CN203778475U - Dust removing excess material recovery equipment for hot-blast stove for drying high-humidity material - Google Patents
Dust removing excess material recovery equipment for hot-blast stove for drying high-humidity material Download PDFInfo
- Publication number
- CN203778475U CN203778475U CN201420144632.0U CN201420144632U CN203778475U CN 203778475 U CN203778475 U CN 203778475U CN 201420144632 U CN201420144632 U CN 201420144632U CN 203778475 U CN203778475 U CN 203778475U
- Authority
- CN
- China
- Prior art keywords
- deduster
- hot
- blast stove
- conveying auger
- dust collector
- 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 - Lifetime
Links
- 239000000463 material Substances 0.000 title claims abstract description 34
- 238000011084 recovery Methods 0.000 title abstract description 7
- 238000001035 drying Methods 0.000 title abstract description 6
- 239000000428 dust Substances 0.000 title abstract 12
- 238000007599 discharging Methods 0.000 claims description 11
- 239000006148 magnetic separator Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 abstract description 8
- 239000000843 powder Substances 0.000 abstract description 6
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000001816 cooling Methods 0.000 description 6
- 238000005469 granulation Methods 0.000 description 5
- 230000003179 granulation Effects 0.000 description 5
- 238000010298 pulverizing process Methods 0.000 description 5
- 238000012216 screening Methods 0.000 description 5
- 239000002893 slag Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 235000013399 edible fruits Nutrition 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 230000003203 everyday effect Effects 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 240000006063 Averrhoa carambola Species 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 235000013325 dietary fiber Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 238000009700 powder processing Methods 0.000 description 1
Abstract
The utility model belongs to the technical field of excess material recovery of material drying equipment, and in particular relates to dust removing excess material recovery equipment for a hot-blast stove for drying a high-humidity material. The dust removing excess material recovery equipment comprises a feeding mechanism, a hot-blast stove, a material conveying mechanism, a permanent magnet cylinder, a cooler A, a crushing machine, a granulating machine, a cooler B, a vibrating screen separator and dust collectors which are connected in sequence; the dust collectors comprise a dust collector A and a dust collector B which are arranged side by side; the discharge openings of the dust collector A and the dust collector B are respectively communicated with a conveying auger; the conveying auger is communicated with the material conveying mechanism; an air closing device A is arranged between the material discharge opening of the dust collector A and the conveying auger; an air closing device B is arranged between the material discharge opening of the dust collector B and the conveying auger. According to the dust removing excess material recovery equipment, waste powder is recycled; the treatment process is simple; the cost is low.
Description
Technical field
The utility model belongs to drying materials equipment clout recovery technology field, specifically, relates to a kind of high moisture material and dries the reclaimer with hot-blast stove dedusting clout.
Background technology
High moisture material drying system equipment is semi-product material after hot-blast stove, roller drying to be delivered to by the discharging auger under surge bunker through discharging surge bunker again to subsequent processing does degaussing, cooling, pulverizing, granulation, cooling, screening continuously, packaging put finished product and produced, and heat exchange flue gas during process is anhydrated in the oven dry heat exchange in cylinder can absorption under the effect of Wind Volume negative pressure to carry a large amount of oven dry powders moisture after the collection of outdoor large cyclone collecting box emptying.In prior art, the powder after collection is generally that concentrated waste treatment is done in simple hopper collection again, has not only caused the profligacy with higher-value powder, also can have influence on the pollution of environment.Because ash rate in discarded powder is higher, as carry out re-treating process complexity; In addition, as become material up to standard by discarding powder processing, processing cost is higher, and economic benefit is poor.Waste treatment is still done by large-scale oven dry enterprise of domestic several families at present, as An Deli fruit industry, Sanmenxia Gorge fruit industry, the industry of middle Shandong, gloomy U.S. fruit industry etc., does not all realize effective exploitation.
Utility model content
For solving the problems of the technologies described above, the utility model proposes a kind of thorough recycling that realizes discarded powder, and the reclaimer of simple, the lower-cost hot-blast stove dedusting for the treatment of process clout.
The technical solution of the utility model is: a kind of high moisture material is dried the reclaimer with hot-blast stove dedusting clout, comprises the feeding mechanism, hot-blast stove, feeding unit, pipe magnetic separator, cooler A, pulverizer, granulator, cooler B, vibrosieve device, the deduster that connect successively; Described deduster comprises the deduster A and the deduster B that are set up in parallel, and the discharging opening of deduster A and deduster B is communicated with conveying auger respectively, and conveying auger is communicated with feeding unit; Between the discharging opening and conveying auger of described deduster A, be equipped with wind stopping device between the discharging opening of deduster B and conveying auger, be respectively wind stopping device A and wind stopping device B.
The course of work of the present utility model is as follows:
The high moisture materials such as pomace are fed in hot-blast stove by feeding mechanism, after hot-blast stove is dried, slag charge enters pipe magnetic separator by feeding unit, to remove the metal fragment in slag charge, then through cooler A, the material of 60 DEG C-70 DEG C is cooled to 20 DEG C-25 DEG C, then pulverize through pulverizer, material after pulverizing enters granulator and carries out particle compacting, adopt steam method of granulating to granulate, process conditions are temperature 100-110 DEG C, 0.3-0.4MPa, after granulation, through cooler B, the material of 60 DEG C-70 DEG C is cooled to 20 DEG C-25 DEG C, then being delivered to vibrosieve device sieves, mesh size is 5.5mm, after screening, qualified material enters feed bin, and clout, after deduster dedusting, is delivered to feeding unit by conveying auger, follow material that feeding mechanism enters and pass through again together the operations such as pipe magnetic separator degaussing, cooling, pulverizing, granulation, cooling, screening, loop.
Described high moisture material refers to that moisture content is more than 80% material.
The beneficial effects of the utility model are: 1, the utility model improves and installs that simple, disposable to install cost additional relatively low additional, and automation technolo is without additionally keeping an eye on operation, and runnability is stable.2, the utility model has been realized the exploitation of clout, has really realized recycling of discarded object, and economic benefit obviously promotes, and the final finished parameters index of production all reaches roughage top grade.3, the utility model has brought obvious surplus profit to increase volume, and can reduce the disposal cost of a lot of extra discarded objects, has suppressed environmental pollution, and economic benefit is very considerable.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model;
Fig. 2 is part-structure schematic diagram of the present utility model.
Wherein, 1, feeding mechanism; 2, hot-blast stove; 3, feeding unit; 4, pipe magnetic separator; 5, cooler A; 6, pulverizer; 7, granulator; 8, cooler B; 9, vibrosieve device; 10, feed bin; 11, deduster A; 12, deduster B; 13, wind stopping device A; 14, wind stopping device B; 15, conveying auger.
Detailed description of the invention
Illustrate the utility model below in conjunction with drawings and Examples.
Embodiment 1:
As shown in Figure 1-2, the utility model comprises the feeding mechanism 1, hot-blast stove 2, feeding unit 3, pipe magnetic separator 4, cooler A5, pulverizer 6, granulator 7, cooler B8, vibrosieve device 9, the deduster that connect successively; Described deduster comprises the deduster A11 and the deduster B12 that are set up in parallel, and the discharging opening of deduster A11 and deduster B12 is communicated with conveying auger 15 respectively, and conveying auger 15 is communicated with feeding unit 3; Between the discharging opening of described deduster A11 and conveying auger 15, be equipped with wind stopping device between the discharging opening of deduster B12 and conveying auger 15, be respectively wind stopping device A13 and wind stopping device B14.
The course of work of the present utility model is as follows:
The high moisture materials such as pomace are fed in hot-blast stove 2 by feeding mechanism 1, after hot-blast stove 2 is dried, slag charge enters pipe magnetic separator 4 by feeding unit 3, to remove the metal fragment in slag charge, then through cooler A5, the material of 60 DEG C-70 DEG C is cooled to 20 DEG C-25 DEG C, then pulverize through pulverizer 6, material after pulverizing enters granulator 7 and carries out particle compacting, adopt steam method of granulating to granulate, process conditions are temperature 100-110 DEG C, 0.3-0.4MPa, after granulation, through cooler B8, the material of 60 DEG C-70 DEG C is cooled to 20 DEG C-25 DEG C, then being delivered to vibrosieve device 9 sieves, mesh size is 5.5mm, after screening, qualified material enters feed bin 10, and clout, after deduster dedusting, is delivered to feeding unit 3 by conveying auger 15, follow material that feeding mechanism 1 enters and pass through again together the operations such as pipe magnetic separator 4 degaussings, cooling, pulverizing, granulation, cooling, screening, loop.
Dry as example taking the hot-blast stoves of 12 tons, directly discarded compared to existing clout, after the utility model carries out clout recovery, putting into practice output and reclaiming clout amount split run has 2-3 ton, and every day, quantity-produced clout yield arrived all 5 tons of left and right, according to 3000 yuan of left and right/tons of finished product market value, increase volume compared with the surplus profit that probably has 1.5 ten thousand yuan before improving every day, also can reduce the disposal cost of a lot of extra discarded objects, suppress environmental pollution, economic benefit is very considerable.
Claims (1)
1. high moisture material is dried the reclaimer with hot-blast stove dedusting clout, comprises the feeding mechanism, hot-blast stove, feeding unit, pipe magnetic separator, cooler A, pulverizer, granulator, cooler B, vibrosieve device, the deduster that connect successively; It is characterized in that: described deduster comprises the deduster A and the deduster B that are set up in parallel, and the discharging opening of deduster A and deduster B is communicated with conveying auger respectively, and conveying auger is communicated with feeding unit; Between the discharging opening and conveying auger of described deduster A, be equipped with wind stopping device between the discharging opening of deduster B and conveying auger, be respectively wind stopping device A and wind stopping device B.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420144632.0U CN203778475U (en) | 2014-03-28 | 2014-03-28 | Dust removing excess material recovery equipment for hot-blast stove for drying high-humidity material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420144632.0U CN203778475U (en) | 2014-03-28 | 2014-03-28 | Dust removing excess material recovery equipment for hot-blast stove for drying high-humidity material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203778475U true CN203778475U (en) | 2014-08-20 |
Family
ID=51314703
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420144632.0U Expired - Lifetime CN203778475U (en) | 2014-03-28 | 2014-03-28 | Dust removing excess material recovery equipment for hot-blast stove for drying high-humidity material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203778475U (en) |
-
2014
- 2014-03-28 CN CN201420144632.0U patent/CN203778475U/en not_active Expired - Lifetime
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180627 Address after: 341699 navel orange industrial base, west of Xinfeng Industrial Park, Ganzhou, Jiangxi (range of farmer's spring) Patentee after: JIANGXI KENAIER AGRICULTURAL PRODUCTS Co.,Ltd. Address before: 266600 Shandong Laixi Qingdao Economic Development Zone 3 Beijing East Road No. 3 Patentee before: QINGDAO CTC FEED Corp. |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20221214 Address after: 266000 Building 2, No. 3, Beijing East Road, Shuiji Sub district Office, Laixi City, Qingdao, Shandong Province Patentee after: Qingdao Cornell Agricultural Products Co.,Ltd. Address before: 341699 navel orange industrial base, west of Xinfeng Industrial Park, Ganzhou, Jiangxi (range of farmer's spring) Patentee before: JIANGXI KENAIER AGRICULTURAL PRODUCTS Co.,Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20140820 |