CN205556467U - Dust recovery system of slaked lime production line - Google Patents

Dust recovery system of slaked lime production line Download PDF

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Publication number
CN205556467U
CN205556467U CN201620282729.7U CN201620282729U CN205556467U CN 205556467 U CN205556467 U CN 205556467U CN 201620282729 U CN201620282729 U CN 201620282729U CN 205556467 U CN205556467 U CN 205556467U
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CN
China
Prior art keywords
dust
gathering arrester
dust gathering
production line
air exhauster
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
CN201620282729.7U
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Chinese (zh)
Inventor
张锦
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.)
Jingmen Jinke Calcium Industry Co Ltd
Original Assignee
Jingmen Jinke Calcium Industry 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 Jingmen Jinke Calcium Industry Co Ltd filed Critical Jingmen Jinke Calcium Industry Co Ltd
Priority to CN201620282729.7U priority Critical patent/CN205556467U/en
Application granted granted Critical
Publication of CN205556467U publication Critical patent/CN205556467U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The utility model provides a dust recovery system of slaked lime production line, slaked lime production line body also has dust recovery system, dust recovery system includes quick lime recoverable module and white lime recoverable module, quick lime recoverable module includes first dust cage (1), second dust cage (2), first air exhauster (3), first dirt pipeline (4) and the quick lime bag (5) that gathers dust of taking out, first dust cage (1) is through the top of support mounting in breaker (10), the utility model relates to a rationally, can carry out the categorised collection with the dust in the slaked lime production line to the line reuse that can put the dust of collecting again into production has improved the operational environment of factory greatly, has improved the output of production line, has fine practical value.

Description

A kind of fume recovery system of slaked lime production line
Technical field
This utility model slaked lime production technical field, is specifically related to the fume recovery system of a kind of slaked lime production line.
Background technology
Slaked lime is also Calx, and its main component is Ca (OH)2.Calx formulated one-tenth lime white, lime paste, lime mortar etc., as coating material and brick and tile binding agent.Slaked lime composition is calcium hydroxide, in powdery.Chemical formula is Ca (OH)2Slaked lime be calcium hydroxide pure substance slaked lime be exactly 2.24 grams/cc of production methods of Calx slaked lime density: added water by calcium oxide i.e. quick lime be dried, sieve after digestion, selecting crude drugs with winnower (or stage reduction) and finished product.
At present, burnt lime digester is applied in a lot fields producing calcium hydroxide, agglomeration for iron mine in such as calcium hydroxide retrofit, food medicine, petrochemical industry, field of metallurgy and building field etc..Steam and heat that quick lime produces in digestion process run off in a large number, digestive appartus is not collected and is utilized, and heat and steam are precisely and determine whether quick lime digests key factor thoroughly, thus use such digestive appartus, minority stodgy quick lime for want of heat and steam occur most probably, and can not digest, ultimately result in quicklime slaking incomplete, digestive efficiency is the highest, wastes resource simultaneously, reduces benefit.
Number of patent application be 201420483799 utility model patent provide a kind of calcium hydroxide production line, this production line production efficiency is high, but in process of production due to calcium hydroxide raw material and the dust characteristic of finished product, the dust causing plant area fills the air, not only it is degrading plant area's working environment, dust concentration arrives the most also can exist explosion danger, also results in the significant wastage of raw material simultaneously.
Summary of the invention
The purpose of this utility model is contemplated to solve above-mentioned technical problem, and provides the fume recovery system of a kind of slaked lime production line.
nullThis utility model includes slaked lime production line body,Described slaked lime production line body is by disintegrating machine、A elevator、Raw material case、Predigestion machine、Two grades of digestion machines、Conveying worm、B elevator、Select powder reclaiming device、B conveying worm and finished pot composition,Described slaked lime production line body also has fume recovery system,Described fume recovery system includes quick lime recycling module and Calx recycling module,Described quick lime recycling module includes the first dust gathering arrester、Second dust gathering arrester、First air exhauster、First takes out dirt pipeline and quick lime dust collecting sleeve,Described first dust gathering arrester is arranged on the top of disintegrating machine by support,Described second dust gathering arrester is arranged on the top of raw material case by support,First dust gathering arrester and the second dust gathering arrester are communicated by the first suction opeing taking out dirt pipeline and the first air exhauster respectively,The bag mouth of described quick lime dust collecting sleeve and the air outlet of the first air exhauster communicate,Described Calx recycling module includes the 3rd dust gathering arrester、4th dust gathering arrester、Second air exhauster、Second takes out dirt pipeline and Calx dust collecting sleeve,Described 3rd dust gathering arrester and the 4th dust gathering arrester are arranged on the top selecting powder reclaiming device and finished pot respectively by support,3rd dust gathering arrester and the 4th dust gathering arrester are communicated by the second suction opeing taking out dirt pipeline and the second air exhauster respectively,The bag mouth of described Calx dust collecting sleeve and the air outlet of the second air exhauster communicate.
Described first air exhauster and the second air exhauster are industry high pressure air exhauster respectively.
This utility model advantage is: this utility model is reasonable in design, dust in slaked lime production line can be carried out categorised collection, and line recycling of again being put into production by the dust of collection, substantially improve the working environment of plant area, improve the yield of production line, there is good practical value.
Accompanying drawing explanation
Fig. 1 is this utility model structural representation.
Detailed description of the invention
nullAs shown in Figure 1,This utility model includes slaked lime production line body,Described slaked lime production line body is by disintegrating machine 10、A elevator 11、Raw material case 12、Predigestion machine 14、Two grades of digestion machines 15、Conveying worm 16、B elevator 17、Select powder reclaiming device 18、B conveying worm 19 and finished pot 20 form,Described slaked lime production line body also has fume recovery system,Described fume recovery system includes quick lime recycling module and Calx recycling module,Described quick lime recycling module includes the first dust gathering arrester 1、Second dust gathering arrester 2、First air exhauster 3、First takes out dirt pipeline 4 and quick lime dust collecting sleeve 5,Described first dust gathering arrester 1 is arranged on the top of disintegrating machine 10 by support,Described second dust gathering arrester 2 is arranged on the top of raw material case 12 by support,First dust gathering arrester 1 and the second dust gathering arrester 2 are taken out dirt pipeline 4 by first respectively and are communicated with the suction opeing of the first air exhauster 3,The bag mouth of described quick lime dust collecting sleeve 5 and the air outlet of the first air exhauster 3 communicate,Described Calx recycling module includes the 3rd dust gathering arrester 6、4th dust gathering arrester 7、Second air exhauster 8、Second takes out dirt pipeline 9 and Calx dust collecting sleeve 21,Described 3rd dust gathering arrester 6 and the 4th dust gathering arrester 7 are arranged on by support respectively and select powder reclaiming device 18 and the top of finished pot 20,3rd dust gathering arrester 6 and the 4th dust gathering arrester 7 are taken out dirt pipeline 9 by second respectively and are communicated with the suction opeing of the second air exhauster 8,The bag mouth of described Calx dust collecting sleeve 21 and the air outlet of the second air exhauster 8 communicate.
Described first air exhauster 3 and the second air exhauster 8 are industry high pressure air exhauster respectively.
Working method and principle: during the running of slaked lime (calcium hydroxide) production line body, disintegrating machine 10, raw material case 12, the top dust selecting powder reclaiming device 18 and finished pot 20 is concentrated the most, wherein disintegrating machine 10 and raw material case 12 are arranged above quick lime dust, that selects powder reclaiming device 18 and finished pot 20 is arranged above Calx dust, first dust gathering arrester 1 and the second dust gathering arrester 2 are respectively by quick lime dust collection, and after eventually passing through the filtration of quick lime dust collecting sleeve 5, lose no time air row in air, quick lime dust is stayed in quick lime dust collecting sleeve 5, in like manner Calx dust is collected by Calx dust collecting sleeve 21, thus can greatly reduce plant area and produce the dust brought, and the dust of collection can be direct plungeed into production line use.

Claims (2)

  1. null1. the fume recovery system of a slaked lime production line,Including slaked lime production line body,Described slaked lime production line body is by disintegrating machine (10)、A elevator (11)、Raw material case (12)、Predigestion machine (14)、Two grades of digestion machines (15)、Conveying worm (16)、B elevator (17)、Select powder reclaiming device (18)、B conveying worm (19) and finished pot (20) composition,It is characterized in that described slaked lime production line body also has fume recovery system,Described fume recovery system includes quick lime recycling module and Calx recycling module,Described quick lime recycling module includes the first dust gathering arrester (1)、Second dust gathering arrester (2)、First air exhauster (3)、First takes out dirt pipeline (4) and quick lime dust collecting sleeve (5),Described first dust gathering arrester (1) is arranged on the top of disintegrating machine (10) by support,Described second dust gathering arrester (2) is arranged on the top of raw material case (12) by support,First dust gathering arrester (1) and the second dust gathering arrester (2) are taken out dirt pipeline (4) by first respectively and are communicated with the suction opeing of the first air exhauster (3),The bag mouth of described quick lime dust collecting sleeve (5) and the air outlet of the first air exhauster (3) communicate,Described Calx recycling module includes the 3rd dust gathering arrester (6)、4th dust gathering arrester (7)、Second air exhauster (8)、Second takes out dirt pipeline (9) and Calx dust collecting sleeve (21),Described 3rd dust gathering arrester (6) and the 4th dust gathering arrester (7) are arranged on by support respectively and select powder reclaiming device (18) and the top of finished pot (20),3rd dust gathering arrester (6) and the 4th dust gathering arrester (7) are taken out dirt pipeline (9) by second respectively and are communicated with the suction opeing of the second air exhauster (8),The bag mouth of described Calx dust collecting sleeve (21) and the air outlet of the second air exhauster (8) communicate.
  2. The fume recovery system of a kind of slaked lime production line the most according to claim 1, it is characterised in that described first air exhauster (3) and the second air exhauster (8) are industry high pressure air exhauster respectively.
CN201620282729.7U 2016-04-07 2016-04-07 Dust recovery system of slaked lime production line Expired - Fee Related CN205556467U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620282729.7U CN205556467U (en) 2016-04-07 2016-04-07 Dust recovery system of slaked lime production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620282729.7U CN205556467U (en) 2016-04-07 2016-04-07 Dust recovery system of slaked lime production line

Publications (1)

Publication Number Publication Date
CN205556467U true CN205556467U (en) 2016-09-07

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CN201620282729.7U Expired - Fee Related CN205556467U (en) 2016-04-07 2016-04-07 Dust recovery system of slaked lime production line

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106977212A (en) * 2017-04-07 2017-07-25 佛山欧神诺陶瓷股份有限公司 A kind of method and its recovery system of powder classification recycling
CN110342466A (en) * 2019-06-25 2019-10-18 扬州市海纳源科技服务有限责任公司 A kind of production technology of bleaching powder

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106977212A (en) * 2017-04-07 2017-07-25 佛山欧神诺陶瓷股份有限公司 A kind of method and its recovery system of powder classification recycling
CN110342466A (en) * 2019-06-25 2019-10-18 扬州市海纳源科技服务有限责任公司 A kind of production technology of bleaching powder

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

Granted publication date: 20160907

Termination date: 20190407