CN205127747U - Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment - Google Patents
Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment Download PDFInfo
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- CN205127747U CN205127747U CN201520987090.8U CN201520987090U CN205127747U CN 205127747 U CN205127747 U CN 205127747U CN 201520987090 U CN201520987090 U CN 201520987090U CN 205127747 U CN205127747 U CN 205127747U
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Abstract
Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment is including centrifugation reaction mouse wheel and gas - water separation tower, centrifugation reaction mouse wheel is provided with the support blade including barrel shell, rotation mouse wheel, rotary drive motor, admission line, pivot, the tip of pivot, and the support blade is taken turns along the radial and rotatory mouse of rotatory mouse wheel and is linked to each other, is provided with the filter screen on the periphery of rotatory mouse wheel, and the admission line is located one side that rotatory mouse wheel was provided with the support blade, is provided with the spray pipe outside the support blade, is provided with high pressure nozzle on the spray pipe, the gas outlet of barrel shell is located the circumference of rotatory mouse wheel, and the barrel shell passes through connecting tube and gas - water separation tower intercommunication, the gas - water separation tower is including admitting air chamber, disengagement chamber and play air cavity, and the chamber of admitting air links to each other with the connecting tube, and it is provided with the division board between chamber and the disengagement chamber to admit air, is provided with in admit air chamber and/or the disengagement chamber and strains a section of thick bamboo. The utility model discloses the desulfurization is efficient, and the gas -water ratio is little, and required power is little, saves water and energy, and area is little, and the cost is lower.
Description
Technical field
The utility model relates to a kind of environmental protection equipment, particularly relates to the desulfurization used in a kind of ammonia desulfurizing process, de-liquid equipment.
Background technology
Along with expanding economy, the progress of society and the enhancing of people's environmental consciousness, industrial smoke removes SO2, day by day comes into one's own.In recent years, country strengthened supervision to atmospheric environment and improvement, had formulated relevant policies and standard limit of smog release, had made strict rules in standard limit of smog release to SO2 content.Various sulfur removal technology arises at the historic moment under these circumstances.Sulfur removal technology divides wet method, dry method and semidry method.Dry method and semidry method seldom adopt because of shortcomings such as desulfurization degree are low, operating cost is high.The great majority of present use are wet desulfurizing process.Wet desulphurization method is a lot, as alkali lye desulfurization, the ammonia process of desulfurization, lime desulfurization, lime stone desulfurization of gypsum etc.Ammonia desulfurizing process reacts according to ammonia and sulfur dioxide, water the Basic Mechanism generating desulfurization product to carry out, and mainly contains wet-type ammonia, EA-FGD, impulse electric corona ammonia process, simple and easy ammonia process etc.
The patent No. is that the Chinese invention patent of 95110084.X discloses a kind of survey spray type centrifugal desulfurizing and dedusting device, and it is desulfurization dust-removal system in a kind of pipeline.Its operation principle installs this system additional between deduster and air-introduced machine or between air-introduced machine and chimney, and it is made up of flue, spray equipment, swirl-flow devices, expansion joint, moisture trap and water system.The course of work of this system be flow through deduster sulfurous gas after entering house outlet, in the side of its pipeline, high-pressure nozzle is installed, after the calcium hydroxide water atomization that high-pressure nozzle is got with perpendicular through collide containing the flue gas of sulfur dioxide, decompose, its moisture gas is under the effect of air-introduced machine negative pressure, in the process that swirl-flow devices tube wall is descending, through expansion joint, because caliber tapering expands, wind speed at this place reduces, make moisture gas obtain a part at this place to be separated, it is multiplexing that the pipeline of water after separation bottom expansion joint enters circulating water pool, moisture gas carries out secondary drainage after entering moisture trap, gas is after moisture trap, enter expansion joint and carry out three drainages, the pipeline of water after separation bottom expansion joint enters moisture trap hypocentrum, circulating water pool is entered multiplexing through flapper, flue gas after drainage, through air-introduced machine pressurization, enters chimney and enters air.But this system is only as the coarse filtration system of flue gas desulphurization system, desulfuration efficiency is within 70%, and in the course of work, the time of contact of flue gas and calcium hydroxide aqueous solution is short, the sulfur dioxide in gas effectively cannot be decomposed at short notice; And containing granule impurity in calcium hydroxide aqueous solution, easily make high-pressure nozzle block, cause water-aspirator pressure large, burn-down of electric motor, water spray reduce, do not reach desulfurized effect; Dehydration carries out in the duct simultaneously, and owing to limitting by field condition, the dehydrating effect between deduster and blower fan can not be very good, easily to cause on draught fan impeller with aqueous particulate thing, causes draught fan impeller uneven, cause blower fan vibrations greatly, chimney rains lime; The calcium sulfate produced in process of production is without value, and containing nuisance, carry out after harmless treatment can landfill, and the later stage is very expensive.
The patent No. be 200620028221.0 Chinese utility model patent disclose a kind of dust-remover machine, it is that a kind of minitype vertical type rotates desulfurizer, this device has inlet and outlet, when sulfurous gas enters the cigarette channel excessively of the machine from air inlet, the doctor solution sprayed with spray equipment mixes, the centrifugal desulfurizing device that mixed gas-liquid is rotating falls out filter course, and carry out gas-liquid separation, liquid after separation flows into desulfurization liquid pool from separating tank through pipeline, recycle, gas inlet and outlet enters air-introduced machine, emptying through chimney.This device is vertical desulfurizer, when installing filter course and changing bearing, the pipeline connecting air outlet must be removed together, repair time is long, and maintenance cost is large, and moisture trap is in centrifugal separation processes, because pipe diameter is little, wind speed can not reduce, and part water can enter air-introduced machine through wind pipe, causes draught fan impeller band water unbalance, cause vibrations, chimney can discharge a large amount of acidity, alkaline water, contaminated environment, water resource waste simultaneously.Quick lime has particle in the process of hydrolysis, easily stifled match shower nozzle, and changes difficulty; The aqua calcis that shower nozzle sprays simultaneously easily blocks filter course, causes blower negative pressure to increase, and power consumption improves, and desulfuration efficiency reduces; Doctor solution easily forms secondary pollution, and the calcium sulfate of generation has harmful components, and without value, landfill easily produces pollution.Present country forbids landfill, and processing cost is very high.
Summary of the invention
The purpose of this utility model is to provide the centrifugal desulfurizing that a kind of cost is low, desulfuration efficiency is high, de-liquid equipment.
To achieve these goals, the utility model takes following technical solution:
The wheeled head-on collision centrifugal desulfurizing of mouse, de-liquid equipment, comprise centrifugal reaction mouse wheel and gas-water separation tower, described centrifugal reaction mouse wheel comprises cylinder shell, be arranged at the rotation mouse wheel in described cylinder shell, drive the rotary drive motor that described rotation mouse wheel rotates, the admission line be communicated with in described cylinder shell, along the rotating shaft that the axis of described rotation mouse wheel is taken turns through described rotation mouse, the end of described rotating shaft is provided with support blade, described support blade rotates mouse along the radial direction of described rotation mouse wheel and takes turns with described and be connected, the periphery of described rotation mouse wheel is provided with screen pack, described admission line is positioned at the side that described rotation mouse wheel is provided with support blade, described support blade arranged outside has sparge pipe, described sparge pipe is provided with high-pressure nozzle, the gas outlet of described cylinder shell is positioned at described rotation mouse wheel circumferentially, and described cylinder shell is communicated with gas-water separation tower by connecting pipe, described gas-water separation tower comprises the inlet chamber, disengagement chamber and the outlet chamber that set gradually from the bottom up, described inlet chamber is connected with connecting pipe, demarcation strip is provided with between described inlet chamber and disengagement chamber, be provided with at least one filter cylinder longitudinally arranged in described inlet chamber and/or described disengagement chamber, the periphery of described demarcation strip and described filter cylinder is provided with multiple through hole.
Further, described rotation mouse wheel is provided with two circle mouse wheel support bars, screen pack is arranged between outer ring mouse wheel support bar and inner ring mouse wheel support bar.
Further, the two ends of described rotating shaft are provided with support blade, described admission line be arranged at described rotation mouse wheel shaft to both sides.
Further, described sparge pipe is annular, and described high-pressure nozzle is circumferentially arranged at intervals on described sparge pipe.
Further, the water spraying direction of described high-pressure nozzle is parallel with the tangential direction on described support blade blade face.
Further, described filter cylinder is arranged on described demarcation strip.
Further, described demarcation strip is provided with 3 filter cylinders.
From above technical scheme, desulphurization plant of the present utility model comprises centrifugal reaction mouse wheel and gas-water separation tower, utilize the centrifugal force rotating mouse wheel and produce, catalyst and flue gas are fully clashed in rotation mouse wheel, mixing, under the effect of catalyst, and the screen pack utilizing mouse to take turns on periphery forms rapid reaction zone, catalyst and flue gas fully can be reacted in screen pack, hydrone containing catalyst is when by screen pack, it becomes brin from drop, become liquid film again, specific area expands original 100 times ~ 500 times to, effectively can make catalyst and sulfur dioxide generation fast reaction, make the absorption of catalyzed dose of sulfur dioxide, then the gas-vapor mix after adopting gas-water separation tower to make abundant hybrid reaction is separated.Compared with spray type desulphurization equipment, sulfurous gas and high pressure are brought in the wheeled reactor of mouse containing the aqueous solution of catalyst by the negative pressure that the utility model utilizes axial blade to produce, by side air inlet formed head-on collision high pressure catalyst and sulfurous gas carry out high speed head-on collision, pass through screen pack through reduction of speed simultaneously, under the effect of the centrifugal force of middling speed rotation, the brin that sulfur dioxide is filtered in net fully exchanges, and is converted into ammonium sulfate; The water smoke produced is with flue gas after moisture trap is separated, and ammonium sulfate solution enters catalyst solution pond, and recycling, the high clean air (sulfur-bearing 15%) after separation enters air through chimney.It is little that this equipment has floor space, the concentration of production, and automaticity is high, and energy consumption is low, water saving, the ammonium sulfate simultaneously produced by dehydration, distillation after for agricultural production, gas-water ratio is little, and desulfuration efficiency is higher.This technology is compared with traditional desulfurization, its water saving is 1/40, economize on electricity is 1/10, floor space saves 1/10, and can carry out newly-built or reconstruction, discharge can reach ultra-clean discharge standard 30mg/Nm3(15mg/Nm3) below, and desulfurization afterproduct can generate ammonium sulfate solids thing after distillation, be applied to agrochemical, can turn waste into wealth, benefit the nation and the people.
Accompanying drawing explanation
Fig. 1 is the structural representation figure of the utility model embodiment.
Fig. 2 is the front view of the utility model embodiment.
Fig. 3 is the top view of Fig. 1.
Fig. 4 is the side view of Fig. 1.
Fig. 5 is the structural representation of the utility model centrifugal reaction mouse wheel.
Fig. 6 is the structural representation after centrifugal reaction mouse wheel removes shell.
Fig. 7 is the top view of Fig. 6.
Fig. 8 is the structural representation of the utility model gas-water separation tower.
Fig. 9 is the decomposition texture schematic diagram of the utility model gas-water separation tower.
Below in conjunction with accompanying drawing, detailed description of the invention of the present utility model is described in more detail.
Detailed description of the invention
Referring to figs. 1 through Fig. 4, centrifugal desulfurizing of the present utility model, de-liquid equipment comprise centrifugal reaction mouse and take turns 1 and reacted mouse by connecting pipe 2 take turns 1 gas-water separation tower be connected 3 with centrifugal.Composition graphs 5, Fig. 6 and Fig. 7, centrifugal reaction mouse wheel 1 comprises cylinder shell 1-1, admission line 1-2, rotary drive motor 1-3, rotates mouse wheel 1-4, support blade 1-5, rotating shaft 1-6, sparge pipe 1-7 and high-pressure nozzle 1-8.
Rotating mouse wheel 1-4 is arranged in cylinder shell 1-1, rotating shaft 1-6 is along rotating the axis of mouse wheel 1-4 through rotating mouse wheel 1-4, rotating shaft 1-6 takes turns 1-4 by support blade 1-5 with rotation mouse and is connected, support blade 1-5 is along rotating the radial direction of mouse wheel 1-4 and rotating mouse and take turns 1-4 and to be connected and circumferentially uniform intervals is arranged, support blade is the connecting framework between the reel of inlet end mouse wheel and rotor cover plate, is again the axial blade between them.The rotating shaft 1-6 of the present embodiment is connected with rotary drive motor 1-3 by reductor and driving belt.The periphery rotating mouse wheel 1-4 is provided with screen pack or filter pulp (not shown), preferably, during in order to ensure that rotating mouse wheel 1-4 rotates, screen pack or filter pulp can not depart from from rotation mouse wheel 1-4 under centrifugal action, the rotation mouse wheel 1-4 of the present embodiment is provided with two circle mouse wheel support bar 1-10, screen pack or filter pulp are arranged between outer ring mouse wheel support bar and inner ring mouse wheel support bar, with this fixing screen pack or filter pulp.The thickness of screen pack or filter pulp can be 50 ~ 400mm.
Admission line 1-2 is arranged at the side rotating mouse wheel 1-4 axis, and it is communicated with in cylinder shell 1-1, and flue gas enters in cylinder shell 1 from admission line 1-2, and enters rotation mouse wheel 1-4 from the gap (wind channel) between support blade 1-5.As a preferred embodiment of the present utility model, admission line 1-2 is arranged at the both sides rotating mouse wheel 1-4 axis, and flue gas can enter from both sides simultaneously rotate in mouse wheel 1-4.Sparge pipe 1-7 is arranged at the outside of support blade 1-5, and the sparge pipe 1-7 of the present embodiment is annular, and on sparge pipe 1-7, circumferentially interval is furnished with high-pressure nozzle 1-8, and sparge pipe 1-7 is connected with outside water tank by inlet channel 1-9.Further, high-pressure nozzle 1-8 water spraying direction parallel with the tangential direction on support blade 1-5 blade face, thus can by catalyst by high-pressure nozzle correlation, clash into enter rotate mouse wheel 1-4 in.The gas outlet of cylinder shell 1-1 is positioned on the periphery of rotation mouse wheel 1-4, and cylinder shell 1-1 is communicated with gas-water separation tower 3 by connecting pipe 2.
Composition graphs 8 and Fig. 9, gas-water separation tower 3 comprises inlet chamber 3-1, disengagement chamber 3-2, outlet chamber 3-3, demarcation strip 3-4, filter cylinder 3-5.Inlet chamber 3-1, disengagement chamber 3-2, outlet chamber 3-3 sets gradually from the bottom up, inlet chamber 3-1 is connected with connecting pipe 2, demarcation strip 3-4 is arranged between inlet chamber 3-1 and disengagement chamber 3-2, demarcation strip 3-4 is processed with multiple through hole, demarcation strip 3-4 is provided with at least one filter cylinder 3-5, filter cylinder 3-5 is longitudinally arranged on demarcation strip 3-4, the periphery of filter cylinder 3-5 is provided with multiple through hole equally, by arranging through hole on the periphery of filter cylinder 3-5, the contact area of filter cylinder 3-5 and gas-vapor mix can be increased, further, filtrate can be added outside the periphery of filter cylinder 3-5, when being with liquid gas by filtrate, water is intercepted by filtrate, clean gas is discharged by filtrate, owing to increasing the resistance of gas-vapor mix flowing, ensure gas-water separation effect.
Below the course of work of the utility model desulphurization plant is described:
Sulfur-containing smoke gas enters cylinder shell 1-1 through admission line 1-2 from the axial side rotating mouse wheel 1-4, rotary drive motor 1-3 drive shaft 1-6 rotates, thus rotation mouse wheel 1-4 is rotated in cylinder shell 1-1, sulfur-containing smoke gas enters from the wind channel between support blade 1-5 and rotates in mouse wheel 1-4, catalyst passes in sparge pipe 1-7 through inlet channel 1-9 simultaneously, spraying into through high-pressure nozzle 1-9 rotates in mouse wheel 1-4 again, because high-pressure nozzle 1-9 is positioned at outside support blade 1-5, when high-pressure nozzle 1-9 sprays water in rotation mouse wheel 1-4, can the support blade 1-5 rotating mouse wheel 1-4 rotation be followed to cut, thus formation water smoke, water smoke and flue gas are taken turns in 1-4 and are fully mixed rotating mouse, in order to extend the reaction time of water smoke and flue gas, the periphery position that the utility model is rotating mouse wheel 1-4 arranges screen pack or filter pulp, when water smoke and flue gas are got rid of to screen pack or filter pulp under centrifugal action, meeting abundant hybrid reaction on screen pack or filter pulp, then gas-vapor mix is thrown out of outside screen pack or filter pulp under the further effect of rotary centrifugal force rotating mouse wheel 1-4, enter in gas-water separation tower 3 by connecting pipe 2, after gas-vapor mix enters the inlet chamber 3-1 of gas-water separation tower 3, enter in disengagement chamber 3-2 by the through hole on demarcation strip 3-4, and be separated further by filter cylinder 3-5, liquid is blocked by filter cylinder 3-5 and demarcation strip 3-4, fall back into bottom air cavity 3-1, and entering in circulation, gas then discharges through outlet chamber 3-3.
Centrifugal desulfurizing equipment desulfuration efficiency of the present utility model is high, and gas-water ratio is little, and required drive is little, saves water and energy, and compared with tower desulphurization plant, floor space is little, and cost is lower.
Certainly, technical conceive of the present utility model is not limited in above-described embodiment, many different concrete schemes can also be obtained according to design of the present utility model, such as, in previous embodiment, in the both sides of centrifugal reaction mouse wheel, all admission line is set, but also only admission line can be set one-sided, sparge pipe can be annular, also can be square, triangle or other shape, filter cylinder can be arranged at above demarcation strip or below demarcation strip, or all arranges filter cylinder above and below demarcation strip; Rotating shaft also can directly be driven by rotary drive motor, and without the need to reductor and driving member; Support blade also can adopt cylindricality etc., and such as these change and equivalent transformation all should be included within scope described in the utility model.
Claims (9)
1. the wheeled head-on collision centrifugal desulfurizing of mouse, de-liquid equipment, is characterized in that, comprises centrifugal reaction mouse wheel and gas-water separation tower;
Described centrifugal reaction mouse wheel comprises cylinder shell, be arranged at the rotation mouse wheel in described cylinder shell, drive the rotary drive motor that described rotation mouse wheel rotates, the admission line be communicated with in described cylinder shell, along the rotating shaft that the axis of described rotation mouse wheel is taken turns through described rotation mouse, the end of described rotating shaft is provided with support blade, described support blade rotates mouse along the radial direction of described rotation mouse wheel and takes turns with described and be connected, the periphery of described rotation mouse wheel is provided with screen pack, described admission line is positioned at the side that described rotation mouse wheel is provided with support blade, described support blade arranged outside has sparge pipe, described sparge pipe is provided with high-pressure nozzle,
The gas outlet of described cylinder shell is positioned at described rotation mouse wheel circumferentially, and described cylinder shell is communicated with gas-water separation tower by connecting pipe; Described gas-water separation tower comprises the inlet chamber, disengagement chamber and the outlet chamber that set gradually from the bottom up, described inlet chamber is connected with connecting pipe, demarcation strip is provided with between described inlet chamber and disengagement chamber, be provided with at least one filter cylinder longitudinally arranged in described inlet chamber and/or described disengagement chamber, the periphery of described demarcation strip and described filter cylinder is provided with multiple through hole.
2. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: described rotation mouse wheel is provided with two circle mouse wheel support bars, screen pack is arranged between outer ring mouse wheel support bar and inner ring mouse wheel support bar.
3. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: the two ends of described rotating shaft are provided with support blade, described admission line be arranged at described rotation mouse wheel shaft to both sides.
4. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: described sparge pipe is annular, and described high-pressure nozzle is circumferentially arranged at intervals on described sparge pipe.
5. the wheeled head-on collision centrifugal desulfurizing of the mouse according to claim 1 or 4, de-liquid equipment, is characterized in that: the water spraying direction of described high-pressure nozzle is parallel with the tangential direction on described support blade blade face.
6. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: described filter cylinder is arranged on described demarcation strip.
7. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 6, de-liquid equipment, is characterized in that: described demarcation strip is provided with 3 filter cylinders.
8. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: described screen pack thickness is 50 ~ 400mm.
9. the wheeled head-on collision centrifugal desulfurizing of mouse according to claim 1, de-liquid equipment, is characterized in that: the periphery arranged outside of described filter cylinder has filtrate.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520987090.8U CN205127747U (en) | 2015-12-02 | 2015-12-02 | Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520987090.8U CN205127747U (en) | 2015-12-02 | 2015-12-02 | Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment |
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| Publication Number | Publication Date |
|---|---|
| CN205127747U true CN205127747U (en) | 2016-04-06 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520987090.8U Expired - Fee Related CN205127747U (en) | 2015-12-02 | 2015-12-02 | Centrifugal desulfurization of wheeled head -on collision of mouse, take off liquid equipment |
Country Status (1)
| Country | Link |
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| CN (1) | CN205127747U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289296A (en) * | 2015-12-02 | 2016-02-03 | 宝鸡市晋旺达机械设备有限公司 | Mouse wheel type centrifugal desulfurization and liquid-removal equipment |
| CN113164865A (en) * | 2019-03-08 | 2021-07-23 | 北京康肯环保设备有限公司 | Exhaust gas purification device and exhaust gas harmful removal device using same |
| CN117547920A (en) * | 2024-01-09 | 2024-02-13 | 三鑫特材(常州)股份有限公司 | Dust collector of rolling mill export |
-
2015
- 2015-12-02 CN CN201520987090.8U patent/CN205127747U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105289296A (en) * | 2015-12-02 | 2016-02-03 | 宝鸡市晋旺达机械设备有限公司 | Mouse wheel type centrifugal desulfurization and liquid-removal equipment |
| CN113164865A (en) * | 2019-03-08 | 2021-07-23 | 北京康肯环保设备有限公司 | Exhaust gas purification device and exhaust gas harmful removal device using same |
| CN117547920A (en) * | 2024-01-09 | 2024-02-13 | 三鑫特材(常州)股份有限公司 | Dust collector of rolling mill export |
| CN117547920B (en) * | 2024-01-09 | 2024-04-02 | 三鑫特材(常州)股份有限公司 | Dust collector of rolling mill export |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160406 Termination date: 20201202 |
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| CF01 | Termination of patent right due to non-payment of annual fee |