CN204799092U - Set up glass fiber stove waste gas desulphurization unit of turbocharged torrent ware - Google Patents
Set up glass fiber stove waste gas desulphurization unit of turbocharged torrent ware Download PDFInfo
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- CN204799092U CN204799092U CN201520366926.2U CN201520366926U CN204799092U CN 204799092 U CN204799092 U CN 204799092U CN 201520366926 U CN201520366926 U CN 201520366926U CN 204799092 U CN204799092 U CN 204799092U
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Abstract
The utility model discloses set up glass fiber stove waste gas desulphurization unit of turbocharged torrent ware relates to the environmental protection technology field. Its stove flue gas pipe and benefit blast gate, forced air cooling tower and cooling cooling tower, the cooling cooling tower is fixed by the pipeline with the desulfurizing tower, stove flue gas pipe and air -cooled tower, the cooling cooling tower is organized fixedly with atomizing nozzle, cooling cooling tower and the pipeline that inserts the circulating slot, the pipeline that receives the groove and insert the circulating slot is fixed, the desulfurizing tower inner wall is organized with the (operating) water nozzle in proper order, the desulfurization injector set, turbocharged torrent ware, it is fixed to receive the groove, establish the agitator in the circulating slot, circulating slot and desulfurization pump and with the atomizing pump, desulfurization pump and desulfurization injector set, the atomizing pump is organized by the pipeline fixedly with atomizing nozzle, desulfurizing tower and secondary tower flue, secondary tower flue and draught fan, draught fan and chimney, the circulating slot is fixed by the pipeline with the blowoff valve. Be used for the flue gas desulfurization defluorinate. It is steady to install skilful technology letter effect.
Description
Technical field
The utility model arranges the glass fibre stove flue gas desulphurization unit of turbocharging turbulator, relates to environmental technology field.
Background technology
At present, in domestic and international glass fibre production process, the toxic emission of glass fibre stove, containing harmful exhausts such as a certain amount of sulfur dioxide and hydrogen fluoride, due to sulfur dioxide and hydrogen fluoride gas not only to the health effect of human body very greatly, but also very large to the destruction of environment, so country always manages just relatively stricter, especially in recent years, requirement that is stricter, that upgrade be also been proposed to the exhaust emissions containing above-mentioned waste gas.For this situation, in the past traditional tail gas sulphur removal defluorinating equipment can not adapt to the requirement of new situations, as in the past traditional tail gas treatment device, or just with water, tail gas/or flue gas simply to be sprayed or the solution adding alkali with water sprays tail gas/or flue gas.For existing known technology and present situation, also exist that sulphur removal defluorination effect is not good enough and efficiency is low, do not reach the deficiency of New emission standard requirement, defect and drawback.Based on the professional knowledge of inventor and working experience and to the excelsior unremitting pursue of cause, conscientiously and fully investigating, understand, analyze, sum up, research has on known technology and present situation basis, take " to arrange turbocharging turbulator, air cooling tower, cooling down tower " key technology, make tail gas/or flue gas in turbine turbulent flow and mix with desulfurization defluorinating agent solution (calcium hydroxide or sodium hydroxide solution) organically blending property and fully carry out chemical reaction under pressurized state, thus compensate for existing known technology and present situation---tail gas/or flue gas and Water spray/or water add aqueous slkali spray time---the mutual Combination of the two is poor, sufficient chemical reaction cannot be obtained---cause the problem that sulphur removal defluorination effect is not good enough, succeed in developing " the glass fibre stove flue gas desulphurization unit of turbocharging turbulator is set " (comprising ' the glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set ' and ' technique of the glass fibre stove flue gas desulphurization unit of turbocharging turbulator is set '), effectively solve the deficiency of existing known technology and present situation, defect and drawback.
Utility model content
The utility model adopts and " arranges turbocharging turbulator, air cooling tower, cooling down tower " key technology, succeed in developing " glass fibre stove flue gas desulphurization unit and the technique of turbocharging turbulator are set ", its device is furnace flue gas pipe and benefit air-valve, air cooling tower and cooling down tower, cooling down tower and desulfurizing tower are fixed by pipeline, furnace flue gas pipe and air cooling tower, cooling down tower and atomizer group are fixed, cooling down tower and the pipeline inserting circulating slot, groove is fixed with the pipeline inserting circulating slot, desulfurizing tower inwall successively with (operating) water nozzle group, desulfurization nozzle group, turbocharging turbulator, groove is fixed, agitator is established in circulating slot, circulating slot and desulfur pump and and atomizer pump, desulfur pump and desulfurization nozzle group, atomizer pump and atomizer group are fixed by pipeline, desulfurizing tower and secondary tower flue, secondary tower flue and air-introduced machine, air-introduced machine and chimney, circulating slot and blowoff valve are fixed by pipeline.
The object reached by the utility model is: (1), employing " arranging turbocharging turbulator, air cooling tower, cooling down tower " key technology, provide the process of " the glass fibre stove flue gas desulphurization unit arranging turbocharging turbulator " Special desulfurizing defluorinating equipment and this equipment.(2), the utility model is provided with " device such as first turbine turbulent pressurization device (can also arrange two-stage turbine turbulent pressurization device, three grades of turbine turbulent pressurization devices), cooling down tower and air cooling tower ", glass fibre stove tail gas/or flue gas acquisition turbulent flow stage by stage and supercharging can be made, thus strengthening mixes and sufficient chemical reaction with the mutual of desulfurization defluorinating agent solution (calcium hydroxide or sodium hydroxide solution), and obtain best sulphur removal defluorination effect with this, improve the efficiency of desulfurization defluorinate, reach the requirement of discharge standard.(3), the utility model is " being provided with atomizer group " in cooling down tower, desulfurization defluorinating agent solution (calcium hydroxide or sodium hydroxide solution) can be made with the form of mist state mutually mixing with tail gas/or flue gas and carry out chemical reaction and make flue gas cool-down stage by stage, reach most suitable temperature, for absorption tower (desulfurizing tower and desulfurization defluorinate tower) more high efficiency desulfurization defluorinate prepare.(4), the utility model is provided with air cooling tower, supplement a certain amount of air, make high-temperature flue gas be reduced to suitable temperature, avoid cooling down tower to absorb anticorrosive coat in temperature too high generation deformation and failure tower, and save the energy, be beneficial to the better absorption of desulfurization defluorinating agent.Basic solvent in cooling down tower described in the utility model by circulating slot 10, through the bottom of atomizer pump 13, atomizer group 5, cooling down tower 4, be back in circulating slot 10 again, just constitute the circulation of basic solvent.(5) basic solvent, in desulfurizing tower described in the utility model is also a cyclic process, namely described basic solvent by circulating slot 10, through desulfur pump 12, desulfurization nozzle group 7, groove 9, be back in circulating slot 10 again, just constitute the circulation of another basic solvent.(6), the utility model is provided with demister, under the effect when tail gas/or flue gas run into demister just at demister, residual mist condensation entrained in tail gas/or flue gas formed liquid, and the liquid condensed into is with nature sinking of conduct oneself with dignity.(7), the utility model just met the requirement of discharge standard through the tail gas/of demister demist or flue gas, just under air-introduced machine effect from secondary tower flue, through air-introduced machine, discharged by chimney.(8), the utility model is provided with (operating) water nozzle group, and (operating) water nozzle group timing open, can remove the impurity on demister.(9), the utility model is provided with blowoff valve, can carry out blowdown as the case may be by blowoff valve in good time.(10), the utility model is connected easily with the equipment of upstream, floor space is little, desulfurization defluorinate efficiency is high, effect stability is reliable, equipment investment expense is low, be convenient to make and enforcement, upper detective, maintenance cost low.(11), design science of the present utility model is novel, design is firm rationally, simple and ingenious structure, convenience simple to operation.(12), the utility model solves the deficiency of existing known technology and present situation, defect and drawback, not only be applicable to newly-built glass fibre stove exhuast gas desulfurization defluorinate project, but also be applicable to the glass fibre stove exhuast gas desulfurization defluorinate project of transformation, can be applicable widely.
For achieving the above object, the technical scheme that the utility model provides is:
A glass fibre stove flue gas desulphurization unit for turbocharging turbulator is set, is made up of the agitator in the groove in the desulfurization nozzle group in furnace flue gas pipe, the atomizer group of mending in air-valve, air cooling tower, cooling down tower, cooling down tower, desulfurizing tower, desulfurizing tower, the (operating) water nozzle group in desulfurizing tower, the turbocharging turbulator in desulfurizing tower, desulfurizing tower, circulating slot, circulating slot, desulfur pump, atomizer pump, secondary tower flue, air-introduced machine, chimney, blowoff valve;
The described glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set, its furnace flue gas pipe is fixedly connected with by pipeline with benefit air-valve, the port of export of its furnace flue gas pipe is fixedly connected with the side of air cooling tower, the upper end of its air cooling tower is fixedly connected with by pipeline with the upper end of cooling down tower, the inwall of its cooling down tower is fixedly connected with atomizer group, the lower end fragment position of its cooling down tower is fixedly connected with by pipeline with the lower end fragment position of desulfurizing tower, the lower end of its cooling down tower is fixedly connected with the pipeline inserted in circulating slot, the inwall of its desulfurizing tower from top to bottom successively with (operating) water nozzle group, desulfurization nozzle group, turbocharging turbulator, groove is fixedly connected with, the lower end of its groove is fixedly connected with the pipeline inserted in circulating slot, agitator is provided with in its circulating slot, its circulating slot and desulfur pump and and atomizer pump, desulfur pump and desulfurization nozzle group, atomizer pump is all fixedly connected with by pipeline with atomizer group, the side of its desulfurizing tower upper end and the side of secondary tower flue upper end, the opposite side of secondary tower flue lower end and air-introduced machine one end, the air-introduced machine other end is all fixedly connected with by pipeline with the side of chimney lower end, its circulating slot is fixedly connected with by pipeline with blowoff valve.
The described glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set, described furnace flue gas pipe is tubular structure, described benefit air-valve, blowoff valve is valve shape structure, described air cooling tower is cyclone separator shape structure, described cooling down tower, desulfurizing tower is the tubular structure of closed at both ends, described atomizer group, desulfurization nozzle group, the nozzle sets of (operating) water nozzle group all for being made up of multiple nozzle, described groove is the structure that the bottom of circular peviform is provided with drain pipe, described circulating slot is pond shape structure, described agitator is the agitator of flaabellum shape, described desulfur pump, atomizer pump is pump shape structure, described secondary tower flue is the tubular structure of closed at both ends, described air-introduced machine is the air-introduced machine of flue gas, described chimney is taper tubular structure, described turbocharging turbulator is the structure being provided with multi-disc fan slab in a welding manner in circular cylinder and leaving gap between described thin plate.
Owing to have employed the technical scheme that the utility model provides, because the utility model have employed " arranging turbocharging turbulator, air cooling tower, cooling down tower " key technology, because its device of the utility model is furnace flue gas pipe and benefit air-valve, air cooling tower and cooling down tower, cooling down tower and desulfurizing tower are fixed by pipeline, furnace flue gas pipe and air cooling tower, cooling down tower and atomizer group are fixed, cooling down tower and the pipeline inserted in circulating slot, groove is fixed with the pipeline inserted in circulating slot, desulfurizing tower inwall successively with (operating) water nozzle group, desulfurization nozzle group, turbocharging turbulator, groove is fixed, agitator is established in circulating slot, circulating slot and desulfur pump and and atomizer pump, desulfur pump and desulfurization nozzle group, atomizer pump and atomizer group are fixed by pipeline, desulfurizing tower and secondary tower flue, secondary tower flue and air-introduced machine, air-introduced machine and chimney, circulating slot and blowoff valve are fixed by pipeline.Make the utility model compared with existing known technology and present situation, there is following beneficial effect:
1, the utility model adopts " arranging turbocharging turbulator, air cooling tower, cooling down tower " key technology, provides the process of " the glass fibre stove flue gas desulphurization unit arranging turbocharging turbulator " Special desulfurizing defluorinating equipment and this equipment.
2, the utility model is provided with " device such as first turbine turbulent pressurization device (can also arrange two-stage turbine turbulent pressurization device, three grades of turbine turbulent pressurization devices), cooling down tower and air cooling tower ", glass fibre stove tail gas/or flue gas acquisition turbulent flow stage by stage and supercharging can be made, thus strengthening mixes and sufficient chemical reaction with the mutual of desulfurization defluorinating agent solution (calcium hydroxide or sodium hydroxide solution), and obtain best sulphur removal defluorination effect with this, improve the efficiency of desulfurization defluorinate, reach the requirement of discharge standard.
3, the utility model is " being provided with atomizer group " in cooling down tower, desulfurization defluorinating agent solution (calcium hydroxide or sodium hydroxide solution) can be made with the form of mist state mutually mixing with tail gas/or flue gas and carry out sufficient chemical reaction and make flue gas cool-down stage by stage, reach most suitable temperature, for absorption tower (desulfurizing tower and desulfurization defluorinate tower) more high efficiency desulfurization defluorinate prepare.
4, the utility model is provided with air cooling tower, a certain amount of air can be supplemented, make high-temperature flue gas be reduced to suitable temperature, avoid cooling down tower to absorb anticorrosive coat in temperature too high generation deformation and failure tower, and save the energy, be beneficial to the better absorption of desulfurization defluorinating agent.
5, the basic solvent in cooling down tower described in the utility model by circulating slot 10, through the bottom of atomizer pump 13, atomizer group 5, cooling down tower 4, be back in circulating slot 10 again, just constitute the circulation of basic solvent.
6, the basic solvent in desulfurizing tower described in the utility model is also a cyclic process, namely described basic solvent by circulating slot 10, through desulfur pump 12, desulfurization nozzle group 7, groove 9, be back in circulating slot 10 again, just constitute the circulation of another basic solvent.
7, the utility model is provided with demister, under the effect when tail gas/or flue gas run into demister just at demister, residual mist condensation entrained in tail gas/or flue gas is formed liquid, and the liquid condensed into sinks with nature of conducting oneself with dignity.
8, the utility model has just met the requirement of discharge standard through the tail gas/of demister demist or flue gas, just under air-introduced machine effect from secondary tower flue, through air-introduced machine, discharged by chimney.
9, the utility model is provided with (operating) water nozzle group, and (operating) water nozzle group timing open, can remove the impurity on demister.
10, flue gas described in the utility model air-cooled, flue gas cool-down, fume desulfurizing, defluorinating, flue gas demist, liquid backflow, fume emission are the common Automatic continuous processes forming an organic whole.
11, the utility model is provided with blowoff valve, can carry out blowdown as the case may be by blowoff valve in good time.
12, technical process of the present utility model is that flue gas discharges and liquid backflow organic whole Automatic continuous after air-cooled, cooling, desulfurization defluorinate, demist, and in good time blowdown, design science is reasonable.
13, the utility model is connected easily with the equipment of upstream, floor space is little, desulfurization defluorinate efficiency is high, effect stability is reliable, equipment investment expense is low, be convenient to make and enforcement, upper detective, maintenance cost low.
14, design science of the present utility model is novel, design is firm rationally, simple and ingenious structure, convenience simple to operation.
15, the utility model solves the deficiency of existing known technology and present situation, defect and drawback, has not only been applicable to newly-built glass fibre stove exhuast gas desulfurization defluorinate project, but also has been applicable to the glass fibre stove exhuast gas desulfurization defluorinate project of transformation, can be applicable widely.
Accompanying drawing explanation
Figure of description is the schematic diagram of the utility model detailed description of the invention.
Label in figure: 1, furnace flue gas pipe, 2, mend air-valve, 3, air cooling tower, 4, cooling down tower, 5, atomizer group, 6, desulfurizing tower, 7, desulfurization nozzle group, 8, (operating) water nozzle group, 9, groove, 10, circulating slot, 11, agitator, 12, desulfur pump, 13, atomizer pump, 14, secondary tower flue, 15, air-introduced machine, 16, chimney, 17, blowoff valve, 18, turbocharging turbulator.
Detailed description of the invention
Detailed description of the invention one
Below in conjunction with Figure of description, the utility model is described in detail.Shown in Figure of description:
A glass fibre stove flue gas desulphurization unit for turbocharging turbulator is set, is made up of the agitator 11 in the groove 9 in the desulfurization nozzle group 7 in furnace flue gas pipe 1, the atomizer group 5 of mending in air-valve 2, air cooling tower 3, cooling down tower 4, cooling down tower 4, desulfurizing tower 6, desulfurizing tower 6, the (operating) water nozzle group 8 in desulfurizing tower 6, the turbocharging turbulator 18 in desulfurizing tower 6, desulfurizing tower 6, circulating slot 10, circulating slot 10, desulfur pump 12, atomizer pump 13, secondary tower flue 14, air-introduced machine 15, chimney 16, blowoff valve 17;
The described glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set, its furnace flue gas pipe 1 is fixedly connected with by pipeline with benefit air-valve 2, the port of export of its furnace flue gas pipe 1 is fixedly connected with the side of air cooling tower 3, the upper end of its air cooling tower 3 is fixedly connected with by pipeline with the upper end of cooling down tower 4, the inwall of its cooling down tower 4 is fixedly connected with atomizer group 5, the lower end fragment position of its cooling down tower 4 is fixedly connected with by pipeline with the lower end fragment position of desulfurizing tower 6, the lower end of its cooling down tower 4 is fixedly connected with the pipeline inserted in circulating slot 10, the inwall of its desulfurizing tower 6 from top to bottom successively with (operating) water nozzle group 8, desulfurization nozzle group 7, turbocharging turbulator 18, groove 9 is fixedly connected with, the lower end of its groove 9 is fixedly connected with the pipeline inserted in circulating slot 10, agitator 11 is provided with in its circulating slot 10, its circulating slot 10 with desulfur pump 12 and with atomizer pump 13, desulfur pump 12 and desulfurization nozzle group 7, atomizer pump 13 is all fixedly connected with by pipeline with atomizer group 5, the side of its desulfurizing tower 6 upper end and the side of secondary tower flue 14 upper end, the opposite side of secondary tower flue 14 lower end and air-introduced machine 15 one end, air-introduced machine 15 other end is all fixedly connected with by pipeline with the side of chimney 16 lower end, its circulating slot 10 is fixedly connected with by pipeline with blowoff valve 17.
The described glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set, described furnace flue gas pipe 1 is tubular structure, described benefit air-valve 2, blowoff valve 17 is valve shape structure, described air cooling tower 3 is cyclone separator shape structure, described cooling down tower 4, desulfurizing tower 6 is the tubular structure of closed at both ends, described atomizer group 5, desulfurization nozzle group 7, the nozzle sets of (operating) water nozzle group 8 all for being made up of multiple nozzle, described groove 9 is the structure that the bottom of circular peviform is provided with drain pipe, described circulating slot 10 is pond shape structure, described agitator 11 is the agitator of flaabellum shape, described desulfur pump 12, atomizer pump 13 is pump shape structure, described secondary tower flue 14 is the tubular structure of closed at both ends, described air-introduced machine 15 is the air-introduced machine of flue gas, described chimney 16 is taper tubular structure, described turbocharging turbulator 18 is the structure being provided with multi-disc fan slab in a welding manner in circular cylinder and leaving gap between described thin plate.
The described glass fibre stove flue gas desulphurization unit arranging turbocharging turbulator, described cooling down tower 4 is select a kind of material in stainless steel, fiberglass to make.
In above-mentioned specific implementation process: carried out making implementing with stainless steel material, glass-reinforced plastic material respectively to described cooling down tower 4; All obtain the good result of expection.
Detailed description of the invention two
Detailed description of the invention one practice processes is implemented, namely applies the described process that the glass fibre stove flue gas desulphurization unit of turbocharging turbulator is set.
Arrange a technique for the glass fibre stove flue gas desulphurization unit of turbocharging turbulator, apply the described glass fibre stove flue gas desulphurization unit arranging turbocharging turbulator, technique is as follows:
1., flue gas is air-cooled: the flue gas from glass fibre stove enters air cooling tower 3 through furnace flue gas pipe 1 and carries out air-cooled, and passes through to mend air-valve 2 supplements cold according to air quantity situation;
2., flue gas cool-down: after the flue gas after air-cooled enters cooling down tower 4 by air cooling tower 3, just run into and flow to by circulating slot 10 basic solvent mist that atomizer group 5 sprays by atomizer pump 13 and obtain cooling and carry out corresponding desulfurization defluorinate, through cooling and the basic solvent mist carrying out corresponding desulfurization defluorinate is gathered into liquid is back to again in circulating slot 10, described basic solvent by circulating slot 10, through the bottom of atomizer pump 13, atomizer group 5, cooling down tower 4, be back in circulating slot 10 again, just constitute the circulation of a basic solvent;
3., fume desulfurizing, defluorinating: through cooling and after the flue gas carrying out corresponding desulfurization defluorinate enters desulfurizing tower 6 by cooling down tower 4, first turbocharging turbulator 18 is run into, under the effect of turbocharging turbulator 18, through cooling and the flue gas carrying out corresponding desulfurization defluorinate just obtains supercharging under turbulence state, subsequently, obtain the supercharging flue gas of turbulent flow just to run into and flow to by circulating slot 10 basic solvent mist that desulfurization nozzle group 7 sprays by desulfur pump 12 and obtain abundant desulfurization defluorinate, sink after the basic solvent mist of abundant desulfurization defluorinate condenses into liquid, described basic solvent is in the process also by circulating slot 10, through desulfur pump 12, desulfurization nozzle group 7, groove 9, be back in circulating slot 10 again, just the circulation of another basic solvent is constituted,
4., flue gas demist: the flue gas through abundant desulfurization defluorinate continues to rise in desulfurizing tower 6, just runs into the water smoke that (operating) water nozzle group 8 sprays, and water smoke sinks after residual mist condensation entrained in flue gas is formed liquid;
5., liquid backflow: the liquid that the basic solvent mist fully after desulfurization defluorinate condenses into and the liquid that residual mist condensation entrained in flue gas is formed all is sunk to groove 9, the back of pipeline connected by groove 9 bottom flows in circulating slot 10;
6., fume emission: to through abundant desulfurization defluorinate and demist meet discharge standard require flue gas, under the effect of air-introduced machine 15, by desulfurizing tower 6, through secondary tower flue 14, discharged by chimney 16;
7., blowdown: according to the situation of dirt deposition in circulating slot 10, carry out blowdown by opening blowoff valve 17;
8., flue gas air-cooled, flue gas cool-down, fume desulfurizing, defluorinating, flue gas demist, liquid backflow, fume emission are the common Automatic continuous processes forming an organic whole.
The described technique arranging the glass fibre stove flue gas desulphurization unit of turbocharging turbulator, be mixed with calcium hydroxide or Sodium Hydroxide Alkaline solvent in described circulating slot 10, described basic solvent is uniformly mixed by agitator 11.
In above-mentioned specific implementation process: described basic solvent is implemented with calcium hydroxide, NaOH respectively; All obtain the good result of expection.
Be more than preferred embodiment of the present utility model, not any pro forma restriction done to the utility model; The those of ordinary skill of all industry, all can implement the utility model with the above shown in by specification accompanying drawing swimmingly; But not departing from technical solutions of the utility model and make the equivalent variations of differentiation, be Equivalent embodiments of the present utility model, all belong to the technical solution of the utility model.
Claims (2)
1. one kind arranges the glass fibre stove flue gas desulphurization unit of turbocharging turbulator, it is characterized in that: by furnace flue gas pipe (1), mend air-valve (2), air cooling tower (3), cooling down tower (4), atomizer group (5) in cooling down tower (4), desulfurizing tower (6), desulfurization nozzle group (7) in desulfurizing tower (6), (operating) water nozzle group (8) in desulfurizing tower (6), turbocharging turbulator (18) in desulfurizing tower (6), groove (9) in desulfurizing tower (6), circulating slot (10), agitator (11) in circulating slot (10), desulfur pump (12), atomizer pump (13), secondary tower flue (14), air-introduced machine (15), chimney (16), blowoff valve (17) is formed,
The described glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set, its furnace flue gas pipe (1) is fixedly connected with by pipeline with benefit air-valve (2), the port of export of its furnace flue gas pipe (1) is fixedly connected with the side of air cooling tower (3), the upper end of its air cooling tower (3) is fixedly connected with by pipeline with the upper end of cooling down tower (4), the inwall of its cooling down tower (4) is fixedly connected with atomizer group (5), the lower end fragment position of its cooling down tower (4) is fixedly connected with by pipeline with the lower end fragment position of desulfurizing tower (6), the lower end of its cooling down tower (4) is fixedly connected with the pipeline inserted in circulating slot (10), the inwall of its desulfurizing tower (6) from top to bottom successively with (operating) water nozzle group (8), desulfurization nozzle group (7), turbocharging turbulator (18), groove (9) is fixedly connected with, the lower end of its groove (9) is fixedly connected with the pipeline inserted in circulating slot (10), agitator (11) is provided with in its circulating slot (10), its circulating slot (10) and desulfur pump (12) and with atomizer pump (13), desulfur pump (12) and desulfurization nozzle group (7), atomizer pump (13) is all fixedly connected with by pipeline with atomizer group (5), the side of its desulfurizing tower (6) upper end and the side of secondary tower flue (14) upper end, the opposite side of secondary tower flue (14) lower end and air-introduced machine (15) one end, air-introduced machine (15) other end is all fixedly connected with by pipeline with the side of chimney (16) lower end, its circulating slot (10) is fixedly connected with by pipeline with blowoff valve (17).
2. the glass fibre stove flue gas desulphurization unit that turbocharging turbulator is set according to claim 1, it is characterized in that: described furnace flue gas pipe (1) is tubular structure, described benefit air-valve (2), blowoff valve (17) is valve shape structure, described air cooling tower (3) is cyclone separator shape structure, described cooling down tower (4), desulfurizing tower (6) is the tubular structure of closed at both ends, described atomizer group (5), desulfurization nozzle group (7), (operating) water nozzle group (8) nozzle sets all for being made up of multiple nozzle, the bottom that described groove (9) is circular peviform is provided with the structure of drain pipe, described circulating slot (10) is pond shape structure, the agitator that described agitator (11) is flaabellum shape, described desulfur pump (12), atomizer pump (13) is pump shape structure, the tubular structure that described secondary tower flue (14) is closed at both ends, the air-introduced machine that described air-introduced machine (15) is flue gas, described chimney (16) is taper tubular structure, described turbocharging turbulator (18) is for being provided with multi-disc fan slab in a welding manner in circular cylinder and leaving the structure in gap between described thin plate.
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Publication number | Priority date | Publication date | Assignee | Title |
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CN104841263A (en) * | 2015-06-02 | 2015-08-19 | 刘启杰 | Glass fiber furnace kiln waste gas desulfurization device with turbo-charging turbulator and process |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
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CN104841263A (en) * | 2015-06-02 | 2015-08-19 | 刘启杰 | Glass fiber furnace kiln waste gas desulfurization device with turbo-charging turbulator and process |
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