CN101792130B - Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production - Google Patents

Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production Download PDF

Info

Publication number
CN101792130B
CN101792130B CN2009101029966A CN200910102996A CN101792130B CN 101792130 B CN101792130 B CN 101792130B CN 2009101029966 A CN2009101029966 A CN 2009101029966A CN 200910102996 A CN200910102996 A CN 200910102996A CN 101792130 B CN101792130 B CN 101792130B
Authority
CN
China
Prior art keywords
electrostatic precipitator
insulator
hot
tail gas
gas
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.)
Active
Application number
CN2009101029966A
Other languages
Chinese (zh)
Other versions
CN101792130A (en
Inventor
杨毅
付勇
岑祖望
汪勇平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wengfu Group Co Ltd
Original Assignee
Wengfu Group Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Wengfu Group Co Ltd filed Critical Wengfu Group Co Ltd
Priority to CN2009101029966A priority Critical patent/CN101792130B/en
Publication of CN101792130A publication Critical patent/CN101792130A/en
Application granted granted Critical
Publication of CN101792130B publication Critical patent/CN101792130B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Abstract

The invention discloses a hot-air blowing method for a supporting insulator of an electrostatic precipitator in pyrite-based sulfuric acid production. The process equipment in the method consists of a demisting chamber 3, a draught fan 4, an insulator chamber 5, the electrostatic precipitator 6 and connected process pipelines. In the method, a pipeline is introduced into the demisting chamber 3 from a channel for tail gas 1 absorbed by an absorbing system to discharge into atmosphere 2; the tail gas is delivered to the insulator chamber 5 for blowing through the draught fan 4 which is connected with the demisting chamber 3; then, the tail gas enters the electrostatic precipitator 6 and is discharged, wherein the introduced tail gas is at about 75 DEG C, and the gas is dried hot gas; the hot gas can be used for hot air blowing for the insulator of the electrostatic precipitator by pumping of the draught fan 4; temperatures of the inner wall and the outer wall of the insulator can be the same by heating so as to avoid dewing phenomenon; and an electric heater is closed when a device works, the power consumption of the device can be effectively reduced by utilizing heat energy of the tail gas in the pyrite-based sulfuric acid production, and part of sulphur dioxide in the tail gas can be reclaimed by a demister 3 and the electrostatic precipitator 6. Therefore, the method is advantageous to environmental protection.

Description

Hot-air blowing method for supporting insulator of electrostatic precipitator in the pyrite-based sulfuric acid production
Technical field
The invention belongs to production field in the pyrite-based sulfuric acid production, relate in particular to hot-air blowing method for supporting insulator of electrostatic precipitator in the pyrite-based sulfuric acid production.
Background technology
In the pyrite-based sulfuric acid production, electrostatic precipitator is one of device key equipment, its work ultimate principle is to utilize high-voltage dc, remove the sulfuric acid mist that produces in the pyrite burning process, in order to ensure the stability of high-voltage dc, its supporting insulator all adopts external type of heating to carry out hot-air blowing, has caused the plant energy consumption increase.
For cutting down the consumption of energy, researcher is constantly attempted various effective ways both at home and abroad, and to so far, comparatively sophisticated is the cold wind purging system of Qingdao these research and development of Harrar, and this system can satisfy the production demand substantially when the device ordinary production; But this system has following shortcoming:
1) electrostatic precipitator electric current and voltage under original driving situation is lower, the demist decrease in efficiency.
2) after stopping in emergency appearred in device, baking flue gas was scurried into insulator chamber, caused supporting insulator creepage, after need cleaning supporting insulator, and can works better.
3) at the electrostatic precipitator that old device is transformed in normal productive process, demist efficient descends to some extent.If will reach original demist efficient, need the energy that expands to electrostatic precipitator, investment increases.
In addition, in Chinese patent literature, aspect electrostatic precipitator, many patent application documents are arranged also, as application number is 200510041490.0, and name is called " assembled smoke gas denitration, dedusting, desulfurizer ", is the smoke eliminator that pollutes control or association area about power-plant flue gas.Relatively to have technology more reasonable with the smoke eliminator of routine, system layout compactness, investment and the low characteristics of working cost.Electric precipitator (and electrostatic precipitator is arranged; Application number 200620137691.0, name are called " a kind of electrostatic precipitator " and just relate to a kind of the be used for dedusting of gas cleaning, the electrostatic precipitator improvement of demist process.Convert anode tube the leaking outside of causing of breaking to interior leakage, increase the characteristics in its work-ing life.In addition; at application number is 200820031741.6; name is called " electric mist insulator gas shield device " and discloses the interior electric mist insulator gas shield device of static demist technical field; can replenish a spot of exsiccant air by inlet pipe; insulator inside and outside wall temperature is equated; no dewfall phenomenon can keep the state of insulation of insulator.The utility model is applied on the high pressure static electricity mist eliminator, can save a large amount of electric energy.
Do not find the relevant patent documentation of electrostatic precipitator in the pyrite-based sulfuric acid production by retrieval.
Summary of the invention
Purpose of the present invention is energy-saving and cost-reducing, be to come from the casing of electric mist insulated case to be provided with the piped insulator, some electric heating tubes are installed on the cabinet wall of insulator periphery, by heating insulator inside and outside wall temperature is equated, no dewfall phenomenon produces, guaranteeing that demist is working properly carries out, and this need consume a large amount of electric energy; The contriver is for saves energy, under the dedusting working order, can close electric heating tube, can allow insulator inside and outside wall temperature can not differ greatly again and produce the dewfall phenomenon, destroy the state of insulation of insulator, adopt the method that feeds the exsiccant tail gas of preparing discharging, insulator inside and outside wall temperature is equated, no dewfall phenomenon, can keep the state of insulation of insulator can utilize the pyrite-based sulfuric acid production exhaust heat-energy again, effectively reduce the consumption of plant energy consumption, reclaimed the part sulfurous gas in the tail gas simultaneously, reached energy saving purposes, invention has the benefit of tangible environmental protection.
The present invention adopts following method and apparatus to finish above purpose:
Hot-air blowing method for supporting insulator of electrostatic precipitator in the pyrite-based sulfuric acid production of the present invention, its processing unit is by removing fog chamber 3, induced draft fan 4, insulator chamber 5, electrostatic precipitator 6 and the process pipe composition that connects; Introduce a pipeline from the tail gas 1 after the absorption system absorption to the pipeline that enters atmosphere 2 to removing fog chamber 3, by connecting the induced draft fan 4 that removes fog chamber 3, the insulator chamber 5 of delivering to pipe connection purges, and then, enters electrostatic precipitator 6 discharges; Enter about 75 ℃ of atmospheric exhaust temperature after the absorption tower absorbs, moiety is that content of sulfur dioxide is 960mg/m 3, acid mist is 30mg/m 3, all the other are nitrogen, because this part gas is the exsiccant hot gas, through induced draft fan 4 suctions,, insulator inside and outside wall temperature is equated by heating as electrostatic precipitator insulator hot-air blowing, not having the dewfall phenomenon produces, just can close electric heater during work,, effectively reduce the consumption of device electric energy by utilizing the pyrite-based sulfuric acid production exhaust heat-energy, simultaneously, mist eliminator 3, electrostatic precipitator 6 have reclaimed the part sulfurous gas in the tail gas.
Effect of the present invention or advantage, 1) effectively utilized the heat energy of tail gas in the pyrite-based sulfuric acid production process, saving supporting insulator simultaneously need adopt external heating or carry out the energy consumption of hot-air blowing, reclaimed the sulfurous gas of part in the tail gas, both reached energy saving purposes, tangible environmental benefit had been arranged again.2) easy with the reducing energy consumption of original pyrite-based sulfuric acid production device, former main device is not changed, only increase equipment component, do not influence the main operation control of original device.
Description of drawings
Fig. 1 is a process flow diagram of the present invention.
In Fig. 1, the tail gas after 1. absorption system absorbs 2. enters atmosphere, 3. removes fog chamber, 4. induced draft fan, 5. insulator chamber, 6. electrostatic precipitator.
Embodiment
Embodiment 1, introduce a muffler from tail gas discharging pipe.Tail gas 1 after promptly absorbing from absorption system is introduced a pipeline to removing fog chamber 3 to the pipeline that enters atmosphere 2, by connecting the induced draft fan 4 that removes fog chamber 3, tail gas is delivered to insulator chamber 5 purge, and then, enters electrostatic precipitator 6 demists; Enter about 75 ℃ of atmospheric exhaust temperature after the absorption tower absorbs, moiety is that content of sulfur dioxide is 960mg/Nm 3, acid mist is 30mg/Nm 3, all the other are nitrogen, because this part gas is the exsiccant hot gas, through induced draft fan 4 suctions,, insulator inside and outside wall temperature is equated by heating as electrostatic precipitator insulator hot-air blowing, not having the dewfall phenomenon produces, just can close electric heater during electrostatic precipitator 6 work,, effectively reduce the consumption of plant energy consumption by utilizing the pyrite-based sulfuric acid production exhaust heat-energy, simultaneously, mist eliminator 3, electrostatic precipitator 6 have reclaimed the part sulfurous gas in the tail gas.Reached energy saving purposes, tangible environmental benefit has been arranged.

Claims (1)

1. hot-air blowing method for supporting insulator of electrostatic precipitator in the pyrite-based sulfuric acid production of the present invention is characterized in that processing unit is by removing fog chamber (3), induced draft fan (4), insulator chamber (5), electrostatic precipitator (6) and the process pipe composition that connects; Introduce a pipeline from the tail gas (1) after the absorption system absorption to the pipeline that enters atmosphere (2) to removing fog chamber (3),, deliver to insulator chamber (5) purging, then, enter electrostatic precipitator (6) and discharge by connecting the induced draft fan (4) that removes fog chamber (3); Enter 75 ℃ of atmospheric exhaust temperatures after the absorption tower absorbs, content of sulfur dioxide is 960mg/m in the composition of composition 3, acid mist is 30mg/m 3, all the other are nitrogen, this part gas is the exsiccant hot gas, aspirate through induced draft fan (4), behind electrostatic precipitator insulator hot-air blowing, just close electric heater during work, by utilizing the pyrite-based sulfuric acid production exhaust heat-energy, effectively reduce the device power consumption, mist eliminator (3), electrostatic precipitator (6) have reclaimed the part sulfurous gas in the tail gas.
CN2009101029966A 2009-12-30 2009-12-30 Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production Active CN101792130B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009101029966A CN101792130B (en) 2009-12-30 2009-12-30 Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009101029966A CN101792130B (en) 2009-12-30 2009-12-30 Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production

Publications (2)

Publication Number Publication Date
CN101792130A CN101792130A (en) 2010-08-04
CN101792130B true CN101792130B (en) 2011-10-05

Family

ID=42585086

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009101029966A Active CN101792130B (en) 2009-12-30 2009-12-30 Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production

Country Status (1)

Country Link
CN (1) CN101792130B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014001638A1 (en) * 2012-06-28 2014-01-03 Metso Power Oy Arrangement and method in electric filter

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014001638A1 (en) * 2012-06-28 2014-01-03 Metso Power Oy Arrangement and method in electric filter
EP2866940A4 (en) * 2012-06-28 2016-02-24 Valmet Technologies Oy Arrangement and method in electric filter
US9845952B2 (en) 2012-06-28 2017-12-19 Valmet Technologies Oy Arrangement and method in electric filter

Also Published As

Publication number Publication date
CN101792130A (en) 2010-08-04

Similar Documents

Publication Publication Date Title
CN205007792U (en) Wet flue gas desulfurization flue gas processing mechanism
CN201429307Y (en) Energy-saving dryer
CN201991580U (en) Flue gas waste heat power generating system comprising ammonia steam turbine
CN103255260A (en) Converter flue gas purifying and waste heat recovering system and bag-type dust removing technology
WO2012037828A1 (en) Energy-saving dust collector
CN105091633A (en) Flue heat exchange device for hot-air sealing of insulation piece incubators of electric precipitator
CN201443950U (en) Grain drier energy-saving purification device
CN207816009U (en) A kind of ferromanganese smelting electric furnace flue gas recovery system
CN101792130B (en) Hot-air blowing method for supporting insulator of electrostatic precipitator in pyrite-based sulfuric acid production
CN204460852U (en) Air source heat pump heat supply and blower fan generate electricity association system
CN201560207U (en) Blast furnace blast-dehumidification device utilizing waste heat of flue gas from hot blast furnace
CN103521200A (en) Activated carbon regeneration equipment
CN103277988B (en) Solar composite dryer
CN105333700A (en) Heat exchanging and recycling device of plastic dehumidifying and drying machine
CN104384021A (en) Electrostatic precipitator
CN201614284U (en) Hot air blowing device for electric mist precipitator supporting insulators in pyrite-based sulfuric acid production
CN207822773U (en) Exhaust treatment system
CN216631187U (en) White flue gas treatment system
CN205119109U (en) Flue gas recovery system
CN210176892U (en) Dry electric bag combined dust removal system for eliminating smoke plume by ultra-low emission of primary smoke of converter
CN203525725U (en) Regeneration equipment of active carbon
CN203307196U (en) Sludge dryer with a waste gas treatment function and capable of preventing secondary pollution
CN201725633U (en) Waste gas heat energy utilizing device of lacquered wire baking furnace
CN101954237B (en) Flue gas desulfurization equipment and method for float glass exhaust-heat boiler
CN206027935U (en) Wet -type is hot air blowing system for electrostatic precipitator

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CP02 Change in the address of a patent holder

Address after: 550500 Guizhou Province, Qiannan Buyei and Miao Autonomous Prefecture Fuquan Racecourse town Yingbin Road No. 1 Wengfu group

Patentee after: WENGFU GROUP Co.,Ltd.

Address before: 550002, International Building, No. 57, South City Road, Nanming District, Guizhou, Guiyang

Patentee before: WENGFU GROUP Co.,Ltd.

CP02 Change in the address of a patent holder