CN203862137U - Reducing agent measuring and control system for cement clinker production line SNCR flue gas denitration - Google Patents
Reducing agent measuring and control system for cement clinker production line SNCR flue gas denitration Download PDFInfo
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- CN203862137U CN203862137U CN201420199444.8U CN201420199444U CN203862137U CN 203862137 U CN203862137 U CN 203862137U CN 201420199444 U CN201420199444 U CN 201420199444U CN 203862137 U CN203862137 U CN 203862137U
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Abstract
The utility model discloses a reducing agent measuring and control system for cement clinker production line SNCR flue gas denitration. The system comprises a reducing agent measuring and control system, and a decomposing furnace, a level-V preheater, a humidifying tower, a raw mill, an electric suction cleaner and a kiln tail chimney connected in sequence, a reducing agent allocation cabinet connected with the decomposing furnace, a secondary CEMS analyser and a secondary ammonia escape analyser arranged at the kiln tail chimney, a temperature probe arranged at the outlet of the decomposing furnace, a first CEMS sampling probe and a first ammonia escape probe arranged at the outlet of a C1 level preheater as well as a corresponding first CEMS analyser and a corresponding first ammonia escape analyser, and a second CEMS sampling probe and a second ammonia escape probe arranged in the kiln tail chimney, wherein all the CEMS analysers and ammonia escape analysers are connected with the reducing agent measuring and control system. The system solves the problem that the manner that the kiln tail chimney CEMS data used as ammonia water demanded quantity calculation reference is hysteretic in nature.
Description
Technical field
The utility model relates to environmental protection and wants technical field of automatic control, is specifically related to a kind of reductant metering and control system of cement clinker production line SNCR denitrating flue gas.
Background technology
SNCR (SNCR) denitration technology refers under the effect of catalyst-free, in suitable temperature window, spray into reducing agent, by the reduction of nitrogen oxide in flue gas, being water and the nitrogen being safe from harm, is utilization in domestic and international cement industry furnace flue gas denitration engineering technology the most widely.
For example, publication number is control method and the device that the Chinese invention patent application document of CN102921284A discloses NOx concentration in a kind of cement furnace flue gas, device comprises decomposition kiln, preheater and reducer feeding device, described decomposition kiln bottom is communicated with the kiln tail chimney of described cement furnace by inlet flue duct, the top of described decomposition kiln is communicated with described preheater by exhaust pass, the middle and upper part of described decomposition kiln or/and in described exhaust pass layering be provided with the spray guns that some handles is connected with described reducer feeding device; Also comprise and be connected in the central controller of described reducer feeding device and the described kiln tail chimney of monitoring NOx concentration and flue gas flow information and be transferred to the flue gas automatic monitored control system of described central controller.
Publication number is that the Chinese invention patent application document of CN103691290A discloses the cement furnace SNCR flue gas denitrification system of planting raising denitration security, comprises dore furnace, reducing agent distribution module, denitration control module, soft water conveyor module, ammoniacal liquor supplying module; The first spray equipment of ammoniacal liquor Unload module, the temperature sensor at tank used for storing ammonia top, pressure sensor and the unrestrained valve of safety, the second spray equipment of tank used for storing ammonia top, the first ammonia leakage detector and the first sound light crossing-signal of ammoniacal liquor conveyor module; The second ammonia leakage detector, rising tone light crossing-signal and the exhaust fan of reducing agent distribution module; Temperature sensor, pressure sensor, the first ammonia leakage detector and the second ammonia leakage detector are all connected denitration control module; The unrestrained valve of safety, the second spray equipment, first sound light crossing-signal, rising tone light crossing-signal are all connected denitration control module with exhaust fan.
At present, most of cement furnace SNCR denitrating system adopts the Gas Parameters of kiln tail chimney as payment foundation, but, ubiquity system hardware configuration is simple, control mode is extensive, system with load fluctuation response not in time, majority do not include the escaping of ammonia index in calculating, cause excess ammonia to exceed effluent standard requirement, discontented toe ring is protected supervision requirement, has also caused the waste of reducing agent.
The calculating of cement clinker production line SNCR gas denitrifying technology reducing agent demand, generally continuous on line monitor (the Continous Emission Monitor System that introduces kiln tail chimney, CEMS data), mainly comprise flue gas flow rate (or flow), NOx concentration, O
2, the parameter such as humidity, calculate ammoniacal liquor demand.The problem existing is: kiln tail chimney has the hysteresis of long period apart from injection of reducing agent exit point position, regulate insensitive, emission intensity particularly, after waste heat boiler, deduster significantly by adsorbing powder dust, excessive reducing agent can not be characterized in time, and reducing agent accounts for the more than 95% of clinker SNCR denitrating flue gas operating cost, economical and practical not in operation.
Utility model content
The utility model provides a kind of reductant metering and control system of cement clinker production line SNCR denitrating flue gas, solves and quotes the hysteresis quality that kiln tail chimney CEMS data exist as ammoniacal liquor demand basis.
Reductant metering and the control system of cement clinker production line SNCR denitrating flue gas, comprising:
Reductant metering control system;
The dore furnace, Pyatyi preheater, conditioning Tower, raw mill, electric vacuum cleaner and the kiln tail chimney that connect successively;
The reducing agent that connects described dore furnace and be controlled by reductant metering control system distributes cabinet;
Be arranged on kiln tail chimney place and be controlled by the 2nd CEMS analyzer and the second the escaping of ammonia analyzer of reductant metering control system;
Also comprise:
Temp probe, is arranged on decomposition furnace outlet place, gathers decomposition furnace outlet temperature and is transferred to reductant metering control system;
The one CEMS sampling probe, is arranged on the C1 level preheater exit of described Pyatyi preheater, gathers the flue gas information at this place;
The one CEMS analyzer, receives the flue gas information from a CEMS sampling probe, and is transferred to reductant metering control system;
The first the escaping of ammonia is popped one's head in, and is arranged on the C1 level preheater exit of described Pyatyi preheater, gathers the escaping of ammonia information at this place;
The first the escaping of ammonia analyzer, receives the escaping of ammonia information from the first the escaping of ammonia probe, is transferred to reducing agent control system;
The 2nd CEMS sampling probe, is arranged in described kiln tail chimney, gathers the flue gas information in kiln tail chimney, and is transferred to described the 2nd CEMS analyzer;
The second the escaping of ammonia probe, is arranged in described kiln tail chimney, gathers the escaping of ammonia information in kiln tail chimney, and is transferred to described the second the escaping of ammonia analyzer.
Reductant metering control system receives the information of a CEMS analyzer, the first the escaping of ammonia analyzer, the 2nd CEMS analyzer and the second the escaping of ammonia analyzer, reducing agent is measured, and distribute cabinet to control the straying quatity of reducing agent in dore furnace by reducing agent.
As preferably, be also provided with pretreatment unit, this pretreatment unit receives the flue gas from a CEMS sampling probe and the first the escaping of ammonia probe, and flue gas is implemented after pretreatment, and correspondence flows to a CEMS analyzer and the first the escaping of ammonia analyzer.
Pretreatment unit carries out pretreatment to flue gas, makes flue gas reach after the low dirt of the low temperature that can survey correspondence again and sends into a CEMS analyzer and the first the escaping of ammonia analyzer.
As preferably, described pretreatment unit comprises successively the refrigeration system of the sampling probe that connects, companion hot gas road, built-in sampling pump, through humidity sensor and spinner flowmeter, described sampling probe adopts the husky filter core of considering, and is also furnished with for clean husky sampling probe blow device of considering filter core.
Husky filter filter core for the sampling head of pretreatment unit, processes for strong jamming item flue dust, and pretreatment unit is supporting small size back blower pump also, keeps the cleannes of cartridge surface, pressure loss when minimizing correspondence analysis instrument is bled.
As preferably, described C1 level preheater is parallel with one another two, and the exhaust pass of two C1 level preheaters is compiled in one section of main chimney flue mutually, and this main chimney flue connects conditioning Tower, and a described CEMS sampling probe is arranged on main chimney flue.
As preferably, described the first the escaping of ammonia probe is arranged on main chimney flue.
As preferably, described the 2nd CEMS sampling probe is arranged on the middle part of kiln tail chimney.
As preferably, described the second the escaping of ammonia probe is arranged on the middle part of kiln tail chimney.
Reductant metering control system and reducing agent distribute cabinet all to adopt existing technologic common equipment.
The utility model solves quotes the hysteresis quality that kiln tail chimney CEMS data exist as ammoniacal liquor demand basis, by setting up a CEMS in the outlet of C1 level preheater, main contral parameter as the metering of denitration control system ammoniacal liquor, the first the escaping of ammonia detector is set up in the outlet of C1 level preheater, as the auxiliary control parameter of denitration control system ammoniacal liquor metering; By introducing kiln tail chimney the 2nd CEMS (generally the 2nd CEMS exists) as the standby main contral parameter of denitration control system ammoniacal liquor metering, kiln tail chimney is set up the second the escaping of ammonia detector, as the standby auxiliary control parameter of denitration control system ammoniacal liquor metering; Decomposition furnace outlet temperature signal is introduced to denitration control system, shift to an earlier date NOx variation tendency in anticipation flue gas, the preposition parameter of calculating as reducing agent demand.
The parameter of the CEMS sampling probe collection that the outlet of kiln tail C1 level preheater is set up at least includes but not limited to following fume indication: flue gas flow/flow velocity, flue-gas temperature, O
2, NOx etc., in the outlet of C1 level preheater, the one CEMS sampling probe is set, nearer apart from the spray site position of ammoniacal liquor, feed back sensitiveer.
The first the escaping of ammonia probe is set up in the outlet of kiln tail C1 level preheater, and acquisition parameter comprises following fume indication: ammonia concentration and light transmittance.
Original the 2nd CEMS signal of cement producing line is delivered to denitration control system, and the parameter of delivering to denitration control system at least includes but not limited to following fume indication: flue gas flow/flow velocity, flue-gas temperature, O
2, NOx, SO
2, dust, humidity etc., as to the reduced parameter of main contral parameter and standby master control input parameter, improve the stability of a system; In addition, as data formation curve and the form of denitrating system environmental protection supervision, characterize denitrating system ruuning situation up to standard.
At original the 2nd CEMS sampling instrument of cement producing line, with layer platform, set up the second the escaping of ammonia detector, comprise following fume indication: ammonia concentration, light transmittance; As reduced parameter and the standby auxiliary control input parameter of auxiliary control parameter, improve the stability of a system; In addition, as data formation curve and the form of denitrating system environmental protection supervision, characterize denitrating system ruuning situation up to standard.
The original decomposition furnace outlet temperature signal of cement production process and CO signal are delivered to cement denitration control system, as the advance signal of the initial NOx change in concentration of judgement, as the corrected parameter that calculates NOx initial concentration, anticipation NOx change in concentration;
Ammoniacal liquor demand computing formula is as follows:
Q＝A×B×NSR×K1×K2×K3×17/46/E×10
-6
Wherein:
Q: ammoniacal liquor flow (units/kg/h);
A: the flue gas flow (Nm of unit
3/ h), preferentially choose a CEMS flue gas flow, if fault is selected the 2nd CEMS flue gas flow;
B: the initial NOx concentration (mg/Nm of unit
3), manually input or be averaging automatic generation according to the NOx concentration of 30min before denitrating system startup;
C: the target NOx controlled concentration (mg/Nm of unit
3), artificially input; According to < < cement industry atmosphere pollutants emission standards > > (GB4915-2013): if environmental protection supervision requires to control NOx concentration of emission 320mg/Nm
3below, according to debugging situation, be conventionally set to 100～300mg/Nm
3if environmental protection supervision requires to control NOx concentration of emission 400mg/Nm
3below, according to debugging situation, be conventionally set to 150～350mg/Nm
3.C is the first Variable Factors of NSR value in ammoniacal liquor flow rate calculation formula.
D: the actual measurement NOx concentration (mg/Nm of unit
3), preferentially choose NOx concentration in a CEMS, if fault is selected the 2nd CEMS flue gas flow, survey as NO, need convert as NO
2at 10%O
2data under content.D is the first Variable Factors of NSR value in ammoniacal liquor flow rate calculation formula.
E: ammoniacal liquor mass concentration (wt%);
NSR: ammonia nitrogen mol ratio, according to theoretical denitration rate η
0system generates automatically;
K1: temperature corrected parameter;
K2: the escaping of ammonia corrected parameter;
K3: by the automatic generation of ratio valve system of theoretical denitration rate and actual denitration rate.
η
0: theoretical denitration rate η
0=(B-C)/B * 100%; η
0the first Variable Factors for K3 value in ammoniacal liquor flow rate calculation formula.
η: actual denitration rate η=(B-D)/B * 100%; η is the second Variable Factors of K3 value in ammoniacal liquor flow rate calculation formula.
Compare with existing measurement control method, the utlity model has following beneficial effect:
(1) selected technology, selects C1 level preheater outlet Gas Parameters as main contral parameter, and flue gas measuring point is nearer apart from dore furnace ammonia water spray point position herein, and data feedback is more timely, measures more accurate;
(2) in the outlet of C1 level preheater, the first the escaping of ammonia detector is set, monitors more accurately excess ammonia, as input parameter, participate in calculating, save reducing agent consumption, save operating cost;
(3) original CEMS data and the escaping of ammonia monitored data of kiln tail chimney are also delivered to denitration control system, generally as environmental protection supervision data, if C1 outlet flue gas analyzer or the escaping of ammonia detector malfunction, can be used as standby input parameter, system is more stable.
(4) decomposition furnace outlet temperature signal is as preposition parameter, as the anticipation parameter of initial NOx change in concentration, controls more steady while making the reply fluctuation of operating conditions of reducing agent consumption.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model hardware device.
Fig. 2 is composition of the control system schematic diagram of the present utility model.
Fig. 3 is that 2500t/d cement furnace SNCR Flue Gas Denitrification Engineering ammoniacal liquor consumption is with working conditions change figure.
Fig. 4 is that 5000t/d cement furnace SNCR Flue Gas Denitrification Engineering ammoniacal liquor consumption is with working conditions change figure.
Shown in figure, Reference numeral is as follows:
1-dore furnace 2-temp probe
3-Pyatyi preheater 4-conditioning Tower
5-waste heat boiler 6-raw mill
7-electric vacuum cleaner 8-kiln tail chimney
9-reductant metering control system 10-reducing agent distributes cabinet
11-the one CEMS sampling probe 12-the first the escaping of ammonia probe
13-pretreatment unit 14-the one CEMS analyzer
15-the first the escaping of ammonia analyzer 16-the 2nd CEMS analyzer
17-the second the escaping of ammonia analyzer 18-the 2nd CEMS sampling probe
19-the second the escaping of ammonia probe.
The specific embodiment
A kind of reductant metering and control system of cement clinker production line SNCR denitrating flue gas, its hardware configuration schematic diagram as shown in Figure 1, technique main body hardware facility is existing equipment, comprise the dore furnace 1, Pyatyi preheater 3, conditioning Tower 4 (or waste heat boiler 5 in parallel with conditioning Tower), raw mill 6, electric vacuum cleaner 7 and the kiln tail chimney 8 that connect successively, also comprise that reductant metering control system 9 and reducing agent distribute cabinet 10, reducing agent distributes cabinet 10 to be controlled by reductant metering control system 9, and is connected to dore furnace 1.
Improvement of the present utility model is mainly reductant metering Control Component, at the exit of dore furnace 1 set temperature probe 2, Pyatyi preheater 3 to dore furnace rises and is followed successively by C5, C4, C3, C2 and C1 level preheater, C1 level preheater is set to two parallel with one another, the exhaust pass of two C1 level preheaters is compiled in one section of main chimney flue mutually, this main chimney flue connects conditioning Tower, on this main chimney flue, arrange up and down a CEMS sampling probe 11 and a first the escaping of ammonia probe 12, in identical platform, arrange a corresponding CEMS analyzer 14 and the first the escaping of ammonia analyzer 15 arranged, at a CEMS sampling probe 11, the first the escaping of ammonia probe the 12 and the one CEMS analyzer 14, a pretreatment unit 13 is set between the first the escaping of ammonia analyzer 15, information correspondence after pretreatment unit pretreatment that the one CEMS sampling probe 11 and the first the escaping of ammonia probe 12 gather transfers to a CEMS analyzer 14 and the first the escaping of ammonia analyzer 15, the one CEMS analyzer 14 and the first the escaping of ammonia analyzer 15 are all connected to reductant metering control system 9.
Pretreatment unit comprises successively the refrigeration system of the sampling probe that connects, companion hot gas road, built-in sampling pump, through humidity sensor and spinner flowmeter, this sampling probe adopts the husky filter core of considering, and is also furnished with for clean husky sampling probe blow device of considering filter core.
A the 2nd CEMS sampling probe 18 and a second the escaping of ammonia probe 19 are arranged in middle part in kiln tail chimney 8, identical platform is corresponding arranges that a 2nd CEMS analyzer 16 and second the escaping of ammonia analyzer 17, the two CEMS analyzer 16 and the second the escaping of ammonia analyzer 17 all link to reductant metering control system 9.
Reducing agent control procedure of the present utility model is as illustrated in fig. 1 and 2:
Temp probe 2 gathers dore furnace 1 outlet temperature and is transferred to reductant metering control system 9;
The one CEMS sampling probe 11 gathers flue gas information (flue gas flow/flow velocity, flue-gas temperature, the O in C1 level preheater exit
2, NOx), be transferred to pretreatment unit 13, after pretreatment unit pretreatment, be transferred to CEMS analyzer 14, the one CEMS analyzers 14 and using the data message of collection as main contral parameter, be transferred to reductant metering control system 9;
The first the escaping of ammonia probe 12 gathers the escaping of ammonia information (ammonia concentration and light transmittance) in C1 level preheater exit, be transferred to pretreatment unit 13, after pretreatment unit pretreatment, be transferred to the first the escaping of ammonia analyzer 15, the first the escaping of ammonia analyzers 15 data message of collection is transferred to reductant metering control system 9 as auxiliary control parameter;
The 2nd CEMS sampling probe 18 gathers the flue gas information in kiln tail chimney, is transferred to described the 2nd CEMS analyzer 16, the two CEMS analyzers 16 data message of collection is transferred to reductant metering control system 9 as standby main contral parameter;
The second the escaping of ammonia probe 19 gathers the escaping of ammonia information in kiln tail chimney, is transferred to described the second the escaping of ammonia analyzer 17, the second the escaping of ammonia analyzers 17 data message of collection is transferred to reductant metering control system 9 as standby auxiliary control parameter;
Reductant metering control system 9 receives the data message that temp probe 2, a CEMS analyzer 14, the first the escaping of ammonia analyzer 15, the 2nd CEMS analyzer 16 and the second the escaping of ammonia analyzer 17 transmission come, preferential main contral parameter and the auxiliary control parameter of adopting measured reducing agent, and distributes cabinet 10 to control the straying quatity of reducing agent in dore furnace by reducing agent.
When a CEMS sampling probe and the normal work of the first the escaping of ammonia employing probe, standby main contral parameter and standby auxiliary control parameter correspondence are as the reduced parameter of main contral parameter and auxiliary control parameter; When a CEMS sampling probe and the first the escaping of ammonia adopt probe, occur when abnormal, corresponding main contral parameter and the auxiliary control parameter of substituting of standby main contral parameter and standby auxiliary control parameter, as the data foundation of the metering of reductant metering control system.
Adopt the device of present embodiment to apply as follows:
Embodiment 1
Adopt ammoniacal liquor as reducing agent: the TDF type dore furnace of daily output 2500t grog, decomposition furnace outlet is provided with Pt100 temp probe, and signal is delivered to cement production process DCS, decomposition furnace outlet mean temperature.Before denitrification apparatus is built, kiln tail chimney is provided with the 2nd CEMS, and fume indication has: flue gas flow, NOx, SO
2, dust, temperature, humidity, O
2.Carry out after the transformation of SNCR denitrating flue gas, at C1 level preheater, converge flue numerical value and set up a CEMS sampling probe and the first the escaping of ammonia detector probe on lower flue, be positioned at same layer platform different level, and set up the second the escaping of ammonia detector at the same layer platform of original the 2nd CEMS sampling probe of kiln tail chimney.All signals are all delivered to denitration control system.
Ammonia volume input data has: the flue gas flow (287500Nm of a CEMS
3/ h), NOx initial concentration by denitrating system, started before mean value automatically generate that (front halfhour data generate mean value 720mg/Nm automatically
3); Manually target NOx controlled concentration after input denitration, arranges 280mg/Nm herein
3can calculate thus theoretical denitration rate is 61.1%, control system will generate corresponding NSR=1.6 automatically, add up 11 groups of data variation trend as shown in Figure 3, if adopt temperature corrected parameter from curve, the fluctuation ratio of ammoniacal liquor flow is larger without the fluctuation of the ammoniacal liquor flow of temperature correction: when the 4th group of data are surveyed NOx concentration lower than goal-setting value, ammoniacal liquor flow is in low value level, after temperature correction, the low value of ammoniacal liquor flow is lower, can be more immediately, effectively promote actual measurement NOx concentration to level off to target NOx concentration, can also save ammoniacal liquor consumption; The 11st group of data temperature is in relative low value level, initial NOx concentration reduces in theory, ammoniacal liquor flow declines, and denitration reaction speed also can reduce, and ammoniacal liquor utilization rate declines, ammoniacal liquor flow increases, now survey NOx concentration higher than goal-setting value, after temperature correction, improve ammoniacal liquor flow, can be more immediately, effectively promote the high value concentration of actual measurement Nox to level off to target NOx concentration, guarantee that system stability reliable standard moves.
Embodiment 2
Adopt ammoniacal liquor as reducing agent: specification is the TDF type dore furnace of daily output 5000t grog, and the actual daily output of grog is 5800t, and decomposition furnace outlet is provided with Pt100 temp probe, and signal is delivered to cement production process DCS, decomposition furnace outlet mean temperature.Before denitrification apparatus is built, kiln tail chimney is provided with the 2nd CEMS, and fume indication has: flue gas flow, NOx, SO
2, dust, temperature, humidity, O
2.Carry out after the transformation of SNCR denitrating flue gas, at C1 level preheater, converge flue numerical value and set up a CEMS sampling probe and the first the escaping of ammonia detector probe on lower flue, be positioned at same layer platform different level, and set up the second the escaping of ammonia detector at the same layer platform of original the 2nd CEMS sampling probe of kiln tail chimney.All signals are all delivered to denitration control system.
Ammonia volume input data has: the flue gas flow (475681Nm of a CEMS
3/ h), Nox initial concentration by denitrating system, started before mean value automatically generate that (front halfhour data generate mean value 800mg/Nm automatically
3); Manually target Nox controlled concentration after input denitration, arranges 260mg/Nm herein
3, can calculate thus theoretical denitration rate is 61.1%, and control system will generate corresponding NSR=1.8 automatically, and under various operating modes, ammoniacal liquor flow is as shown in Figure 4.
In the present embodiment, smoke components and NOx fluctuation of concentration are all very violent, from curve, can see, adopt temperature corrected parameter, the fluctuation ratio of ammoniacal liquor flow is larger without the fluctuation of the ammoniacal liquor flow of temperature correction: 9-11 organizes data, while there is peak value in NOx measured concentration, the revised ammoniacal liquor flow-rate ratio of temperature unmodified large, strengthens the ammoniacal liquor amount of coming into operation, and is more conducive to promote actual measurement NOx to level off to target NOx concentration; The 19th group of data, when valley appears in NOx measured concentration, the revised ammoniacal liquor flow-rate ratio of temperature unmodified little, reduces the ammoniacal liquor amount of coming into operation, and is more conducive to promote actual measurement NOx to level off to target NOx concentration, and saves ammonia volume.The 25th group of data, when NOx measured concentration is returned to peak value, ammonia volume is greater than again the ammoniacal liquor flow that goes out without temperature corrected Calculation, makes NOx be returned to sooner target level, guarantees that denitrating system response is more timely, more steady reliable standard operation.
Claims (7)
1. the reductant metering of cement clinker production line SNCR denitrating flue gas and a control system, comprising:
Reductant metering control system;
The dore furnace, Pyatyi preheater, conditioning Tower, raw mill, electric vacuum cleaner and the kiln tail chimney that connect successively;
The reducing agent that connects described dore furnace and be controlled by reductant metering control system distributes cabinet;
Be arranged on kiln tail chimney place and be controlled by the 2nd CEMS analyzer and the second the escaping of ammonia analyzer of reductant metering control system;
It is characterized in that, also comprise:
Temp probe, is arranged on decomposition furnace outlet place, gathers decomposition furnace outlet temperature and is transferred to reductant metering control system;
The one CEMS sampling probe, is arranged on the C1 level preheater exit of described Pyatyi preheater, gathers the flue gas information at this place;
The one CEMS analyzer, receives the flue gas information from a CEMS sampling probe, and is transferred to reductant metering control system;
The first the escaping of ammonia is popped one's head in, and is arranged on the C1 level preheater exit of described Pyatyi preheater, gathers the escaping of ammonia information at this place;
The first the escaping of ammonia analyzer, receives the escaping of ammonia information from the first the escaping of ammonia probe, is transferred to reducing agent control system;
The 2nd CEMS sampling probe, is arranged in described kiln tail chimney, gathers the flue gas information in kiln tail chimney, and is transferred to described the 2nd CEMS analyzer;
The second the escaping of ammonia probe, is arranged in described kiln tail chimney, gathers the escaping of ammonia information in kiln tail chimney, and is transferred to described the second the escaping of ammonia analyzer.
2. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 1, it is characterized in that, also be provided with pretreatment unit, this pretreatment unit receives the flue gas from a CEMS sampling probe and the first the escaping of ammonia probe, flue gas is implemented after pretreatment, and correspondence flows to a CEMS analyzer and the first the escaping of ammonia analyzer.
3. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 2, it is characterized in that, described pretreatment unit comprises successively the refrigeration system of the sampling probe that connects, companion hot gas road, built-in sampling pump, through humidity sensor and spinner flowmeter, described sampling probe adopts the husky filter core of considering, and is also furnished with for clean husky sampling probe blow device of considering filter core.
4. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 1, it is characterized in that, described C1 level preheater is parallel with one another two, the exhaust pass of two C1 level preheaters is compiled in one section of main chimney flue mutually, this main chimney flue connects conditioning Tower, and a described CEMS sampling probe is arranged on main chimney flue.
5. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 4, is characterized in that, described the first the escaping of ammonia probe is arranged on main chimney flue.
6. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 1, is characterized in that, described the 2nd CEMS sampling probe is arranged on the middle part of kiln tail chimney.
7. the reductant metering of cement clinker production line SNCR denitrating flue gas and control system according to claim 1, is characterized in that, described the second the escaping of ammonia probe is arranged on the middle part of kiln tail chimney.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103977705A (en) * | 2014-04-23 | 2014-08-13 | 浙江省环境保护科学设计研究院 | Reducing agent metering for cement clinker production line SNCR flue gas denitration and control system and method thereof |
| CN107362668A (en) * | 2016-05-12 | 2017-11-21 | 南京凯盛国际工程有限公司 | Cement kiln desulphurization system and sulfur method |
| CN109055733A (en) * | 2018-10-29 | 2018-12-21 | 中冶长天国际工程有限责任公司 | A kind of grate kiln NOx removal method, apparatus and system |
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2014
- 2014-04-23 CN CN201420199444.8U patent/CN203862137U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103977705A (en) * | 2014-04-23 | 2014-08-13 | 浙江省环境保护科学设计研究院 | Reducing agent metering for cement clinker production line SNCR flue gas denitration and control system and method thereof |
| CN107362668A (en) * | 2016-05-12 | 2017-11-21 | 南京凯盛国际工程有限公司 | Cement kiln desulphurization system and sulfur method |
| CN109055733A (en) * | 2018-10-29 | 2018-12-21 | 中冶长天国际工程有限责任公司 | A kind of grate kiln NOx removal method, apparatus and system |
| CN109055733B (en) * | 2018-10-29 | 2020-02-14 | 中冶长天国际工程有限责任公司 | Method, device and system for removing NOx from grate-rotary kiln |
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