CN103816736B - Realize the phosphorus steam dust removing device that high-purity phosphorus reclaims - Google Patents
Realize the phosphorus steam dust removing device that high-purity phosphorus reclaims Download PDFInfo
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- CN103816736B CN103816736B CN201410042893.6A CN201410042893A CN103816736B CN 103816736 B CN103816736 B CN 103816736B CN 201410042893 A CN201410042893 A CN 201410042893A CN 103816736 B CN103816736 B CN 103816736B
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- Prior art keywords
- filter screen
- drum type
- type brake
- storage chamber
- dust
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- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 title claims abstract description 53
- 229910052698 phosphorus Inorganic materials 0.000 title claims abstract description 53
- 239000011574 phosphorus Substances 0.000 title claims abstract description 53
- 239000000428 dust Substances 0.000 title claims abstract description 47
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 52
- 238000003860 storage Methods 0.000 claims abstract description 36
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 26
- 238000007599 discharging Methods 0.000 claims abstract description 15
- 210000002268 wool Anatomy 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 6
- 230000001680 brushing effect Effects 0.000 claims abstract description 4
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000001816 cooling Methods 0.000 claims description 4
- 230000000630 rising effect Effects 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims 1
- 238000005201 scrubbing Methods 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000011084 recovery Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000009866 aluminium metallurgy Methods 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000009867 copper metallurgy Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000002309 gasification Methods 0.000 description 1
- BHEPBYXIRTUNPN-UHFFFAOYSA-N hydridophosphorus(.) (triplet) Chemical compound [PH] BHEPBYXIRTUNPN-UHFFFAOYSA-N 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 238000009628 steelmaking Methods 0.000 description 1
- OBSZRRSYVTXPNB-UHFFFAOYSA-N tetraphosphorus Chemical compound P12P3P1P32 OBSZRRSYVTXPNB-UHFFFAOYSA-N 0.000 description 1
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- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The present invention relates to a kind of phosphorus steam dust removing device and method of work thereof, dust arrester comprises: column-shaped barrel, be located at this column-shaped barrel top for inputting the first flange-interface of phosphorus steam, be located on the sidewall of this column-shaped barrel for exporting the second flange-interface of phosphorus steam, be located at the drum type brake filter screen in this column-shaped barrel, drive the driving mechanism of this drum type brake filter screen rotation, air jet pipe for the inwall nitrogen-blow to this drum type brake filter screen with removal dust, for brushing away the wool yarn plate of the dust on drum type brake filter screen, be connected in obconic conically shaped of being of column-shaped barrel lower end, be located at the blanking seal valve of this conically shaped lower end, be located at the storage chamber of this first blanking seal valve bottom, be located at the discharging seal valve of this storage chamber bottom, be located at the heater in this storage chamber, be located at nitrogen air inlet pipe and air exhaust duct on storage chamber, and be located at respectively being suitable in nitrogen air inlet pipe and air exhaust duct and open and close nitrogen intake valve and air exhaust-valve simultaneously.
Description
The application is divisional application, the application number of original application: 201210222666.2, and invention and created name: phosphorus steam dust removing device and method of work thereof, the applying date: on June 29th, 2012.
Technical field
The present invention relates to the technical field of cleaner, specifically a kind of phosphorus steam dust removing device and method of work thereof.
Background technology
Phosphorus production is highly energy-consuming industry, and 1 ton of yellow phosphorus of every production at least will consume 1.4 ten thousand kilowatt hour electricity and 1.6 tons of carbon, and Chinese existing annual capacity is 800,000 tons. In phosphorus production process, will produce a large amount of phosphorus steam, phosphorus furnace exhaust gas and high temperature furnace slag. Equally,, also there are a large amount of high temperature furnace slags in the industries such as steel-making, aluminium metallurgy, copper metallurgy.
The more dust that often adulterates in phosphorus steam, is unfavorable for the recovery of phosphorus.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of simple in structure, phosphorus steam dust removing device and the method for work thereof of the dust in energy filtering phosphorus steam.
For solving the problems of the technologies described above, phosphorus steam dust removing device provided by the invention, comprising: column-shaped barrel 1, be located at this column-shaped barrel 1 top for inputting the first flange-interface 14 of phosphorus steam, be located on the sidewall of this column-shaped barrel 1 for exporting the second flange-interface 15 of described phosphorus steam, be located at the drum type brake filter screen 2 in this column-shaped barrel 1, drive the driving mechanism of this drum type brake filter screen 2 around its central shaft rotation, axially be located at the air jet pipe 3 with removal dust for the inwall nitrogen-blow to this drum type brake filter screen 2 of the bottom interior wall setting of described drum type brake filter screen 2 interior and contiguous these drum type brake filter screens 2, axially be located at described drum type brake filter screen 2 outsides for brushing away the wool yarn plate 4 of the dust on described drum type brake filter screen 2, be connected in the obconic conically shaped 5 that is of described column-shaped barrel 1 lower end, be located at the blanking seal valve 6 of these conically shaped 5 lower ends, be located at the storage chamber 7 of these blanking seal valve 6 bottoms, be located at the discharging seal valve 9 of these storage chamber 7 bottoms, be located at the heater 8 in this storage chamber 7, be located at nitrogen air inlet pipe and air exhaust duct on storage chamber 7, and be located at respectively being suitable in described nitrogen air inlet pipe and air exhaust duct and open and close nitrogen intake valve 12 and air exhaust-valve 10 simultaneously.
The method of work of described phosphorus steam dust removing device, comprises the steps:
A, to being filled with nitrogen in described column-shaped barrel 1, conically shaped 5 and storage chamber 7 to discharge air; Then closed blanking seal valve 6, discharging seal valve 9, nitrogen intake valve 12 and air exhaust-valve 10;
B, phosphorus steam is sent into column-shaped barrel 1 through the first flange-interface 14, then enter drum type brake filter screen 2 downwards, then export from the second flange-interface 15;
Driving mechanism drives described drum type brake filter screen 2 around its central shaft rotation, and air jet pipe 3 sprays high pressure nitrogen, and the dust being attached on described drum type brake filter screen 2 is blown off to described conically shaped 5; The dust brush being attached on described drum type brake filter screen 2 is dropped down onto described conically shaped 5 by wool yarn plate 4;
C, when the Dust Capacity in described conically shaped 5 reach setting value open described blanking seal valve 6, dust in described conically shaped 5 is dropped down onto in storage chamber 7, then heater 8 heats the dust in storage chamber 7, make the phosphorus condensing on dust evaporate into phosphorus steam, phosphorus steam rising reenters after described drum type brake filter screen 2, exports through the second flange-interface 15; Until when the interior without phosphorus steam output of storage chamber 7, described blanking seal valve 6 closures, close heater 8;
D until storage chamber 7 cooling after, open described discharging seal valve 9, draw off described dust;
E, closed discharging seal valve 9, open nitrogen intake valve 12 and air exhaust-valve 10, and the air in storage chamber 7 is drained stand-by; Repeat above-mentioned steps C.
The present invention has positive effect with respect to prior art: phosphorus steam dust removing device of the present invention, adopt filter cylinder (being drum type brake filter screen) by after phosphorus Steam Dust, send into successively heat exchanger and scrubbing tower, the bottom discharge mouth of heat exchanger and scrubbing tower immerses downwards to be received in phosphorus groove, realizes the recovery of high-purity phosphorus.
Brief description of the drawings
Fig. 1 is the structural representation of phosphorus steam dust removing device in embodiment 1;
Fig. 2 is the A-A cross-sectional view of Fig. 1.
Detailed description of the invention
Embodiment 1
See Fig. 1 to 2, the phosphorus steam dust removing device of the present embodiment comprises: column-shaped barrel 1, be located at this column-shaped barrel 1 top for inputting the first flange-interface 14 of described phosphorus steam, be located on the sidewall of this column-shaped barrel 1 for exporting the second flange-interface 15 of described phosphorus steam, be located at the drum type brake filter screen 2 in this column-shaped barrel 1, drive the driving mechanism of this drum type brake filter screen 2 around its central shaft rotation, axially be located at the air jet pipe 3 with removal dust for the inwall nitrogen-blow to this drum type brake filter screen 2 of the bottom interior wall setting of described drum type brake filter screen 2 interior and contiguous these drum type brake filter screens 2, axially be located at described drum type brake filter screen 2 outsides for brushing away the wool yarn plate 4 of the dust on described drum type brake filter screen 2, be connected in the obconic conically shaped 5 that is of described column-shaped barrel 1 lower end, be located at the blanking seal valve 6 of these conically shaped 5 lower ends, be located at the storage chamber 7 of these blanking seal valve 6 bottoms, be located at the discharging seal valve 9 of these storage chamber 7 bottoms, be located at the heater 8 in this storage chamber 7, be located at nitrogen air inlet pipe and air exhaust duct on storage chamber 7, be located at respectively being suitable in described nitrogen air inlet pipe and air exhaust duct and open and close nitrogen intake valve 12 and air exhaust-valve 10 simultaneously, the downstream pipeline of this air exhaust-valve 10 is provided with check valve 11. after blanking seal valve 6, discharging seal valve 9 closures, open nitrogen intake valve 12 and air exhaust-valve 10 simultaneously, be suitable for the air in storage chamber 7 to drain.
On air jet pipe 3, be distributed with fumarole down, for spraying nitrogen, prevent that described drum type brake filter screen 2 from stopping up.
The reduction box 13 that described driving mechanism comprises motor 16 and is in transmission connection with this motor 16, an end part seal of described drum type brake filter screen 2, the center of this end is provided with a rotating shaft, and the output shaft of this rotating shaft and described reduction box 13 is in transmission connection.
The other end of described drum type brake filter screen 2 is open type port, the second flange-interface 15 and the adjacent setting of described open type port. Preferably, the second flange-interface 15 is coaxially set with described open type port.
Preferably, described wool yarn plate 4 is located at the outside of the middle and lower part of described drum type brake filter screen 2, so that the dust that brush falls enters described conically shaped 5 fast.
While starting working, in described column-shaped barrel 1, conically shaped 5 and storage chamber 7, by being filled with the mode of nitrogen, discharge air, after phosphorus steam from mixing with air, blast preventing. Then closed blanking seal valve 6, discharging seal valve 9, nitrogen intake valve 12 and air exhaust-valve 10.
Phosphorus steam is sent into column-shaped barrel 1 through the first flange-interface 14, then enters drum type brake filter screen 2 downwards, then exports from the second flange-interface 15; Driving mechanism drives this drum type brake filter screen 2 around its central shaft rotation, and air jet pipe 3 sprays high pressure nitrogen, and the dust being attached on described drum type brake filter screen 2 is blown off to described conically shaped 5; The dust brush being attached on described drum type brake filter screen 2 is dropped down onto described conically shaped 5 by wool yarn plate 4.
Open blanking seal valve 6, dust in described conically shaped 5 is dropped down onto in storage chamber 7, and then heater 8 heats the dust in storage chamber 7, makes the phosphorus condensing on dust evaporate into phosphorus steam, phosphorus steam rising reenters after described drum type brake filter screen 2, exports through the second flange-interface 15; Until when the interior without phosphorus steam output of storage chamber 7, described blanking seal valve 6 closures, close heater 8; Until after storage chamber 7 is cooling, open described discharging seal valve 9, draw off described dust. Then closed discharging seal valve 9, opens nitrogen intake valve 12 and air exhaust-valve 10, and the air in storage chamber 7 is drained stand-by. Because the gasification temperature of phosphorus is lower, until storage chamber 7 is opened described discharging seal valve 9 after cooling again, can guarantee safety. Avoid occurring the risk of blasting after high temperature phosphorous steam mixes with air.
The present embodiment, adopts filter cylinder (being drum type brake filter screen) by after phosphorus Steam Dust, to send into successively heat exchanger and scrubbing tower, and the bottom discharge mouth of heat exchanger and scrubbing tower immerses downwards to be received in phosphorus groove, realizes the recovery of high-purity phosphorus.
Claims (2)
1. a phosphorus steam dust removing device, it is characterized in that comprising: column-shaped barrel (1), be located at this column-shaped barrel (1) top for inputting first flange-interface (14) of phosphorus steam, be located on the sidewall of this column-shaped barrel (1) for exporting second flange-interface (15) of described phosphorus steam, be located at the drum type brake filter screen (2) in this column-shaped barrel (1), drive the driving mechanism of this drum type brake filter screen (2) around its central shaft rotation, axially be located at the air jet pipe (3) with removal dust for the inwall nitrogen-blow to this drum type brake filter screen (2) of the bottom interior wall setting of interior and contiguous this drum type brake filter screen (2) of described drum type brake filter screen (2), axially be located at described drum type brake filter screen (2) outside for brushing away the wool yarn plate (4) of the dust on described drum type brake filter screen (2), what be connected in described column-shaped barrel (1) lower end is obconic conically shaped (5), be located at the blanking seal valve (6) of this conically shaped (5) lower end, be located at the storage chamber (7) of this blanking seal valve (6) bottom, be located at the discharging seal valve (9) of this storage chamber (7) bottom, be located at the heater (8) in this storage chamber (7), be located at nitrogen air inlet pipe and air exhaust duct on storage chamber (7), and be located at respectively the nitrogen intake valve (12) that is suitable for simultaneously opening and closing and the air exhaust-valve (10) in described nitrogen air inlet pipe and air exhaust duct,
Air jet pipe is distributed with fumarole down on (3);
One end part seal of described drum type brake filter screen (2), the other end is open type port;
The reduction box (13) that described driving mechanism comprises motor (16) and is in transmission connection with this motor (16), the center of the hermetic terminal of described drum type brake filter screen (2) is provided with a rotating shaft, and the output shaft of this rotating shaft and described reduction box (13) is in transmission connection;
Described wool yarn plate (4) is located at the outside of the middle and lower part of described drum type brake filter screen (2).
2. the method for work of phosphorus steam dust removing device according to claim 1, is characterized in that comprising the steps:
A, to being filled with nitrogen in described column-shaped barrel (1), conically shaped (5) and storage chamber (7) to discharge air; Then closed blanking seal valve (6), discharging seal valve (9), nitrogen intake valve (12) and air exhaust-valve (10);
B, phosphorus steam is sent into column-shaped barrel (1) through the first flange-interface (14), then enter drum type brake filter screen (2) downwards, then export from the second flange-interface (15);
Driving mechanism drives described drum type brake filter screen (2) around its central shaft rotation, and air jet pipe (3) ejection high pressure nitrogen, blows off the dust being attached on described drum type brake filter screen (2) to described conically shaped (5); The dust brush being attached on described drum type brake filter screen (2) is dropped down onto described conically shaped (5) by wool yarn plate (4);
C, when the Dust Capacity in described conically shaped (5) reach setting value open described blanking seal valve (6), dust in described conically shaped (5) is dropped down onto in storage chamber (7), then the dust in heater (8) heating storage chamber (7), make the phosphorus condensing on dust evaporate into phosphorus steam, phosphorus steam rising reenters after described drum type brake filter screen (2), exports through the second flange-interface (15); Until when in storage chamber (7), without phosphorus steam is exported, described blanking seal valve (6) closure, closes heater (8);
D until storage chamber (7) cooling after, open described discharging seal valve (9), draw off described dust;
E, closed discharging seal valve (9), open nitrogen intake valve (12) and air exhaust-valve (10), and the air in storage chamber (7) is drained stand-by.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410042893.6A CN103816736B (en) | 2012-06-29 | 2012-06-29 | Realize the phosphorus steam dust removing device that high-purity phosphorus reclaims |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410042893.6A CN103816736B (en) | 2012-06-29 | 2012-06-29 | Realize the phosphorus steam dust removing device that high-purity phosphorus reclaims |
| CN201210222666.2A CN102698541B (en) | 2012-06-29 | 2012-06-29 | Phosphorus steam dust cleaning device and working method thereof |
Related Parent Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210222666.2A Division CN102698541B (en) | 2012-06-29 | 2012-06-29 | Phosphorus steam dust cleaning device and working method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103816736A CN103816736A (en) | 2014-05-28 |
| CN103816736B true CN103816736B (en) | 2016-05-04 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201410042893.6A Expired - Fee Related CN103816736B (en) | 2012-06-29 | 2012-06-29 | Realize the phosphorus steam dust removing device that high-purity phosphorus reclaims |
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| Country | Link |
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| CN (1) | CN103816736B (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN117900968B (en) * | 2024-03-20 | 2024-05-24 | 摩多利智能传动(江苏)有限公司 | Surface machining device with protection function for planetary reducer |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003065030A (en) * | 2001-08-24 | 2003-03-05 | Koji Iizuka | Rotary filter type particulate removal device |
| CN1480239A (en) * | 2003-08-08 | 2004-03-10 | 暴辰生 | Filtration type gas separation and purification equipment with rapid moving filtering layer |
| CN101829461A (en) * | 2009-03-13 | 2010-09-15 | 北京柯林柯尔科技发展有限公司 | Method and device for purifying furnace gas generated by producing phosphoric acid through blast furnace process |
| CN201664557U (en) * | 2010-04-19 | 2010-12-08 | 上虞市锐新环境设备有限公司 | Welding fume purifier |
-
2012
- 2012-06-29 CN CN201410042893.6A patent/CN103816736B/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2003065030A (en) * | 2001-08-24 | 2003-03-05 | Koji Iizuka | Rotary filter type particulate removal device |
| CN1480239A (en) * | 2003-08-08 | 2004-03-10 | 暴辰生 | Filtration type gas separation and purification equipment with rapid moving filtering layer |
| CN101829461A (en) * | 2009-03-13 | 2010-09-15 | 北京柯林柯尔科技发展有限公司 | Method and device for purifying furnace gas generated by producing phosphoric acid through blast furnace process |
| CN201664557U (en) * | 2010-04-19 | 2010-12-08 | 上虞市锐新环境设备有限公司 | Welding fume purifier |
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| CN103816736A (en) | 2014-05-28 |
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Address after: Lishui District of Nanjing City, Jiangsu province 211219 zone five peak Honglan Town Industrial Road No. 55 Applicant after: Zou Yueming Address before: 213000 Tongjiang City, Jiangsu Province, North Road, No. 600 middle Jiangsu Yangtze River plastics market, building No. 9, No. 15, No. Applicant before: Zou Yueming |
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Inventor after: Zhong Jiong Inventor after: Wang Shaojing Inventor after: Hou Qunxiang Inventor after: Zou Yueming Inventor before: Zou Yueming |
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Address after: 225323, 1, Huan Xi Road, Diao Town, high port area, Jiangsu, Taizhou Patentee after: Zou Yueming Address before: Lishui District of Nanjing City, Jiangsu province 211219 zone five peak Honglan Town Industrial Road No. 55 Patentee before: Zou Yueming |
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Address after: 225321 Taizhou Province, high port road, Port Road, Hong Kong, South Road, 2 Patentee after: Zou Yueming Address before: 225323, 1, Huan Xi Road, Diao Town, high port area, Jiangsu, Taizhou Patentee before: Zou Yueming |
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Address after: High port Diao 225323 Jiangsu city in Taizhou Province, the Yangtze River Road No. 118 Patentee after: Zou Yueming Address before: 225321 Taizhou Province, high port road, Port Road, Hong Kong, South Road, 2 Patentee before: Zou Yueming |
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Granted publication date: 20160504 Termination date: 20180629 |