CN103657317A - Flue gas dust removal and gas desulfurization system capable of intelligently controlling smoke discharge speed - Google Patents
Flue gas dust removal and gas desulfurization system capable of intelligently controlling smoke discharge speed Download PDFInfo
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- CN103657317A CN103657317A CN201310631783.9A CN201310631783A CN103657317A CN 103657317 A CN103657317 A CN 103657317A CN 201310631783 A CN201310631783 A CN 201310631783A CN 103657317 A CN103657317 A CN 103657317A
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Abstract
The invention relates to a flue gas dust removal and gas desulfurization system capable of intelligently controlling smoke discharge speed. The flue gas dust removal and gas desulfurization system comprises a flue gas pre-processing device and a flue gas desulfurization device which are sequentially connected through a flue gas pipeline. A physical filtering mode and an electrostatic adsorption mode are adopted to repeatedly filter and effectively settle and separate out coarse and fine particle dust in the high temperature flue gas, and the residual volatile matter and the powdered carbon in the high temperature flue gas are burned, so that the flue gas is well purified to facilitate the subsequent loading of flue gas desulfurization equipment. Digital detection equipment is also provided, and digital detection signals are outputted to a master control device so as to fulfill the purpose of automatic control. The system comprises multiple fans capable of intelligently controlling the smoke discharge speed to effectively avoid the smoke backflow and the like. In addition, the gas desulfurization device of the system is simple in structure and convenient to maintain, so that the operation cost of processing the flue gas by a dry processing method is greatly lowered.
Description
Technical field
The present invention relates to a kind of useless flue-gas dust-removing and desulfurization treating apparatus.
Background technology
China is that a few take one of country that coal is main energy sources in the world, coal accounts for the ratio of China's primary energy production and consumption always more than 70%, burnt gas has formed huge environmental pollution as the discharge of sulfur dioxide, nitrogen oxide, fundamentally administers the pollution that the discharge of sulfur dioxide and nitrogen oxide causes imperative.
Owing to can inevitably produce a large amount of flue gases and flying dust in industrial production, in flue gas, also contain a large amount of fine particles dust, these dust directly discharge meeting cause severe contamination to environment, to ecological environment, cause destruction in various degree, bring harm to people's Health and Living.Countries in the world environmental protection organization constantly strengthens the improvement of protection, especially atmosphere pollution to environment, industrial gas emission is enforced to control techniques, so some gas cleaning cleaners arise at the historic moment; In quite a while in the past, electric cleaner has been played the part of very important role therein; Yet along with improving constantly that people require living environment, environmental protection organization is also corresponding has both at home and abroad put into effect new discharge standard, and the control of pollution sources has been had to higher requirement.
During burning, the sulfur dioxide of a large amount of discharges, causes China to occur large-area acid rain, and development.In the eighties, the acid rain of China mainly occurs in take the southwest that Chongqing, Kweiyang and Liuzhou is representative, and Acid Rain Zone area is about 1,700,000 square kilometres.To the mid-90, acid rain has developed on the south the Changjiang river, the wide geographic area in to the east of Qinghai-Tibet Platean and the Sichuan Basin, Acid Rain Zone enlarged areas more than 100 ten thousand square kilometres.Take the Acid Rain Zone, Central China that Changsha, Ganzhou, Nanchang, Huaihua is representative has become the most serious area of national Acid Rain Pollution now, and the average annual Precipitation pH in its center is lower than 4.0, acid rain frequency is up to more than 90%, has arrived the degree of " meet rain must acid "; Take the Coastal East China that Nanjing, Shanghai, Hangzhou, Foochow and Xiamen be representative also becomes the main Acid Rain Area of China; It should be noted that the Beijing-Tianjin in North China, acid precipitation also appears in the areas such as the Dandong in northeast, Tumen again and again, average annual precipitation pH value has accounted for 30% left and right of national area lower than 5.6 region area.Visible, the development speed of China's acid rain is very surprising, is still the trend increasing the weight of year by year at present.Research shows, in China's acid precipitation, sulfate radical is approximately 10: 1 with the ratio of the equivalent of nitrate anion, and therefore, the acid rain of China is sulfuric acid type, mainly by anthropogenic discharge's sulfur dioxide, is caused.China is because acid rain and sulfur dioxide pollution cause the economic loss of the aspects such as crops, forest and health to be about more than 1,100 hundred million yuan, approaches 2% of gross national product then, becomes the key factor of restriction China's economy and social development.Administer Chinese Acid Rain Pollution, will control sulfur dioxide (SO2) emissions total amount.
Summary of the invention
The technical problem to be solved in the present invention is: propose a kind ofly can be before flue gas discharges flue gas to be carried out to a kind of flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate of dust-removal and desulfurizing.
The present invention is that the technical scheme that solves the problems of the technologies described above proposition is: a kind of flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate, comprise the Flue Gas Pretreatment Device and the flue gas desulfur device that by flue, join in turn, described flue gas desulfur device is mainly by by flue successively connected flue gas oxidizing tower, flue gas desulfurization device and flue gas drying tower form, the inside of described flue gas drying tower is provided with heating wire, the top of described flue gas drying tower is fume emission mouth, described fume emission mouth is provided with chimney, the inside of described chimney is interval with a plurality of ventilating fans from top to bottom successively, described Flue Gas Pretreatment Device is mainly by smoke-intake pipe road, controller, be arranged on the elementary control of dust filter screen in described smoke-intake pipe road, smoke pipeline, described in being connected to, enter, electrostatic precipitation case between smoke pipeline, digital altimeter, asepwirator pump and rotor type gas flowmeter form, described elementary control of dust screen cover is located at the porch in described smoke-intake pipe road, described asepwirator pump is arranged on described smoke pipeline exit, described digital altimeter and rotor type gas flowmeter are installed in described smoke pipeline and signal outputs to described controller, the control end of described controller is also connected with the controlled end of described a plurality of ventilating fans respectively.
Further; described flue gas desulfurization device comprises spiral flue gas delivery pipe; the inwall top of described spiral flue gas delivery pipe is interval with a plurality of ammonia water spray mouths; the inwall bottom interval of described spiral flue gas delivery pipe offers plasma discharge mouth; the below of described plasma discharge mouth is provided with feeder; in described feeder, be provided with agitator, the floss hole place of described feeder is provided with high-temperature oscillation comminutor, from described feeder floss hole, is connected with the charging aperture of described high-temperature oscillation comminutor.
Further, described Flue Gas Pretreatment Device also comprises the dust particle concentration monitor that is located at the smoke-intake pipe road that is positioned at described elementary control of dust filter screen top, the signal output part of described dust particle concentration monitor is connected to the signal input part of described controller, described dust particle concentration monitor is mainly to consist of main control chip and the generating laser, the light sensor that are oppositely arranged, and described light sensor is exported to described main control chip by the strength signal of Ear Mucosa Treated by He Ne Laser Irradiation; Described electrostatic precipitation case is at least two, the described electrostatic precipitation case that is at least two all has controlled end and is serially connected by pipeline, the controlled end of described electrostatic precipitation case is connected to the control end of described controller, and described smoke pipeline is connected to the exit of the electrostatic precipitation case that is positioned at least significant end.
Further, described flue gas oxidizing tower mainly consists of flue gas oxidizing tower tower body and ozone generating pipe, the both sides of described flue gas oxidizing tower tower body are respectively equipped with into mouth and outlet flue, and described ozone generating pipe is located at the described flue gas oxidizing tower tower body entering between mouth and outlet flue inner.
The invention has the beneficial effects as follows:
The invention provides a kind of flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate, first mode multiple times of filtration and the sedimentation effectively by physical filtering and Electrostatic Absorption, isolated thick, the particle dust in high-temperature flue gas, remaining fugitive constituent and the powdered carbon in high-temperature flue gas that burnt, makes flue gas obtain good purification.The load that is conducive to ensuing flue gas desulfurization device, digitized checkout equipment is also provided, can export to master control set to reach the object of automatic control by these digital detection signals, if the work number of controlling electrostatic precipitation case by controller by dust particle concentration monitor monitors again to the dust particle concentration in flue gas is in the present invention to reach the object of Based Intelligent Control, also having can be according to a plurality of fan of the data measured Based Intelligent Control exhaust rate of rotator type air volume meter, has effectively avoided falling the appearance of the situations such as cigarette.
In addition; simple in structure, the easy to maintenance and operating cost while greatly having reduced dry processing device smoke treatment of desulfurizer in the present invention; also be provided with plasma discharge mouth, the intermediate product that ammoniacal liquor can be reacted with sulfur dioxide in flue gas by plasma discharge mouth is discharged and is passed through granulator granulation again.And desulfurized effect is good, can make desulfuration byproduct.
Accompanying drawing explanation
Below in conjunction with accompanying drawing, a kind of flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate of the present invention is described further.
Fig. 1 is the structural representation of flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate in the present invention.
Fig. 2 is the structural representation of spiral flue gas delivery pipe.
The specific embodiment
Embodiment
As depicted in figs. 1 and 2, flue-gas dust-removing and desulfurization system that can Based Intelligent Control exhaust rate in the present invention, comprises the Flue Gas Pretreatment Device and the flue gas desulfur device that by flue, join in turn.
Flue Gas Pretreatment Device mainly by smoke-intake pipe road 1, controller 3, be arranged on elementary control of dust filter screen 2, smoke pipeline 5 in smoke-intake pipe road 1, be connected to into and out of electrostatic precipitation case 4, digital altimeter 9, asepwirator pump 8 and rotor type gas flowmeter 10 between smoke pipeline 1,5 and form, elementary control of dust filter screen 2 is located at the porch in smoke-intake pipe road 1, asepwirator pump 8 is arranged on smoke pipeline 5 exits, and digital altimeter 9 and rotor type gas flowmeter 10 are installed in smoke pipeline 5 and signal outputs to controller 3.
Flue Gas Pretreatment Device also comprises the dust particle concentration monitor that is located at the smoke-intake pipe road 1 that is positioned at elementary control of dust filter screen 2 tops, the signal output part of dust particle concentration monitor is connected to the signal input part of controller 3, dust particle concentration monitor is mainly to consist of main control chip and the generating laser, the light sensor that are oppositely arranged, and light sensor is exported to main control chip by the strength signal of Ear Mucosa Treated by He Ne Laser Irradiation; Electrostatic precipitation case 4 is two, is that the electrostatic precipitation case 4 of two all has controlled end and is serially connected by pipeline, and the controlled end of electrostatic precipitation case 4 is connected to the control end of controller 3, and smoke pipeline 5 is connected to the exit of the electrostatic precipitation case 4 that is positioned at least significant end.
Flue gas desulfur device is mainly by consisting of flue successively connected flue gas oxidizing tower 11, flue gas desulfurization device 12 and flue gas drying tower 13.
The inside of flue gas drying tower 13 is provided with heating wire, the top of flue gas drying tower 13 is fume emission mouth, fume emission mouth is provided with chimney, and the inside of chimney is interval with a plurality of ventilating fans 14 from top to bottom successively, and the control end of controller 3 is also connected with the controlled end of a plurality of ventilating fans 14 respectively.
Flue gas desulfurization device 12 comprises spiral flue gas delivery pipe 15; the inwall top of spiral flue gas delivery pipe 15 is interval with a plurality of ammonia water spray mouths; the inwall bottom interval of spiral flue gas delivery pipe 15 offers plasma discharge mouth; the below of plasma discharge mouth is provided with feeder; in feeder, be provided with agitator; the floss hole place of feeder is provided with high-temperature oscillation comminutor (not shown), from feeder floss hole, is connected with the charging aperture of high-temperature oscillation comminutor.
Flue gas oxidizing tower 11 mainly consists of flue gas oxidizing tower 11 tower bodies and ozone generating pipe, and the both sides of flue gas oxidizing tower 11 tower bodies are respectively equipped with into mouth and outlet flue, and ozone generating pipe is located at flue gas oxidizing tower 11 tower bodies that enter between mouth and outlet flue inner.
The above-described embodiment that is not limited to of the present invention, all employings are equal to replaces the technical scheme forming, and all drops in the protection domain of requirement of the present invention.
Claims (4)
- One kind can Based Intelligent Control exhaust rate flue-gas dust-removing and desulfurization system, it is characterized in that: comprise the Flue Gas Pretreatment Device and the flue gas desulfur device that by flue, join in turn, described flue gas desulfur device is mainly by consisting of flue successively connected flue gas oxidizing tower, flue gas desulfurization device and flue gas drying tower, the inside of described flue gas drying tower is provided with heating wire, the top of described flue gas drying tower is fume emission mouth, described fume emission mouth is provided with chimney, and the inside of described chimney is interval with a plurality of ventilating fans from top to bottom successively, described Flue Gas Pretreatment Device is mainly by smoke-intake pipe road, controller, be arranged on the elementary control of dust filter screen in described smoke-intake pipe road, smoke pipeline, described in being connected to, enter, electrostatic precipitation case between smoke pipeline, digital altimeter, asepwirator pump and rotor type gas flowmeter form, described elementary control of dust screen cover is located at the porch in described smoke-intake pipe road, described asepwirator pump is arranged on described smoke pipeline exit, described digital altimeter and rotor type gas flowmeter are installed in described smoke pipeline and signal outputs to described controller, the control end of described controller is also connected with the controlled end of described a plurality of ventilating fans respectively.
- 2. flue-gas dust-removing and desulfurization system that according to claim 1 can Based Intelligent Control exhaust rate, it is characterized in that: described flue gas desulfurization device comprises spiral flue gas delivery pipe, the inwall top of described spiral flue gas delivery pipe is interval with a plurality of ammonia water spray mouths, the inwall bottom interval of described spiral flue gas delivery pipe offers plasma discharge mouth, the below of described plasma discharge mouth is provided with feeder, in described feeder, be provided with agitator, the floss hole place of described feeder is provided with high-temperature oscillation comminutor, from described feeder floss hole, be connected with the charging aperture of described high-temperature oscillation comminutor.
- 3. flue-gas dust-removing and desulfurization system that according to claim 2 can Based Intelligent Control exhaust rate, it is characterized in that: described Flue Gas Pretreatment Device also comprises the dust particle concentration monitor that is located at the smoke-intake pipe road that is positioned at described elementary control of dust filter screen top, the signal output part of described dust particle concentration monitor is connected to the signal input part of described controller, described dust particle concentration monitor is mainly to consist of main control chip and the generating laser, the light sensor that are oppositely arranged, and described light sensor is exported to described main control chip by the strength signal of Ear Mucosa Treated by He Ne Laser Irradiation; Described electrostatic precipitation case is at least two, the described electrostatic precipitation case that is at least two all has controlled end and is serially connected by pipeline, the controlled end of described electrostatic precipitation case is connected to the control end of described controller, and described smoke pipeline is connected to the exit of the electrostatic precipitation case that is positioned at least significant end.
- 4. flue-gas dust-removing and desulfurization system that according to claim 3 can Based Intelligent Control exhaust rate, it is characterized in that: described flue gas oxidizing tower mainly consists of flue gas oxidizing tower tower body and ozone generating pipe, the both sides of described flue gas oxidizing tower tower body are respectively equipped with into mouth and outlet flue, and described ozone generating pipe is located at the described flue gas oxidizing tower tower body entering between mouth and outlet flue inner.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310631783.9A CN103657317A (en) | 2013-11-26 | 2013-11-26 | Flue gas dust removal and gas desulfurization system capable of intelligently controlling smoke discharge speed |
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| CN201310631783.9A CN103657317A (en) | 2013-11-26 | 2013-11-26 | Flue gas dust removal and gas desulfurization system capable of intelligently controlling smoke discharge speed |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108452655A (en) * | 2017-12-04 | 2018-08-28 | 盐城市兰丰环境工程科技有限公司 | A kind of flue gas desulfunzation denitrating system |
| CN108744759A (en) * | 2018-05-24 | 2018-11-06 | 安徽国能亿盛环保科技有限公司 | Detect the device of pulse bag type dust collector cloth bag breakage |
| CN111841202A (en) * | 2020-06-29 | 2020-10-30 | 沈春丰 | Spray foam desulfurization dust remover |
-
2013
- 2013-11-26 CN CN201310631783.9A patent/CN103657317A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108452655A (en) * | 2017-12-04 | 2018-08-28 | 盐城市兰丰环境工程科技有限公司 | A kind of flue gas desulfunzation denitrating system |
| CN108744759A (en) * | 2018-05-24 | 2018-11-06 | 安徽国能亿盛环保科技有限公司 | Detect the device of pulse bag type dust collector cloth bag breakage |
| CN111841202A (en) * | 2020-06-29 | 2020-10-30 | 沈春丰 | Spray foam desulfurization dust remover |
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Application publication date: 20140326 |