower fan 13 of fluid bed, material is subjected to the fluid bed 10 of heated drying therein, elevator 11 with the material lifting, the cooling tower 12 that material cools off therein, waste material elevator 9 and the dustbin 7 of handling waste material constitute, heating furnace 8 air outlets are communicated with blower fan 13 and insert fluid bed 10 air inlets, the discharging opening of fluid bed 10 links to each other with grain elevator 11, cooling tower 12 is positioned at grain elevator bottom, dustbin 7 is connected by refuse elevator 9 and fluid bed 10 air inlet tops, at the fluid bed front end the adjustable baffle plate 1 that the goods fluid thickness of material in fluid mapper process is controlled is set, the fluid bed bracing frame 2 that can regulate its height is set in the fluid bed bottom.Import department at grain elevator 11 is provided with the control valve 4 of controlling the flow size, and the adjustable hyoplastron 3 of control material outlet flow velocity is set at discharge end.The wind wing 5 of blower fan 13 is short type.Radiating tube 6 on the cooling tower 12 is five jiaos of types.Controllable register 1 in the utility model is identical with the structure of control valve 4, constitutes by a fixed head, a portable plate and two adjusting nuts, and the fluid bed bracing frame is that an adjusting screw(rod) and corresponding fixed mount constitute in fact.

Claims (4)

1, a kind of foodstuff drying device, by the heating furnace (8) that produces hot blast, hot blast is blasted the blower fan (13) of fluid bed, material is subjected to the fluid bed (10) of heated drying therein, elevator (11) with the material lifting, the cooling tower that material cools off therein (12), waste material elevator (9) and the dustbin (7) of handling waste material constitute, the air outlet of heating furnace (8) is communicated with blower fan (13) and inserts fluid bed (10) air inlet, fluid bed (10) discharging opening links to each other with grain elevator (11), cooling tower (12) is positioned at grain elevator bottom, dustbin (7) is connected by refuse elevator (9) and fluid bed (10) air inlet top, it is characterized in that the adjustable baffle plate (1) that the goods fluid thickness of material in fluid mapper process is controlled being set, the fluid bed bracing frame (2) that can regulate height is set in the fluid bed bottom at the fluid bed front end.
2, require 1 described foodstuff drying device according to the right profit, it is characterized in that being provided with the control valve (4) of control flow size, the adjustable hyoplastron (3) of control material outlet flow velocity is set at discharge end in the import department of grain elevator (11).
3, require 1 described foodstuff drying device according to the right profit, it is characterized in that the wind wing (5) of blower fan (13) is short type.
4, require 1 described foodstuff drying device according to the right profit, it is characterized in that the radiating tube (6) on the cooling tower (12) is five jiaos of types.
CN 01273765 2001-12-26 2001-12-26 Grain-drying machine Expired - Fee Related CN2522808Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 01273765 CN2522808Y (en) 2001-12-26 2001-12-26 Grain-drying machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 01273765 CN2522808Y (en) 2001-12-26 2001-12-26 Grain-drying machine

Publications (1)

Publication Number Publication Date
CN2522808Y true CN2522808Y (en) 2002-11-27

Family

ID=33678625

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 01273765 Expired - Fee Related CN2522808Y (en) 2001-12-26 2001-12-26 Grain-drying machine

Country Status (1)

Country Link
CN (1) CN2522808Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101806534A (en) * 2010-04-22 2010-08-18 山东天力干燥设备有限公司 Pulse combustion tail gas flow and overheat steam mixed drying system and process
CN101701763B (en) * 2009-11-24 2011-03-16 山东天力干燥设备有限公司 Positive-pressure combustion device and process thereof
CN104215038A (en) * 2014-08-26 2014-12-17 嘉兴石化有限公司 Fluidized drying method for PTA (purified terephthalic acid) wet material

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101701763B (en) * 2009-11-24 2011-03-16 山东天力干燥设备有限公司 Positive-pressure combustion device and process thereof
CN101806534A (en) * 2010-04-22 2010-08-18 山东天力干燥设备有限公司 Pulse combustion tail gas flow and overheat steam mixed drying system and process
CN104215038A (en) * 2014-08-26 2014-12-17 嘉兴石化有限公司 Fluidized drying method for PTA (purified terephthalic acid) wet material

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GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee