CN2238406Y - Fluidization microboiling drier - Google Patents

Fluidization microboiling drier Download PDF

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Publication number
CN2238406Y
CN2238406Y CN 94207707 CN94207707U CN2238406Y CN 2238406 Y CN2238406 Y CN 2238406Y CN 94207707 CN94207707 CN 94207707 CN 94207707 U CN94207707 U CN 94207707U CN 2238406 Y CN2238406 Y CN 2238406Y
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CN
China
Prior art keywords
fluidization
precipitator
drying machine
dust
drier
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 94207707
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Chinese (zh)
Inventor
赵介山
吴斌
贺新亚
吴玲娥
张文明
Original Assignee
黄有丰
贺新亚
卢满松
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
Application filed by 黄有丰, 贺新亚, 卢满松 filed Critical 黄有丰
Priority to CN 94207707 priority Critical patent/CN2238406Y/en
Application granted granted Critical
Publication of CN2238406Y publication Critical patent/CN2238406Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a fluidization micro-boiling drier, which is mainly composed of a fluidization boiling furnace and a fluidization micro-boiling vibration drier. The spring link and the drive link of the drier are both arranged on the outside of a casing. An ash collecting bucket and a secondary dust collector are additionally arranged on the utility model. The driving of the complete machine is steady and reliable. The drier can be used in cement mill for drying raw material of clay soil and slag, etc. The heat efficiency arrives 75% to 85%, and the dust-collecting efficiency arrives 99%.

Description

The little boiled bed dryer of fluidization
The utility model is to belong to the component invention of flue gas fluidized bed furnace and vibration drying machine and the improvement of structure thereof.This machine is applied to the oven dry of raw materials such as cement industry clay, slag, in order to the calcining of cement kiln.
The dryer assembly of prior art cement raw material has following several:
1. hand burns formula hot-blast stove and the assembly of swinging rotary drum dryer;
2. high-temperature flue gas stove and the assembly of swinging rotary drum dryer;
3. high-temperature flue gas stove and the assembly of vibration drying machine.
Above-mentioned three kinds of assembly are reflection technical development processes, but existing high-temperature flue gas stove has two smoke chambers of U type, and the hot-fluid resistance is big, hot heterodyne, all in casing, parts are very fragile under the high temperature running for the drive disk assembly of vibration drying machine again, often be out of order, so dryer efficient is not high.
The purpose of this utility model is to adopt fluidized bed furnace and the assembly of vibration drying machine, with the raising thermal efficiency, and vibration drying machine driving member is done significant improvement.
Content of the present utility model is:
The little boiled bed dryer general construction of fluidization as shown in Figure 1, having 17 parts forms, it is mainly linked to each other with electric and magnetic oscillation feeding machine 2 by the wet feed storehouse 1 at top, divide into belt weigher 3, the tremie pipe 6 of scale and the exhanst gas outlet of fluidization fluidized bed furnace 4 all link to each other with vibration drying machine 7, blast pipe 13 1 ends are connected with vibration drying machine 7 tops, the other end and one-level cyclone type dust-precipitator 14 join, material conveyor 11 all joins with hopper 10 and one-level cyclone type dust-precipitator 14, and feature of the present utility model is:
(1) this machine adopts fluidization fluidized bed furnace 4 to be connected assembly with vibration drying machine 7;
(2) this fluidization fluidized bed furnace 4 is that the improvement of high-temperature flue gas stove is made up of combustion chamber and smoke chamber two parts, and is simple in structure;
(3) this vibration dryer 7 as shown in Figure 4, its spring link 20, kinematic link 23 all is assembled on the main shaft 25 that extends to outside the body fuselage 19, buncher 21 also is contained in outside the casing, the material of the comb bed 22 in the casing adopts heat resisting steel, its mounted angle is controlled at the 9.5-13 degree, makes the bed operation in the best condition of combing;
(4) body of vibration drying machine 7 is divided into 6 flue-dust retainers 8, has all adorned two-door turnover panel lock wind unloading valve 9 in each bucket, leaks out to reduce complete machine, and each end of struggling against all joins with material conveyor 11;
(5) this machine has been set up the secondary resistive connection and is revealed vertical electrostatic precipitator 15 or resistive connection and reveal bag filter 16 (selected according to using field condition), to improve dust-collecting efficiency, the secondary dust-precipitator is suitable for reading to link to each other with exhaust blower 17, middle mouthful links to each other with one-level cyclone type dust-precipitator 14, and end opening links to each other with material conveyor 11.
Advantage of the present utility model:
1. the best assembly of thermal source and dryer, the thermal efficiency that makes dryer system are brought up to about 75--85% from 40%, and can utilize lower calorific value fuel and industrial residues such as colm, gangue, flyash;
2. after increasing the secondary dust-precipitator, its dust-collecting efficiency is about 99%;
3. the dryer transmission is stable, reliable, and assurance equipment is running rate under hot state.
The utility model description of drawings:
Fig. 1 is that the little boiled bed dryer of fluidization is always schemed;
Fig. 2 is the fluidization fluidized bed furnace;
Fig. 3 is the utility model vibration drying machine;
Fig. 4 is this vibration dryer running part A-A cutaway view;
Embodiment:
In second cement plant, Zunhua City, Hebei province oven dry shop applications, concrete structure is configured to the utility model as shown in Figure 1: wet feed storehouse 1, electric and magnetic oscillation feeding machine 2, belt weigher 3, fluidization fluidized bed furnace 4, combustion chamber air blast 5, tremie pipe 6, vibration drying machine 7, flue-dust retainer 8, two-door turnover panel lock wind unloading valve 9, hopper 10, material conveyor 11, butterfly valve 12, blast pipe 13, one-level cyclone type dust-precipitator 14, secondary resistive connection reveal vertical electrostatic precipitator 15, the secondary resistive connection reveals bag filter 16, exhaust blower 17.The structure of this fluidization fluidized bed furnace 4 is pressed Fig. 2 configuration.The structure of this vibration dryer 7 is pressed Fig. 3 and Fig. 4 configuration, shown in the figure: hot blast import 18, casing 19, spring link 20, buncher 21, comb bed 22, kinematic link 23, feed opening 24 (material bin), main shaft 25.Its secondary dust-precipitator adopts resistive connection to reveal bag filter.

Claims (2)

1. little boiled bed dryer of fluidization, it is linked to each other with electric and magnetic oscillation feeding machine 2 by the wet feed storehouse 1 at top, divide into belt weigher 3, the tremie pipe 6 of scale and the exhanst gas outlet of fluidization fluidized bed furnace 4 all join with vibration drying machine 7, blast pipe 13 1 ends are connected with vibration drying machine 7 tops, the other end and one-level cyclone type dust-precipitator 14 join, and material conveyor 11 all joins with hopper 10 and one-level cyclone type dust-precipitator, and feature of the present utility model is:
(1) this fluidization fluidized bed furnace 4 is made up of combustion chamber and smoke chamber two parts;
(2) spring link 20 of this vibration dryer, kinematic link 23 all are assembled on the main shaft 25 that extends to outside the casing 19, and buncher 21 also is contained in outside the casing, and comb bed 22 materials in the casing adopt heat resisting steel, and its mounted angle is controlled at the 9.5--13 degree;
(3) body of vibration drying machine 7 is divided into 6 flue-dust retainers 8, has all adorned two-door turnover panel lock wind unloading valve 9 in each bucket, and each end of struggling against all joins with material conveyor 11;
(4) this machine has been set up the secondary resistive connection and is revealed vertical electrostatic precipitator 15 or resistive connection and reveal bag filter 16, and the secondary dust-precipitator is suitable for reading to link to each other with exhaust blower 17, and middle mouth links to each other with one-level cyclone type dust-precipitator 14, and end opening links to each other with material conveyor 11.
2. vibration drying machine 7 according to claim 1 is characterized in that: bed 22 materials of combing adopt heat resisting steel, and its setting angle is the 9.5--13 degree.
CN 94207707 1994-04-09 1994-04-09 Fluidization microboiling drier Expired - Fee Related CN2238406Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 94207707 CN2238406Y (en) 1994-04-09 1994-04-09 Fluidization microboiling drier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 94207707 CN2238406Y (en) 1994-04-09 1994-04-09 Fluidization microboiling drier

Publications (1)

Publication Number Publication Date
CN2238406Y true CN2238406Y (en) 1996-10-23

Family

ID=33825955

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 94207707 Expired - Fee Related CN2238406Y (en) 1994-04-09 1994-04-09 Fluidization microboiling drier

Country Status (1)

Country Link
CN (1) CN2238406Y (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111380A (en) * 2013-02-27 2013-05-22 攀钢集团攀枝花钢铁研究院有限公司 Cyclone dust collection device
CN105018719A (en) * 2015-08-10 2015-11-04 中国瑞林工程技术有限公司 Concentrate processing method and system
CN105066644A (en) * 2015-08-22 2015-11-18 何英好 Plate-type dryer

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103111380A (en) * 2013-02-27 2013-05-22 攀钢集团攀枝花钢铁研究院有限公司 Cyclone dust collection device
CN105018719A (en) * 2015-08-10 2015-11-04 中国瑞林工程技术有限公司 Concentrate processing method and system
CN105066644A (en) * 2015-08-22 2015-11-18 何英好 Plate-type dryer

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C19 Lapse of patent right due to non-payment of the annual fee
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