CN208076173U - A kind of wet method fume desulfurizing system demister performance test experimental system - Google Patents

A kind of wet method fume desulfurizing system demister performance test experimental system Download PDF

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Publication number
CN208076173U
CN208076173U CN201820494211.9U CN201820494211U CN208076173U CN 208076173 U CN208076173 U CN 208076173U CN 201820494211 U CN201820494211 U CN 201820494211U CN 208076173 U CN208076173 U CN 208076173U
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China
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demister
particle size
magnesium ion
air
entrance
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CN201820494211.9U
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Inventor
刘帅
王建军
潘静娜
白翔宇
刘宏宇
杨子晗
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China University of Petroleum East China
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China University of Petroleum East China
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Abstract

The utility model belongs to gas-liquid separation technical field of research, is related to a kind of wet method fume desulfurizing system demister performance test experimental system.Including atomization system, demister system, induced draught system, mist droplet particle size measuring system, magnesium ion isokinetic sampling system, Pitot tube measuring system;The droplet that atomization system generates is delivered to demister system by induced draught system as hydrodynamic source, demister system completes demisting process, mist droplet particle size measuring system carries out demister entrance and demister outlet mist droplet particle size measures, magnesium ion isokinetic sampling's system carries out demister system demisting efficiency measurement, and Pitot tube measuring system measures pressure drop and linear speed;The invention also discloses the methods tested based on above system.The utility model switches over experiment type and experiment condition is very convenient, can meet different type demister performance test requirement, and data guidance is provided for the research and development of high-performance demister.

Description

A kind of wet method fume desulfurizing system demister performance test experimental system
Technical field
The utility model belongs to gas-liquid separation technical field of research, is related to a kind of wet method fume desulfurizing system demister performance Testing experimental system.
Background technology
SO is controlled using flue gas desulfurization device2Discharge has become the common recognition of each stratum of the whole society, Wet Flue Gas Desulfurization Technology It is most widely used method, wherein lime stone-gypsum desulfurization is that technology is most ripe in the world, most widely used one kind Desulfurization technology, this technique of the flue gas desulfurization device use in 90% or more thermal power plant.Demister is technique One of key equipment, performance directly affect the operation conditions of entire wet method fume desulfurizing system.Demister fog removal performance does not reach Rotating savings directly affects the normal operation of flue gas reheater, causes its fouling and corrosion, and also has to downstream flue and wind turbine huge It is big to influence, or even " gypsum rain " is formed, cause the secondary pollution of environment.It is evaluation demisting that demister exiting flue gas, which carries drop amount, Therefore one of the important indicator of device performance measures demister exiting flue gas carrying drop amount and may determine that demister fog removal performance Whether meet wet method fume desulfurizing system requirement, demister exiting flue gas is generally required to carry drop amount no more than 75mg/m3, Also realize that minimum discharge provides data and supports for research and development high efficiency demister simultaneously.
The test of demister fog removal performance is examined by the scientific research of object, new-product development and product export of demister The important test content tested etc..Currently, China is complete there are no being measured to demister fog removal performance in wet method fume desulfurizing system Whole experimental system and a whole set of experimental method cause China to research and develop large-scale, high-performance demister ability wretched insufficiency, crucial skill Art parameter is under one's control.Moreover, the existing experimental system measured to demister fog removal performance domestic at present and experimental method lack Convincingness, exist operation it is lack of standardization, measurement data is unreliable and experimental situation differs larger with demister actual operating mode The shortcomings that.
Utility model content
Technical problem to be solved in the utility model is to overcome the shortage of prior art, and providing one kind can be in truly Existing demister fog removal performance, and a kind of wet method fume desulfurizing system demister of laboratory experiment condition feature can be given full play to It can testing experimental system.
The utility model solves the scheme that its technical problem is taken:A kind of wet method fume desulfurizing system demister performance Testing experimental system includes atomization system, demister system, induced draught system, mist droplet particle size measuring system, magnesium ion isokinetic sampling system System, Pitot tube measuring system.
The atomization system includes motor, air compressor, high pressure buffer gas tank, air dryer, 2 adjustings Valve, feed pipe, metering water tank, thermometer, screw pump, flowmeter, two-fluid spray nozzle, motor is as driving device and air pressure Contracting machine coordinates, and air compressor, high pressure buffer gas tank, air dryer, regulating valve and two-fluid spray nozzle are defeated along high pressure gas Direction is sent to be sequentially connected with by high-pressure air pipe;Feed pipe is connected to metering water tank, and thermometer is placed in the middle part of metering water tank, measures water Case, screw pump, regulating valve, flowmeter and two-fluid spray nozzle are sequentially connected with along flow conveying direction by water-supply-pipe.
The demister system includes thermometer, dust-collecting bucket, organic glass encapsulation cylinder, demister outlet, demister, demister Entrance, organic glass encapsulation cylinder are measured with atomization system, demister system, induced draught system, mist droplet particle size respectively as main body frame System, magnesium ion isokinetic sampling system are connected with Pitot tube measuring system, and demister is with demister entrance under, demister outlet It is placed in inside organic glass encapsulation cylinder in upper mode, dust-collecting bucket is placed in organic glass encapsulation cylinder bottom, for collecting demister The droplet separated, thermometer is placed in below demister entrance, for measuring demister inlet droplet temperature.
The induced draught system includes protecting wind turbine gravity separator, regulating valve, air-introduced machine, adjustable frequency motor, frequency converter, Protection wind turbine gravity separator, regulating valve, air-introduced machine and the adjustable frequency motor defeated direction outside gas are sequentially connected with by pipeline, Frequency converter is connected by cable with variable-frequency motor as controller.
The mist droplet particle size measuring system includes computer, 2 spraying laser particle size analyzers, 2 spraying laser particle sizes point Analyzer is respectively placed in demister entrance and demister exit, the droplet grain for measuring demister entrance and demister exit Diameter, and connect respectively with computer by data line.
The magnesium ion isokinetic sampling system includes heater, superfluorescent fiber filter, thermometer, flowmeter, flow-rate adjustment Valve, vacuum pump, motor, heater, superfluorescent fiber filter, flowmeter, flow control valve and vacuum pump pass through along pumping direction Pipeline is sequentially connected with, and thermometer is placed in superfluorescent fiber filter rear portion, and motor drives vacuum pump work by V belt translation.
The Pitot tube measuring system is connect with demister system and induced draught system respectively, for measure linear speed in demister, Pressure drop in air inducing pipeline between linear speed and the outlet of demister entrance and demister.
It is a kind of based on above-mentioned wet method fume desulfurizing system demister performance test that the purpose of this utility model also resides in offer A kind of wet method fume desulfurizing system demister performance test Thermal-state test method of experimental system, this method is successively according to the following steps It carries out:
First step is test preparation process:First check for the pipeline leakproofness and circuit reliability of a whole set of experimental system; Enough water is added into metering water tank by feed pipe, then opens metering heating water tanks power supply, sets atomization temperature progress Heating, after reaching set temperature, the concentration that appropriate magnesium ion reaches experimental design requirement is added into water;Run air compression Machine sets experimental pressure and carries out high pressure gas deposit;Computer and spraying laser particle size analyzer are finally opened, is opened mating soft Part carries out instrument preheating after regulating mist droplet particle size testing background.
Second step is demister system moistening step:It is first turned on induced draught system power supply, is become by adjusting Frequency Converter Control Frequency motor speed, and then air inducing fan delivery is adjusted, it monitors whether to reach in experimentation in real time by Pitot tube measuring system The predetermined initial linear speed of demister, and record the pressure drop between demister entrance at this time and demister outlet;Then atomization is opened The regulating valve of system simultaneously runs screw pump, controls water flow and high pressure air flow by regulating valve, reaches requirement of experiment Liquid load value and atomizing effect, and pass through laser particle size analyzer real time on-line monitoring demister entrance mist droplet particle size value of spraying Whether reach requirement of experiment, after aforesaid operations are adjusted to requirement of experiment, keep experimental system present situation to run 5 minutes, make the atomization be The temperature value of thermometer measure in the temperature value and demister system of thermometer measure in system is equal, and makes reality in the process Check system pipeline complete wetting.
Third step is DATA REASONING step:Experimental design requirement, based on the stable state of second step, The measurement that spraying laser particle size analyzer completes demister entrance and demister outlet mist droplet particle size, note are controlled by computer software The record stabilization data that Pitot tube measuring system monitors in real time at this time;In addition, opening magnesium ion isokinetic sampling's system power supply, start pair Demister exit carries out isokinetic sampling and passes through flow-rate adjustment valve regulation sampling conduit by motor drive vacuum pump work Interior linear speed is equal to linear speed in demister, and ensures that sample temperature is consistent with experimental system set temperature by heater, keeps steady Surely it runs 20 minutes, isokinetic sampling is then carried out to demister inlet with same method with magnesium ion isokinetic sampling system.
Four steps is experimental facilities reconstitution steps:After the completion of DATA REASONING needed for experiment, magnesium ion out of service first Isokinetic sampling's system, then the spraying laser particle size analyzer in mist droplet particle size measuring system out of service, atomization system successively And induced draught system;It is last to close all regulating valves successively, complete primary complete fog removal performance test experiments.
5th step is that demisting efficiency calculates step, takes out the microfibre filter in magnesium ion isokinetic sampling's system first Device is rinsed with pure water, it is believed that the concentration of magnesium ion and exports institute in demister entrance and demister in atomization system The concentration of magnesium ion is equal in the drop of carrying, by magnesium ion compleximetry, to magnesium ion mass concentration in atomization system It measures the magnesium ion mass concentration carried with demister entrance and demister exit gas in drop to measure, can be counted by formula The mass concentration of drop in gas is calculated, and then calculates the demisting efficiency of demister;It is calculated in demister first with formula (1) Microfilter after outlet sampling rinses magnesium ion content in filtrate:
In formula:
M1The content of magnesium ion, mol in-flushing filtrate;
25:- liquid moves pipe liquid relief 25ml;
V0Total filtrate volume after-probe tube and microfilter flushing, mL;
V1The volume of-titration magnesium ion consumption EDTA standard solution, mL;
c1- EDTA marks the actual concentrations of solution, mol.
Separately a new microfilter is taken to make blank sample, the content for measuring magnesium ion is M0, mol.Then according to formula (2) it calculates demister exit gas and carries drop amount:
In formula:
M0The content of magnesium ion, mol are measured in-microfilter blank sample;
M1The content of magnesium ion, mol in-flushing filtrate;
c2Magnesium ion content concentration, mol/L in-spraying liquid;
ρ1The density of-spraying liquid, kg/m3
Using the microfilter after the processing demister entrance sampling of same method, obtains demister inlet gas and take Band drop amount mEntrance, then demister demisting efficiency η is according to formula (3) calculating:
The droplet grain that demister entrance and demister are exported using spraying laser particle size analyzer mating computer software Diameter is for statistical analysis to obtain median, taper end grain size and butt end grain size therein.
It is a kind of based on above-mentioned wet method fume desulfurizing system demister performance test that the purpose of this utility model also resides in offer A kind of wet method fume desulfurizing system demister performance test Cold simulating test method of experimental system, this method is successively according to the following steps It carries out:
First step is test preparation process:First check for the pipeline leakproofness and circuit reliability of a whole set of experimental system; Enough normal-temperature waters are added into metering water tank by feed pipe, is not required to open metering heating water tanks power supply at this time, is added into water Appropriate magnesium ion reaches the concentration of experimental design requirement;Air compressor is run, experimental pressure is set and carries out high pressure gas storage It is standby;Computer and spraying laser particle size analyzer are finally opened, software kit is opened, is carried out after regulating mist droplet particle size testing background Instrument preheats.
Second step is demister system moistening step:It is first turned on induced draught system power supply, is become by adjusting Frequency Converter Control Frequency motor speed, and then air inducing fan delivery is adjusted, it monitors whether to reach in experimentation in real time by Pitot tube measuring system The predetermined initial linear speed of demister, and record the pressure drop between demister entrance at this time and demister outlet;Then atomization is opened The regulating valve of system simultaneously runs screw pump, controls water flow and high pressure air flow by regulating valve, reaches requirement of experiment Liquid load value and atomizing effect, and pass through laser particle size analyzer real time on-line monitoring demister entrance mist droplet particle size value of spraying Whether reach requirement of experiment, after aforesaid operations are adjusted to requirement of experiment, keeps experimental system present situation to run 5 minutes, in this process In make experimental system pipeline complete wetting.
Third step is DATA REASONING step:Experimental design requirement, based on the stable state of second step, The measurement that spraying laser particle size analyzer completes demister entrance and demister outlet mist droplet particle size, note are controlled by computer software The record stabilization data that Pitot tube measuring system monitors in real time at this time;In addition, opening magnesium ion isokinetic sampling's system power supply, start pair Demister exit carries out isokinetic sampling and passes through flow-rate adjustment valve regulation sampling conduit by motor drive vacuum pump work Interior linear speed is equal to linear speed in demister, keeps stable operation 20 minutes, then with the same side of magnesium ion isokinetic sampling's system Method carries out isokinetic sampling to demister inlet.
Then repeat a kind of four steps in wet method fume desulfurizing system demister performance test Thermal-state test method and 5th step.
Preferably, the form of demister can need specific setting according to experiment.
Preferably, the liquid of atomization system can be water or lime slurry.
The beneficial effects of the utility model
A kind of wet method fume desulfurizing system demister performance test experimental system of the utility model is structurally consummate, function collection Cheng Hua can be able to be Suresh Kumar, such as baffle plate demister, rotational flow plate defroster and tube bank to the demister of diversified forms Formula demister meets the different experiments research requirement for realizing Thermal-state test and Cold simulating test.
Experimental method operating system based on the utility model, can farthest realize experimental situation and wet flue gas The goodness of fit of desulphurization system demister actual operating mode, the standardization of experimental data measurement method, data are accurate and reliable.
Description of the drawings
Fig. 1 is a kind of tool of wet method fume desulfurizing system demister performance test experimental system provided by the utility model The structure principle chart of body embodiment.
In figure:1. motor, 2. air compressors, 3. high pressure buffer gas tanks, 4. air dryers, 5. regulating valves, 6. Feed pipe, 7. metering water tanks, 8. thermometers, 9. screw pumps, 10. regulating valves, 11. flowmeters, 12. two-fluid spray nozzles, 13. temperature Degree meter, 14. dust-collecting buckets, 15. organic glass encapsulation cylinders, 16. computers, 17. protection wind turbine gravity separators, 18. regulating valves, 19. air-introduced machine, 20. adjustable frequency motors, 21. frequency converters, 22. spraying laser particle size analyzers, the outlet of 23. demisters, 24. demistings Device, 25. demister entrances, 26. spraying laser particle size analyzers, 27. Pitot tube measuring systems, 28. heaters, 29. superfluorescent fibers Filter, 30. thermometers, 31. flowmeters, 32. flow control valves, 33. vacuum pumps, 34. motor.
Specific implementation mode
Direction shown in arrow is the flow direction of fluid at this in Fig. 1.
The following is a combination of the drawings in the embodiments of the present utility model 1, is carried out to the technical solution in embodiment clear, complete Ground describes, and a kind of wet method fume desulfurizing system demister performance test experimental system includes atomization system, demister system, air inducing system System, mist droplet particle size measuring system, magnesium ion isokinetic sampling system, Pitot tube measuring system 27.
The atomization system includes motor 1, air compressor 2, high pressure buffer gas tank 3, air dryer 4, adjusts Valve 5, feed pipe 6, metering water tank 7, thermometer 8, screw pump 9, regulating valve 10, flowmeter 11, two-fluid spray nozzle 12, motor 1 Coordinate as driving device and air compressor 2, air compressor 2, high pressure buffer gas tank 3, air dryer 4, regulating valve 5 It is sequentially connected with by high-pressure air pipe along high pressure gas conveying direction with two-fluid spray nozzle 12;Feed pipe 6 is connected to metering water tank 7, Thermometer 8 is placed in 7 middle part of metering water tank, metering water tank 7, screw pump 9,12 edge of regulating valve 10, flowmeter 11 and two-fluid spray nozzle Flow conveying direction is sequentially connected with by water-supply-pipe, and the pressure-air measured in water and high pressure buffer gas tank 3 in water tank 7 exists Converge at two-fluid spray nozzle 12, high-efficient atomizing is realized using the special cavity body structure inside two-fluid spray nozzle 12.
The demister system includes thermometer 13, dust-collecting bucket 14, organic glass encapsulation cylinder 15, demister outlet 23, demisting Device 24, demister entrance 25, organic glass encapsulation cylinder 15 be used as main body frame, respectively with atomization system, demister system, air inducing system System, mist droplet particle size measuring system, magnesium ion isokinetic sampling system are connected with Pitot tube measuring system 27, and demister 24 is with demister Entrance 25 is under, demister outlet 23 is placed in upper mode inside organic glass encapsulation cylinder 15, and dust-collecting bucket 14 is placed in organic glass 15 bottom of glass encapsulation cylinder, the droplet separated for collecting demister 24, thermometer 13 are placed in 25 lower section of demister entrance, use The droplet temperature at measurement demister entrance 25.
The induced draught system includes protection wind turbine gravity separator 17, regulating valve 18, air-introduced machine 19, adjustable frequency motor 20, frequency converter 21, protection wind turbine gravity separator 17, regulating valve 18, air-introduced machine 19 and adjustable frequency motor 20 are defeated outside gas Direction is sequentially connected with by pipeline, and frequency converter 21 is connected by cable with variable-frequency motor 20 as controller.
The mist droplet particle size measuring system includes computer 16, spraying laser particle size analyzer 22 and spraying laser particle size analysis Instrument 26, spraying laser particle size analyzer 22 are placed at demister outlet 23, and spraying laser particle size analyzer 26 is placed in demister and enters At mouth 25, for measuring the mist droplet particle size at demister entrance 25 and demister outlet 23, and pass through data line and computer respectively 16 connections.
The magnesium ion isokinetic sampling system include heater 28, superfluorescent fiber filter 29, thermometer 30, flowmeter 31, Flow control valve 32, vacuum pump 33, motor 34, heater 28, superfluorescent fiber filter 29, flowmeter 31, flow control valve 32 It is sequentially connected with by pipeline along pumping direction with vacuum pump 33, thermometer 30 is placed in 29 rear portion of superfluorescent fiber filter, motor 34 Vacuum pump 33 is driven to work by V belt translation.
The Pitot tube measuring system 27 is connect with demister system and induced draught system respectively, for measuring 24 interior lines of demister Pressure drop in speed, air inducing pipeline between linear speed and demister entrance 25 and demister outlet 23.
A kind of demisting course of work of wet method fume desulfurizing system demister performance test experimental system:
In induced draught system under the operation of air-introduced machine 19, after sealing piping connection, shape in organic glass encapsulation cylinder 15 At ascending air from bottom to top, the flow of flue gas state in wet flue gas desulfurization tower is simulated, is formed by two-fluid spray nozzle 12 Droplet forms biphase gas and liquid flow under the rolling action of ascending air, enters gas-liquid inside demister 24 from demister entrance 25 Droplet in two phase flow removes, and contains the air-flow for failing to remove droplet on a small quantity at this time and enters protection through pipeline from demister outlet 23 Wind turbine is further removed the remaining droplet in air-flow, is prevented droplet from corroding 19 inner vanes of air-introduced machine in gravity separator 17, Then it will be arranged outside clean air-flow by air-introduced machine 19 through piping, complete entire demisting process.
The utility model is also disclosed a kind of based on above-mentioned wet method fume desulfurizing system demister performance test experimental system A kind of wet method fume desulfurizing system demister performance test Thermal-state test method, carries out according to the following steps successively:
First step is test preparation process:First check for the pipeline leakproofness and circuit reliability of a whole set of experimental system; By feed pipe 6 to metering water tank 7 in enough water is added, then open metering 7 heating power supply of water tank, set atomization temperature into Row heating, after reaching set temperature, the concentration that appropriate magnesium ion reaches experimental design requirement is added into water;Run air compression Machine 2 sets experimental pressure and carries out high pressure gas deposit;Finally open computer 16, spraying laser particle size analyzer 22 and spraying Laser particle size analyzer 26 opens software kit, and instrument preheating is carried out after regulating mist droplet particle size testing background.
Second step is demister system moistening step:It is first turned on induced draught system power supply, is controlled by adjusting frequency converter 21 20 rotating speed of adjustable frequency motor, and then 19 air quantity of air-introduced machine is adjusted, it monitors whether to reach real in real time by Pitot tube measuring system 27 The predetermined initial linear speed of demister 24 during testing, and record the pressure between demister entrance 25 at this time and demister outlet 23 Drop;Then it opens the regulating valve 10 of atomization system and runs screw pump 9, flow is controlled by regulating valve 10 and regulating valve 5 respectively Flow and high pressure air flow reach the liquid load value and atomizing effect of requirement of experiment, and pass through laser particle size analysis of spraying Whether 26 real time on-line monitoring demister entrance of instrument, 25 mist droplet particle size value reaches requirement of experiment, and aforesaid operations are adjusted to requirement of experiment Afterwards, it keeps experimental system present situation to run 5 minutes, makes in the temperature value and demister system that the thermometer 8 in atomization system measures The temperature value that thermometer 13 measures is equal, and makes experimental system pipeline complete wetting in the process.
Third step is DATA REASONING step:Experimental design requirement, based on the stable state of second step, Spraying laser particle size analyzer 26 is controlled by 16 software of computer and spraying laser particle size analyzer 22 is respectively completed demister and enters Mouth 25 and demister export the measurement of 23 mist droplet particle sizes, the record stabilization data that Pitot tube measuring system 27 monitors in real time at this time; In addition, opening magnesium ion isokinetic sampling's system power supply, start, to carrying out isokinetic sampling at demister outlet 23, to pass through motor 34 Vacuum pump 33 is driven to work, adjusting linear speed in sampling conduit by flow control valve 32 is equal to linear speed in demister 24, and passes through Heater 28 ensures that sample temperature is consistent with experimental system set temperature, stable operation 20 minutes is kept, then with magnesium ion etc. Fast sampling system is with same method to carrying out isokinetic sampling at demister entrance 25.
Four steps is experimental facilities reconstitution steps:After the completion of DATA REASONING needed for experiment, magnesium ion out of service first Isokinetic sampling's system, then the spraying laser particle size analyzer 22 in mist droplet particle size measuring system out of service, spraying swash successively Light Particle Size Analyzer 26, atomization system and induced draught system;Finally all regulating valves 5, regulating valve 10, flow control valve are closed successively 32 and regulating valve 18, complete primary complete fog removal performance test experiments.
5th step is that demisting efficiency calculates step, takes out the microfilter in magnesium ion isokinetic sampling's system first 29, it is rinsed with pure water, it is believed that the concentration of magnesium ion and exported in demister entrance 25 and demister in atomization system The concentration of magnesium ion is equal in drop entrained by 23, by magnesium ion compleximetry, to magnesium ion quality in atomization system Measurement of concetration and demister entrance 25 and demister export the magnesium ion mass concentration that 23 gases carry in drop and measure, and lead to The mass concentration of drop in gas can be calculated by crossing formula, and then calculate the demisting efficiency of demister 24;First with formula (1) It calculates the microfilter 29 after 23 sampling of demister outlet and rinses magnesium ion content in filtrate:
In formula:
M1The content of magnesium ion, mol in-flushing filtrate;
25:- liquid moves pipe liquid relief 25ml;
V0Total filtrate volume after-probe tube and the flushing of microfilter 29, mL;
V1The volume of-titration magnesium ion consumption EDTA standard solution, mL;
c1- EDTA marks the actual concentrations of solution, mol.
Separately a new microfilter 29 is taken to make blank sample, the content for measuring magnesium ion is M0, mol.Then basis Formula (2) calculates demister and exports 23 gases carrying drop amount:
In formula:
M0The content of magnesium ion, mol are measured in 29 blank sample of-microfilter;
M1The content of magnesium ion, mol in-flushing filtrate;
c2Magnesium ion content concentration, mol/L in-spraying liquid;
ρ1The density of-spraying liquid, kg/m3
Microfilter 29 after being sampled using same method processing demister entrance 25, obtains demister entrance 25 Gas carries drop amount mEntrance, then 24 demisting efficiency η of demister is according to formula (3) calculating:
Using spraying laser particle size analyzer 26 and mating 16 software of computer of laser particle size analyzer 22 of spraying to demisting Device entrance 25 and the mist droplet particle size of demister outlet 23 for statistical analysis obtain median, taper end grain size and butt end therein Grain size.
The invention also discloses one kind being based on above-mentioned wet method fume desulfurizing system demister performance test experimental system A kind of wet method fume desulfurizing system demister performance test Cold simulating test method, carry out according to the following steps successively:
First step is test preparation process:First check for the pipeline leakproofness and circuit reliability of a whole set of experimental system; Enough normal-temperature waters are added into metering water tank 7 by feed pipe 6, is not required to open metering 7 heating power supply of water tank at this time, add into water Enter the concentration that appropriate magnesium ion reaches experimental design requirement;Air compressor 2 is run, experimental pressure is set and carries out high pressure gas Deposit;Computer 16 and spraying laser particle size analyzer 22 and spraying laser particle size analyzer 26 are finally opened, software kit is opened, Instrument preheating is carried out after regulating mist droplet particle size testing background.
Second step is demister system moistening step:It is first turned on induced draught system power supply, is controlled by adjusting frequency converter 21 20 rotating speed of adjustable frequency motor, and then 19 air quantity of air-introduced machine is adjusted, it monitors whether to reach real in real time by Pitot tube measuring system 27 The predetermined initial linear speed of demister 24 during testing, and record the pressure between demister entrance 25 at this time and demister outlet 23 Drop;Then it opens the regulating valve 5 of atomization system and regulating valve 10 and runs screw pump 9, pass through regulating valve 10 and regulating valve 5 is distinguished Water flow and high pressure air flow are controlled, reaches the liquid load value and atomizing effect of requirement of experiment, and pass through laser of spraying Whether 26 real time on-line monitoring demister entrance of Particle Size Analyzer, 25 mist droplet particle size value reaches requirement of experiment, and aforesaid operations are adjusted to After requirement of experiment, keeps experimental system present situation to run 5 minutes, make experimental system pipeline complete wetting in the process.
Third step is DATA REASONING step:Experimental design requirement, based on the stable state of second step, Spraying laser particle size analyzer 26 is controlled by 16 software of computer and spraying laser particle size analyzer 22 completes demister entrance 25 The measurement of 23 mist droplet particle sizes, the record stabilization data that Pitot tube measuring system 27 monitors in real time at this time are exported with demister;In addition, It is pre-recorded and open magnesium ion isokinetic sampling's system power supply, it drives vacuum pump 33 to work by motor 34, passes through flow tune It saves linear speed in the adjusting sampling conduit of valve 32 and is equal to linear speed in demister 24, stable operation 20 minutes is kept, then with magnesium ion etc. Fast sampling system is with same method to carrying out isokinetic sampling at demister entrance 25.
Then repeat a kind of four steps in wet method fume desulfurizing system demister performance test Thermal-state test method and 5th step.
Preferably, the form of demister 24 can need specific setting according to experiment.
Preferably, the liquid of atomization system can be water or lime slurry.
The basic principles and main features and advantage of the utility model have been shown and described above.The technical staff of the industry It should be appreciated that the present utility model is not limited to the above embodiments, the above embodiments and description only describe this The principle of utility model, on the premise of not departing from the spirit and scope of the utility model, the utility model also has various change And improvement, these various changes and improvements fall within the scope of the claimed invention.

Claims (1)

1. a kind of wet method fume desulfurizing system demister performance test experimental system, it is characterised in that:Including atomization system, demisting System, induced draught system, mist droplet particle size measuring system, magnesium ion isokinetic sampling system, Pitot tube measuring system;
The atomization system include motor, air compressor, high pressure buffer gas tank, air dryer, 2 regulating valves, to Water pipe, metering water tank, thermometer, screw pump, flowmeter, two-fluid spray nozzle, motor is as driving device and air compressor Cooperation, air compressor, high pressure buffer gas tank, air dryer, regulating valve and two-fluid spray nozzle are along high pressure gas conveying side It is sequentially connected with to by high-pressure air pipe;Feed pipe is connected to metering water tank, and thermometer is placed in the middle part of metering water tank, metering water tank, Screw pump, regulating valve, flowmeter and two-fluid spray nozzle are sequentially connected with along flow conveying direction by water-supply-pipe;
The demister system includes that thermometer, dust-collecting bucket, organic glass encapsulation cylinder, demister outlet, demister, demister enter Mouthful, organic glass encapsulation cylinder measures system with atomization system, demister system, induced draught system, mist droplet particle size respectively as main body frame System, magnesium ion isokinetic sampling system be connected with Pitot tube measuring system, demister with demister entrance under, demister export exist On mode be placed in inside organic glass encapsulation cylinder, dust-collecting bucket is placed in organic glass encapsulation cylinder bottom, for collecting demister point From the droplet to get off, thermometer is placed in below demister entrance, for measuring demister inlet droplet temperature;
The induced draught system includes protection wind turbine gravity separator, regulating valve, air-introduced machine, adjustable frequency motor, frequency converter, protection Wind turbine gravity separator, regulating valve, air-introduced machine and the adjustable frequency motor defeated direction outside gas are sequentially connected with by pipeline, frequency conversion Device is connected by cable with variable-frequency motor as controller;
The mist droplet particle size measuring system includes computer, 2 spraying laser particle size analyzers, 2 spraying laser particle size analyzers It is respectively placed in demister entrance and demister exit, the mist droplet particle size for measuring demister entrance and demister exit, And it is connect respectively with computer by data line;
The magnesium ion isokinetic sampling system includes heater, superfluorescent fiber filter, thermometer, flowmeter, flow control valve, true Sky pump, motor, heater, superfluorescent fiber filter, flowmeter, flow control valve and vacuum pump are suitable by pipeline along pumping direction Secondary connection, thermometer are placed in superfluorescent fiber filter rear portion, and motor drives vacuum pump work by V belt translation;
The Pitot tube measuring system is connect with demister system and induced draught system respectively, for measuring linear speed in demister, air inducing Pressure drop in pipeline between linear speed and the outlet of demister entrance and demister.
CN201820494211.9U 2018-04-09 2018-04-09 A kind of wet method fume desulfurizing system demister performance test experimental system Expired - Fee Related CN208076173U (en)

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CN108303280A (en) * 2018-04-09 2018-07-20 中国石油大学(华东) A kind of wet method fume desulfurizing system demister performance test experimental system and experimental method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108303280A (en) * 2018-04-09 2018-07-20 中国石油大学(华东) A kind of wet method fume desulfurizing system demister performance test experimental system and experimental method

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