CN203291673U - Purifying and dust-collecting system - Google Patents
Purifying and dust-collecting system Download PDFInfo
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- CN203291673U CN203291673U CN201320335832XU CN201320335832U CN203291673U CN 203291673 U CN203291673 U CN 203291673U CN 201320335832X U CN201320335832X U CN 201320335832XU CN 201320335832 U CN201320335832 U CN 201320335832U CN 203291673 U CN203291673 U CN 203291673U
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- purification
- dust collectors
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Abstract
The utility model relates to the technical field of waste gas purification, and discloses a purifying and dust-collecting system. The purifying and dust-collecting system comprises two hydrocyclones, two bag type dust collectors, two water bath dust collectors, and two dust storage bins, wherein the hydrocyclones are positioned above the dust storage bins, overflowing ports of the hydrocyclones are communicated with the bag type dust collectors, and outlets of the bag type dust collectors are communicated with the water bath dust collectors. The purification and dust collection are performed through the three-stage purification system including the hydrocyclones, the bag type dust collectors and the water bath dust collectors, the purification and dust collection effects are better, the atmospheric pollution can be greatly alleviated, and the risk of harming the human body health can be reduced.
Description
Technical field
The utility model relates to the waste gas purification technical field, especially relates to a kind of purification dust removal system of good purification.
Background technology
In the processes such as industry smelting or oven dry, often have a large amount of flue dust and discharge,, if these flue dust directly are discharged in atmosphere,, with the severe contamination air ambient, to the healthy of the mankind, may cause very big harm.Before entering atmosphere, these flue dust to carry out purified treatment for this reason.
Existing technology is generally to adopt sack cleaner or wet dust collector to carry out separately purified treatment.But effect is general, still has the part harmful substance and enters in atmosphere.
The utility model content
The utility model, for overcoming above-mentioned deficiency of the prior art, provides a kind of clean-up effect better purification dust removal system.
The utility model is achieved through the following technical solutions above-mentioned purpose.
A kind of purification dust removal system, comprise cyclone, sack cleaner, wet dust collector, ash-storing bin, and wherein cyclone is positioned at the top of ash-storing bin, and the overfall of cyclone is communicated with sack cleaner, and the outlet of sack cleaner is communicated with wet dust collector.
Described ash-storing bin below is provided with vibratory sieve, and the below output of vibratory sieve is communicated with the waste material conveyer, and the top output of vibratory sieve is communicated with the recovery conveyer.Ash-storing bin is used for storing the bulky grain raw material that cyclone is separated, in these bulky grain raw materials, some can recycle, but may mix the granule waste material in the bulky grain raw material, therefore screen through vibratory sieve, the bulky grain raw material screening, to reclaiming in conveyer, is screened the granule waste material to the waste material conveyer and transports.This scheme has improved recovery utilization rate greatly.
The output of described recovery conveyer is communicated with elevator, so that the operation of recycling work.
The utility model compared with prior art mainly has following beneficial effect: adopted cyclone, sack cleaner, wet dust collector to form three grades of cleaning systems and carried out purifying and dedusting, be particularly useful in the production field of reduced iron powder.Flue dust first separates through cyclone, and the bulky grain raw material in flue dust is separated, and as breeze, and makes breeze fall into the ash-storing bin of below; Make simultaneously flue dust after separation enter sack cleaner and carry out purifying and dedusting; Flue dust is flue gas substantially after sack cleaner, but still has some fine particles, then through wet dust collector, carries out purifying and dedusting.The purifying and dedusting better effects if, greatly reduced the pollution to atmosphere, reduced the risk that human body health is worked the mischief.
Description of drawings
Fig. 1 is the system architecture schematic diagram of embodiment.
The specific embodiment
Below in conjunction with accompanying drawing, the utility model is described further.Accompanying drawing only is used for exemplary illustration, can not be interpreted as the restriction to this patent.
For more succinct explanation the present embodiment, in accompanying drawing or explanation, some well known to a person skilled in the art but with the incoherent parts of main contents of the present invention, can omit to some extent.For ease of statement, in accompanying drawing, some parts has omission, zooms in or out, but does not represent size or the entire infrastructure of actual product in addition.
Embodiment:
As shown in Figure 1, a kind of purification dust removal system, comprise two cyclones 1, two sack cleaners 2, two wet dust collectors 3, two ash-storing bins 4, a vibratory sieve 5.
Wherein two cyclones 1 lay respectively at the top of two ash-storing bins 4, and the overfall of two cyclones 1 is communicated with two sack cleaners 2 respectively, and the outlet of two sack cleaners 2 is communicated with two wet dust collectors 3 respectively.
In the present embodiment, the outlet of two ash-storing bins 4 is communicated to vibratory sieve 5 jointly, and the below output of vibratory sieve 5 is communicated with waste material conveyer 6, and the top output of vibratory sieve 5 is communicated with and reclaims conveyer 7.Ash-storing bin 4 is used for storing the bulky grain raw material that cyclone 1 is separated, as breeze, some can recycle these breezes, but may mix the granule waste material in these breezes, therefore screen through vibratory sieve 5, the larger particles raw material screening, to reclaiming in conveyer 7, is screened the granule waste material to waste material conveyer 6 and transports.The present embodiment has improved recovery utilization rate and utilization rate of equipment and installations greatly.
The output that reclaims conveyer 7 in the present embodiment is communicated with elevator 8, so that the operation of recycling work.
The present embodiment is particularly useful in the production field of reduced iron powder, and its purification process is: flue dust first separates through cyclone 1, and the bulky grain raw materials such as breeze in flue dust are separated; Then flue dust carries out purifying and dedusting through sack cleaner 2 again; Flue dust is flue gas substantially after sack cleaner 2, but still has some fine particles, then through wet dust collector 3, carries out purifying and dedusting, is discharged in atmosphere finally.
The present embodiment carries out purifying and dedusting by three grades of cleaning systems that adopt cyclone, sack cleaner, wet dust collector to form, and the purifying and dedusting better effects if, greatly reduced the pollution to atmosphere, reduced the risk that human body health is worked the mischief.
These are only a specific embodiment of the present utility model, but design concept of the present utility model is not limited to this, all insubstantial modifications of utilizing the utility model design to make the utility model, within all falling into protection domain of the present utility model.
Claims (3)
1. purification dust removal system, it is characterized in that: comprise cyclone, sack cleaner, wet dust collector, ash-storing bin, wherein cyclone is positioned at the top of ash-storing bin, and the overfall of cyclone is communicated with sack cleaner, and the outlet of sack cleaner is communicated with wet dust collector.
2. purification dust removal system according to claim 1 is characterized in that: described ash-storing bin below is provided with vibratory sieve, and the below output of vibratory sieve is communicated with the waste material conveyer, and the top output of vibratory sieve is communicated with the recovery conveyer.
3. purification dust removal system according to claim 2, it is characterized in that: the output of described recovery conveyer is communicated with elevator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320335832XU CN203291673U (en) | 2013-06-13 | 2013-06-13 | Purifying and dust-collecting system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320335832XU CN203291673U (en) | 2013-06-13 | 2013-06-13 | Purifying and dust-collecting system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203291673U true CN203291673U (en) | 2013-11-20 |
Family
ID=49567714
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320335832XU Expired - Lifetime CN203291673U (en) | 2013-06-13 | 2013-06-13 | Purifying and dust-collecting system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203291673U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106938339A (en) * | 2017-04-14 | 2017-07-11 | 湖南旭博冶金科技有限公司 | A kind of efficient gas-atomized powder equipment of big yield |
-
2013
- 2013-06-13 CN CN201320335832XU patent/CN203291673U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106938339A (en) * | 2017-04-14 | 2017-07-11 | 湖南旭博冶金科技有限公司 | A kind of efficient gas-atomized powder equipment of big yield |
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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: 20220914 Address after: 122304 Duanzhenggouliang Village, Gongyingzi Town, Kazuo County, Chaoyang City, Liaoning Province Patentee after: Chaoyang Bosheng Metallurgical Technology Co.,Ltd. Address before: Metallurgical Foundry Park, Gongyingzi Town, Kazuo County, Chaoyang City, Liaoning Province, 122304 Patentee before: CHAOYANG GOLDEN RIVER POWDER METALLURGY MATERIALS CO.,LTD. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20131120 |