CN202902292U - Saliferous waste residue pyrolysis device - Google Patents

Saliferous waste residue pyrolysis device Download PDF

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Publication number
CN202902292U
CN202902292U CN 201220357515 CN201220357515U CN202902292U CN 202902292 U CN202902292 U CN 202902292U CN 201220357515 CN201220357515 CN 201220357515 CN 201220357515 U CN201220357515 U CN 201220357515U CN 202902292 U CN202902292 U CN 202902292U
Authority
CN
China
Prior art keywords
waste residue
saliferous waste
saliferous
cylindrical shell
barrel body
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 201220357515
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Chinese (zh)
Inventor
糜茂俊
朱平
郭俊伟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Quanneng Environmental Protection Science & Technology Co Ltd
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Jiangsu Quanneng Environmental Protection Science & Technology Co Ltd
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 Jiangsu Quanneng Environmental Protection Science & Technology Co Ltd filed Critical Jiangsu Quanneng Environmental Protection Science & Technology Co Ltd
Priority to CN 201220357515 priority Critical patent/CN202902292U/en
Application granted granted Critical
Publication of CN202902292U publication Critical patent/CN202902292U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a saliferous waste residue pyrolysis device. The saliferous waste residue pyrolysis device comprises a barrel body and a driving device, wherein the barrel body is in a jacketed structure, a driving shaft of the driving device is fixed on cover plates at two ends of a jacket through a bearing, a scratch plate device is connected with the driving shaft in a welding mode, and a scratch plate is driven by the driving device and rotates in the barrel body along an inner wall of the barrel body. High temperature exhaust gas enters the saliferous waste residue pyrolysis device, spirally moves forward along a spiral plate in the jacket and passes heat to an inner layer of the jacket. The saliferous waste residue is placed in an inner barrel of the device through a feeding port to exchange heat with a steel plate, under the effect of oxygenating air, organic matters in the waste residue volatilize and aerobically decomposes, under the effect of the scratch plate, the saliferous waste residue rolls forward in the barrel body, inorganic salt is discharged from the discharging port, and pyrolysis gas produced is burnt in an incinerator. By means of he saliferous waste residue pyrolysis device, the saliferous waste residue can be disposed effectively, and problems of melting and crystallization caused by direct burning are avoided.

Description

Saliferous waste residue pyrolysis installation
Affiliated technical field
The utility model relates to a kind of saliferous waste residue pyrolysis installation.This device is mainly used in the fields such as incinerator, chemical industry.
Background technology
At present, in the incinerator system, the saliferous waste residue all is to adopt the method for directly burning, the melting problem that may have inorganic salts in the burning process, cause high-temperature refractory can not continue to use, after waste residue burns simultaneously, the inorganic salts of the melting that may carry secretly in the flue gas of generation, crystallisation by cooling in the cooling device makes back equipment can not continue to use in the back.
In order to overcome existing issue, the utility model provides a kind of saliferous waste residue pyrolysis installation, this device adopts the cylindrical shell of a cover jacketed, scraper plate is set in the middle of the cylindrical shell, high-temperature flue gas in the chuck is by the saliferous waste residue heat exchange in chuck and the cylindrical shell, so that organic matter gasification, pyrolysis in the waste residue behind the pyrolysis gas process desalination powder of generation, goes incinerator to burn.
Summary of the invention
The technical scheme that its technical problem that solves the utility model adopts is: cylindrical shell is jacket type structure, drive unit is fixed on the chuck two end cover plate with bearing, drive unit is rotated by motor-driven, the scraper plate that is welded on the driving shaft rotates along cylinder inboard wall in cylindrical shell, be provided with spiral plate in the chuck of cylindrical shell, the high-temperature flue gas import is arranged on the chuck tangential position, and device front end cover plate adopts flange to be connected with cylindrical shell, can open flange the cylindrical shell inner driver is taken out cleaning or maintenance.High-temperature flue gas enters saliferous waste residue pyrolysis installation, advance along chuck inside spin plate spiral, heat is passed to the chuck internal layer, the saliferous waste residue carries out heat exchange with steel plate, under the oxygenating air effect by in the charging aperture adding apparatus inner core, organic matter volatilization, oxidation Decomposition in the waste residue, the saliferous waste residue rolls under the scraper plate effect in cylindrical shell and advances, and inorganic salts are discharged from discharge gate, and the pyrolysis gas of generation goes incinerator to burn.
The beneficial effects of the utility model are, can effectively solve the melting problem of inorganic salts in the saliferous waste residue and the crystallisation problems of follow-up equipment, do not affect the operation of incinerator system.
Description of drawings
Accompanying drawing 1 is installation drawing
1. saliferous waste residue imports among the figure, 2. front shroud, 3. air intlet, 4. front support bearing, 5. gas approach, 6. chuck, 7. scraper plate, 8. driving shaft, 9. exhanst gas outlet, 10. pyrolysis gas dedusting filter screen, 11. drive unit, 12. supports, 13. inorganic salts outlets, 14. spiral plates.
The specific embodiment
High-temperature flue gas enters saliferous waste residue pyrolysis installation from gas approach 5, advance along chuck 6 inside spin plates 14 spirals, heat is passed to chuck 6 internal layers, flue gas is discharged from exhanst gas outlet 9, the saliferous waste residue is by in the charging aperture 1 adding apparatus inner core, carry out heat exchange with chuck 6 inner layer steel plates, the oxygenating air enters from air intlet 3, organic matter volatilization in the waste residue, oxidation Decomposition, the pyrolysis gas of generation is discharged after dedusting filter screen 10 is except the powder that desalts from pyrolysis gas outlet, goes incinerator to burn, driving shaft 8 rotates under drive unit 11 effects, drive scraper plate 7 and rotate, the saliferous waste residue is rolled in cylindrical shell advance, inorganic salts are discharged from discharge gate 13..

Claims (4)

1. saliferous waste residue pyrolysis installation, it comprises cylindrical shell and driving whirligig, and it is characterized in that: cylindrical shell is jacket type structure, and drive unit is fixed on the chuck two end cover plate with bearing, drive unit is rotated by motor-driven, and the scraper plate that is welded on the driving shaft rotates along cylinder inboard wall in cylindrical shell.
2. saliferous waste residue pyrolysis installation according to claim 1 is characterized in that: be provided with spiral plate in the chuck of cylindrical shell.
3. saliferous waste residue pyrolysis installation according to claim 1, it is characterized in that: the high-temperature flue gas import is arranged on the chuck tangential position.
4. saliferous waste residue pyrolysis installation according to claim 1 is characterized in that: install the front end cover plate and adopt flange to be connected with cylindrical shell, can open flange the cylindrical shell inner driver is taken out cleaning or maintenance.
CN 201220357515 2012-07-14 2012-07-14 Saliferous waste residue pyrolysis device Expired - Fee Related CN202902292U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201220357515 CN202902292U (en) 2012-07-14 2012-07-14 Saliferous waste residue pyrolysis device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201220357515 CN202902292U (en) 2012-07-14 2012-07-14 Saliferous waste residue pyrolysis device

Publications (1)

Publication Number Publication Date
CN202902292U true CN202902292U (en) 2013-04-24

Family

ID=48122953

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201220357515 Expired - Fee Related CN202902292U (en) 2012-07-14 2012-07-14 Saliferous waste residue pyrolysis device

Country Status (1)

Country Link
CN (1) CN202902292U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104438294A (en) * 2014-11-28 2015-03-25 常州市姚氏铸造材料有限公司 Pyrolysis device for treating chemical waste salts and waste residues
CN104566406A (en) * 2014-12-04 2015-04-29 浙江理工大学 Incinerator for crop straws
CN108479088A (en) * 2018-03-02 2018-09-04 东南大学 Salty organic waste liquid desalination pyrolysis treating method and system
CN112303650A (en) * 2020-11-17 2021-02-02 江苏森茂能源发展有限公司 Vertical regenerated oil furnace

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104438294A (en) * 2014-11-28 2015-03-25 常州市姚氏铸造材料有限公司 Pyrolysis device for treating chemical waste salts and waste residues
CN104438294B (en) * 2014-11-28 2016-07-06 常州市姚氏铸造材料有限公司 Process the pyrolysis installation of chemical industry abraum salt waste residue
CN104566406A (en) * 2014-12-04 2015-04-29 浙江理工大学 Incinerator for crop straws
CN104566406B (en) * 2014-12-04 2016-12-07 浙江理工大学 A kind of incinerator of crop material
CN108479088A (en) * 2018-03-02 2018-09-04 东南大学 Salty organic waste liquid desalination pyrolysis treating method and system
CN112303650A (en) * 2020-11-17 2021-02-02 江苏森茂能源发展有限公司 Vertical regenerated oil furnace

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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: 20130424

Termination date: 20140714

EXPY Termination of patent right or utility model