CN104307290A - Fertilizer producing exhaust gas dedusting device - Google Patents
Fertilizer producing exhaust gas dedusting device Download PDFInfo
- Publication number
- CN104307290A CN104307290A CN201410613990.6A CN201410613990A CN104307290A CN 104307290 A CN104307290 A CN 104307290A CN 201410613990 A CN201410613990 A CN 201410613990A CN 104307290 A CN104307290 A CN 104307290A
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- CN
- China
- Prior art keywords
- cyclone
- housing
- wall
- screen collector
- outlet
- 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.)
- Granted
Links
- 239000003337 fertilizer Substances 0.000 title claims abstract description 34
- 239000007788 liquid Substances 0.000 claims abstract description 28
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000855 fermentation Methods 0.000 claims abstract description 13
- 230000004151 fermentation Effects 0.000 claims abstract description 13
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 230000005855 radiation Effects 0.000 claims abstract description 5
- 239000000428 dust Substances 0.000 claims description 25
- 238000004140 cleaning Methods 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 8
- 238000007599 discharging Methods 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 4
- 239000000523 sample Substances 0.000 claims description 4
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 3
- 238000009413 insulation Methods 0.000 claims description 2
- 238000005507 spraying Methods 0.000 abstract description 3
- 238000004064 recycling Methods 0.000 abstract 1
- 239000000126 substance Substances 0.000 description 18
- 239000008187 granular material Substances 0.000 description 13
- 238000004519 manufacturing process Methods 0.000 description 9
- 238000000034 method Methods 0.000 description 5
- 239000007921 spray Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 230000003340 mental effect Effects 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000010257 thawing Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Landscapes
- Cyclones (AREA)
- Fertilizers (AREA)
Abstract
A fertilizer producing exhaust gas dedusting device comprises a shell and an inner space thereof, wherein a water curtain deduster and a plurality of swirlers distributed on the periphery of the water curtain deduster are arranged inside the shell; a liquid draining opening of the water curtain deduster is connected to a raw material recycling pipeline; the shell comprises an outer wall, an inner wall, and a cavity defined by the outer wall and the inner wall; an inlet and an outlet which can be communicated with the cavity are formed in the outer wall; the outer wall is a heat-insulating layer; the inner wall is a heat-conducting layer; molasses alcohol fermentation broth is communicated with the inlet, is heated through heat radiation of high-temperature gas, flows out from the outlet, and is conveyed to a liquid spraying device of the water curtain deduster through a diversion pipe. The fertilizer producing exhaust gas dedusting device is energy-saving, reasonable in design and easy to popularize.
Description
Technical field
The present invention relates to a kind of deduster, specifically, relate to a kind of cyclone type screen collector of fertilizer production.
Background technology
In chemical fertilizer production, modal technique is slurry-spraying pelletizing technique, and most chemical fertilizer granule is packed to be transported, but has small part particle because volume and quality is small swims in plant building, in order to remove these tiny chemical fertilizer granules, just need to use cleaner.But the cleaner that general factory uses is that many devices in series form, and floor space is excessive.Can produce a large amount of heat in chemical fertilizer production, these chemical fertilizer granules are by the process of removal of impurities, and these heats are often out in the cold, reasonably do not utilized.
Summary of the invention
The present invention has designed and developed a kind of dust arrester, and to solve, vent gas treatment in chemical fertilizer production is incomplete, dust arrester takes up an area huge, the irrational problem of using energy source.
Technical scheme provided by the invention is: a kind of fertilizer tail gas dust cleaning apparatus, and it comprises the space of housing and its inside, and described enclosure interior arranges screen collector and is distributed in several cyclones of described screen collector surrounding; Described housing is provided with air intake, gas outlet and loading head; Housing gas outlet is connected with blower and pipeline; Described cyclone comprises cyclone admission line, cyclone discharge duct and cyclone removing ash pipeline; Described screen collector comprises the leakage fluid dram of screen collector air inlet, screen collector gas outlet, liquid-jet device and bottom, and described liquid-jet device is one piece of high-voltage probe, and its front end arranges a umbrella baffle plate; Described cyclone admission line is connected to the air intake of housing parallel to each other, and described cyclone outlet pipe is connected to air intake corresponding to screen collector respectively, and the gas outlet of described housing is positioned at case top, and is communicated with described screen collector gas outlet; Being provided with the water curtain baffle plate that multiple height is straggly between described screen collector air intake to gas outlet, all there is the downward inclination angle of level in described water curtain baffle plate; Described cyclone ash discharging hole passes into the loading head of described housing, and described screen collector leakage fluid dram is connected to raw materials recovery pipeline.
Preferably, the cavity that described housing comprises outer wall, inwall and limited by this outer wall and inwall, described outer wall is provided with can with the entrance and exit of this cavity connects, described outer wall is heat insulation layer, described inwall is heat-conducting layer, molasses alcohol fermentation liquid is communicated to described entrance, and the thermal energy radiation through high-temperature gas flows out from described outlet, and described outlet is connected with described liquid-jet device by catheter.
Preferably, described housing comprises the back taper shell of the conical shell on top, the tubular shell at middle part and bottom, and described air intake is arranged on housing central section, and described loading head is arranged at the bottom of the cone of back taper housing.
Preferably, described cyclone admission line is the pipeline that one section of sectional dimension gradually changes.
Preferably, bottom described loading head or sidewall be provided with the opening can discharging gleanings.
Preferably, described screen collector and cyclone device fixture respectively and between housing.
Preferably, described shell of dust remover outer wall is fixed with mounting bracket.
The invention has the beneficial effects as follows: screen collector surrounding is arranged multiple cyclone dust collectors, reduce the floor space of cleaner greatly, multiple cyclone dust collectors are together in parallel and carry out first time dedusting to tail gas, save the time, again unified water curtain dedusting is carried out to the tail gas through cyclone dust collectors, ensure that purification efficiency; Because one of raw materials for production that the liquid of spray is used: molasses alcohol fermentation liquid needs to carry out preheating thawing and just can spray, so the shell of this dust arrester have employed double-decker, the high temperature of device inside is utilized to carry out preheating to the molasses alcohol fermentation liquid passed in cavity pocket of outer cover, be transferred to spray equipment again, such liquid sprayed out can directly reflux to the production equipment of upstream after mixed fertilizer granule, reaches the object of economize energy.
Accompanying drawing explanation
Fig. 1 is the structural representation of fertilizer tail gas dust cleaning apparatus of the present invention.
Fig. 2 is cyclone inside top figure.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is described in further detail, can implement according to this with reference to description word to make those skilled in the art.
As shown in Figure 1 and Figure 2, a kind of fertilizer tail gas dust cleaning apparatus, it comprises the space of housing 3 and its inside, and enclosure interior arranges screen collector 1 and is distributed in 2 cyclones 2,2 ' of described screen collector 1 surrounding; Housing is provided with air intake 31, gas outlet 32 and loading head 33, and housing gas outlet 32 is connected by pipeline 8 with blower fan 7; Cyclone comprises cyclone admission line 21, cyclone discharge duct 22 and cyclone removing ash pipeline 23; Screen collector 1 comprises the leakage fluid dram 14 of screen collector air inlet 11, screen collector gas outlet 12, liquid-jet device 13 and bottom; Liquid-jet device is one piece of high-voltage probe, pressure is 1500bar, environment-friendly high-efficiency, its front end arranges a umbrella baffle plate 15, its umbrella baffle plate height is 20cm, radius is 40cm, and this baffle plate distance probe distance is 15cm, can ensure that liquid can form the complete liquid film layer blocking screen collector cross section in splash after umbrella baffle plate 15 with this understanding; Cyclone admission line 21 is connected to the air intake 31 of housing parallel to each other, and cyclone outlet pipe 22 is connected to air intake corresponding to screen collector respectively, and the gas outlet 32 of housing is positioned at case top, and screen collector gas outlet 12 is communicated with; Being provided with the water curtain baffle plate 16 that multiple height is straggly between screen collector air intake to gas outlet, all there is level downward 10 in water curtain baffle plate.Inclination angle, facilitate liquid flow; Cyclone ash discharging hole 23 passes into the loading head 33 of described housing, screen collector leakage fluid dram 14 is connected to raw materials recovery pipeline, the liquid of liquid-jet device spray is molasses alcohol fermentation liquid, molasses alcohol fermentation liquid is the one of chemical fertilizer production raw material, now be used as the fluid of water curtain dedusting, then can be communicated in raw material liquid pool after being mixed with chemical fertilizer granule and carry out chemical fertilizer production.
The cavity that housing comprises outer wall, inwall and limited by this outer wall and inwall, outer wall makes by pressing from both sides glass fibre cotton in stainless steel iron sheet, this material thermal conductivity is low, sound-absorbing effect is good, therefore both can ensure that the heat in housing was not wasted, also can completely cut off the noise sent when dust arrester runs; Inwall is the alloy material of 3-5mm by thickness, outer wall is provided with and with the entrance 34 of this cavity connects and 35 can be exported, molasses alcohol fermentation liquid is communicated to described entrance 34, and the thermal energy radiation through high-temperature gas flows out from outlet 35, and described outlet 35 is connected with liquid-jet device 13 by mozzle.
Housing comprises the back taper shell of the conical shell on top, the tubular shell at middle part and bottom, and air intake is arranged on housing central section, and loading head is arranged at the bottom of the cone of back taper housing.
Cyclone admission line is the pipeline that one section of sectional dimension gradually changes, and can accelerate air-flow mobility.
Bottom loading head or sidewall be provided with the opening 331 can discharging gleanings, be provided with butterfly valve herein, be convenient to control dust discharge.
Respectively and be provided with fixture 4 between housing, the equipment that ensure that keeps firm under high flow rate gas impacts for screen collector and cyclone.
Be fixed with mounting bracket 5 at shell of dust remover outer wall, it adopts crashproof reinforcing bar to be made, and support is provided with the cross bar that many rows trample for people, facilitates workman to check dust arrester.
During the work of this equipment, the air being mingled with chemical fertilizer granule enters housing through air intake, then enter in cyclone dust collectors by cyclone admission line in parallel, at this moment air directly enters cyclone blast pipe, and the large chemical fertilizer granule of relative weight is subject to circle mental power function, circle round in cyclone fuselage, along with the air being mingled with dust constantly enters in cyclone, air and chemical fertilizer granule are pushed to cyclone blast pipe and cyclone removing ash pipeline respectively.Because cyclone separator can only be separated the particle that diameter is greater than 5 microns, enter in screen collector together with air so contain the chemical fertilizer granule that diameter is less than 5 microns.
In the process of removal of impurities, because chemical fertilizer granule is obtained by slurry-spraying pelletizing technique, so a large amount of heat energy can be carried, cavity be in the housing provided with can with the entrance and exit of this cavity connects, molasses alcohol fermentation liquid is communicated to described entrance, thermal energy radiation through high-temperature gas flows out from described outlet, find by measuring, through the molasses alcohol fermentation liquid of heat exchange, 73 DEG C can be risen to from original 25 DEG C of normal temperature, now molasses alcohol fermentation liquid melts completely, liquid-jet device is delivered to by catheter, during high-pressure nozzle running, the liquid that high-pressure nozzle spouting velocity is exceedingly fast, when liquid runs into umbrella baffle plate, liquid leaves to surrounding, thus form one liquid barrier, water curtain dirt pocket is separated, when the air being mingled with small chemical fertilizer granule moves to housing outlets, air is directly through liquid barrier, small chemical fertilizer granule is then left in liquid, and the water curtain baffle plate in screen collector also can form cascade, thus magazins' layout is carried out to air, the liquid used due to water curtain dedusting is molasses alcohol fermentation liquid, it itself is one of raw material of chemical fertilizer production, so the molasses alcohol fermentation liquid being mingled with chemical fertilizer granule is connected to raw materials recovery pipeline through screen collector leakage fluid dram, achieve the repeatedly utilization of material, economize in raw materials.
Although embodiment of the present invention are open as above, but it is not restricted to listed in description and embodiment utilization, it can be applied to various applicable the field of the invention completely, for those skilled in the art, can easily realize other amendment, therefore do not deviating under the universal that claim and equivalency range limit, the present invention is not limited to specific details and illustrates here and the legend described.
Claims (7)
1. a fertilizer tail gas dust cleaning apparatus, it comprises the space of housing and its inside, it is characterized in that:
Described enclosure interior arranges screen collector and is distributed in several cyclones of described screen collector surrounding; Described housing is provided with air intake, gas outlet and loading head; Housing gas outlet is connected with blower and pipeline; Described cyclone comprises cyclone admission line, cyclone discharge duct and cyclone removing ash pipeline; Described screen collector comprises the leakage fluid dram of screen collector air inlet, screen collector gas outlet, liquid-jet device and bottom, and described liquid-jet device is one piece of high-voltage probe, and its front end arranges a umbrella baffle plate; Described cyclone admission line is connected to the air intake of housing parallel to each other, and described cyclone outlet pipe is connected to air intake corresponding to screen collector respectively, and the gas outlet of described housing is positioned at case top, and is communicated with described screen collector gas outlet; Being provided with the water curtain baffle plate that multiple height is straggly between described screen collector air intake to gas outlet, all there is the downward inclination angle of level in described water curtain baffle plate; Described cyclone ash discharging hole passes into the loading head of described housing, and described screen collector leakage fluid dram is connected to raw materials recovery pipeline.
2. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, it is characterized in that: the cavity that described housing comprises outer wall, inwall and limited by this outer wall and inwall, described outer wall is provided with can with the entrance and exit of this cavity connects, described outer wall is heat insulation layer, described inwall is heat-conducting layer, molasses alcohol fermentation liquid is communicated to described entrance, and the thermal energy radiation through high-temperature gas flows out from described outlet, and described outlet is connected with described liquid-jet device by catheter.
3. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, it is characterized in that: described housing comprises the back taper shell of the conical shell on top, the tubular shell at middle part and bottom, described air intake is arranged on housing central section, and described loading head is arranged at the bottom of the cone of back taper housing.
4. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, is characterized in that: described cyclone admission line is the pipeline that one section of sectional dimension gradually changes.
5. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, is characterized in that: bottom described loading head or sidewall be provided with the opening can discharging gleanings.
6. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, is characterized in that: described screen collector and cyclone device fixture respectively and between housing.
7. fertilizer tail gas dust cleaning apparatus as claimed in claim 1, is characterized in that: described shell of dust remover outer wall is fixed with mounting bracket.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410613990.6A CN104307290B (en) | 2014-11-04 | 2014-11-04 | Fertilizer tail gas dust cleaning apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410613990.6A CN104307290B (en) | 2014-11-04 | 2014-11-04 | Fertilizer tail gas dust cleaning apparatus |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN104307290A true CN104307290A (en) | 2015-01-28 |
| CN104307290B CN104307290B (en) | 2015-12-09 |
Family
ID=52362684
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410613990.6A Active CN104307290B (en) | 2014-11-04 | 2014-11-04 | Fertilizer tail gas dust cleaning apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104307290B (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105214429A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | Be applicable to the cyclone dust collector of high temperature dust tail gas recycle |
| CN105214430A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | High temperature dust tail gas dust cleaning apparatus |
| CN105214428A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | Be applicable to the dust arrester of high temperature dust tail gas recycle |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62144733A (en) * | 1977-11-17 | 1987-06-27 | チバ・ガイギ−，アクチエンゲゼルシヤフト | Method for purifying waste gas |
| CN201208539Y (en) * | 2008-05-09 | 2009-03-18 | 苏州艾特斯环保材料有限公司 | Combined purifying device for coking waste gas |
| CN201231130Y (en) * | 2008-07-29 | 2009-05-06 | 中冶集团北京冶金设备研究设计总院 | Flue gas desulfurization device for producing ammonia sulfate fertilizer |
| CN201277580Y (en) * | 2008-09-23 | 2009-07-22 | 单既建 | Boiler dust remover |
| CN203329566U (en) * | 2013-07-05 | 2013-12-11 | 河南晋开化工投资控股集团有限责任公司 | Compound fertilizer tail-gas washing device |
| CN204073769U (en) * | 2014-11-04 | 2015-01-07 | 广西天源生物之本环保科技有限公司 | Fertilizer tail gas dust cleaning apparatus |
-
2014
- 2014-11-04 CN CN201410613990.6A patent/CN104307290B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS62144733A (en) * | 1977-11-17 | 1987-06-27 | チバ・ガイギ−，アクチエンゲゼルシヤフト | Method for purifying waste gas |
| CN201208539Y (en) * | 2008-05-09 | 2009-03-18 | 苏州艾特斯环保材料有限公司 | Combined purifying device for coking waste gas |
| CN201231130Y (en) * | 2008-07-29 | 2009-05-06 | 中冶集团北京冶金设备研究设计总院 | Flue gas desulfurization device for producing ammonia sulfate fertilizer |
| CN201277580Y (en) * | 2008-09-23 | 2009-07-22 | 单既建 | Boiler dust remover |
| CN203329566U (en) * | 2013-07-05 | 2013-12-11 | 河南晋开化工投资控股集团有限责任公司 | Compound fertilizer tail-gas washing device |
| CN204073769U (en) * | 2014-11-04 | 2015-01-07 | 广西天源生物之本环保科技有限公司 | Fertilizer tail gas dust cleaning apparatus |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105214429A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | Be applicable to the cyclone dust collector of high temperature dust tail gas recycle |
| CN105214430A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | High temperature dust tail gas dust cleaning apparatus |
| CN105214428A (en) * | 2015-10-31 | 2016-01-06 | 张继金 | Be applicable to the dust arrester of high temperature dust tail gas recycle |
Also Published As
| Publication number | Publication date |
|---|---|
| CN104307290B (en) | 2015-12-09 |
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