CN110124441A - A kind of judgement of rotary valve gas leakage and processing method and its system - Google Patents

A kind of judgement of rotary valve gas leakage and processing method and its system Download PDF

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Publication number
CN110124441A
CN110124441A CN201910417963.4A CN201910417963A CN110124441A CN 110124441 A CN110124441 A CN 110124441A CN 201910417963 A CN201910417963 A CN 201910417963A CN 110124441 A CN110124441 A CN 110124441A
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gas
pipeline
rotary valve
value
conveying
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CN110124441B (en
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魏进超
李俊杰
傅旭明
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Zhongye Changtian International Engineering Co Ltd
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Zhongye Changtian International Engineering Co Ltd
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • G—PHYSICS
    • G01—MEASURING; TESTING
    • G01M—TESTING STATIC OR DYNAMIC BALANCE OF MACHINES OR STRUCTURES; TESTING OF STRUCTURES OR APPARATUS, NOT OTHERWISE PROVIDED FOR
    • G01M3/00—Investigating fluid-tightness of structures
    • G01M3/02—Investigating fluid-tightness of structures by using fluid or vacuum
    • G01M3/26—Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors
    • G01M3/28—Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors for pipes, cables or tubes; for pipe joints or seals; for valves ; for welds
    • G01M3/2876—Investigating fluid-tightness of structures by using fluid or vacuum by measuring rate of loss or gain of fluid, e.g. by pressure-responsive devices, by flow detectors for pipes, cables or tubes; for pipe joints or seals; for valves ; for welds for valves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10—Inorganic adsorbents
    • B01D2253/102—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2259/00—Type of treatment
    • B01D2259/40—Further details for adsorption processes and devices
    • B01D2259/40003—Methods relating to valve switching
    • B01D2259/40005—Methods relating to valve switching using rotary valves

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  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • General Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Treating Waste Gases (AREA)

Abstract

A kind of judgement and processing method of rotary valve gas leakage, method includes the following steps: 1) flue gas after the activated carbon adsorption purification in adsorption tower by discharging；The active carbon for having adsorbed pollutant in flue gas enters Analytic Tower and is parsed, and the active carbon after parsing enters adsorption tower；2) in the second rotary valve initial operation stage, the blower motor frequency F of the second dust pelletizing system is recorded2And the show value P of second pressure meter2；3) the second rotary valve continuous service keeps the value of second pressure meter constant, observes the variation of the blower motor frequency of the second dust pelletizing system；4) variation range of the blower motor frequency of the second dust pelletizing system is set, if the variation of blower motor frequency, in the frequency range of setting, the second rotary valve, which is in, to be operated normally；If the variation of blower motor frequency is more than the frequency range of setting, determine that the second rotary valve leaks out.This method is easy to operate, can effectively judge the case where whether rotary valve of adsorption tower top or bottom leaks air.

Description

A kind of judgement of rotary valve gas leakage and processing method and its system
Technical field
The present invention relates to the judgements of the rotary valve gas leakage of activated carbon system and processing method, the judgement of rotary valve gas leakage and place Reason system belongs to flue gases purification field.
Background technique
For sintering flue gas after main exhaust fan between about 110-170 DEG C of exhaust temperature, SO is contained in the inside2、NOx, dust, two The multiple pollutants such as English, heavy metal are disliked, and active carbon flue gases purification is suitable for that sintering flue gas temperature discharges section just, it can be real The collaboration high-efficient purification of existing multi-pollutant, can remove multiple pollutant simultaneously on a set of equipment, realize by-product SO2Resource Change and utilize, and the technology has pollutant removing high-efficient, does not consume water resource substantially, it is without secondary pollution the advantages that.Activity Charcoal flue gas purification device is provided with multiple subsystems such as adsorption system, resolution system, acid making system, and flue gas passes through activated carbon adsorption Unit after-purification, active carbon particle circulate between absorbing unit and resolution unit, realize " absorption pollutant (adsorption tower Interior completion) → heating parsing activation (Analytic Tower in complete, escape pollutant) → cooling → absorption pollutant is (complete in adsorption tower At) " recycle.
Former flue gas enters adsorption tower through booster fan, is discharged after active carbon bed realization gas cleaning.In order to prevent Flue gas is revealed by adsorption tower active carbon material feeding mouth and discharge port, is all made of at present in adsorption tower upper feed inlet, lower part discharge port Rotary valve realizes active carbon conveying and smoke impervious.Enter suction through conveyer, rotary valve by active carbon regenerated in Analytic Tower Attached tower, the active carbon that pollutant has been adsorbed in adsorption tower enter conveyer through rotary valve and are being delivered to Analytic Tower, equal during this Certain fugitive dust can be generated, the air sucked from conveyer air inlet brings the fugitive dust in conveyer into dust pelletizing system.Rotary valve (is inhaled Rotary valve at attached tower inlet port and outlet port) it is generally made of feed inlet, discharge port, blade, spool and valve casing, all entrance The active carbon of adsorption tower is required by feeding rotary valve, and the active carbon of all discharge adsorption towers is both needed to by the rotary valve that discharges, Therefore, the blade of rotary valve is worn and hard object gets stuck and is easily deformed due to active carbon.Since flue gas purifying equipment is necessary and host Therefore (equipment such as sintering machine) synchronous operation when gas leak phenomenon occurs for rotary valve deformable blade, still can not stop immediately Machine overhauling or replacement, it is necessary to until host (such as sintering machine) is shut down, maintenance down rotary valve could be synchronized.Moreover, rotation A large amount of flue gases can be made to leak in conveyer after valve deformation is serious, that is, former smoke conveying duct delivers into the flue gas of adsorption tower, The flue gas is by being easy the flue gas revealed, and revealed from adsorption tower feed inlet or the rotary valve of discharge port position inside adsorption tower In contain certain sulfur dioxide, nitrogen oxides, 8%~10% vapor, 0.6%~1% carbon monoxide, 4%~6% Carbon dioxide, conveyer corrosion will be will cause after the flue gas condensing, portion gas enters dust pelletizing system, also will cause dust removing tube Road blocking, the gas of discharge also pollute the environment.
Rotary valve in activated carbon system under the prior art as a result, existing defect mainly has in production:
Can not (1) it see how to find whether rotary valve deformable blade, gas leakage serious inside rotary valve?
(2) if abnormal conditions the case where (deformation, gas leakage) occurs in rotary valve, can not horse back maintenance down, (produced in host The system of raw original flue gas) shut down before, how to handle rotary valve leakage problem? while handling rotary valve leakage problem, it is desirable that nothing Pollution, do not condense blocking pipeline.
Summary of the invention
For above-mentioned defect existing in the prior art, the purpose of the present invention is to provide a kind of judgements of rotary valve gas leakage Method.The blower motor frequency of dust pelletizing system that this method control is connected with conveyer is constant (or to be controlled and connects conveyer and remove The flow of the conveyance conduit interior air-flow of dirt system is constant), by the pressure change for observing conveyor channel；Alternatively, control conveying Pressure in machine pipeline is constant, the blower motor frequency variation of observation observation dust pelletizing system (or observation connection conveyer and dedusting The changes in flow rate of the conveyance conduit interior air-flow of system)；Judge that the rotary valve for adsorbing column overhead (feeds rotation by the above method Valve or the second rotary valve) or adsorption tower tower bottom rotary valve (discharge rotary valve or the first rotary valve) whether in work normally shape State, whether there is or not leak out.This method is easy to operate, does not need investment complicated pipe-line equipment and reaction unit, input cost It is low, and significant effect.
The first purpose of this invention be judgement absorption column overhead rotary valve (charging rotary valve or the second rotary valve) or With the presence or absence of gas leakage situation.
Second object of the present invention be if the rotary valve (charging rotary valve or the second rotary valve) of absorption column overhead or There are gas leakage situations, propose a kind of processing rotary valve (charging rotary valve or the second rotary valve) gas leakage method.
Third object of the present invention is to judge that the rotary valve (discharge rotary valve or the first rotary valve) of adsorption tower tower bottom is It is no that there are gas leakage situations.
Fourth object of the present invention is if the rotary valve (discharge rotary valve or the first rotary valve) of adsorption tower tower bottom is deposited In gas leakage situation, a kind of processing rotary valve (discharge rotary valve or the first rotary valve) gas leakage method is proposed.
A further object of the present invention is to also proposed corresponding rotary valve on the basis of judging the method for rotary valve gas leakage Gas leak treatment method and system, the flue gas which will leak to conveyer with system are taken away, guarantee flue gas not from rotation Rotary valve leaks to conveyer, the corrosion and destruction so as to avoid flue gas to conveyer and dust pelletizing system；Simultaneously by reasonable Control guarantees the reasonability for extracting air quantity, the flue gas that will be taken away from charging discharge valve material downstream, discharge rotary valve material upstream It is delivered to former smoke conveying duct, while guaranteeing that air draft pipeline (transfer pipeline of flue gas) is not blocked because flue gas condensing condenses, nothing Pollution.
The first embodiment according to the present invention provides the judgement and processing method of a kind of rotary valve gas leakage.
A kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower via former smoke conveying duct, by discharging after the activated carbon adsorption purification in adsorption tower； The active carbon for having adsorbed pollutant in flue gas enters the first conveyer, the first conveyer via the first rotary valve of absorption tower bottom Active carbon is delivered to Analytic Tower to be parsed, regenerate；Active carbon after Analytic Tower parses enters second conveyor, via The second rotary valve at the top of adsorption tower enters adsorption tower；
2) in the second rotary valve initial operation stage, the blower motor for the second dust pelletizing system being connected with second conveyor is recorded Original frequency F2Or the initial flow of record connection second conveyor and the second flowmeter on the conveyance conduit of the second dust pelletizing system Measure Q2, and record the initial pressure P for being arranged on second conveyor and being located at the second pressure meter of the second rotary valve upstream2；
3) the second rotary valve continuous service keeps the value of second pressure meter not become initial pressure P2, observe the second dedusting The real-time frequency F of the blower motor of system2' or observation second flowmeter real-time traffic Q2'；If the wind of the second dust pelletizing system The real-time frequency F of electromechanical machine2' it is equal to original frequency F2Or the real-time traffic Q of second flowmeter2' it is equal to initial flow Q2, then Second rotary valve is in normal operating condition, continues to observe；If the real-time frequency F of the blower motor of the second dust pelletizing system2' no Equal to original frequency F2Or the real-time traffic Q of second flowmeter2' it is not equal to initial flow Q2, then determine the second rotary valve gas leakage
In the present invention, step 3) may be: the second rotary valve continuous service, keep the blower electricity of the second dust pelletizing system The frequency of machine does not become original frequency F2Or the flow of second flowmeter is kept not become initial flow Q2, observe second pressure meter Real-time pressure P2'；If the real-time pressure P of second pressure meter2' it is equal to initial pressure P2, then the second rotary valve is in normal fortune Row state continues to observe；If the real-time pressure P of second pressure meter2' it is not equal to initial pressure P2, then determine that the second rotary valve leaks Gas.
Preferably, step 3) are as follows: the second rotary valve continuous service keeps the value of second pressure meter not become initial pressure P2, observe the real-time frequency F of the blower motor of the second dust pelletizing system2' or observation second flowmeter real-time traffic Q2'；If the The real-time frequency F of the blower motor of two dust pelletizing systems2' value in original frequency F2Preferably exist in the range of the 80-120% of value Original frequency F2In the range of the 85-115% of value, more preferably in original frequency F2In the range of the 90-110% of value or The real-time traffic Q of two flowmeters2' value in initial flow Q2Preferably in initial flow Q in the range of the 80-120% of value2Value 85-115% in the range of, more preferably in initial flow Q2In the range of the 90-110% of value, then the second rotary valve is in Normal operating condition continues to observe；If the real-time frequency F of the blower motor of the second dust pelletizing system2' value exceed original frequency F2The 80-120%'s of value ranges preferably from beyond original frequency F2The range of the 85-115% of value, more preferably beyond initial frequency Rate F2The range of the 90-110% of value or the real-time traffic Q of second flowmeter2' value exceed initial flow Q2The 80- of value 120% ranges preferably from beyond initial flow Q2The range of the 85-115% of value more preferably exceeds initial flow Q2Value The range of 90-110% then determines the second rotary valve gas leakage.
Preferably, step 3) may be: the second rotary valve continuous service keeps the blower motor of the second dust pelletizing system Frequency do not become original frequency F2Or the flow of second flowmeter is kept not become initial flow Q2, observation second pressure meter Real-time pressure P2'；If the real-time pressure P of second pressure meter2' value in initial pressure P2It is excellent in the range of the 80-120% of value It is selected as in initial pressure P2In the range of the 85-115% of value, more preferably in initial pressure P2In the range of the 90-110% of value, Then the second rotary valve is in normal operating condition, continues to observe；If the real-time pressure P of second pressure meter2' value beyond initial Pressure P2The 80-120%'s of value ranges preferably from beyond initial pressure P2The range of the 85-115% of value, more preferably beyond just Beginning pressure P2The range of the 90-110% of value then determines the second rotary valve gas leakage.
Second of embodiment according to the present invention provides a kind of processing method of rotary valve gas leakage or handles the first reality The method for applying the second rotary valve gas leakage in scheme.
A kind of processing method of rotary valve gas leakage or the method for handling the second rotary valve gas leakage in the first embodiment, should Method is further comprising the steps of:
4) the 4th pipeline is added between the top of adsorption tower and the second rotary valve, the flue gas of the second rotary valve lower part is via Four pipelines are delivered to former smoke conveying duct after mixing with both the gas that the second foreign gas conveyance conduit conveys；
5) real-time frequency that the second valve being arranged on the 4th pipeline makes the blower motor of the second dust pelletizing system is adjusted F2' revert to equal to original frequency F2Or make the real-time traffic Q of second flowmeter2' revert to equal to initial flow Q2；Alternatively, The second valve being arranged on the 4th pipeline is adjusted, so that the real-time pressure P of second pressure meter2' revert to equal to initial pressure P2。
Preferably, the step 5) of this programme is also possible to: adjusting the second valve for being arranged on the 4th pipeline and make the The real-time frequency F of the blower motor of two dust pelletizing systems2' value revert in original frequency F2In the range of the 80-120% of value or So that the real-time traffic Q of second flowmeter2' value revert in initial flow Q2In the range of the 80-120% of value；Alternatively, adjusting Save the real-time pressure P that the second valve being arranged on the 4th pipeline makes second pressure meter2' value revert in initial pressure P2 In the range of the 80-120% of value.
Preferably, this method is further comprising the steps of:
6a) other end of the second foreign gas conveyance conduit is connected with the cooling section gas vent of Analytic Tower, adjusts setting The 4th valve on the second foreign gas conveyance conduit, so that the flue gas of the 4th pipeline and the second foreign gas delivery pipe The temperature of the mixed mixed gas of both the gas of road conveying is higher than the acid dew point of the flue gas of the 4th pipeline.
Preferably, after the flue gas of the 4th pipeline is mixed with both the gas that the second foreign gas conveyance conduit conveys Via the 5th pipeline to former smoke conveying duct.5th pipeline is equipped with second temperature meter.Second temperature meter on-line checking The temperature of mixed gas in the pipeline of corresponding position.
Preferably, step 6a) described in adjust the 4th valve that is arranged on the second foreign gas conveyance conduit so that The temperature of the mixed mixed gas of both the flue gas of 4th pipeline and the gas of the second foreign gas conveyance conduit conveying Higher than the acid dew point of the flue gas of the 4th pipeline, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline: measuring dioxy in the flue gas of the 4th pipeline Change sulphur concentration beAs a result, in the flue gas of the 4th pipeline sulfur trioxide concentrationAre as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-48%, more preferably 0.5-3%；
2. calculating the acid dew point of the flue gas of the 4th pipeline: measuring the concentration of vapor in the flue gas of the 4th pipeline ForThe acid dew point t of the flue gas of the 4th pipeline can be obtained as a result,ld2Are as follows:
In formula (4),For the concentration of vapor in the flue gas of the 4th pipeline, %；For the 4th pipeline Flue gas in sulfur trioxide concentration, %；
The 4th valve on the second foreign gas conveyance conduit is adjusted, so that the reading of the second temperature meter on the 5th pipeline t2> tld2。
Preferably, this method may also comprise the following steps::
The 4th valve being arranged on the second foreign gas conveyance conduit 6b) is adjusted, so that the flue gas of the 4th pipeline The acid dew point of the mixed mixed gas of both the gas conveyed with the second foreign gas conveyance conduit is lower than environment temperature.
Preferably, after the flue gas of the 4th pipeline is mixed with both the gas that the second foreign gas conveyance conduit conveys Via the 5th pipeline to former smoke conveying duct.5th pipeline is equipped with the 2nd CO (or CO2) detector.2nd CO detection In the pipeline of instrument on-line checking corresponding position in mixed gas CO concentration.
Preferably, step 6b) described in adjust the 4th valve that is arranged on the second foreign gas conveyance conduit so that The acid of the mixed mixed gas of both the flue gas of 4th pipeline and the gas of the second foreign gas conveyance conduit conveying reveals Point is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline: measuring dioxy in the flue gas of the 4th pipeline Change sulphur concentration beAs a result, in the flue gas of the 4th pipeline sulfur trioxide concentrationAre as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. both the gas that the flue gas for calculating the 4th pipeline is conveyed with the second foreign gas conveyance conduit is mixed The acid dew point of mixed gas: the concentration for measuring vapor in the flue gas of the 4th pipeline isIf the second foreign gas is defeated Sending the gas of pipeline is n2 to the extension rate of the flue gas of the 4th pipeline, as a result, the acid dew point t of mixed gasld2' Are as follows:
In formula (8),For the concentration of vapor in mixed gas, %；For three oxygen in mixed gas Change the concentration of sulphur, %；
3. being t according to environment temperature is measuredEnvironment, defeated by the flue gas and the second foreign gas conveyance conduit of the 4th pipeline The acid dew point of the mixed mixed gas of both gas sent is lower than environment temperature, can obtain:
tld2' < tEnvironment；………(9)；
The gas of the second foreign gas conveyance conduit conveying can be acquired to the flue gas of the 4th pipeline according to formula (9) Extension rate n2；
4. both the gas that the flue gas for calculating the 4th pipeline is conveyed with the second foreign gas conveyance conduit is mixed The concentration of CO in mixed gas:
The concentration for measuring CO in the flue gas of the 4th pipeline is CCO2, as a result, in the 5th pipeline in mixed gas CO it is dense Spend CCO2' are as follows:
CCO2'=CCO2/n2；………(10)；
The 4th valve on the second foreign gas conveyance conduit is adjusted, so that the reading of the second carbon monoxide detector on the 5th pipeline Number is CCO2’。
The third embodiment provided according to the present invention, provides the method for judging rotary valve gas leakage at discharge position.It should Method is further comprising the steps of:
7) in the first rotary valve initial operation stage, the blower motor for the first dust pelletizing system being connected with the first conveyer is recorded Original frequency F1Or the initial flow of record the first conveyer of connection and the first flowmeter on the conveyance conduit of the first dust pelletizing system Measure Q1, and record the initial pressure P for being arranged on the first conveyer and being located at the first pressure meter in the first rotary valve downstream1；
8) the first rotary valve continuous service keeps the value of first pressure meter not become initial pressure P1, observe the first dedusting The real-time frequency F of the blower motor of system1' or observation first flowmeter real-time traffic Q1'；If the wind of the first dust pelletizing system The real-time frequency F of electromechanical machine1' it is equal to original frequency F1Or the real-time traffic Q of first flowmeter1' it is equal to initial flow Q1, then First rotary valve is in normal operating condition, continues to observe；If the real-time frequency F of the blower motor of the first dust pelletizing system1' no Equal to original frequency F1Or the real-time traffic Q of first flowmeter1' it is not equal to initial flow Q1, then determine that the first rotary valve leaks Gas.
In the present solution, step 8) is also possible to: the first rotary valve continuous service keeps the blower electricity of the first dust pelletizing system Unit frequency does not become original frequency F1Or the flow of first flowmeter is kept not become initial flow Q1, observation first pressure meter Real-time pressure P1'；If the real-time pressure P of first pressure meter1' it is equal to initial pressure P1, then the first rotary valve, which is in, operates normally State continues to observe；If the real-time pressure P of first pressure meter1' it is not equal to initial pressure P1, then determine that the first rotary valve leaks Gas.
Preferably, step 8) are as follows: the first rotary valve continuous service keeps the value of first pressure meter not become initial pressure P1, observe the real-time frequency F of the blower motor of the first dust pelletizing system1' or observation first flowmeter real-time traffic Q1'；If the The real-time frequency F of the blower motor of one dust pelletizing system1' value in original frequency F1Preferably exist in the range of the 80-120% of value Original frequency F1In the range of the 85-115% of value, more preferably in original frequency F1In the range of the 90-110% of value or The real-time traffic Q of flow meters1' value in initial flow Q1Preferably in initial flow Q in the range of the 80-120% of value1Value 85-115% in the range of, more preferably in initial flow Q1In the range of the 90-110% of value, then the first rotary valve is in Normal operating condition continues to observe；If the real-time frequency F of the blower motor of the first dust pelletizing system1' value exceed original frequency F1The 80-120%'s of value ranges preferably from beyond original frequency F1The range of the 85-115% of value, more preferably beyond initial frequency Rate F1The range of the 90-110% of value or the real-time traffic Q of first flowmeter1' value exceed initial flow Q1The 80- of value 120% ranges preferably from beyond initial flow Q1The range of the 85-115% of value more preferably exceeds initial flow Q1Value The range of 90-110% then determines the first rotary valve gas leakage.
Preferably, step 8) is it may also is that the first rotary valve continuous service, keeps the blower motor of the first dust pelletizing system Frequency does not become original frequency F1Or the flow of first flowmeter is kept not become initial flow Q1, observe the reality of first pressure meter When pressure P1'；If the real-time pressure P of first pressure meter1' value in initial pressure P1In the range of the 80-120% of value preferably For in initial pressure P1In the range of the 85-115% of value, more preferably in initial pressure P1In the range of the 90-110% of value, then First rotary valve is in normal operating condition, continues to observe；If the real-time pressure P of first pressure meter1' value beyond initial pressure Power P1The 80-120%'s of value ranges preferably from beyond initial pressure P1The range of the 85-115% of value, more preferably beyond initial Pressure P1The range of the 90-110% of value then determines the first rotary valve gas leakage.
The 4th kind of embodiment provided according to the present invention provides the method for rotary valve gas leakage at processing discharge position.It should Method is further comprising the steps of:
9) it adsorbs between tower bottom and the first rotary valve and adds first pipe, the flue gas on the first rotary valve top is via first Pipeline is delivered to former smoke conveying duct after mixing with both the gas that the first foreign gas conveyance conduit conveys；
10) the first valve being arranged in first pipe is adjusted, so that the real-time frequency of the blower motor of the first dust pelletizing system Rate F1' revert to equal to original frequency F,1Or make the real-time traffic Q of first flowmeter1' revert to equal to initial flow Q1.Or Person adjusts the first valve being arranged in first pipe, so that the real-time pressure P of first pressure meter1' it is equal to initial pressure P1。
In the present solution, step 10) may also is that the first valve for adjusting and being arranged in first pipe, so that first removes The real-time frequency F of the blower motor of dirt system1' value restore original frequency F1In the range of the 80-120% of value or make first The real-time traffic Q of flowmeter1' value restore initial flow Q1In the range of the 80-120% of value.It is arranged alternatively, adjusting first The first valve on pipeline, so that the real-time pressure P of first pressure meter1' value restore initial pressure P1The model of the 80-120% of value In enclosing.
Preferably, this method is further comprising the steps of:
11a) other end of the first foreign gas conveyance conduit is connected with the cooling section gas vent of Analytic Tower, adjusts setting Third valve on the first foreign gas conveyance conduit, so that the flue gas and the first foreign gas delivery pipe of first pipe conveying The temperature of the mixed mixed gas of both the gas of road conveying is higher than the acid dew point of the flue gas of first pipe conveying.
Preferably, after the flue gas of first pipe conveying is mixed with both the gas that the first foreign gas conveyance conduit conveys Former smoke conveying duct is delivered to via second pipe.Second pipe is equipped with the first thermometer.First thermometer on-line checking The temperature of mixed gas in the pipeline of corresponding position.
Preferably, step 11a) described in adjust the third valve that is arranged on the first foreign gas conveyance conduit, make Obtain the temperature of the mixed mixed gas of both the flue gas of first pipe conveying and the gas of the first foreign gas conveyance conduit conveying Degree is higher than the acid dew point of the flue gas of first pipe conveying, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe conveying: measuring dioxy in the flue gas of first pipe conveying Change sulphur concentration beThe concentration of sulfur trioxide in the flue gas that first pipe conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. calculating the acid dew point of the flue gas of first pipe conveying: measuring the concentration of vapor in the flue gas of first pipe conveying ForThe acid dew point t of the flue gas of first pipe conveying can be obtained as a result,ld1Are as follows:
In formula (2),For the concentration of vapor in the flue gas of first pipe conveying, %；For first pipe conveying Flue gas in sulfur trioxide concentration, %；
The third valve on the first foreign gas conveyance conduit is adjusted, so that the reading of the first thermometer on second pipe t1> tld1。
Preferably, this method may also comprise the following steps::
The third valve being arranged on the first foreign gas conveyance conduit 11b) is adjusted, so that the flue gas of first pipe conveying The acid dew point of the mixed mixed gas of both the gas conveyed with the first foreign gas conveyance conduit is lower than environment temperature.
Preferably, after the flue gas of first pipe conveying is mixed with both the gas that the first foreign gas conveyance conduit conveys Former smoke conveying duct is delivered to via second pipe.Second pipe is equipped with the first CO (or CO2) detector.First CO detection CO in mixed gas in the pipeline of instrument on-line checking corresponding position (or CO2) concentration.
Preferably, step 11b) described in adjust the third valve that is arranged on the first foreign gas conveyance conduit, make Obtain the acid of the mixed mixed gas of both the flue gas of first pipe conveying and the gas of the first foreign gas conveyance conduit conveying Dew point is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe conveying: measuring dioxy in the flue gas of first pipe conveying Change sulphur concentration beThe concentration of sulfur trioxide in the flue gas that first pipe conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. both the gas that the flue gas for calculating first pipe conveying is conveyed with the first foreign gas conveyance conduit is mixed The acid dew point of mixed gas: measuring the concentration of vapor in the flue gas of first pipe conveying isIf the first foreign gas is defeated Sending the gas of pipeline is n1 to the extension rate for the flue gas that first pipe conveys, as a result, the acid dew point t of mixed gasld1' Are as follows:
In formula (5),For the concentration of vapor in mixed gas, %；For three oxidation in mixed gas The concentration of sulphur, %；
3. being t according to environment temperature is measuredEnvironment, defeated by the flue gas and the first foreign gas conveyance conduit of first pipe conveying The acid dew point of the mixed mixed gas of both gas sent is lower than environment temperature, can obtain:
tld1' < tEnvironment；………(6)；
Flue gas first pipe conveyed according to the gas that formula (6) can acquire the conveying of the first foreign gas conveyance conduit Extension rate n1；
4. both the gas that the flue gas for calculating first pipe conveying is conveyed with the first foreign gas conveyance conduit is mixed The concentration of CO in mixed gas:
The concentration for measuring CO in the flue gas of first pipe conveying is CCO1, as a result, in second pipe in mixed gas CO it is dense Spend CCO1' are as follows:
CCO1'=CCO1/n1；………(7)；
The third valve on the first foreign gas conveyance conduit is adjusted, so that the reading of the first carbon monoxide detector on second pipe Number is CCO1’。
Preferably, the first dust pelletizing system is connected by third pipeline with the first conveyer.It is preferred that third pipeline is equipped with First flowmeter.
Preferably, the second dust pelletizing system is connected by the 6th pipeline with second conveyor.It is preferred that the 6th pipeline is equipped with Second flowmeter.
5th kind of embodiment according to the present invention provides a kind of judgement system of rotary valve gas leakage or for the first reality Apply the judgement system of scheme judgment method.
A kind of judgement and processing system of rotary valve gas leakage, the system include adsorption tower, Analytic Tower, the second rotary valve, Two conveyers, the second dust pelletizing system, second pressure meter, former smoke conveying duct, the 6th pipeline；Wherein, former smoke conveying duct It is connected to the smoke inlet of adsorption tower；Second conveyor connects the active carbon entrance of the active carbon outlet and adsorption tower of Analytic Tower； The active carbon inlet of adsorption tower is equipped with the second rotary valve；Second dust pelletizing system is connect by the 6th pipeline with second conveyor； Second conveyor is equipped with second pressure meter.
Preferably, the 6th pipeline is equipped with second flowmeter.
6th kind of embodiment according to the present invention provides a kind of second of reality of processing system or processing of rotary valve gas leakage Apply the processing system of scheme processing method.
The system includes system described in the 5th kind of embodiment, further includes: the active carbon entrance of adsorption tower and second Feeding pipe is equipped between conveyer.Second rotary valve is arranged on feeding pipe.From feeding pipe and it is located at the second rotation Both the 4th pipeline that the downstream of valve is drawn and second foreign gas conveyance conduit pass through after merging and are connected to former cigarette by the 5th pipeline Letter shoot road.
It is preferred that the 4th pipeline is equipped with the second valve.
Preferably, the second foreign gas conveyance conduit is equipped with the 4th valve.
Preferably, the 5th pipeline is equipped with second detection device；
Preferably, second detection device is second temperature meter or the 2nd CO (or CO2) detector.
Preferably, feeding pipe is equipped with the second online flue gas analyzer.
Preferably, the other end of the second foreign gas conveyance conduit is connected to the cooling section gas vent of Analytic Tower.
7th kind of embodiment according to the present invention provides a kind of judgement system of rotary valve gas leakage or for the third reality Apply the judgement system of scheme judgment method.
The system includes system described in the 5th kind of embodiment, further includes: the first rotary valve, the first conveyer, One dust pelletizing system, first pressure meter, third pipeline；Wherein, the active carbon outlet of the first conveyer connection adsorption tower and Analytic Tower Active carbon entrance；The active carbon exit of adsorption tower is equipped with the first rotary valve；First dust pelletizing system passes through third pipeline and the The connection of one conveyer；First conveyer is equipped with first pressure meter.
Preferably, third pipeline is equipped with first flowmeter.
8th kind of embodiment according to the present invention provides a kind of the 4th kind of reality of processing system or processing of rotary valve gas leakage Apply the processing system of scheme processing method.
The system includes system described in the 6th kind and the 7th kind of embodiment, further includes: the active carbon of adsorption tower goes out Blanking pipeline is equipped between mouth and the first conveyer；First rotary valve is arranged on feeder pipe road；From feeder pipe road and it is located at Both the first pipe that the upstream of first rotary valve is drawn and first foreign gas conveyance conduit pass through after merging to be connected by second pipe It is connected to former smoke conveying duct.
Preferably, first pipe is equipped with the first valve.
Preferably, the first foreign gas conveyance conduit is equipped with third valve.
Preferably, second pipe is equipped with the first detection device；It is preferred that the first detection device is the first thermometer or the One CO (or CO2) detector.
Preferably, feeder pipe road is equipped with the first online flue gas analyzer.
Preferably, the other end of the first foreign gas conveyance conduit is connected to the cooling section gas vent of Analytic Tower.
In the present invention, flue gas enters adsorption tower under the action of booster fan, net by the activated carbon adsorption in adsorption tower It is discharged after change.The active carbon for having adsorbed pollutant in flue gas enters the first conveyer via the first rotary valve of absorption tower bottom, Active carbon is delivered to Analytic Tower and is parsed, regenerates by the first conveyer, and the active carbon after parsing enters second conveyor, via The second rotary valve at the top of adsorption tower enters adsorption tower, carries out purified treatment via to flue gas, completes primary complete material and follows Ring.
In the present invention, according to adsorption tower, conveyer, dust pelletizing system, connection feature between this three, if rotary valve Gas leakage, the flue gas for being delivered to adsorption tower can be revealed when passing through the second rotary valve from the top of adsorption tower by adsorption tower, then Into second conveyor.Inherently there is fixed gas circulation inside second conveyor, if the second rotary valve does not leak The case where gas, pressure in second conveyor, second are delivered to the throughput of dust pelletizing system, the blower frequency of the second dust pelletizing system It is fixed and invariable (or variation is in the range of setting).If gas leakage situation occurs for the second rotary valve, into adsorption tower Flue gas is revealed from the position of the second rotary valve, into second conveyor.In this application, on second conveyor and it is located at the Second pressure meter is arranged in two rotary valve discharge stream downstreams, if the second rotary valve gas leakage, the pressure of second pressure meter is aobvious Show, connect the blower frequency of second conveyor and throughput, the second dust pelletizing system in the pipeline of dust pelletizing system, always has in three The reading of position can change at one, the present invention according to the variation principle of throughput judge the second rotary valve whether gas leakage.
In the present invention, the judgment method of the second rotary valve gas leakage are as follows: 1. in the second rotary valve initial operation stage or When two rotary valves are in normal operating conditions, the blower motor for the second dust pelletizing system that typing is connected with second conveyor it is initial Frequency F2, and the initial pressure P of second pressure meter being arranged on second conveyor2Size；2. the second rotary valve is persistently transported Row keeps the value of second pressure meter not become initial pressure P2, observe the real-time frequency of the blower motor of the second dust pelletizing system Variation；3. the variation range of the real-time frequency of the blower motor of the second dust pelletizing system is set, if the blower electricity of the second dust pelletizing system The real-time frequency F of machine2' variation (or the blower motor of the second dust pelletizing system is real-time in the frequency range of setting Frequency F2' it is equal to original frequency F2), then determine that the second rotary valve is in normal operating condition, continues to observe the second dust pelletizing system The real-time frequency F of blower motor2' variation.If the real-time frequency F of the blower motor of dust pelletizing system2' variation be more than set Fixed frequency range (or the real-time frequency F of the blower motor of the second dust pelletizing system2' it is not equal to original frequency F2), then sentence The case where fixed second rotary valve leaks out.
In the present invention, the judgment method of another rotary valve gas leakage are as follows: 1. in the second rotary valve initial operation stage, either When second rotary valve is in normal operating conditions, the initial frequency of the blower motor for the dust pelletizing system that typing is connected with second conveyor Rate F2, and the initial pressure P of second pressure meter being arranged on second conveyor2Size；2. the second rotary valve continuous service, Keeping the blower motor frequency of the second dust pelletizing system does not become original frequency F2, observe the real-time pressure P of second pressure meter2'；③ Set the real-time pressure P of second pressure meter2' variation range, if the real-time pressure P of second pressure meter2' variation in setting In pressure range (or the real-time pressure P of second pressure meter2' it is equal to initial pressure P2), then the second rotary valve is in just Normal operating status continues the variation for observing the real-time frequency of the blower motor of the second dust pelletizing system.If second pressure meter Real-time pressure P2' variation be more than setting pressure range (or the real-time pressure P of second pressure meter2' not equal to just Beginning pressure P2), then determine the case where the second rotary valve leaks out.
Preferably, the present invention is equipped with second flow on the 6th pipeline between second conveyor and the second dust pelletizing system Meter.This method is not required to consider the blower motor frequency of the second dust pelletizing system, matches contract by second flowmeter and second pressure meter The judgement to the second rotary valve gas leakage may be implemented in sample.Specifically: 1) it is rotated in the second rotary valve initial operation stage or second When valve is in normal operating conditions, the initial flow Q of typing second flowmeter2, and the second pressure being arranged on second conveyor The initial pressure P of power meter2；2) the second rotary valve continuous service keeps the value of second pressure meter not become initial pressure P2It is big It is small, observe the real-time traffic Q of second flowmeter2'；3) the variation model of the real-time traffic of second flowmeter on the 6th pipeline is set It encloses, if the reading of second flowmeter changes within the scope of the changes in flow rate of setting (or the real-time traffic Q of second flowmeter2' etc. In initial flow Q2), then the second rotary valve is in normal operating condition, continues the real-time traffic Q for observing second flowmeter2' i.e. It can；If the real-time traffic variation of second flowmeter is more than changes in flow rate range (or the real-time traffic of second flowmeter of setting Q2' it is not equal to initial flow Q2), then determine the case where the second rotary valve leaks out.
In the present invention, the judgment method of another the second rotary valve gas leakage are as follows: 1. in the second rotary valve initial operation stage, or When person is that the second rotary valve is in normal operating conditions, the initial flow for the second flowmeter that typing is connected with second conveyor Q2, and the initial pressure P of second pressure meter being arranged on second conveyor2Size；2. the second rotary valve continuous service is protected Hold the real-time traffic Q of second flowmeter2' do not become initial flow Q2, observe the real-time pressure P of second pressure meter2'；3. setting The real-time pressure P of two pressure gauges2' variation range, if the real-time pressure P of second pressure meter2' variation setting pressure become Change (either, the real-time pressure P of second pressure meter in range2' it is equal to initial pressure P2), then the second rotary valve is in normal fortune Row state continues the real-time pressure P for observing second pressure meter2' variation.If the real-time pressure P of second pressure meter2' change Changing is more than pressure range (either, the real-time pressure P of second pressure meter set2' it is not equal to initial pressure P2), then sentence The case where fixed second rotary valve leaks out.
In the present invention, frequency range of the variation of the real-time frequency of the blower motor of the second dust pelletizing system in setting It is interior, refer to: real-time frequency F2' value be original frequency F2Within the scope of the 80-120% of value, preferably original frequency F2The 85- of value In the range of 115%, more preferably original frequency F2In the range of the 90-110% of value.That is real-time frequency F2' value be (80- 120%) * F2In the range of, preferably real-time frequency F2' value be (85-115%) * F2In the range of, more preferably frequently in real time Rate F2' value be (90-110%) * F2In the range of.Correspondingly, the variation of the real-time frequency of the blower motor of the second dust pelletizing system More than the frequency range of setting, as exceed above range.
In the present invention, the real-time pressure P of second pressure meter2' variation in the frequency range of setting, refer to: Real-time pressure P2' value be initial pressure P2Within the scope of the 80-120% of value, preferably initial pressure P2The model of the 85-115% of value In enclosing, more preferably initial pressure P2In the range of the 90-110% of value.That is real-time pressure P2' value be (80-120%) * P2's In range, preferably real-time pressure P2' value be (85-115%) * P2In the range of, more preferably real-time pressure P2' value be (90-110%) * P2In the range of.Correspondingly, the real-time pressure P of second pressure meter2' variation be more than setting pressure change model It encloses, as exceeds above range.
In the present invention, the reading of second flowmeter changes within the scope of the changes in flow rate of setting, refers to: real-time traffic Q2' value be initial flow Q2Within the scope of the 80-120% of value, preferably initial flow Q2In the range of the 85-115% of value, more Preferably initial flow Q2In the range of the 90-110% of value.That is real-time traffic Q2' value be (80-120%) * Q2In the range of, Preferably real-time traffic Q2' value be (85-115%) * Q2In the range of, more preferably real-time traffic Q2' value be (90- 110%) * Q2In the range of.Correspondingly, the real-time traffic variation of second flowmeter is more than the changes in flow rate range of setting, as Beyond above range.
The present invention can in time, accurately judge the second rotary valve with the presence or absence of gas leakage situation by the above method.This hair The method of bright offer does not need to see the specific structure situation inside the second rotary valve, that is, does not need to see the second rotary valve Internal blade destroys situation with the presence or absence of abrasion etc., and whether the blade that can be detected to the second rotary valve deforms.Meanwhile passing through In the real-time frequency of the blower motor of second dust pelletizing system, the real-time pressure of second pressure meter or the real-time traffic of second flowmeter Any one parameter variation, and the amplitude range of variation can judge the seriousness of the second rotary valve gas leakage；It is above-mentioned Any one of three's data data variation amplitude is bigger, illustrates that the second rotary valve gas leakage is more serious；Amplitude of variation is smaller, illustrates Two rotary valve gas leakage are slighter or even air tight.
In the present invention, the processing method of the second rotary valve gas leakage are as follows: the flue gas that will leak to second conveyor is taken away, And avoid flue gas from entering second conveyor condensation post-etching second conveyor, and then flue gas is avoided to enter the second dust pelletizing system, it makes Corrode at the second dedusting pipeline blockage and the second dust pelletizing system；Meanwhile it being conveyed by the second foreign gas conveyance conduit Corresponding air quantity is mixed with the flue gas to be leaked, to avoid air draft pipeline (pipeline that conveying will reveal flue gas) because of flue gas condensing Clog occurs for moisture condensation.In addition, the flue gas to be leaked and the gas of the second foreign gas conveyance conduit conveying pass through original together Smoke conveying duct enters adsorption tower and carries out purified treatment, decreases pollution of the discharge to environment of flue gas.
In the embodiment for judging rotary valve gas leakage of the invention, outside the 4th pipeline and second that feeding pipe is drawn Come after both gas transmission pipelines merge through being connected to former smoke conveying duct by the 5th pipeline.Preferably, the second extraneous gas The other end of body conveyance conduit is connected to the cooling section gas vent of Analytic Tower.In general, former smoke conveying duct is equipped with The link position of booster fan, the 5th pipeline and former smoke conveying duct is located at the upstream of booster fan, and (" upstream " herein is According to the flow direction setting of flue gas in former smoke conveying duct).The present invention passes through the using the negative pressure of booster fan entrance Four pipelines extract the flue gas that will leak to conveyer, while the cooling of Analytic Tower is extracted by the second foreign gas conveyance conduit The cooling wind of section gas vent discharge.Adjust the second valve for being arranged on the 4th pipeline so that second pressure meter value not In the case where change, so that the blower motor frequency retrieval of the second dust pelletizing system is original frequency F0(or it is restored to setting range It is interior)；Alternatively, the second valve being arranged on the 4th pipeline is adjusted, so that in the case where the value of second pressure meter is constant, second The reading of flowmeter reverts to initial flow Q0(or being restored in setting range)；To prevent flue gas in adsorption tower by In the second rotary valve deformation and leak in second conveyor, also ensure extract air quantity reasonability.Either, adjusting is set Set the second valve on the 4th pipeline so that the second dust pelletizing system blower motor frequency or second flowmeter reading not In the case where change, so that the value in second pressure meter reverts to initial pressure P0(or being restored in setting range)；To anti- Flue gas in adsorption tower is stopped to leak in second conveyor due to the deformation of the second rotary valve, has also ensured and extract air quantity Reasonability.
Since high temperature active charcoal in cooling section and cooling wind carries out indirect heat exchange, the analytically cooling of tower in Analytic Tower The temperature of the cooling wind of section gas vent discharge is higher, is 100~130 DEG C.In view of pipeline radiates, the present invention is set by adjusting Set the 4th valve on the second foreign gas conveyance conduit, come control extraction Analytic Tower cooling section gas vent cooling wind Air quantity so that Analytic Tower outlet cooling wind and to leak to the mixed mixed gas of both flue gases of second conveyor Temperature is higher than the acid dew point of mixed gas, the i.e. gas of the second foreign gas conveyance conduit conveying and the flue gas of the 4th pipeline The temperature of the mixed mixed gas of the two is higher than the acid dew point of mixed gas, so that air draft pipeline be avoided to condense because of flue gas condensing Clog occurs.
According to relational expression, the acid dew point of flue gas(its In,For the concentration of vapor in the flue gas of the 4th pipeline (L6) conveying, %；For the cigarette of the 4th pipeline (L6) conveying The concentration of sulfur trioxide, % in gas), it is known that the acid dew point of flue gas is related with the content of vapor in flue gas and sulfur trioxide, when After the flue gas to be leaked is mixed with the cooling wind that Analytic Tower exports, the content of vapor and sulfur trioxide is reduced in mixed gas, Correspondingly, the acid dew point of gas reduces after mixing.Therefore, to avoid air draft pipeline that clog occurs because flue gas condensing condenses, The acid dew point that the 4th valve makes the temperature of mixed gas be higher than mixed gas is adjusted, and the acid dew point of mixed gas is lower than wanting The acid dew point of fume leakage then only needs to adjust the 4th valve and the temperature of mixed gas is made to be higher than the acid dew point that reveal flue gas , i.e. the mixed mixed gas of both flue gases of gas and the 4th pipeline that the second foreign gas conveyance conduit conveys Temperature be higher than the 4th pipeline flue gas acid dew point.
In the present invention, the concentration of the concentration of the sulfur dioxide in flue gas of the 4th pipeline and vapor is It is measured by the second online flue gas analyzer of active carbon flue gas purification system.Second online flue gas analyzer is arranged in adsorption tower Feeding pipe on, measure the concentration of sulfur dioxide in flue gas and vapor at the position, that is, measure and will leak to The concentration of sulfur dioxide and vapor in the flue gas of two conveyers.Concentration by measuring sulfur dioxide in flue gas can acquire The concentration of sulfur trioxide in flue gas, so that the acid dew point that will leak to the flue gas of second conveyor be calculated.Adjust second The 4th valve on foreign gas conveyance conduit controls the cooling air quantity of the Analytic Tower outlet of extraction, so that the temperature of mixed gas Degree is that the reading of the thermometer on the 5th pipeline is greater than the acid dew point for wanting fume leakage, to avoid air draft pipeline because of flue gas condensing Clog occurs for moisture condensation.
In the present invention, the method for handling the second rotary valve gas leakage may also is that the 4th pipeline drawn from feeding pipe Through being connected to former smoke conveying duct by the 5th pipeline after merging with both the second foreign gas conveyance conduits.Second foreign gas Conveyance conduit is not connect with Analytic Tower cooling section gas vent, directly transports diluent gas (such as air) dilution cigarette to be leaked Gas.The present invention is by adjusting the 4th valve being arranged on the second foreign gas conveyance conduit, to control conveying diluent gas Air quantity, so that the mixed gaseous mixture of both the cold wind of the second foreign gas conveyance conduit conveying and the flue gas of the 4th pipeline The acid dew point of body is lower than environment temperature, to avoid air draft pipeline that clog occurs because flue gas condensing condenses.
It is lower than environment temperature according to the acid dew point of mixed gas, the cold of the second foreign gas conveyance conduit conveying can be acquired Extension rate n2 of the wind to the flue gas of the 4th pipeline.Since the content of CO in flue gas is relatively fixed, and in atmosphere substantially not Containing CO (or the content of CO is few), can be ignored, thus in mixed gas CO concentration CCO2' it is the 4th pipeline Flue gas in CO concentration CCO2Concentration after n2 times of dilution, i.e. CCO2'=CCO2/n2.It adjusts on the second foreign gas conveyance conduit The 4th valve, control the air quantity of transporting cold wind so that the reading of the second carbon monoxide detector on the 5th pipeline be CCO2', thus real The acid dew point of existing mixed gas is lower than environment temperature, avoids air draft pipeline that clog occurs because flue gas condensing condenses.
Further, since CO in flue gas2Content it is also relatively fixed, and CO in atmosphere2Content it is also very low, be 0.03~ 0.04% (volume ratio), can be ignored.Therefore, in the third embodiment of the invention and the 4th kind of embodiment, The second detection device being arranged on 5th pipeline replaces with the 2nd CO2The technical solution equally may be implemented in detector.
In the present invention, the concentration of sulfur dioxide in flue gas of the 4th pipeline and the concentration of vapor and CO in the flue gas of four pipelines (or CO2) concentration, be by the second online flue gas of active carbon flue gas purification system point Analyzer measures.
In the present invention, the frequency of the blower motor of the second dust pelletizing system can be shown by blower motor itself and be obtained. Second flowmeter detection connects conveyance conduit (i.e. the 6th pipeline) interior gas between second conveyor and the second dust pelletizing system Flow.Second pressure meter is used to detect the pressure value that gas circulates in second conveyor.4th pipeline is used for will be above rotary valve The flue gas that will be revealed is delivered to former smoke conveying duct, avoids the leakage of the second rotary valve.Second foreign gas conveyance conduit For mixing with the flue gas in the 4th pipeline, the 5th pipeline of merga pass is to former smoke conveying duct after mixing.Outside second Carry out the temperature that gas is used to adjust mixed gas in the 5th pipeline, so that the temperature of mixed gas is higher than the acid dew of the mixed gas Point temperature；Or the acid dew-point temperature of mixed gas in the 5th pipeline is adjusted, so that the acid dew-point temperature of mixed gas is lower than ring Border temperature；So as to avoid conveying mixed gas pipeline there is a situation where corrode.
In the present invention, according to adsorption tower, the first conveyer, the first dust pelletizing system, connection feature between this three, such as Fruit the first rotary valve gas leakage, the flue gas for being delivered to adsorption tower can pass through the first rotary valve from the bottom of adsorption tower by adsorption tower Shi Fasheng leakage, enters back into the first conveyer.Inherently there is fixed gas circulation inside first conveyer, if the first rotation Gas of the rotary valve not there is a situation where gas leakage, in the pipeline of pressure, the first conveyer of connection and dust pelletizing system in the first conveyer Flow, the first dust pelletizing system blower frequency be fixed and invariable (or variation in the range of setting).If the first rotation Gas leakage situation occurs for valve, reveals into the flue gas of adsorption tower from the position of the first rotary valve, into the first conveyer.In the application In, on the first conveyer and it is located at the first rotary valve discharge stream downstream setting first pressure meter, if the first rotary valve Gas leakage, then the pressure of first pressure meter shows, connects the first conveyer and throughput in the pipeline of dust pelletizing system, first removes The blower frequency of dirt system always has the reading of position at one that can change in three, and the present invention is former according to the variation of throughput Reason judge the first rotary valve whether gas leakage.
In the present invention, the judgment method of the first rotary valve gas leakage are as follows: 1. in the first rotary valve initial operation stage or When one rotary valve is in normal operating conditions, the blower motor for the first dust pelletizing system that typing is connected with the first conveyer it is initial Frequency F1, and the initial pressure P of first pressure meter being arranged on the first conveyer1Size；2. the first rotary valve is persistently transported Row keeps the value of first pressure meter not become initial pressure P1, observe the real-time frequency of the blower motor of the first dust pelletizing system Variation；3. the variation range of the real-time frequency of the blower motor of the first dust pelletizing system is set, if the blower electricity of the first dust pelletizing system The real-time frequency F of machine1' variation (or the blower motor of the first dust pelletizing system is real-time in the frequency range of setting Frequency F1' it is equal to original frequency F1), then determine that the first rotary valve is in normal operating condition, continues to observe the first dust pelletizing system The real-time frequency F of blower motor1' variation.If the real-time frequency F of the blower motor of dust pelletizing system1' variation be more than set Fixed frequency range (or the real-time frequency F of the blower motor of the first dust pelletizing system1' it is not equal to original frequency F1), then sentence The case where fixed first rotary valve leaks out.
In the present invention, the judgment method of another rotary valve gas leakage are as follows: 1. in the first rotary valve initial operation stage, either When first rotary valve is in normal operating conditions, the initial frequency of the blower motor for the dust pelletizing system that typing is connected with the first conveyer Rate F1, and the initial pressure P of first pressure meter being arranged on the first conveyer1Size；2. the first rotary valve continuous service, Keeping the blower motor frequency of the first dust pelletizing system does not become original frequency F1, observe the real-time pressure P of first pressure meter1'；③ Set the real-time pressure P of first pressure meter1' variation range, if the real-time pressure P of first pressure meter1' variation in setting In pressure range (or the real-time pressure P of first pressure meter1' it is equal to initial pressure P1), then the first rotary valve is in just Normal operating status continues the variation for observing the real-time frequency of the blower motor of the first dust pelletizing system.If first pressure meter Real-time pressure P1' variation be more than setting pressure range (or the real-time pressure P of first pressure meter1' not equal to just Beginning pressure P1), then determine the case where the first rotary valve leaks out.
Preferably, the present invention is equipped with first flow on the third pipeline between the first conveyer and the first dust pelletizing system Meter.This method is not required to consider the blower motor frequency of the first dust pelletizing system, matches contract by first flowmeter and first pressure meter The judgement to the first rotary valve gas leakage may be implemented in sample.Specifically: 1) it is rotated in the first rotary valve initial operation stage or first When valve is in normal operating conditions, the initial flow Q of typing first flowmeter1, and the first pressure being arranged on the first conveyer The initial pressure P of power meter1；2) the first rotary valve continuous service keeps the value of first pressure meter not become initial pressure P1It is big It is small, observe the real-time traffic Q of first flowmeter1'；3) the variation model of the real-time traffic of first flowmeter on third pipeline is set It encloses, if the reading of first flowmeter changes within the scope of the changes in flow rate of setting (or the real-time traffic Q of first flowmeter1' etc. In initial flow Q1), then the first rotary valve is in normal operating condition, continues the real-time traffic Q for observing first flowmeter1' i.e. It can；If the real-time traffic variation of first flowmeter is more than changes in flow rate range (or the real-time traffic of first flowmeter of setting Q1' it is not equal to initial flow Q1), then determine the case where the first rotary valve leaks out.
In the present invention, the judgment method of another the first rotary valve gas leakage are as follows: 1. in the first rotary valve initial operation stage, or When person is that the first rotary valve is in normal operating conditions, the initial flow for the first flowmeter that typing is connected with the first conveyer Q1, and the initial pressure P of first pressure meter being arranged on the first conveyer1Size；2. the first rotary valve continuous service is protected Hold the real-time traffic Q of first flowmeter1' do not become initial flow Q1, observe the real-time pressure P of first pressure meter1'；3. setting The real-time pressure P of one pressure gauge1' variation range, if the real-time pressure P of first pressure meter1' variation setting pressure become Change (either, the real-time pressure P of first pressure meter in range1' it is equal to initial pressure P1), then the first rotary valve is in normal fortune Row state continues the real-time pressure P for observing first pressure meter1' variation.If the real-time pressure P of first pressure meter1' change Changing is more than pressure range (either, the real-time pressure P of first pressure meter set1' it is not equal to initial pressure P1), then sentence The case where fixed first rotary valve leaks out.
In the present invention, frequency range of the variation of the real-time frequency of the blower motor of the first dust pelletizing system in setting It is interior, refer to: real-time frequency F1' value be original frequency F1Within the scope of the 80-120% of value, preferably original frequency F1The 85- of value In the range of 115%, more preferably original frequency F1In the range of the 90-110% of value.That is real-time frequency F1' value be (80- 120%) * F1In the range of, preferably real-time frequency F1' value be (85-115%) * F1In the range of, more preferably frequently in real time Rate F1' value be (90-110%) * F1In the range of.Correspondingly, the variation of the real-time frequency of the blower motor of the first dust pelletizing system More than the frequency range of setting, as exceed above range.
In the present invention, the real-time pressure P of first pressure meter1' variation in the frequency range of setting, refer to: Real-time pressure P1' value be initial pressure P1Within the scope of the 80-120% of value, preferably initial pressure P1The model of the 85-115% of value In enclosing, more preferably initial pressure P1In the range of the 90-110% of value.That is real-time pressure P1' value be (80-120%) * P1's In range, preferably real-time pressure P1' value be (85-115%) * P1In the range of, more preferably real-time pressure P1' value be (90-110%) * P1In the range of.Correspondingly, the real-time pressure P of first pressure meter1' variation be more than setting pressure change model It encloses, as exceeds above range.
In the present invention, the reading of first flowmeter changes within the scope of the changes in flow rate of setting, refers to: real-time traffic Q1' value be initial flow Q1Within the scope of the 80-120% of value, preferably initial flow Q1In the range of the 85-115% of value, more Preferably initial flow Q1In the range of the 90-110% of value.That is real-time traffic Q1' value be (80-120%) * Q1In the range of, Preferably real-time traffic Q1' value be (85-115%) * Q1In the range of, more preferably real-time traffic Q1' value be (90- 110%) * Q1In the range of.Correspondingly, the real-time traffic variation of first flowmeter is more than the changes in flow rate range of setting, as Beyond above range.
The present invention can in time, accurately judge the first rotary valve with the presence or absence of gas leakage situation by the above method.This hair The method of bright offer does not need to see the specific structure situation inside the first rotary valve, that is, does not need to see the first rotary valve Internal blade destroys situation with the presence or absence of abrasion etc., and whether the blade that can be detected to the first rotary valve deforms.Meanwhile passing through In the real-time frequency of the blower motor of first dust pelletizing system, the real-time pressure of first pressure meter or the real-time traffic of first flowmeter Any one parameter variation, and the amplitude range of variation can judge the seriousness of the first rotary valve gas leakage；It is above-mentioned Any one of three's data data variation amplitude is bigger, illustrates that the first rotary valve gas leakage is more serious；Amplitude of variation is smaller, illustrates One rotary valve gas leakage is slighter or even air tight.
In the present invention, the processing method of the first rotary valve gas leakage are as follows: the flue gas that will leak to the first conveyer is taken away, And avoid flue gas from entering the first conveyer and condense the first conveyer of post-etching, and then flue gas is avoided to enter the first dust pelletizing system, it makes Corrode at the first dedusting pipeline blockage and the first dust pelletizing system；Meanwhile it being conveyed by the first foreign gas conveyance conduit Corresponding air quantity is mixed with the flue gas to be leaked, to avoid air draft pipeline (pipeline that conveying will reveal flue gas) because of flue gas condensing Clog occurs for moisture condensation.In addition, the flue gas to be leaked and the gas of the first foreign gas conveyance conduit conveying pass through original together Smoke conveying duct enters adsorption tower and carries out purified treatment, decreases pollution of the discharge to environment of flue gas.
In the embodiment for judging rotary valve gas leakage of the invention, outside the first pipe and first that feeder pipe pass goes out Come after both gas transmission pipelines merge through being connected to former smoke conveying duct by second pipe.Preferably, the first extraneous gas The other end of body conveyance conduit is connected to the cooling section gas vent of Analytic Tower.In general, former smoke conveying duct is equipped with The link position of booster fan, first pipe and former smoke conveying duct is located at the upstream of booster fan, and (" upstream " herein is According to the flow direction setting of flue gas in former smoke conveying duct).The present invention passes through the using the negative pressure of booster fan entrance One pipeline extracts the flue gas that will leak to conveyer, while the cooling of Analytic Tower is extracted by the first foreign gas conveyance conduit The cooling wind of section gas vent discharge.Adjust the first valve for being arranged in first pipe so that first pressure meter value not In the case where change, so that the blower motor frequency retrieval of the first dust pelletizing system is original frequency F1(or it is restored to setting range It is interior)；Alternatively, the first valve being arranged in first pipe is adjusted, so that in the case where the value of first pressure meter is constant, first The reading of flowmeter reverts to initial flow Q1(or being restored in setting range)；To prevent flue gas in adsorption tower by In the first rotary valve deformation and leak in the first conveyer, also ensure extract air quantity reasonability.Either, adjusting is set Set the first valve in first pipe so that the first dust pelletizing system blower motor frequency or first flowmeter reading not In the case where change, so that the value in first pressure meter reverts to initial pressure P1(or being restored in setting range)；To anti- Flue gas in adsorption tower is stopped to leak in the first conveyer due to the deformation of the first rotary valve, has also ensured and extract air quantity Reasonability.
Since high temperature active charcoal in cooling section and cooling wind carries out indirect heat exchange, the analytically cooling of tower in Analytic Tower The temperature of the cooling wind of section gas vent discharge is higher, is 100~130 DEG C.In view of pipeline radiates, the present invention is set by adjusting Set the 4th valve on the first foreign gas conveyance conduit, come control extraction Analytic Tower cooling section gas vent cooling wind Air quantity so that Analytic Tower outlet cooling wind and to leak to the mixed mixed gas of both flue gases of the first conveyer Temperature is higher than the acid dew point of mixed gas, the i.e. gas of the first foreign gas conveyance conduit conveying and the flue gas of first pipe conveying The temperature of the mixed mixed gas of the two is higher than the acid dew point of mixed gas, so that air draft pipeline be avoided to condense because of flue gas condensing Clog occurs.
According to relational expression, the acid dew point t of flue gasld2':
(wherein, For the concentration of vapor in mixed gas, %；For the concentration of sulfur trioxide in mixed gas, %), it is known that flue gas Acid dew point is related with the content of vapor in flue gas and sulfur trioxide, when the cooling wind of the flue gas to be leaked and Analytic Tower outlet is mixed After conjunction, the content of vapor and sulfur trioxide is reduced in mixed gas, correspondingly, the acid dew point of gas reduces after mixing.Therefore, To avoid air draft pipeline that clog occurs because flue gas condensing condenses, to adjust the 4th valve and the temperature of mixed gas is higher than The acid dew point of mixed gas, and the acid dew point of mixed gas is lower than the acid dew point for wanting fume leakage, then only needs to adjust the 4th valve Door makes the temperature of mixed gas be higher than the acid dew point that reveal flue gas, the i.e. gas of the first foreign gas conveyance conduit conveying The acid for the flue gas that the temperature of the mixed mixed gas of both body and the flue gas of first pipe conveying is higher than first pipe conveying reveals Point.
In the present invention, the concentration for the sulfur dioxide in flue gas that the first pipe conveys and the concentration of vapor are It is measured by the first online flue gas analyzer of active carbon flue gas purification system.First online flue gas analyzer is arranged in adsorption tower Feeding pipe on, measure the concentration of sulfur dioxide in flue gas and vapor at the position, that is, measure and will leak to The concentration of sulfur dioxide and vapor in the flue gas of one conveyer.Concentration by measuring sulfur dioxide in flue gas can acquire The concentration of sulfur trioxide in flue gas, so that the acid dew point that will leak to the flue gas of the first conveyer be calculated.Adjust first Third valve on foreign gas conveyance conduit controls the cooling air quantity of the Analytic Tower outlet of extraction, so that the temperature of mixed gas Degree is that the reading of the thermometer on second pipe is greater than the acid dew point for wanting fume leakage, to avoid air draft pipeline because of flue gas condensing Clog occurs for moisture condensation.
In the present invention, the method for handling the first rotary valve gas leakage may also is that the first pipe gone out from feeder pipe pass Through being connected to former smoke conveying duct by second pipe after merging with both the first foreign gas conveyance conduits.First foreign gas Conveyance conduit is not connect with Analytic Tower cooling section gas vent, directly transports diluent gas (such as air) dilution cigarette to be leaked Gas.The present invention is by adjusting the third valve being arranged on the first foreign gas conveyance conduit, to control conveying diluent gas Air quantity, so that the mixed gaseous mixture of both the cold wind of the first foreign gas conveyance conduit conveying and the flue gas of first pipe conveying The acid dew point of body is lower than environment temperature, to avoid air draft pipeline that clog occurs because flue gas condensing condenses.
It is lower than environment temperature according to the acid dew point of mixed gas, the cold of the first foreign gas conveyance conduit conveying can be acquired Extension rate n2 of the wind to the flue gas of the 4th pipeline.Since the content of CO in flue gas is relatively fixed, and in atmosphere substantially not Containing CO (or the content of CO is few), can be ignored, thus in mixed gas CO concentration CCO2' it is the 4th pipeline Flue gas in CO concentration CCO2Concentration after n2 times of dilution, i.e. CCO2'=CCO2/n2.It adjusts on the first foreign gas conveyance conduit Third valve, control the air quantity of transporting cold wind so that the reading of the first carbon monoxide detector on second pipe be CCO2', thus real The acid dew point of existing mixed gas is lower than environment temperature, avoids air draft pipeline that clog occurs because flue gas condensing condenses.
Further, since CO in flue gas2Content it is also relatively fixed, and CO in atmosphere2Content it is also very low, be 0.03~ 0.04% (volume ratio), can be ignored.Therefore, in embodiments of the invention, the first inspection being arranged on second pipe It surveys device and replaces with the first CO2The technical solution equally may be implemented in detector.
In the present invention, the concentration of sulfur dioxide in flue gas and the concentration of vapor of first pipe conveying and the CO in the flue gas of four pipelines (or CO2) concentration, be by the first online flue gas of active carbon flue gas purification system point Analyzer measures.
In the present invention, the frequency of the blower motor of the first dust pelletizing system can be shown by blower motor itself and be obtained. First flowmeter detection connects conveyance conduit (i.e. third pipeline) interior gas between the first conveyer and the first dust pelletizing system Flow.First pressure meter is used to detect the pressure value that gas circulates in the first conveyer.First pipe is used for will be above rotary valve The flue gas that will be revealed is delivered to former smoke conveying duct, avoids the leakage of the first rotary valve.First foreign gas conveyance conduit For mixing with the flue gas in first pipe, merga pass second pipe is delivered to former smoke conveying duct after mixing.Outside first Carry out the temperature that gas is used to adjust mixed gas in second pipe, so that the temperature of mixed gas is higher than the acid dew of the mixed gas Point temperature；Or the acid dew-point temperature of mixed gas in second pipe is adjusted, so that the acid dew-point temperature of mixed gas is lower than ring Border temperature；So as to avoid conveying mixed gas pipeline there is a situation where corrode.
That is, can use the negative of booster fan entrance when judging the second rotary valve gas leakage at the top of adsorption tower Pressure extracts the flue gas that will leak to second conveyor by the 4th pipeline, adjusts the second valve being arranged on the 4th pipeline, Guarantee to extract the reasonability for wanting fume leakage amount；The cooling section gas of Analytic Tower is extracted by the second foreign gas conveyance conduit simultaneously The cooling wind of body outlet discharge, adjusts the 4th valve being arranged on the second foreign gas conveyance conduit, to control cigarette to be leaked It is blended into the amount of Analytic Tower cooling wind in gas, is adjusted using the waste heat of Analytic Tower cooling wind so that the second foreign gas conveyance conduit is defeated The temperature of the mixed mixed gas of both flue gases of the gas and the 4th pipeline that send is higher than the flue gas of the 4th pipeline Acid dew point, thus avoid air draft pipeline because flue gas condensing condense occur clog.In addition, when judging the second rotary valve gas leakage When, the second foreign gas conveyance conduit can not also be connect with the cooling section gas vent of Analytic Tower, and directly transport carrier gas Body (such as air) dilutes the flue gas to be leaked, and the 4th valve being arranged on the second foreign gas conveyance conduit is adjusted, to control The amount of system conveying diluent gas, so that both flue gases of the cold wind of the second foreign gas conveyance conduit conveying and the 4th pipeline The acid dew point of mixed mixed gas is lower than environment temperature, can equally occur to avoid air draft pipeline because flue gas condensing condenses rotten Erosion blocking.
Correspondingly, can use the negative pressure of booster fan entrance when the first rotary valve gas leakage of judgement absorption tower bottom The flue gas that will leak to the first conveyer is extracted by first pipe, adjusts the first valve being arranged in first pipe, is protected Card extracts the reasonability for wanting fume leakage amount；The cooling section gas of Analytic Tower is extracted by the first foreign gas conveyance conduit simultaneously The cooling wind of discharge is exported, the third valve being arranged on the first foreign gas conveyance conduit is adjusted, wants fume leakage to control In be blended into the amount of Analytic Tower cooling wind, adjusted using the waste heat of Analytic Tower cooling wind so that the first foreign gas conveyance conduit conveys Gas and the temperature of the mixed mixed gas of both flue gases of first pipe conveying be higher than the flue gas of first pipe conveying Acid dew point, to avoid air draft pipeline that clog occurs because flue gas condensing condenses.Likewise, when judging the first rotary valve gas leakage When, the first foreign gas conveyance conduit can not also be connect with the cooling section gas vent of Analytic Tower, and directly transport carrier gas Body (such as air) dilutes the flue gas to be leaked, and the third valve being arranged on the first foreign gas conveyance conduit is adjusted, to control The amount of system conveying diluent gas, so that both flue gases of the cold wind of the first foreign gas conveyance conduit conveying and first pipe conveying The acid dew point of mixed mixed gas is lower than environment temperature, can equally occur to avoid air draft pipeline because flue gas condensing condenses rotten Erosion blocking.
In the present invention, rotary valve and discharge valve are general, are the same part.Adsorption tower and desulfurizing tower, out of stock tower, desulfurization take off Nitre tower is general.Analytic Tower is general with regenerator.Conveyer is that active carbon conveying device can be to the effect of conveying active carbon The conveying equipments such as conveyer belt.Conveyer is equipped with gas access, and for the gas circulation in conveyer, this is designed as existing set Meter.Dust pelletizing system can use existing any cleaner.Pressure gauge is used to detect the pressure size of conveyer interior air-flow.
In the present invention, the height of adsorption tower is 5-80m, preferably 8-60m, more preferably 10-40m.
The height of Analytic Tower is 5-80m, preferably 8-60m, more preferably 10-40m.
The outer diameter of first rotary valve is 0.1-5m, preferably 0.2-3m, further preferably 0.3-2m, more preferably 0.4- 1m。
The outer diameter of second rotary valve is 0.1-5m, preferably 0.2-3m, further preferably 0.3-2m, more preferably 0.4- 1m。
The diameter of 6th pipeline (for conveying the pipeline of the second rotary valve material downstream fume gas) is 10-1000mm, preferably For 20-800mm, further preferably 30-500mm, more preferably 50-300mm.
The diameter of third pipeline (for conveying the pipeline of the first rotary valve material upstream flue gas) is 10-1000mm, preferably For 20-800mm, further preferably 30-500mm, more preferably 50-300mm.
In this application, " upstream ", " downstream " are set according to the flow direction of active carbon in adsorption tower." top ", " bottom " is set according to the short transverse of device.
Compared with prior art, the present invention has following advantageous effects:
1, the method for the present invention controls the blower motor frequency for the dust pelletizing system being connected with conveyer or connect conveyer and remove The case where pressure change in gas flow and conveyer in dirt system pipeline, come judge to adsorb column overhead rotary valve or Whether the rotary valve of adsorption tower tower bottom is in normal operating conditions；This method is easy to operate, can effectively judge that rotary valve is No the case where leaking air；
2, it is directed to the case where rotary valve gas leakage, the flue gas that the method for the present invention will leak to conveyer is taken away, guarantees simultaneously The reasonability for extracting air quantity avoids flue gas from entering conveyer condensation post-etching conveyer, and then flue gas is avoided to enter dust pelletizing system, It causes dedusting pipeline and dust pelletizing system to block, decreases the pollution of environment；
3, the method for the present invention is conveyed while the flue gas of conveyer will be leaked to by extracting by foreign gas conveyance conduit Corresponding air quantity is mixed with the flue gas to be leaked, and clog occurs because flue gas condensing condenses to avoid air draft pipeline；
4, the cooling wind of the method for the present invention effective use Analytic Tower cooling section gas vent discharge, it is rationally cold using the part But the residual heat resources of wind, while reducing environmental pollution；
5, present system structure is simple, does not need investment complicated pipe-line equipment and reaction unit, and input cost is low, and Significant effect.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of rotary valve；
Fig. 2 is the structural schematic diagram of active carbon smoke processing system in the prior art；
Fig. 3 is a kind of judgement of absorption column overhead rotary valve gas leakage of the invention and the structural schematic diagram of processing system；
Fig. 4 is the judgement of another absorption column overhead rotary valve gas leakage of the invention and the structural schematic diagram of processing system；
Fig. 5 is a kind of absorption column overhead rotary valve and the judgement of tower bottom rotary valve gas leakage and the knot of processing system of the invention Structure schematic diagram；
Fig. 6 is the judgement and processing system of another absorption column overhead rotary valve and the gas leakage of tower bottom rotary valve of the invention Structural schematic diagram.
Appended drawing reference: 1: adsorption tower；201: the first rotary valves；202: the second rotary valves；301: the first conveyers；302: the Two conveyers；401: the first dust pelletizing systems；402: the second dust pelletizing systems；501: first pressure meter；502: second pressure meter；601: First valve；602: the second valves；7: Analytic Tower；701: cooling section gas vent；801: third valve；802: the four valves； 901: the first thermometers；902: second temperature meter；1001: the one CO (or CO2) detector；1002: the two CO (or CO2) detection Instrument；1101: first flowmeter；1102: second flowmeter；1201: the first online flue gas analyzers；1202: the second online flue gases Analyzer；
L0: former smoke conveying duct；L1: first pipe；L2: the first foreign gas conveyance conduit；L3: second pipe；L4: Third pipeline；L5: blanking pipeline；L6: the four pipeline；L7: the second foreign gas conveyance conduit；L8: the five pipeline；L9: the six Pipeline；L10: feeding pipe.
Specific embodiment
The first embodiment according to the present invention provides a kind of judgement system of rotary valve gas leakage.
A kind of judgement and processing system of rotary valve gas leakage, the system include adsorption tower 1, Analytic Tower 7, the second rotary valve 202, second conveyor 302, the second dust pelletizing system 402, second pressure meter 502, former smoke conveying duct L0, the 6th pipeline L9. Wherein, former smoke conveying duct L0 is connected to the smoke inlet of adsorption tower 1.The active carbon of the connection Analytic Tower 7 of second conveyor 302 The active carbon entrance of outlet and adsorption tower 1.The active carbon inlet of adsorption tower 1 is equipped with the second rotary valve 202.Second dust pelletizing system 402 are connect by the 6th pipeline L9 with second conveyor 302.Second conveyor 302 is equipped with second pressure meter 502.
Preferably, the 6th pipeline L9 is equipped with second flowmeter 1102.
Second of embodiment according to the present invention provides a kind of processing system of rotary valve gas leakage.The system includes upper State system described in the first embodiment, further includes: set between the active carbon entrance and second conveyor 302 of adsorption tower 1 There is feeding pipe L10.Second rotary valve 202 is arranged on feeding pipe L10.From feeding pipe L10 and it is located at the second rotation Both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 of the downstream extraction of valve 202 are passed through after merging to be connected by the 5th pipeline L8 It is connected to former smoke conveying duct L0.
It is preferred that the 4th pipeline L6 is equipped with the second valve 602.
Preferably, the second foreign gas conveyance conduit L7 is equipped with the 4th valve 802.
Preferably, the 5th pipeline L8 is equipped with second detection device.
Preferably, second detection device is second temperature meter 902 or the 2nd CO (or CO2) detector 1002.
Preferably, feeding pipe L10 is equipped with the second online flue gas analyzer 1202.
Preferably, the other end of the second foreign gas conveyance conduit L7 is connected to the cooling section gas vent of Analytic Tower 7 701。
The third embodiment according to the present invention provides a kind of judgement system of rotary valve gas leakage.The system includes the Judgement system described in a kind of embodiment, further includes: the first rotary valve 201, the first conveyer 301, the first dust pelletizing system 401, first pressure meter 501, third pipeline L4.Wherein, the active carbon outlet and parsing of the first conveyer 301 connection adsorption tower 1 The active carbon entrance of tower 7.The active carbon exit of adsorption tower 1 is equipped with the first rotary valve 201.First dust pelletizing system 401 passes through the Three pipeline L4 are connect with the first conveyer 301.First conveyer 301 is equipped with first pressure meter 501.
Preferably, third pipeline L4 is equipped with first flowmeter 1101.
4th kind of embodiment according to the present invention, provides a kind of processing system of rotary valve gas leakage.The system includes upper State second and system described in the third embodiment, further includes: active carbon outlet and the first conveyer of adsorption tower 1 Blanking pipeline L5 is equipped between 301.First rotary valve 201 is arranged on blanking pipeline L5.From blanking pipeline L5 and it is located at the Both the first pipe L1 and the first foreign gas conveyance conduit L2 of the upstream extraction of one rotary valve 201 are passed through after merging by the second pipe Road L3 is connected to former smoke conveying duct L0.
Preferably, first pipe L1 is equipped with the first valve 601.
Preferably, the first foreign gas conveyance conduit L2 is equipped with third valve 801.
Preferably, second pipe L3 is equipped with the first detection device.
It is preferred that the first detection device is the first thermometer 901 or the first CO (or CO2) detector 1001.
Preferably, blanking pipeline L5 is equipped with the first online flue gas analyzer 1201.
Preferably, the other end of the first foreign gas conveyance conduit L2 is connected to the cooling section gas vent of Analytic Tower 7 701。
In the present invention, the height of adsorption tower is 5-80m, preferably 8-60m, more preferably 10-40m.
The height of Analytic Tower is 5-80m, preferably 8-60m, more preferably 10-40m.
The outer diameter of first rotary valve is 0.1-5m, preferably 0.2-3m, further preferably 0.3-2m, more preferably 0.4- 1m。
The outer diameter of second rotary valve is 0.1-5m, preferably 0.2-3m, further preferably 0.3-2m, more preferably 0.4- 1m。
The diameter of 6th pipeline (for conveying the pipeline of the second rotary valve material downstream fume gas) is 10-1000mm, preferably For 20-800mm, further preferably 30-500mm, more preferably 50-300mm.
The diameter of third pipeline (for conveying the pipeline of the first rotary valve material upstream flue gas) is 10-1000mm, preferably For 20-800mm, further preferably 30-500mm, more preferably 50-300mm.
Embodiment 1
A kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower 1 via former smoke conveying duct L0, purifies heel row by the activated carbon adsorption in adsorption tower 1 It puts；The active carbon for having adsorbed pollutant in flue gas enters the first conveyer 301 via the first rotary valve 201 of 1 bottom of adsorption tower, Active carbon is delivered to Analytic Tower 7 and is parsed, regenerates by the first conveyer 301；Active carbon after the parsing of Analytic Tower 7 enters Second conveyor 302, the second rotary valve 202 via 1 top of adsorption tower enter adsorption tower 1；
2) in 202 initial operation stage of the second rotary valve, the second dust pelletizing system 402 being connected with second conveyor 302 is recorded The original frequency F of blower motor2, and record is arranged on second conveyor 302 and is located at the of 202 upstream of the second rotary valve The initial pressure P of two pressure gauges 5022；
3) 202 continuous service of the second rotary valve keeps the value of second pressure meter 502 not become initial pressure P2, observation the The real-time frequency F of the blower motor of two dust pelletizing systems 4022'；If the real-time frequency of the blower motor of the second dust pelletizing system 402 F2' it is equal to original frequency F2, then the second rotary valve 202 is in normal operating condition, continues to observe；If the second dust pelletizing system 402 Blower motor real-time frequency F2' it is not equal to original frequency F2, then determine 202 gas leakage of the second rotary valve.
Embodiment 2
A kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower 1 via former smoke conveying duct L0, purifies heel row by the activated carbon adsorption in adsorption tower 1 It puts；The active carbon for having adsorbed pollutant in flue gas enters the first conveyer 301 via the first rotary valve 201 of 1 bottom of adsorption tower, Active carbon is delivered to Analytic Tower 7 and is parsed, regenerates by the first conveyer 301；Active carbon after the parsing of Analytic Tower 7 enters Second conveyor 302, the second rotary valve 202 via 1 top of adsorption tower enter adsorption tower 1；
2) in 202 initial operation stage of the second rotary valve, record connection second conveyor 302 is defeated with the second dust pelletizing system 402 Send the initial flow Q of the second flowmeter 1102 on pipeline2, and record setting is on second conveyor 302 and positioned at second The initial pressure P of the second pressure meter 502 of 202 upstream of rotary valve2；
3) 202 continuous service of the second rotary valve keeps the value of second pressure meter 502 not become initial pressure P2, observation the The real-time traffic Q of two flowmeters 11022'；If the real-time traffic Q of second flowmeter 11022' it is equal to initial flow Q2, then second Rotary valve 202 is in normal operating condition, continues to observe；If the real-time traffic Q of second flowmeter 11022' not equal to initial Flow Q2, then determine 202 gas leakage of the second rotary valve.
Embodiment 3
A kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower 1 via former smoke conveying duct L0, purifies heel row by the activated carbon adsorption in adsorption tower 1 It puts；The active carbon for having adsorbed pollutant in flue gas enters the first conveyer 301 via the first rotary valve 201 of 1 bottom of adsorption tower, Active carbon is delivered to Analytic Tower 7 and is parsed, regenerates by the first conveyer 301；Active carbon after the parsing of Analytic Tower 7 enters Second conveyor 302, the second rotary valve 202 via 1 top of adsorption tower enter adsorption tower 1；
2) in 202 initial operation stage of the second rotary valve, the second dust pelletizing system 402 being connected with second conveyor 302 is recorded The original frequency F of blower motor2, and record is arranged on second conveyor 302 and is located at the of 202 upstream of the second rotary valve The initial pressure P of two pressure gauges 5022；
3) 202 continuous service of the second rotary valve keeps the frequency of the blower motor of the second dust pelletizing system 402 not become initial Frequency F2, observe the real-time pressure P of second pressure meter 5022'；If the real-time pressure P of second pressure meter 5022' it is equal to initial pressure Power P2, then the second rotary valve 202 is in normal operating condition, continues to observe；If the real-time pressure P of second pressure meter 5022' no Equal to initial pressure P2, then determine 202 gas leakage of the second rotary valve.
Embodiment 4
A kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower 1 via former smoke conveying duct L0, purifies heel row by the activated carbon adsorption in adsorption tower 1 It puts；The active carbon for having adsorbed pollutant in flue gas enters the first conveyer 301 via the first rotary valve 201 of 1 bottom of adsorption tower, Active carbon is delivered to Analytic Tower 7 and is parsed, regenerates by the first conveyer 301；Active carbon after the parsing of Analytic Tower 7 enters Second conveyor 302, the second rotary valve 202 via 1 top of adsorption tower enter adsorption tower 1；
2) in 202 initial operation stage of the second rotary valve, record connection second conveyor 302 is defeated with the second dust pelletizing system 402 Send the initial flow Q of the second flowmeter 1102 on pipeline2, and record setting is on second conveyor 302 and positioned at second The initial pressure P of the second pressure meter 502 of 202 upstream of rotary valve2；
3) 202 continuous service of the second rotary valve keeps the flow of second flowmeter 1102 not become initial flow Q2, observation The real-time pressure P of second pressure meter 5022'；If the real-time pressure P of second pressure meter 5022' it is equal to initial pressure P2, then second Rotary valve 202 is in normal operating condition, continues to observe；If the real-time pressure P of second pressure meter 5022' not equal to initial pressure Power P2, then determine 202 gas leakage of the second rotary valve.
Embodiment 5
Embodiment 1 is repeated, only step 3) are as follows: 202 continuous service of the second rotary valve keeps the value of second pressure meter 502 Initial pressure P is not become2, observe the real-time frequency F of the blower motor of the second dust pelletizing system 4022'；If the second dust pelletizing system The real-time frequency F of 402 blower motor2' value in original frequency F2In the range of the 80-120% of value, then the second rotary valve 202 In normal operating condition, continue to observe；If the real-time frequency F of the blower motor of the second dust pelletizing system 4022' value exceed Original frequency F2The range of the 80-120% of value then determines 202 gas leakage of the second rotary valve.
Embodiment 6
Embodiment 2 is repeated, only step 3) are as follows: 202 continuous service of the second rotary valve keeps the value of second pressure meter 502 Initial pressure P is not become2, observe the real-time traffic Q of second flowmeter 11022'；If the real-time traffic of second flowmeter 1102 Q2' value in initial flow Q2In the range of the 80-120% of value, then the second rotary valve 202 is in normal operating condition, continues to see It surveys；If the real-time traffic Q of second flowmeter 11022' value exceed initial flow Q2The range of the 80-120% of value, then determine Second rotary valve, 202 gas leakage.
Embodiment 7
Embodiment 3 is repeated, only step 3) are as follows: 202 continuous service of the second rotary valve keeps the second dust pelletizing system 402 The frequency of blower motor does not become original frequency F2；If the real-time pressure P of second pressure meter 5022' value in initial pressure P2 In the range of the 80-120% of value, then the second rotary valve 202 is in normal operating condition, continues to observe；If second pressure meter 502 real-time pressure P2' value exceed initial pressure P2The range of the 80-120% of value then determines 202 gas leakage of the second rotary valve.
Embodiment 8
Embodiment 4 is repeated, only step 3) are as follows: 202 continuous service of the second rotary valve keeps the stream of second flowmeter 1102 Amount does not become initial flow Q2, observe the real-time pressure P of second pressure meter 5022'；If the real-time pressure of second pressure meter 502 P2' value in initial pressure P2In the range of the 80-120% of value, then the second rotary valve 202 is in normal operating condition, continues to see It surveys；If the real-time pressure P of second pressure meter 5022' value exceed initial pressure P2The range of the 80-120% of value then determines Two rotary valves, 202 gas leakage.
Embodiment 9
The method of second rotary valve, 202 gas leakage described in a kind of processing method or Processing Example 1 of rotary valve gas leakage, should Method is further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the second valve 602 being arranged on the 4th pipeline L6 is adjusted, so that the blower motor of the second dust pelletizing system 402 Real-time frequency F2' revert to equal to original frequency F2。
Embodiment 10
The method of second rotary valve, 202 gas leakage described in a kind of processing method or Processing Example 2 of rotary valve gas leakage, should Method is further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the second valve 602 being arranged on the 4th pipeline L6 is adjusted, so that the real-time traffic Q of second flowmeter 11022’ It reverts to and is equal to initial flow Q2。
Embodiment 11
A kind of side of second rotary valve, 202 gas leakage described in the processing method or Processing Example 3 or 4 of rotary valve gas leakage Method, this method are further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the second valve 602 being arranged on the 4th pipeline L6 is adjusted, so that the real-time pressure P of second pressure meter 5022’ It reverts to and is equal to initial pressure P2。
Embodiment 12
The method of second rotary valve, 202 gas leakage described in a kind of processing method or Processing Example 5 of rotary valve gas leakage, should Method is further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the second valve (602) being arranged on the 4th pipeline (L6) is adjusted, so that the blower of the second dust pelletizing system (402) The real-time frequency F of motor2' value revert in original frequency F2In the range of the 80-120% of value.
Embodiment 13
The method of second rotary valve, 202 gas leakage described in a kind of processing method or Processing Example 6 of rotary valve gas leakage, should Method is further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the second valve 602 being arranged on the 4th pipeline L6, the real-time traffic Q of second flowmeter (1102) are adjusted2' Value is reverted in initial flow Q2In the range of the 80-120% of value.
Embodiment 14
A kind of side of second rotary valve, 202 gas leakage described in the processing method or Processing Example 7 or 8 of rotary valve gas leakage Method, this method are further comprising the steps of:
4) the 4th pipeline L6 is added between the top of adsorption tower 1 and the second rotary valve 202,202 lower part of the second rotary valve It is defeated that flue gas is delivered to former flue gas after mixing via both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 gas conveyed Send pipeline L0；
5) the real-time pressure that the second valve (602) being arranged on the 4th pipeline (L6) makes second pressure meter (502) is adjusted Power P2' value revert in initial pressure P2In the range of the 80-120% of value.
Embodiment 15
Embodiment 9 is repeated, only this method is further comprising the steps of:
6a) other end of the second foreign gas conveyance conduit L7 is connected with the cooling section gas vent 701 of Analytic Tower 7, adjusts The 4th valve 802 being arranged on the second foreign gas conveyance conduit L7 is saved, so that the flue gas and second of the 4th pipeline L6 conveying The temperature of the mixed mixed gas of both the gas of foreign gas conveyance conduit L7 conveying is higher than the cigarette of the 4th pipeline L6 conveying The acid dew point of gas.
Both flue gas and the second foreign gas conveyance conduit L7 gas conveyed of 4th pipeline L6 conveying passed through after mixing by 5th pipeline L8 is delivered to former smoke conveying duct L0, and the 5th pipeline L8 is equipped with second temperature meter 902；Second temperature meter 902 The temperature of mixed gas in the pipeline of on-line checking corresponding position.
Step 6a) described in adjust the 4th valve 802 that is arranged on the second foreign gas conveyance conduit L7 so that the 4th The temperature of the mixed mixed gas of both the gas that the flue gas and the second foreign gas conveyance conduit L7 of pipeline L6 conveying convey Higher than the 4th pipeline L6 conveying flue gas acid dew point, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline L6 conveying: in the flue gas for measuring the 4th pipeline L6 conveying The concentration of sulfur dioxide isIt is 0.01%, the concentration of sulfur trioxide in the flue gas that the 4th pipeline L6 is conveyed as a result, Are as follows:
In formula (1), k is constant, k 1.5%；
2. calculating the acid dew point of the flue gas of the 4th pipeline L6 conveying: measuring vapor in the flue gas of the 4th pipeline L6 conveying Concentration isIt is 8%, the acid dew point t of the flue gas of the 4th pipeline L6 conveying can be obtained as a result,ld2Are as follows:
In formula (4),For the concentration of vapor in the flue gas of the 4th pipeline L6 conveying, %；For the 4th pipeline L6 The concentration of sulfur trioxide, % in the flue gas of conveying；
The 4th valve 802 on the second foreign gas conveyance conduit L7 is adjusted, so that the second temperature on the 5th pipeline L8 The reading of meter 902 is 115 DEG C.
Embodiment 16
Embodiment 11 is repeated, only this method is further comprising the steps of:
The 4th valve 802 being arranged on the second foreign gas conveyance conduit L7 6b) is adjusted, so that the 4th pipeline L6 is conveyed Flue gas and the acid dew point of the mixed mixed gas of both gas of the second foreign gas conveyance conduit L7 conveying be lower than environment Temperature.
Both flue gas and the second foreign gas conveyance conduit L7 gas conveyed of 4th pipeline L6 conveying passed through after mixing by 5th pipeline L8 is delivered to former smoke conveying duct L0, and the 5th pipeline L8 is equipped with the second carbon monoxide detector 1002；2nd CO detection In 1002 on-line checking corresponding position pipeline of instrument in mixed gas CO concentration.
Step 6b) described in adjust the 4th valve 802 that is arranged on the second foreign gas conveyance conduit L7 so that the 4th The acid of the mixed mixed gas of both the gas that the flue gas and the second foreign gas conveyance conduit L7 of pipeline L6 conveying convey reveals Point is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline L6 conveying: in the flue gas for measuring the 4th pipeline L6 conveying The concentration of sulfur dioxide isIt is 0.005%, the concentration of sulfur trioxide in the flue gas that the 4th pipeline L6 is conveyed as a result, Are as follows:
In formula (1), k is constant, k 1%；
2. both flue gas and the second foreign gas conveyance conduit L7 gas conveyed that calculate the 4th pipeline L6 conveying mix The acid dew point of mixed gas afterwards: measuring the concentration of vapor in the flue gas of the 4th pipeline L6 conveying isIt is 10%, if the The gas of two foreign gas conveyance conduit L7 conveying is n2 to the extension rate of the 4th pipeline L6 flue gas conveyed, is mixed as a result, The acid dew point t of gasld2' are as follows:
In formula (8),For the concentration of vapor in mixed gas, %；For three oxygen in mixed gas Change the concentration of sulphur, %；
3. being t according to environment temperature is measuredEnvironment, the flue gas and the second foreign gas conveyance conduit that are conveyed by the 4th pipeline L6 The acid dew point of the mixed mixed gas of both the gas of L7 conveying is lower than environment temperature, can obtain:
tld2' < tEnvironment；………(9)；
The cigarette that the 4th pipeline L6 is conveyed according to the gas that formula (9) can acquire the second foreign gas conveyance conduit L7 conveying The extension rate n2 of gas is 40；
4. both flue gas and the second foreign gas conveyance conduit L7 gas conveyed that calculate the 4th pipeline L6 conveying mix The concentration of CO in mixed gas afterwards:
The concentration for measuring CO in the flue gas of the 4th pipeline L6 conveying is CCO2It is 0.4%, is mixed in the 5th pipeline L8 as a result, The concentration C of CO in gasCO2' are as follows:
CCO2'=CCO2/ n2=0.1%；………(10)；
The 4th valve 802 on the second foreign gas conveyance conduit L7 is adjusted, so that the 2nd CO on the 5th pipeline L8 is examined The reading for surveying instrument 1002 is 1000ppm.
Embodiment 17
Embodiment 1 is repeated, only this method is further comprising the steps of:
7) in 201 initial operation stage of the first rotary valve, the first dust pelletizing system 401 being connected with the first conveyer 301 is recorded The original frequency F of blower motor1Or the on record the first conveyer 301 of connection and the conveyance conduit of the first dust pelletizing system 402 The initial flow Q of flow meters 11011, and record setting is on the first conveyer 301 and positioned at 201 downstream of the first rotary valve First pressure meter 501 initial pressure P1；
8) 201 continuous service of the first rotary valve keeps the value of first pressure meter 501 not become initial pressure P1, observation the The real-time frequency F of the blower motor of one dust pelletizing system 4011'；If the real-time frequency of the blower motor of the first dust pelletizing system 401 F1' it is equal to original frequency F1, then the first rotary valve 201 is in normal operating condition, continues to observe；If the first dust pelletizing system 401 Blower motor real-time frequency F1' it is not equal to original frequency F1, then determine 201 gas leakage of the first rotary valve.
Embodiment 18
Embodiment 2 is repeated, only this method is further comprising the steps of:
7) in 201 initial operation stage of the first rotary valve, the first dust pelletizing system 401 being connected with the first conveyer 301 is recorded The original frequency F of blower motor1Or the on record the first conveyer 301 of connection and the conveyance conduit of the first dust pelletizing system 402 The initial flow Q of flow meters 11011, and record setting is on the first conveyer 301 and positioned at 201 downstream of the first rotary valve First pressure meter 501 initial pressure P1；
8) 201 continuous service of the first rotary valve keeps the value of first pressure meter 501 not become initial pressure P1, observation the The real-time traffic Q of flow meters 11011'；If the real-time traffic Q of first flowmeter 11011' it is equal to initial flow Q1, then first Rotary valve 201 is in normal operating condition, continues to observe；If the real-time traffic Q of first flowmeter 11011' not equal to initial Flow Q1, then determine 201 gas leakage of the first rotary valve.
Embodiment 19
Embodiment 3 is repeated, only this method is further comprising the steps of:
7) in 201 initial operation stage of the first rotary valve, the first dust pelletizing system 401 being connected with the first conveyer 301 is recorded The original frequency F of blower motor1Or the on record the first conveyer 301 of connection and the conveyance conduit of the first dust pelletizing system 402 The initial flow Q of flow meters 11011, and record setting is on the first conveyer 301 and positioned at 201 downstream of the first rotary valve First pressure meter 501 initial pressure P1；
8) 201 continuous service of the first rotary valve keeps the blower motor frequency of the first dust pelletizing system 401 not become initial frequency Rate F1, observe the real-time pressure P of first pressure meter 5011'；If the real-time pressure P of first pressure meter 5011' it is equal to initial pressure P1, then the first rotary valve 201 is in normal operating condition, continues to observe；If the real-time pressure P of first pressure meter 5011' differ In initial pressure P1, then determine 201 gas leakage of the first rotary valve.
Embodiment 20
Embodiment 4 is repeated, only this method is further comprising the steps of:
7) in 201 initial operation stage of the first rotary valve, the first dust pelletizing system 401 being connected with the first conveyer 301 is recorded The original frequency F of blower motor1Or the on record the first conveyer 301 of connection and the conveyance conduit of the first dust pelletizing system 402 The initial flow Q of flow meters 11011, and record setting is on the first conveyer 301 and positioned at 201 downstream of the first rotary valve First pressure meter 501 initial pressure P1；
8) 201 continuous service of the first rotary valve keeps the flow of first flowmeter 1101 not become initial flow Q1, observation The real-time pressure P of first pressure meter 5011'；If the real-time pressure P of first pressure meter 5011' it is equal to initial pressure P1, then first Rotary valve 201 is in normal operating condition, continues to observe；If the real-time pressure P of first pressure meter 5011' not equal to initial pressure Power P1, then determine 201 gas leakage of the first rotary valve.
Embodiment 21
Embodiment 17 is repeated, only step 8) are as follows: 201 continuous service of the first rotary valve keeps the value of first pressure meter 501 Initial pressure P is not become1, observe the real-time frequency F of the blower motor of the first dust pelletizing system 4011'；If the first dust pelletizing system The real-time frequency F of 401 blower motor1' value in original frequency F1In the range of the 80-120% of value, then the first rotary valve 201 In normal operating condition, continue to observe；If the real-time frequency F of the blower motor of the first dust pelletizing system 4011' value exceed Original frequency F1The range of the 80-120% of value then determines 201 gas leakage of the first rotary valve.
Embodiment 22
Embodiment 18 is repeated, only step 8) are as follows: 201 continuous service of the first rotary valve keeps the value of first pressure meter 501 Initial pressure P is not become1, observe the real-time traffic Q of first flowmeter 11011'；If the real-time traffic of first flowmeter 1101 Q1' value in initial flow Q1In the range of the 80-120% of value, then the first rotary valve 201 is in normal operating condition, continues to see It surveys；If the real-time traffic Q of first flowmeter 11011' value exceed initial flow Q1The range of the 80-120% of value, then determine First rotary valve, 201 gas leakage.
Embodiment 23
Embodiment 19 is repeated, only step 8) are as follows: 201 continuous service of the first rotary valve keeps the first dust pelletizing system 401 Blower motor frequency does not become original frequency F1, observe the real-time pressure P of first pressure meter 5011'；If first pressure meter 501 Real-time pressure P1' value in initial pressure P1In the range of the 80-120% of value, then the first rotary valve 201, which is in, operates normally State continues to observe；If the real-time pressure P of first pressure meter 5011' value exceed initial pressure P1The model of the 80-120% of value It encloses, then determines 201 gas leakage of the first rotary valve.
Embodiment 24
Embodiment 20 is repeated, only step 8) are as follows: 201 continuous service of the first rotary valve keeps first flowmeter 1101 Flow does not become initial flow Q1, observe the real-time pressure P of first pressure meter 5011'；If the real-time pressure of first pressure meter 501 Power P1' value in initial pressure P1In the range of the 80-120% of value, then the first rotary valve 201 is in normal operating condition, continues Observation；If the real-time pressure P of first pressure meter 5011' value exceed initial pressure P1The range of the 80-120% of value, then determine First rotary valve, 201 gas leakage.
Embodiment 25
Embodiment 17 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, so that the blower motor of the first dust pelletizing system 401 Real-time frequency F1' revert to equal to original frequency F,1。
Embodiment 26
Embodiment 18 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, or makes the real-time traffic of first flowmeter 1101 Q1' it is equal to initial flow Q1。
Embodiment 27
Embodiment 19 or 20 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, so that the real-time pressure P of first pressure meter 5011’ It reverts to and is equal to initial pressure P1。
Embodiment 26
Embodiment 21 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, so that the blower motor of the first dust pelletizing system 401 Real-time frequency F1' value restore original frequency F1In the range of the 80-120% of value.
Embodiment 27
Embodiment 22 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, so that the real-time traffic of first flowmeter 1101 Q1' value restore initial flow Q1In the range of the 80-120% of value.
Embodiment 28
Embodiment 23 or 24 is repeated, only this method further include:
9) first pipe L1, the cigarette on 201 top of the first rotary valve are added between 1 bottom of adsorption tower and the first rotary valve 201 Gas is delivered to former flue gas and conveys after mixing via both first pipe L1 and the first foreign gas conveyance conduit L2 gas conveyed Pipeline L0；
10) the first valve 601 being arranged on first pipe L1 is adjusted, so that the real-time pressure P of first pressure meter 5011’ Value restore initial pressure P1In the range of the 80-120% of value.
Embodiment 29
Embodiment 21 is repeated, only this method further include:
11a) other end of the first foreign gas conveyance conduit L2 is connected with the cooling section gas vent 701 of Analytic Tower 7, adjusts The third valve 801 being arranged on the first foreign gas conveyance conduit L2 is saved, so that the flue gas and first of first pipe L1 conveying The temperature of the mixed mixed gas of both the gas of foreign gas conveyance conduit L2 conveying is higher than the cigarette of first pipe L1 conveying The acid dew point of gas.
Both flue gas and the first foreign gas conveyance conduit L2 gas conveyed of first pipe L1 conveying passed through after mixing by Second pipe L3 is delivered to former smoke conveying duct L0, and second pipe L3 is equipped with the first thermometer 901；First thermometer 901 The temperature of mixed gas in the pipeline of on-line checking corresponding position.
Step 11a) described in adjust the third valve 801 that is arranged on the first foreign gas conveyance conduit L2 so that the The temperature of the mixed mixed gas of both the gas that the flue gas and the first foreign gas conveyance conduit L2 of one pipeline L1 conveying convey Degree is higher than the acid dew point of the flue gas of first pipe L1 conveying, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe L1 conveying: in the flue gas for measuring first pipe L1 conveying The concentration of sulfur dioxide isIt is 0.005%, the concentration of sulfur trioxide in the flue gas that first pipe L1 is conveyed as a result, Are as follows:
In formula (1), k is constant, k 1.2%；
2. calculating the acid dew point of the flue gas of first pipe L1 conveying: measuring vapor in the flue gas of first pipe L1 conveying Concentration isIt is 9%, the acid dew point t of the flue gas of first pipe L1 conveying can be obtained as a result,ld1Are as follows:
In formula (2),For the concentration of vapor in the flue gas of first pipe L1 conveying, %；For first pipe L1 The concentration of sulfur trioxide, % in the flue gas of conveying；
The third valve 801 on the first foreign gas conveyance conduit L2 is adjusted, so that the first temperature on second pipe L3 The reading of meter 901 is 105 DEG C.
Embodiment 30
Embodiment 23 is repeated, only this method further include:
The third valve 801 being arranged on the first foreign gas conveyance conduit L2 11b) is adjusted, so that first pipe L1 is defeated The acid dew point of the mixed mixed gas of both the flue gas sent and the gas of the first foreign gas conveyance conduit L2 conveying is lower than ring Border temperature；
Preferably, both the flue gas of first pipe L1 conveying and the gas of the first foreign gas conveyance conduit L2 conveying are mixed Through being delivered to former smoke conveying duct L0 by second pipe L3 after conjunction, second pipe L3 is equipped with the first CO (or CO2) detector 1001；CO in mixed gas in first carbon monoxide detector, 1001 on-line checking corresponding position pipeline (or CO2) concentration.
Step 11b) described in adjust the third valve 801 that is arranged on the first foreign gas conveyance conduit L2 so that the The acid of the mixed mixed gas of both the gas that the flue gas and the first foreign gas conveyance conduit L2 of one pipeline L1 conveying convey Dew point is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe L1 conveying: in the flue gas for measuring first pipe L1 conveying The concentration of sulfur dioxide isIt is 0.005%, the concentration of sulfur trioxide in the flue gas that first pipe L1 is conveyed as a result, Are as follows:
In formula (1), k is constant, k 1%；
2. both flue gas and the first foreign gas conveyance conduit L2 gas conveyed that calculate first pipe L1 conveying mix The acid dew point of mixed gas afterwards: measuring the concentration of vapor in the flue gas of first pipe L1 conveying isIt is 8%, if the The gas of one foreign gas conveyance conduit L2 conveying is n1 to the extension rate of the first pipe L1 flue gas conveyed, is mixed as a result, The acid dew point t of gasld1' are as follows:
In formula (5),For the concentration of vapor in mixed gas, %；For three oxidation in mixed gas The concentration of sulphur, %；
3. being t according to environment temperature is measuredEnvironmentIt is 25 DEG C, it is defeated by the first pipe L1 flue gas conveyed and the first foreign gas The acid dew point of the mixed mixed gas of both the gas for sending pipeline L2 to convey can be obtained lower than environment temperature:
tld1' < tEnvironment；………(6)；
The cigarette that first pipe L1 is conveyed according to the gas that formula (6) can acquire the first foreign gas conveyance conduit L2 conveying The extension rate n1 of gas is 34；
4. both flue gas and the first foreign gas conveyance conduit L2 gas conveyed that calculate first pipe L1 conveying mix The concentration of CO in mixed gas afterwards:
The concentration for measuring CO in the flue gas of first pipe L1 conveying is CCO1It is 0.45%, is mixed in second pipe L3 as a result, The concentration C of CO in gasCO1' are as follows:
CCO1'=CCO1/n1；………(7)；
The third valve 801 on the first foreign gas conveyance conduit L2 is adjusted, so that the first CO on second pipe L3 is examined The reading for surveying instrument 1001 is 1320ppm.
Embodiment 31
A kind of judgement and processing system of rotary valve gas leakage, the system include adsorption tower 1, Analytic Tower 7, the second rotary valve 202, second conveyor 302, the second dust pelletizing system 402, second pressure meter 502, former smoke conveying duct L0, the 6th pipeline L9； Wherein, former smoke conveying duct L0 is connected to the smoke inlet of adsorption tower 1；The active carbon of the connection Analytic Tower 7 of second conveyor 302 The active carbon entrance of outlet and adsorption tower 1；The active carbon inlet of adsorption tower 1 is equipped with the second rotary valve 202；Second dust pelletizing system 402 are connect by the 6th pipeline L9 with second conveyor 302；Second conveyor 302 is equipped with second pressure meter 502.
Embodiment 32
Embodiment 31 is repeated, only the 6th pipeline L9 is equipped with second flowmeter 1102.
Embodiment 33
Embodiment 32 is repeated, feeding pipe is only equipped between the active carbon entrance and second conveyor 302 of adsorption tower 1 L10；Second rotary valve 202 is arranged on feeding pipe L10；Downstream from feeding pipe L10 and positioned at the second rotary valve 202 Both the 4th pipeline L6 and the second foreign gas conveyance conduit L7 of extraction are passed through after merging and are connected to former flue gas by the 5th pipeline L8 Conveyance conduit L0.4th pipeline L6 is equipped with the second valve 602.Second foreign gas conveyance conduit L7 is equipped with the 4th valve 802。
Embodiment 34
Embodiment 33 is repeated, only the 5th pipeline L8 is equipped with second detection device；Second detection device is second temperature Meter 902.
Embodiment 35
Embodiment 33 is repeated, only the 5th pipeline L8 is equipped with second detection device；Second detection device is the 2nd CO inspection Survey instrument 1002.
Embodiment 36
Embodiment 34 is repeated, only feeding pipe L10 is equipped with the second online flue gas analyzer 1202.Second foreign gas The other end of conveyance conduit L7 is connected to the cooling section gas vent 701 of Analytic Tower 7.
Embodiment 37
Embodiment 31 is repeated, only the system further includes the first rotary valve 201, the first conveyer 301, the first dust pelletizing system 401, first pressure meter 501, third pipeline L4；Wherein, the active carbon outlet and parsing of the first conveyer 301 connection adsorption tower 1 The active carbon entrance of tower 7；The active carbon exit of adsorption tower 1 is equipped with the first rotary valve 201；First dust pelletizing system 401 passes through the Three pipeline L4 are connect with the first conveyer 301；First conveyer 301 is equipped with first pressure meter 501.
Embodiment 38
Embodiment 37 is repeated, only third pipeline L4 is equipped with first flowmeter 1101.
Embodiment 39
Embodiment 38 is repeated, is only equipped with blanking pipeline between the active carbon outlet and the first conveyer 301 of adsorption tower 1 L5；First rotary valve 201 is arranged on blanking pipeline L5；Draw from blanking pipeline L5 and positioned at the upstream of the first rotary valve 201 It is defeated that both first pipe L1 out and first foreign gas conveyance conduit L2 are connected to former flue gas by second pipe L3 after merging Send pipeline L0；First pipe L1 is equipped with the first valve 601.
Embodiment 40
Embodiment 39 is repeated, only the first foreign gas conveyance conduit L2 is equipped with third valve 801.On second pipe L3 Equipped with the first detection device；First detection device is the first thermometer 901
Embodiment 41
Embodiment 39 is repeated, only the first foreign gas conveyance conduit L2 is equipped with third valve 801.On second pipe L3 Equipped with the first detection device；First detection device is the first carbon monoxide detector 1001.
Embodiment 42
Embodiment 40 is repeated, only blanking pipeline L5 is equipped with the first online flue gas analyzer 1201.First foreign gas The other end of conveyance conduit L2 is connected to the cooling section gas vent 701 of Analytic Tower 7.

Claims (25)

1. a kind of judgment method of rotary valve gas leakage, method includes the following steps:
1) flue gas enters adsorption tower (1) via former smoke conveying duct (L0), after the activated carbon adsorption purification in adsorption tower (1) Discharge；The active carbon for having adsorbed pollutant in flue gas enters the first conveying via first rotary valve (201) of adsorption tower (1) bottom Active carbon is delivered to Analytic Tower (7) and is parsed, regenerates by machine (301), the first conveyer (301)；It is parsed by Analytic Tower (7) Active carbon afterwards enters second conveyor (302), enters adsorption tower via the second rotary valve (202) at the top of adsorption tower (1) (1)；
2) in the second rotary valve (202) initial operation stage, the second dust pelletizing system (402) being connected with second conveyor (302) is recorded Blower motor original frequency F2Or the conveyance conduit of record connection second conveyor (302) and the second dust pelletizing system (402) On second flowmeter (1102) initial flow Q2, and record setting is on second conveyor (302) and positioned at the second rotation The initial pressure P of the second pressure meter (502) of rotary valve (202) upstream2；
3) the second rotary valve (202) continuous service keeps the value of second pressure meter (502) not become initial pressure P2, observation second The real-time frequency F of the blower motor of dust pelletizing system (402)2' or observation second flowmeter (1102) real-time traffic Q2'；If the The real-time frequency F of the blower motor of two dust pelletizing systems (402)2' it is equal to original frequency F2Or second flowmeter (1102) is real-time Flow Q2' it is equal to initial flow Q2, then the second rotary valve (202) is in normal operating condition, continues to observe；If the second dedusting The real-time frequency F of the blower motor of system (402)2' it is not equal to original frequency F2Or the real-time traffic of second flowmeter (1102) Q2' it is not equal to initial flow Q2, then determine the second rotary valve (202) gas leakage；
Alternatively, keeping the frequency of the blower motor of the second dust pelletizing system (402) does not become original frequency F2Or keep second flowmeter (1102) flow does not become initial flow Q2, observe the real-time pressure P of second pressure meter (502)2'；If second pressure meter (502) real-time pressure P2' it is equal to initial pressure P2, then the second rotary valve (202) is in normal operating condition, continues to observe；Such as The real-time pressure P of fruit second pressure meter (502)2' it is not equal to initial pressure P2, then determine the second rotary valve (202) gas leakage.
2. judgment method according to claim 1, it is characterised in that: step 3) are as follows: the second rotary valve (202) is persistently transported Row keeps the value of second pressure meter (502) not become initial pressure P2, observe the blower motor of the second dust pelletizing system (402) Real-time frequency F2' or observation second flowmeter (1102) real-time traffic Q2'；If the blower motor of the second dust pelletizing system (402) Real-time frequency F2' value in original frequency F2(preferably in original frequency F in the range of the 80-120% of value2The 85- of value In the range of 115%, more preferably in original frequency F2In the range of the 90-110% of value) or second flowmeter (1102) Real-time traffic Q2' value in initial flow Q2(preferably in initial flow Q in the range of the 80-120% of value2The 85-115% of value In the range of, more preferably in initial flow Q2In the range of the 90-110% of value), then the second rotary valve (202) is in normal Operating status continues to observe；If the real-time frequency F of the blower motor of the second dust pelletizing system (402)2' value beyond initial frequency Rate F2The range of the 80-120% of value (preferably exceeds original frequency F2The range of the 85-115% of value, more preferably beyond initial Frequency F2The range of the 90-110% of value) or second flowmeter (1102) real-time traffic Q2' value exceed initial flow Q2Value 80-120% range (preferably exceed initial flow Q2The range of the 85-115% of value more preferably exceeds initial flow Q2 The range of the 90-110% of value), then determine the second rotary valve (202) gas leakage；
Alternatively, keeping the frequency of the blower motor of the second dust pelletizing system (402) does not become original frequency F2Or keep second flowmeter (1102) flow does not become initial flow Q2, observe the real-time pressure P of second pressure meter (502)2'；If second pressure meter (502) real-time pressure P2' value in initial pressure P2(preferably in initial pressure P in the range of the 80-120% of value2Value In the range of 85-115%, more preferably in initial pressure P2In the range of the 90-110% of value), then the second rotary valve (202) In normal operating condition, continue to observe；If the real-time pressure P of second pressure meter (502)2' value exceed initial pressure P2Value 80-120% range (preferably exceed initial pressure P2The range of the 85-115% of value more preferably exceeds initial pressure P2 The range of the 90-110% of value), then determine the second rotary valve (202) gas leakage.
3. the second rotary valve (202) in the processing method or processing 2 judgment method as claimed in claim 1 or 2 of a kind of rotary valve gas leakage The method of gas leakage, this method are further comprising the steps of:
4) the 4th pipeline (L6) is added between the top of adsorption tower (1) and the second rotary valve (202), under the second rotary valve (202) The flue gas in portion is delivered to after mixing via the 4th pipeline (L6) with both the gas that the second foreign gas conveyance conduit (L7) conveys Former smoke conveying duct (L0)；
5) blower motor that the second valve (602) being arranged on the 4th pipeline (L6) makes the second dust pelletizing system (402) is adjusted Real-time frequency F2' revert to equal to original frequency F2Or make the real-time traffic Q of second flowmeter (1102)2' revert to and be equal to Initial flow Q2It (either, adjusts the second valve (602) being arranged on the 4th pipeline (L6) and makes the second dust pelletizing system (402) the real-time frequency F of blower motor2' value revert in original frequency F2In the range of the 80-120 of value or make second The real-time traffic Q of flowmeter (1102)2' value revert in initial flow Q2In the range of the 80-120 of value)；It is set alternatively, adjusting The second valve (602) on the 4th pipeline (L6) is set, so that the real-time pressure P of second pressure meter (502)2' revert to and be equal to Initial pressure P2It (either, adjusts the second valve (602) being arranged on the 4th pipeline (L6) and makes second pressure meter (502) Real-time pressure P2' value revert in initial pressure P2In the range of the 80-120 of value).
4. according to the method described in claim 3, it is characterized by: this method is further comprising the steps of:
6a) other end of the second foreign gas conveyance conduit (L7) is connected with the cooling section gas vent (701) of Analytic Tower (7), The 4th valve (802) being arranged on the second foreign gas conveyance conduit (L7) is adjusted, so that the cigarette of the 4th pipeline (L6) conveying The temperature of the mixed mixed gas of both gas and the gas of the second foreign gas conveyance conduit (L7) conveying is higher than the 4th pipeline (L6) acid dew point of the flue gas conveyed；
Preferably, both the flue gas of the 4th pipeline (L6) conveying and the gas of the second foreign gas conveyance conduit (L7) conveying are mixed It is delivered to former smoke conveying duct (L0) after conjunction by the 5th pipeline (L8), the 5th pipeline (L8) is equipped with second temperature meter (902)；The temperature of mixed gas in the pipeline of second temperature meter (902) on-line checking corresponding position.
5. according to the method described in claim 4, it is characterized by: step 6a) described in adjust and be arranged in the second foreign gas The 4th valve (802) on conveyance conduit (L7), so that the flue gas and the second foreign gas delivery pipe of the conveying of the 4th pipeline (L6) The temperature of the mixed mixed gas of both the gas of road (L7) conveying is higher than the acid dew point of the flue gas of the 4th pipeline (L6) conveying, Specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline (L6) conveying: in the flue gas for measuring the conveying of the 4th pipeline (L6) The concentration of sulfur dioxide isThe concentration of sulfur trioxide in the flue gas that the 4th pipeline (L6) conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. calculating the acid dew point of the flue gas of the 4th pipeline (L6) conveying: measuring vapor in the flue gas of the 4th pipeline (L6) conveying Concentration isThe acid dew point t of the flue gas of the 4th pipeline (L6) conveying can be obtained as a result,ld2Are as follows:
In formula (4),For the concentration of vapor in the flue gas of the 4th pipeline (L6) conveying, %；For the 4th pipeline (L6) The concentration of sulfur trioxide, % in the flue gas of conveying；
The 4th valve (802) on the second foreign gas conveyance conduit (L7) is adjusted, so that the second temperature on the 5th pipeline (L8) The reading t of degree meter (902)2> tld2。
6. according to the method described in claim 3, it is characterized by: this method is further comprising the steps of:
The 4th valve (802) being arranged on the second foreign gas conveyance conduit (L7) 6b) is adjusted, so that the 4th pipeline (L6) is defeated The acid dew point of the mixed mixed gas of both the gas that the flue gas sent is conveyed with the second foreign gas conveyance conduit (L7) is lower than Environment temperature；
Preferably, both the flue gas of the 4th pipeline (L6) conveying and the gas of the second foreign gas conveyance conduit (L7) conveying are mixed Through being delivered to former smoke conveying duct (L0) by the 5th pipeline (L8) after conjunction, the 5th pipeline (L8) is equipped with the 2nd CO (or CO2) Detector (1002)；In the pipeline of second carbon monoxide detector (1002) on-line checking corresponding position in mixed gas CO concentration.
7. according to the method described in claim 6, it is characterized by: step 6b) described in adjust and be arranged in the second foreign gas The 4th valve (802) on conveyance conduit (L7), so that the flue gas and the second foreign gas delivery pipe of the conveying of the 4th pipeline (L6) The acid dew point of the mixed mixed gas of both the gas of road (L7) conveying is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of the 4th pipeline (L6) conveying: in the flue gas for measuring the conveying of the 4th pipeline (L6) The concentration of sulfur dioxide isThe concentration of sulfur trioxide in the flue gas that the 4th pipeline (L6) conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. the flue gas for calculating the conveying of the 4th pipeline (L6) is mixed with both the gas that the second foreign gas conveyance conduit (L7) conveys The acid dew point of mixed gas afterwards: measuring the concentration of vapor in the flue gas of the 4th pipeline (L6) conveying isIf outside second The extension rate for carrying out the flue gas that the gas of gas transmission pipeline (L7) conveying convey the 4th pipeline (L6) is n2, is mixed as a result, The acid dew point t of gasld2' are as follows:
In formula (8),For the concentration of vapor in mixed gas, %；For sulfur trioxide in mixed gas Concentration, %；
3. being t according to environment temperature is measuredEnvironment, the flue gas and the second foreign gas conveyance conduit that are conveyed by the 4th pipeline (L6) (L7) acid dew point of the mixed mixed gas of both gas conveyed is lower than environment temperature, can obtain:
tld2' < tEnvironment；………(9)；
The cigarette that the 4th pipeline (L6) is conveyed according to the gas that formula (9) can acquire the conveying of the second foreign gas conveyance conduit (L7) The extension rate n2 of gas；
4. the flue gas for calculating the conveying of the 4th pipeline (L6) is mixed with both the gas that the second foreign gas conveyance conduit (L7) conveys The concentration of CO in mixed gas afterwards:
The concentration for measuring CO in the flue gas of the 4th pipeline (L6) conveying is CCO2, CO in mixed gas in the 5th pipeline (L8) as a result, Concentration CCO2' are as follows:
CCO2'=CCO2/n2；………(10)；
The 4th valve (802) on the second foreign gas conveyance conduit (L7) is adjusted, so that the 2nd CO on the 5th pipeline (L8) The reading of detector (1002) is CCO2’。
8. method according to any one of claims 1-7, it is characterised in that: this method is further comprising the steps of:
7) in the first rotary valve (201) initial operation stage, the first dust pelletizing system (401) being connected with the first conveyer (301) is recorded Blower motor original frequency F1Or the conveyance conduit of record connection the first conveyer (301) and the first dust pelletizing system (402) On first flowmeter (1101) initial flow Q1, and record setting is on the first conveyer (301) and positioned at the first rotation The initial pressure P of the first pressure meter (501) in rotary valve (201) downstream1；
8) the first rotary valve (201) continuous service keeps the value of first pressure meter (501) not become initial pressure P1, observation first The real-time frequency F of the blower motor of dust pelletizing system (401)1' or observation first flowmeter (1101) real-time traffic Q1'；If the The real-time frequency F of the blower motor of one dust pelletizing system (401)1' it is equal to original frequency F1Or first flowmeter (1101) is real-time Flow Q1' it is equal to initial flow Q1, then the first rotary valve (201) is in normal operating condition, continues to observe；If the first dedusting The real-time frequency F of the blower motor of system (401)1' it is not equal to original frequency F1Or the real-time traffic of first flowmeter (1101) Q1' it is not equal to initial flow Q1, then determine the first rotary valve (201) gas leakage；
Alternatively, keeping the blower motor frequency of the first dust pelletizing system (401) does not become original frequency F1Or keep first flowmeter (1101) flow does not become initial flow Q1, observe the real-time pressure P of first pressure meter (501)1'；If first pressure meter (501) real-time pressure P1' it is equal to initial pressure P1, then the first rotary valve (201) is in normal operating condition, continues to observe；Such as The real-time pressure P of fruit first pressure meter (501)1' it is not equal to initial pressure P1, then determine the first rotary valve (201) gas leakage.
9. judgment method according to claim 8, it is characterised in that: step 8) are as follows: the first rotary valve (201) is persistently transported Row keeps the value of first pressure meter (501) not become initial pressure P1, observe the blower motor of the first dust pelletizing system (401) Real-time frequency F1' or observation first flowmeter (1101) real-time traffic Q1'；If the blower motor of the first dust pelletizing system (401) Real-time frequency F1' value in original frequency F1(preferably in original frequency F in the range of the 80-120% of value1The 85- of value In the range of 115%, more preferably in original frequency F1In the range of the 90-110% of value) or first flowmeter (1101) Real-time traffic Q1' value in initial flow Q1(preferably value is in initial flow Q in the range of the 80-120% of value1The 85- of value In the range of 115%, more preferably value is in initial flow Q1In the range of the 90-110% of value), then at the first rotary valve (201) In normal operating condition, continue to observe；If the real-time frequency F of the blower motor of the first dust pelletizing system (401)1' value exceed Original frequency F1The range of the 80-120% of value (preferably exceeds original frequency F1The range of the 85-115% of value is more preferably super Original frequency F out1The range of the 90-110% of value) or first flowmeter (1101) real-time traffic Q1' value exceed initial flow Measure Q1The range of the 80-120% of value (preferably exceeds initial flow Q1The range of the 85-115% of value, more preferably beyond initial Flow Q1The range of the 90-110% of value), then determine the first rotary valve (201) gas leakage；
Alternatively, keeping the blower motor frequency of the first dust pelletizing system (401) does not become original frequency F1Or keep first flowmeter (1101) flow does not become initial flow Q1, observe the real-time pressure P of first pressure meter (501)1'；If first pressure meter (501) real-time pressure P1' value in initial pressure P1(preferably in initial pressure P in the range of the 80-120% of value1Value In the range of 85-115%, more preferably in initial pressure P1In the range of the 90-110% of value), then the first rotary valve (201) In normal operating condition, continue to observe；If the real-time pressure P of first pressure meter (501)1' value exceed initial pressure P1Value 80-120% range (preferably exceed initial pressure P1The range of the 85-115% of value more preferably exceeds initial pressure P1 The range of the 90-110% of value), then determine the first rotary valve (201) gas leakage.
10. method according to claim 8 or claim 9, it is characterised in that: this method is further comprising the steps of:
9) it is added between adsorption tower (1) bottom and the first rotary valve (201) first pipe (L1), the first rotary valve (201) top Flue gas mixed via first pipe (L1) with both the gas that the first foreign gas conveyance conduit (L2) conveys after be delivered to original Smoke conveying duct (L0)；
10) the first valve (601) being arranged on first pipe (L1) is adjusted, so that the blower electricity of the first dust pelletizing system (401) The real-time frequency F of machine1' revert to equal to original frequency F1Or make the real-time traffic Q of first flowmeter (1101)1' revert to In initial flow Q1(the first valve (601) being arranged on first pipe (L1) either, is adjusted, so that the first dust pelletizing system (401) the real-time frequency F of blower motor1' value restore original frequency F1In the range of the 80-120% of value or make first-class The real-time traffic Q of meter (1101)1' value restore initial flow Q1In the range of the 80-120% of value)；Exist alternatively, adjusting setting The first valve (601) in first pipe (L1), so that the real-time pressure P of first pressure meter (501)1' revert to equal to initial Pressure P1(the first valve (601) being arranged on first pipe (L1) either, is adjusted, so that the reality of first pressure meter (501) When pressure P1' value restore initial pressure P1In the range of the 80-120% of value).
11. according to the method described in claim 10, it is characterized by: this method is further comprising the steps of:
11a) other end of the first foreign gas conveyance conduit (L2) is connected with the cooling section gas vent (701) of Analytic Tower (7), The third valve (801) being arranged on the first foreign gas conveyance conduit (L2) is adjusted, so that the cigarette of first pipe (L1) conveying The temperature of the mixed mixed gas of both gas and the gas of the first foreign gas conveyance conduit (L2) conveying is higher than first pipe (L1) acid dew point of the flue gas conveyed；
Preferably, both the flue gas of first pipe (L1) conveying and the gas of the first foreign gas conveyance conduit (L2) conveying are mixed It is delivered to former smoke conveying duct (L0) after conjunction by second pipe (L3), second pipe (L3) is equipped with the first thermometer (901)；The temperature of mixed gas in the pipeline of first thermometer (901) on-line checking corresponding position.
12. according to the method for claim 11, it is characterised in that: step 11a) described in adjust be arranged in the first extraneous gas Third valve (801) on body conveyance conduit (L2), so that the flue gas and the first foreign gas of first pipe (L1) conveying convey The temperature of the mixed mixed gas of both the gas of pipeline (L2) conveying is higher than the acid dew of the flue gas of first pipe (L1) conveying Point, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe (L1) conveying: in the flue gas for measuring first pipe (L1) conveying The concentration of sulfur dioxide isThe concentration of sulfur trioxide in the flue gas that first pipe (L1) conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. calculating the acid dew point of the flue gas of first pipe (L1) conveying: measuring vapor in the flue gas of first pipe (L1) conveying Concentration isThe acid dew point t of the flue gas of first pipe (L1) conveying can be obtained as a result,ld1Are as follows:
In formula (2),For the concentration of vapor in the flue gas of first pipe (L1) conveying, %；For first pipe (L1) The concentration of sulfur trioxide, % in the flue gas of conveying；
The third valve (801) on the first foreign gas conveyance conduit (L2) is adjusted, so that the first temperature on second pipe (L3) The reading t of degree meter (901)1> tld1。
13. according to the method described in claim 10, it is characterized by: this method is further comprising the steps of:
The third valve (801) being arranged on the first foreign gas conveyance conduit (L2) 11b) is adjusted, so that first pipe (L1) Both the flue gas of conveying and the gas that the first foreign gas conveyance conduit (L2) the conveys acid dew point of mixed mixed gas is low In environment temperature；
Preferably, both the flue gas of first pipe (L1) conveying and the gas of the first foreign gas conveyance conduit (L2) conveying are mixed Through being delivered to former smoke conveying duct (L0) by second pipe (L3) after conjunction, second pipe (L3) is equipped with the first CO (or CO2) Detector (1001)；CO in mixed gas in the pipeline of first carbon monoxide detector (1001) on-line checking corresponding position (or CO2) Concentration.
14. according to the method for claim 13, it is characterised in that: step 11b) described in adjust be arranged in the first extraneous gas Third valve (801) on body conveyance conduit (L2), so that the flue gas and the first foreign gas of first pipe (L1) conveying convey The acid dew point of the mixed mixed gas of both the gas of pipeline (L2) conveying is lower than environment temperature, specifically:
1. calculating the concentration of sulfur trioxide in the flue gas of first pipe (L1) conveying: in the flue gas for measuring first pipe (L1) conveying The concentration of sulfur dioxide isThe concentration of sulfur trioxide in the flue gas that first pipe (L1) conveys as a result,Are as follows:
In formula (1), k is constant, k 0.1-5%, preferably 0.3-4%, more preferably 0.5-3%；
2. the flue gas for calculating first pipe (L1) conveying is mixed with both the gas that the first foreign gas conveyance conduit (L2) conveys The acid dew point of mixed gas afterwards: measuring the concentration of vapor in the flue gas of first pipe (L1) conveying isIf outside first The extension rate for carrying out the flue gas that the gas of gas transmission pipeline (L2) conveying convey first pipe (L1) is n1, is mixed as a result, The acid dew point t of gasld1' are as follows:
In formula (5),For the concentration of vapor in mixed gas, %；For sulfur trioxide in mixed gas Concentration, %；
3. being t according to environment temperature is measuredEnvironment, the flue gas and the first foreign gas conveyance conduit that are conveyed by first pipe (L1) (L2) acid dew point of the mixed mixed gas of both gas conveyed is lower than environment temperature, can obtain:
tld1' < tEnvironment；………(6)；
The cigarette that first pipe (L1) is conveyed according to the gas that formula (6) can acquire the conveying of the first foreign gas conveyance conduit (L2) The extension rate n1 of gas；
4. the flue gas for calculating first pipe (L1) conveying is mixed with both the gas that the first foreign gas conveyance conduit (L2) conveys The concentration of CO in mixed gas afterwards:
The concentration for measuring CO in the flue gas of first pipe (L1) conveying is CCO1, CO in mixed gas in second pipe (L3) as a result, Concentration CCO1' are as follows:
CCO1'=CCO1/n1；………(7)；
The third valve (801) on the first foreign gas conveyance conduit (L2) is adjusted, so that the first CO on second pipe (L3) The reading of detector (1001) is CCO1’。
15. method described in any one of -14 according to claim 1, it is characterised in that: the first dust pelletizing system (401) passes through the Three pipelines (L4) are connected with the first conveyer (301)；It is preferred that third pipeline (L4) is equipped with first flowmeter (1101)；Absorption The active carbon of tower (1) is exported is equipped with blanking pipeline (L5), first pipe (L1) or blanking pipeline between the first conveyer (301) (L5) it is equipped with the first online flue gas analyzer (1201), the first online flue gas analyzer (1201) tests and analyzes present position pipe The concentration of sulfur dioxide in road or pipeline in flue gasWith the concentration of vaporAnd/or
Second dust pelletizing system (402) is connected by the 6th pipeline (L9) with second conveyor (302)；It is preferred that the 6th pipeline (L9) It is equipped with second flowmeter (1102)；Feeding pipe is equipped between the active carbon entrance and second conveyor (302) of adsorption tower (1) (L10), the 6th pipeline (L9) or feeding pipe (L10) are equipped with the second online flue gas analyzer (1202), the second online flue gas Analyzer (1202) tests and analyzes the concentration of the sulfur dioxide in present position pipeline or pipeline in flue gasWith vapor Concentration
16. a kind of judgement of rotary valve gas leakage and processing system or the rotation for method described in any one of claim 1-15 The judgement and processing system of rotary valve gas leakage, which includes adsorption tower (1), Analytic Tower (7), the second rotary valve (202), second defeated Send machine (302), the second dust pelletizing system (402), second pressure meter (502), former smoke conveying duct (L0), the 6th pipeline (L9)； Wherein, former smoke conveying duct (L0) is connected to the smoke inlet of adsorption tower (1)；Second conveyor (302) connects Analytic Tower (7) Active carbon outlet and adsorption tower (1) active carbon entrance；The active carbon inlet of adsorption tower (1) is equipped with the second rotary valve (202)；Second dust pelletizing system (402) is connect by the 6th pipeline (L9) with second conveyor (302)；Second conveyor (302) It is equipped with second pressure meter (502).
17. system according to claim 16, it is characterised in that: the 6th pipeline (L9) is equipped with second flowmeter (1102)。
18. system according to claim 16 or 17, it is characterised in that: the active carbon entrance of adsorption tower (1) and second defeated It send and is equipped with feeding pipe (L10) between machine (302)；Second rotary valve (202) is arranged on feeding pipe (L10)；From feed pipe On road (L10) and it is located at the 4th pipeline (L6) and the second foreign gas conveyance conduit that the downstream of the second rotary valve (202) is drawn (L7) through being connected to former smoke conveying duct (L0) by the 5th pipeline (L8) after the two merges；
It is preferred that the 4th pipeline (L6) is equipped with the second valve (602).
19. system according to claim 18, it is characterised in that: the second foreign gas conveyance conduit (L7) is equipped with the 4th Valve (802)；And/or
5th pipeline (L8) is equipped with second detection device；Preferably, second detection device is second temperature meter (902) or the Two CO (or CO2) detector (1002).
20. system described in 8 or 19 according to claim 1, it is characterised in that: feeding pipe (L10) is equipped with the second online cigarette Gas analyzer (1202)；And/or
The other end of second foreign gas conveyance conduit (L7) is connected to the cooling section gas vent (701) of Analytic Tower (7).
21. system described in any one of 6-20 according to claim 1, it is characterised in that: the system further includes the first rotary valve (201), the first conveyer (301), the first dust pelletizing system (401), first pressure meter (501), third pipeline (L4)；Wherein, One conveyer (301) connects the active carbon entrance of the active carbon outlet and Analytic Tower (7) of adsorption tower (1)；The activity of adsorption tower (1) Charcoal exit is equipped with the first rotary valve (201)；First dust pelletizing system (401) passes through third pipeline (L4) and the first conveyer (301) it connects；First conveyer (301) is equipped with first pressure meter (501).
22. system according to claim 21, it is characterised in that: third pipeline (L4) is equipped with first flowmeter (1101)。
23. the system according to claim 21 or 22, it is characterised in that: the active carbon of adsorption tower (1) exports and first is defeated It send and is equipped with blanking pipeline (L5) between machine (301)；First rotary valve (201) is arranged on blanking pipeline (L5)；From blanking pipeline (L5) on and it is located at first pipe (L1) and the first foreign gas conveyance conduit (L2) that the upstream of the first rotary valve (201) is drawn The two passes through after merging and is connected to former smoke conveying duct (L0) by second pipe (L3)；
Preferably, first pipe (L1) is equipped with the first valve (601).
24. system according to claim 23, it is characterised in that: the first foreign gas conveyance conduit (L2) is equipped with third Valve (801)；And/or
Second pipe (L3) is equipped with the first detection device；It is preferred that the first detection device is the first thermometer (901) or the first CO (or CO2) detector (1001).
25. the system according to claim 23 or 24, it is characterised in that: blanking pipeline (L5) is equipped with the first online flue gas Analyzer (1201)；And/or
The other end of first foreign gas conveyance conduit (L2) is connected to the cooling section gas vent (701) of Analytic Tower (7).
CN201910417963.4A 2019-05-20 2019-05-20 Method and system for treating air leakage of rotary valve Active CN110124441B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112403183A (en) * 2020-01-07 2021-02-26 中冶长天国际工程有限责任公司 Method and system for detecting production safety of analytical tower

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070295204A1 (en) * 2006-03-31 2007-12-27 Perry Equipment Corporation Systems and methods for flow-through treatment of contaminated fluids
CN102772981A (en) * 2012-03-12 2012-11-14 甘肃银光聚银化工有限公司 Device for continuously adsorbing and desorbing organic waste gas by using active carbon
CN202860364U (en) * 2012-10-20 2013-04-10 福建鑫泽环保设备工程有限公司 Active coke flue gas desulfurization device
CN205308105U (en) * 2015-12-07 2016-06-15 兴边富民（北京）清洁能源技术有限公司 Colliery ventilation air methane and take out mixing processing system of putting gas
US9408938B1 (en) * 2016-02-05 2016-08-09 Energy Engineering Systems, LLC Aspirating photochemical odor control system for wastewater lift station and force main odors
WO2018002159A2 (en) * 2016-06-29 2018-01-04 Koninklijke Philips N.V. Rotary valve assembly for sieve beds for pressure swing adsorption control
CN108362451A (en) * 2018-02-25 2018-08-03 程冬青 A kind of multiple-way valve gas leakage test method
CN108443713A (en) * 2018-04-04 2018-08-24 江苏苏亚迪炭材有限公司 Pot type burner gas bypass valve device for preventing leakage
CN108525473A (en) * 2018-06-14 2018-09-14 河南理工大学 Phase transformation ionic liquid hydration method trapping separation CO2/CH4/N2System and device
CN108873796A (en) * 2017-05-11 2018-11-23 上海苏靖建筑工程有限公司 A kind of dew-point temperature monitoring system and its application method
CN208239396U (en) * 2018-05-14 2018-12-14 中国地质科学院郑州矿产综合利用研究所 Pressure swing adsorption separation CH4/N2Performance evaluation device for adsorbent for mixed gas
CN109432980A (en) * 2018-11-26 2019-03-08 中冶焦耐(大连)工程技术有限公司 The denitration of coke oven flue gas activated carbon desulfurization and byproduct comprehensive utilization technique and system
CN208626952U (en) * 2018-04-08 2019-03-22 中冶长天国际工程有限责任公司 The desulfuring and denitrifying apparatus of NO_x Reduction by Effective

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070295204A1 (en) * 2006-03-31 2007-12-27 Perry Equipment Corporation Systems and methods for flow-through treatment of contaminated fluids
CN102772981A (en) * 2012-03-12 2012-11-14 甘肃银光聚银化工有限公司 Device for continuously adsorbing and desorbing organic waste gas by using active carbon
CN202860364U (en) * 2012-10-20 2013-04-10 福建鑫泽环保设备工程有限公司 Active coke flue gas desulfurization device
CN205308105U (en) * 2015-12-07 2016-06-15 兴边富民（北京）清洁能源技术有限公司 Colliery ventilation air methane and take out mixing processing system of putting gas
US9408938B1 (en) * 2016-02-05 2016-08-09 Energy Engineering Systems, LLC Aspirating photochemical odor control system for wastewater lift station and force main odors
WO2018002159A2 (en) * 2016-06-29 2018-01-04 Koninklijke Philips N.V. Rotary valve assembly for sieve beds for pressure swing adsorption control
CN108873796A (en) * 2017-05-11 2018-11-23 上海苏靖建筑工程有限公司 A kind of dew-point temperature monitoring system and its application method
CN108362451A (en) * 2018-02-25 2018-08-03 程冬青 A kind of multiple-way valve gas leakage test method
CN108443713A (en) * 2018-04-04 2018-08-24 江苏苏亚迪炭材有限公司 Pot type burner gas bypass valve device for preventing leakage
CN208626952U (en) * 2018-04-08 2019-03-22 中冶长天国际工程有限责任公司 The desulfuring and denitrifying apparatus of NO_x Reduction by Effective
CN208239396U (en) * 2018-05-14 2018-12-14 中国地质科学院郑州矿产综合利用研究所 Pressure swing adsorption separation CH4/N2Performance evaluation device for adsorbent for mixed gas
CN108525473A (en) * 2018-06-14 2018-09-14 河南理工大学 Phase transformation ionic liquid hydration method trapping separation CO2/CH4/N2System and device
CN109432980A (en) * 2018-11-26 2019-03-08 中冶焦耐(大连)工程技术有限公司 The denitration of coke oven flue gas activated carbon desulfurization and byproduct comprehensive utilization technique and system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112403183A (en) * 2020-01-07 2021-02-26 中冶长天国际工程有限责任公司 Method and system for detecting production safety of analytical tower
CN112403183B (en) * 2020-01-07 2022-05-03 中冶长天国际工程有限责任公司 Method and system for detecting production safety of analytical tower

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