CN203955008U - Boiler smoke SO 2content control system - Google Patents

Boiler smoke SO 2content control system Download PDF

Info

Publication number
CN203955008U
CN203955008U CN201320836963.6U CN201320836963U CN203955008U CN 203955008 U CN203955008 U CN 203955008U CN 201320836963 U CN201320836963 U CN 201320836963U CN 203955008 U CN203955008 U CN 203955008U
Authority
CN
China
Prior art keywords
lime stone
boiler
outlet
air
introduced machine
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.)
Expired - Lifetime
Application number
CN201320836963.6U
Other languages
Chinese (zh)
Inventor
魏疆
权红军
徐旭东
邓时章
张风芝
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.)
XINJIANG MARKOR CHEM Co Ltd
Original Assignee
XINJIANG MARKOR CHEM 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 XINJIANG MARKOR CHEM Co Ltd filed Critical XINJIANG MARKOR CHEM Co Ltd
Priority to CN201320836963.6U priority Critical patent/CN203955008U/en
Application granted granted Critical
Publication of CN203955008U publication Critical patent/CN203955008U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

The utility model discloses a kind of boiler smoke SO 2content control system, comprises DCS, is arranged on the frequency conversion rotary feeder and the lime stone flowmeter that connect on boiler inlet and lime stone storehouse outlet conduit, and is arranged on the SO connecting on boiler export and chimney breast 2analyzer and air-introduced machine, exit, described lime stone storehouse arranges conveying fan, described frequency conversion rotary feeder is arranged between the outlet of lime stone storehouse and conveying fan, on pipeline between described conveying fan outlet and boiler inlet, lime stone flowmeter is set, described air-introduced machine entrance is connected by pipeline with boiler export, described air-introduced machine outlet is connected by pipeline with chimney, described SO 2analyzer is arranged in the outlet and the pipeline between chimney of air-introduced machine.Realize boiler smoke SO 2automatically control, reduce consumption of limestone amount, reduce labor strength and reduce SO 2the object that air is polluted.

Description

Boiler smoke SO 2content control system
Technical field
The utility model relates to lime stone and generates apparatus field, particularly, relates to a kind of boiler smoke SO 2content control system.
Background technology
At present, a large amount of gaseous contaminant (SO that coal-burning boiler produces 2, NOx, flue dust etc.) be the strict atmosphere pollution of controlling of national environmental protection department, environment is caused to serious pollution, be the polluter that national environmental protection method is clearly stipulated to carry out outer row's monitoring and reached discharge standard, must build CEMS system and carry out outer row's monitoring in real time.
Coal-burning boiler is working condition and the desulfuration efficiency of Real-Time Monitoring, inspection and control desulfurizer, in order to avoid cause desulfurizer to go wrong, carries out at any time the inspection of desulfuration efficiency and calculates monitoring.
At present, my company is only provided with a total CEMS system (flue gas automatic monitored control system) and carries out outer row in real time and monitor (A, B, C stove always discharge) at chimney place, and it is foundation that this result of monitoring also be take in Environmental Protection Agency.And every boiler is not carried out to independent SO 2measure, but boiler be all generally two move simultaneously one standby, when monitoring SO 2exceed standard, operating personnel cannot identification be the SO of which platform boiler actually 2exceed standard, and can only strengthen lime stone inlet amount to two boilers that moving simultaneously, be easy to like this cause lime stone excess, and make lime stone reach full, close, not only waste lime stone but also make to be difficult to reach grey balance, the particle of flue gas is exceeded standard.
The SO moving at present 2control system, cannot meet the emission request of new standard, and consumption of limestone amount is far beyond standard.
Utility model content
The purpose of this utility model is, for the problems referred to above, proposes a kind of boiler smoke SO 2content control system, to realize boiler smoke SO 2automatically control, reduce consumption of limestone amount, reduce labor strength and reduce SO 2the advantage that air is polluted.
For achieving the above object, the technical solution adopted in the utility model is:
A kind of boiler smoke SO 2content control system, comprises DCS, is arranged on the frequency conversion rotary feeder and the lime stone flowmeter that connect on boiler inlet and lime stone storehouse outlet conduit, and is arranged on the SO connecting on boiler export and chimney breast 2analyzer and air-introduced machine, exit, described lime stone storehouse arranges conveying fan, described frequency conversion rotary feeder is arranged between the outlet of lime stone storehouse and conveying fan, on pipeline between described conveying fan outlet and boiler inlet, lime stone flowmeter is set, described air-introduced machine entrance is connected by pipeline with boiler export, described air-introduced machine outlet is connected by pipeline with chimney, described SO 2analyzer is arranged in the outlet and the pipeline between chimney of air-introduced machine, the output of the frequency-variable controller of described frequency conversion rotary feeder and SO 2the input of analyzer is electrically connected to, described SO 2the output of analyzer is electrically connected to the input of DCS, and the output of described DCS is electrically connected to the input of the frequency-variable controller of frequency conversion rotary feeder, frequency conversion rotary feeder, lime stone flowmeter, SO 2analyzer forms a control loop, according to predefined SO2 content, regulates the lime stone batcher frequency conversion of separate unit boiler, controls the lime stone amount consumption of separate unit boiler.
Further, on the pipeline between institute's boiler export and air-introduced machine entrance, electric dust collector is set.
Further, described SO 2analyzer is packed in the outlet of air-introduced machine.
The technical solution of the utility model has following beneficial effect:
The technical solution of the utility model, by the frequency conversion rotary feeder that regulates lime stone addition is set, by lime stone flowmeter, and SO 2analyzer, lime stone flowmeter is for the instantaneous and integrated flow of accurate measurement lime stone, SO 2analyzer is used for analyzing boiler smoke SO 2content, and the data upload detecting is arrived to DCS, DNS regulates the frequency conversion rotary feeder feed frequency of separate unit boiler according to the data that receive, control the lime stone amount consumption of boiler, thereby substitutes the Artificial Control mode of prior art, reaches boiler smoke SO 2the object that content is controlled automatically; Thereby overcome, in prior art, consumption of limestone amount is high, labor strength large, boiler smoke SO 2content fluctuation exceeds standard greatly and frequently, the unsettled defect of technology controlling and process, and to realize, consumption of limestone amount is low, labor strength is little, boiler smoke SO 2content is precisely controlled, steam generator system is stable, reduces SO 2the object that air is polluted.
Accompanying drawing explanation
Fig. 1 is the boiler smoke SO described in the utility model embodiment 2the structural representation of content control system;
Fig. 2 is the boiler smoke SO described in the utility model embodiment 2content control system electrical connection theory diagram.
By reference to the accompanying drawings, in the utility model embodiment, Reference numeral is as follows:
1-conveying fan; 2-lime stone storehouse; 3-lime stone flowmeter; 4-boiler; 5-electric precipitation; 6-air-introduced machine; 7-SO 2analyzer; 8-chimney; 9-frequency conversion rotary feeder.
The specific embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described, should be appreciated that preferred embodiment described herein is only for description and interpretation the utility model, and be not used in restriction the utility model.
As depicted in figs. 1 and 2, a kind of boiler smoke SO 2content control system, comprises DCS, is arranged on the frequency conversion rotary feeder 9 and the lime stone flowmeter 3 that connect on boiler 4 imports and lime stone storehouse 2 outlet conduits, and is arranged on the SO connecting on boiler 4 outlets and chimney 8 pipelines 2analyzer 7 and air-introduced machine 6,2 exits, lime stone storehouse arrange conveying fan 1, frequency conversion rotary feeder 9 is arranged between 2 outlets of lime stone storehouse and conveying fan 1, on pipeline between conveying fan 1 outlet and boiler 4 imports, lime stone flowmeter 3 is set, air-introduced machine 6 entrances are connected by pipeline with boiler 4 outlets, air-introduced machine 6 outlets are connected by pipeline with chimney 8, SO 2analyzer 7 is arranged in the outlet and the pipeline between chimney 8 of air-introduced machine 6, the output of the frequency-variable controller of frequency conversion rotary feeder 9 and SO 2the input of analyzer 7 is electrically connected to, SO 2the output of analyzer 7 is electrically connected to the input of DCS, and the output of DCS (dcs) is electrically connected to the input of the frequency-variable controller of frequency conversion rotary feeder.
Wherein, on the pipeline between boiler export and air-introduced machine entrance, electric dust collector is set.SO 2analyzer 7 is packed in the outlet of air-introduced machine 6.
As shown in Figure 1, boiler smoke SO 2content control system, comprise for regulating the frequency conversion rotary feeder 9 of lime stone addition, the lime stone flowmeter 3 being connected with described frequency conversion rotary feeder outlet by the pipe fitting that is equipped with and valve, and by the pipe fitting that is equipped with and valve installation the SO in air-introduced machine exit 2analyzer.Lime stone flowmeter is for the instantaneous and integrated flow of accurate measurement lime stone, SO 2analyzer is used for analyzing boiler smoke SO 2content, and the data upload detecting is arrived to DCS, DCS is according to predefined SO 2content, regulates the lime stone batcher frequency conversion of separate unit boiler, controls the lime stone amount consumption of boiler, realizes SO in flue gas 2in time, effectively, precisely control.
As Fig. 1, frequency conversion rotary feeder is arranged on the outlet of lime stone feed bin, the import of conveying fan, regulate lime stone addition number.Lime stone flowmeter is installed, instantaneous delivery and the integrated flux of metering lime stone on conveying fan outlet line.SO 2before analyzer is arranged on boiler induced-draft fan outlet and chimney, the SO in monitoring boiler smoke 2content.Three forms a control loop, according to predefined SO 2content, regulates the lime stone batcher frequency conversion of separate unit boiler, controls the lime stone amount consumption of separate unit boiler.
As Fig. 2, frequency conversion rotary feeder, lime stone flowmeter, SO 2analyzer three forms a control loop, according to predefined SO 2content, regulates the lime stone batcher frequency conversion of separate unit boiler, controls the lime stone amount consumption of separate unit boiler, thereby realizes boiler smoke SO 2the automatic control of content.
Finally it should be noted that: the foregoing is only preferred embodiment of the present utility model, be not limited to the utility model, although the utility model is had been described in detail with reference to previous embodiment, for a person skilled in the art, its technical scheme that still can record aforementioned each embodiment is modified, or part technical characterictic is wherein equal to replacement.All within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.

Claims (3)

1. a boiler smoke SO 2content control system, is characterized in that, comprises DCS, is arranged on the frequency conversion rotary feeder and the lime stone flowmeter that connect on boiler inlet and lime stone storehouse outlet conduit, and is arranged on the SO connecting on boiler export and chimney breast 2analyzer and air-introduced machine, exit, described lime stone storehouse arranges conveying fan, described frequency conversion rotary feeder is arranged between the outlet of lime stone storehouse and conveying fan, on pipeline between described conveying fan outlet and boiler inlet, lime stone flowmeter is set, described air-introduced machine entrance is connected by pipeline with boiler export, described air-introduced machine outlet is connected by pipeline with chimney, described SO 2analyzer is arranged in the outlet and the pipeline between chimney of air-introduced machine, the output of the frequency-variable controller of described frequency conversion rotary feeder and SO 2the input of analyzer is electrically connected to, described SO 2the output of analyzer is electrically connected to the input of DCS, and the output of described DCS is electrically connected to the input of the frequency-variable controller of frequency conversion rotary feeder; Frequency conversion rotary feeder, lime stone flowmeter, SO 2analyzer forms a control loop, according to predefined SO 2content, regulates the lime stone batcher frequency conversion of separate unit boiler, controls the lime stone amount consumption of separate unit boiler.
2. boiler smoke SO according to claim 1 2content control system, is characterized in that, on the pipeline between institute's boiler export and air-introduced machine entrance, electric dust collector is set.
3. boiler smoke SO according to claim 1 and 2 2content control system, is characterized in that, described SO 2analyzer is packed in the outlet of air-introduced machine.
CN201320836963.6U 2013-12-18 2013-12-18 Boiler smoke SO 2content control system Expired - Lifetime CN203955008U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320836963.6U CN203955008U (en) 2013-12-18 2013-12-18 Boiler smoke SO 2content control system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320836963.6U CN203955008U (en) 2013-12-18 2013-12-18 Boiler smoke SO 2content control system

Publications (1)

Publication Number Publication Date
CN203955008U true CN203955008U (en) 2014-11-26

Family

ID=51915651

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320836963.6U Expired - Lifetime CN203955008U (en) 2013-12-18 2013-12-18 Boiler smoke SO 2content control system

Country Status (1)

Country Link
CN (1) CN203955008U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105536488A (en) * 2015-12-11 2016-05-04 新疆生产建设兵团农八师天山铝业有限公司 Control method for SO2 during semi-dry desulfurization
CN111760427A (en) * 2020-06-28 2020-10-13 淮南北新建材有限公司 Gypsum board production line, gas treatment device and gas treatment method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105536488A (en) * 2015-12-11 2016-05-04 新疆生产建设兵团农八师天山铝业有限公司 Control method for SO2 during semi-dry desulfurization
CN105536488B (en) * 2015-12-11 2018-04-27 新疆生产建设兵团农八师天山铝业有限公司 A kind of control method using semi-dry desulphurization SO2
CN111760427A (en) * 2020-06-28 2020-10-13 淮南北新建材有限公司 Gypsum board production line, gas treatment device and gas treatment method thereof

Similar Documents

Publication Publication Date Title
CN102032590B (en) Boiler combustion optimizing control system and optimizing control method based on accurate measurement system
CN205461808U (en) SCR denitration catalyst on -line measuring with spout ammonia and optimize automatic regulating system
CN203215651U (en) Remote on-line monitoring system for industrial boiler
CN202838010U (en) DCS (Distributed Control System) for wet flue gas desulfurization of furnace and furnace kiln
CN105536490A (en) Automatic desulfurization system and method for sintering flue gas
CN101576247A (en) Automatic control system for industrial coal powder boiler
CN103364580A (en) System and method for multi-point grid on-line flow velocity measurement
CN103968361A (en) Industrial boiler efficiency remote online monitoring system
CN103017196A (en) Air distribution optimized automatic control system and control method thereof of boiler
CN104296362A (en) Outdoor PM 2.5 concentration based automatic adjusting type air duct filtering device of building
CN201496940U (en) Industrial coal dust boiler automatic control system
CN103076816B (en) Automatic control system and method for emission monitoring of radioactive airborne effluents
CN203752307U (en) Intelligentized steam curing system
CN201748468U (en) Flue gas oxygen content control system of gas boiler
CN104785038A (en) Control apparatus and control method for inlet temperature of bag-type dust collector used for furnace
CN203955008U (en) Boiler smoke SO 2content control system
CN204268501U (en) There is the power station boiler pulverizing system of wind speed calibration equipment
CN201731635U (en) Water boiler automatic control system
CN102095204B (en) Boiler soot blowing control device based on flue fly ash mass flow
CN211262877U (en) Sampling device for measuring nitrogen oxide through full-section subarea round inspection
CN109973989B (en) Equipment for improving abrasion of low-temperature economizer
CN203615353U (en) Desulphurization system of coal power generating unit
CN103712195B (en) A kind of flue-gas temperature control method, Apparatus and system
CN203478274U (en) Gas mixture proportional control device for soot blowing system of boiler
CN202371749U (en) Single-fire-nozzle air powder on-line accurate control system for pulverized coal boiler

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CX01 Expiry of patent term
CX01 Expiry of patent term

Granted publication date: 20141126