CN201852724U - Double-regulating static and unbalanced constant-speed coal dust sampling system - Google Patents
Double-regulating static and unbalanced constant-speed coal dust sampling system Download PDFInfo
- Publication number
- CN201852724U CN201852724U CN2010206170732U CN201020617073U CN201852724U CN 201852724 U CN201852724 U CN 201852724U CN 2010206170732 U CN2010206170732 U CN 2010206170732U CN 201020617073 U CN201020617073 U CN 201020617073U CN 201852724 U CN201852724 U CN 201852724U
- Authority
- CN
- China
- Prior art keywords
- sampling
- differential pressure
- solenoid valve
- static
- double
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 238000005070 sampling Methods 0.000 title claims abstract description 135
- 230000003068 static effect Effects 0.000 title claims abstract description 74
- 239000002817 coal dust Substances 0.000 title abstract description 39
- 239000003245 coal Substances 0.000 claims description 55
- 230000003189 isokinetic effect Effects 0.000 claims description 38
- 238000010438 heat treatment Methods 0.000 claims description 29
- 238000000926 separation method Methods 0.000 claims description 20
- 238000012360 testing method Methods 0.000 abstract description 4
- 238000002485 combustion reaction Methods 0.000 abstract description 3
- 238000005485 electric heating Methods 0.000 abstract 3
- 230000006835 compression Effects 0.000 abstract 2
- 238000007906 compression Methods 0.000 abstract 2
- 239000000523 sample Substances 0.000 description 63
- 238000000034 method Methods 0.000 description 33
- 230000000694 effects Effects 0.000 description 15
- 238000005086 pumping Methods 0.000 description 12
- 238000010926 purge Methods 0.000 description 12
- 238000005259 measurement Methods 0.000 description 11
- 239000000843 powder Substances 0.000 description 11
- 230000001105 regulatory effect Effects 0.000 description 9
- 239000002245 particle Substances 0.000 description 7
- 230000008676 import Effects 0.000 description 6
- 238000013461 design Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 238000007689 inspection Methods 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000000740 bleeding effect Effects 0.000 description 2
- 238000009530 blood pressure measurement Methods 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 239000003500 flue dust Substances 0.000 description 2
- 239000000411 inducer Substances 0.000 description 2
- 238000000691 measurement method Methods 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000009897 systematic effect Effects 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
Images
Landscapes
- Sampling And Sample Adjustment (AREA)
Abstract
The utility model relates to a double-regulating static and unbalanced constant-speed coal dust sampling system, which has the advantages that the structure is simple; the use is convenient; the automatic constant sampling can be realized; the sampling accuracy of coal dust is greatly enhanced; and the real and reliable test data of concentration and density of the coal dust can be obtained, and then the combustion adjustment of the boiler can be reliably performed, and the mistaken adjustment is avoided. The system comprises a static sampling device, wherein the static sampling device is connected with electric heating separating equipment through an electric heating sampling pipeline and a sampling valve; the electric heating separating equipment is connected with a double-regulating device; the double-regulating device is connected with a compression air source; the compression air source is connected with the static sampling device through a differential pressure obtaining device; and the controller is used to respectively control the double-regulating device and the differential pressure obtaining device.
Description
Technical field
The utility model relates to a kind of coal dust sampling system, relates in particular to a kind of two uneven isokinetic sample of pulverized coal of static pressure system that regulates.
Background technology
Coal powder density and fineness of pulverized coal are the important parameters that coal-fired station burning is adjusted, and the safety and economic operation of boiler is had significant impact.Along with the progressively raising of country, adopt the large-scale unit of unit pulverized-coal system to obtain widespread use to environmental protection of thermal power generation unit and energy-conservation requirement.The monitoring of coal powder density and fineness is puzzlement boiler of power plant technician's a difficult problem always in the unit pulverized-coal system.In unit pulverized-coal system, a coal pulverizer has many outlet coal pipes simultaneously, and the coal powder density of each pulverized coal channel is different.If the coal powder density deviation is excessive, can influence the coal-air ratio of each burner, cause problems such as burning efficiency decline, combustion instability, slagging scorification, NOx discharging increase.Fineness of pulverized coal also has considerable influence to burning and coal pulverizer unit consumption, and coal dust is thick excessively, and unburned carbon in flue dust will become greatly, and boiler combustion efficiency can descend; Coal dust is meticulous, the decline of exerting oneself of unit pulverized coal preparation system, and the pulverized coal preparation system unit consumption can raise, and changes under the little situation at unburned carbon in flue dust, and whole boiler unit efficiency also can descend.The coal dust sampling becomes the gordian technique of power plant's energy-saving and emission-reduction gradually and comes into one's own.
All carrying out the research of coal dust line Measurement Technique both at home and abroad at present, as microwave method, capacitance method, excusing from death ripple method etc.But these methods can not adapt to on-the-spot environment complicated and changeable, and versatility and practicality are not strong.Because do not have ripe line Measurement Technique, power plant can't carry out continuous monitoring to the coal dust operation conditions in the unit pulverized-coal system in operational process always.The method that generally adopts is still directly taken a sample to pulverized coal particle from Dual-Phrase Distribution of Gas olid now, to determine coal powder density and fineness of pulverized coal.
When Dual-Phrase Distribution of Gas olid was taken a sample, following four kinds of situations can appear: suction velocity equals, less than or greater than speed of incoming flow; Though or suction velocity equates that with speed of incoming flow sampling probe is not over against airflow direction.The three kinds of situations in back all can make near the air-flow streamline the probe import change direction.Because the density of solid particle is more much bigger than the density of gas particles, so when sampling made suction velocity and speed of incoming flow unequal, solid particle can break away from the air-flow streamline of bending because of the effect of inertial force, causes sampling error.Therefore the accuracy of coal dust sampling to be improved, the isokinetic sampling must be realized.So-called isokinetic sampling promptly allows the air-breathing speed that enters the sampling probe import equate with the preceding speed of incoming flow of popping one's head in.Isokinetic sample of pulverized coal method commonly used has static balance formula isokinetic sample of pulverized coal method and predicted velocity formula isokinetic sample of pulverized coal method, according to different sampling methods, also made multi-form coal fines sampling apparatus, the unit pulverized-coal system coal fines sampling apparatus of present domestic application has following several form:
(1) De Guo AKOMA static balance formula coal fines sampling apparatus
Adopt static balance formula isokinetic sampling method, can realize the total cross-section sampling to pulverized coal channel, the coal dust representativeness is good, but it costs an arm and a leg, and is fit to experimental study, is not suitable for power plant's rig-site utilization, simultaneously because there is the systematic sampling error in the restriction of its sampling theorem.
(2) the PFS coal fines sampling apparatus of Denmark
Belong to portable coal powder sampler, adopt predicted velocity formula isokinetic sampling method, its main deficiency is to have rotating machinery, complex structure, and the equipment failure rate height only is fit to experimental study.
(3) fixed coal fines sampling apparatus
Now a lot of Installation in Plant fixed coal fines sampling apparatus, it is simple in structure, and is easy to operate, shortcoming is really to realize constant speed, institute's pulverized coal sample of getting is representative poor, and equipment gets rusty easily bite, stopple coupon obstruction and can't use.
Isokinetic sample of pulverized coal has static balance formula and two kinds of methods of predicted velocity formula.
The sampling gun that predicted velocity formula isokinetic sample of pulverized coal method is adopted has single-point elbow type, single-point cab over type and multipoint mode.With the single-point elbow type is example, measure the flow velocity of each sample point in airduct road in advance with pitot tube, and calculate the required sampling flow of each point under the constant speed situation by selected sampling probe internal diameter, sampler is put into one time the airduct road then, the bleeding regulating flow can be realized the isokinetic sampling to the sampling flow that calculates.When adopting restriction device monitoring extraction flow, need carry out the temperature and pressure correction to the survey air quantity, according to a measured wind state parameter, sampling flow is converted to the gas meter position locates extraction flow under the gaseous state parameter.If need will to measure the flow velocity of every bit in advance to multidraw, visible predicted velocity method is a more complicated, calculate loaded down with trivial details, bad adaptability.
The used sampling gun of static balance formula isokinetic sample of pulverized coal has two kinds of elbow type and cab over types.With the elbow type sampling gun is that example is introduced static balance formula isokinetic sample of pulverized coal principle.The structure of elbow type sampling probe as shown in Figure 1.The probe outside has pressure tap and is used to measure the incoming flow static pressure, and the probe inboard has pressure tap and is used for air-flow static pressure in the measuring sonde.If think that sampled fluid is an ideal gas, do not consider the influence of resistance, according to bernoulli's equation:
P in the formula
0, p
nStatic pressure in-incoming flow and the probe, Pa;
w
0, w-speed of incoming flow and suction velocity, m/s;
ρ
0, gas density in ρ-incoming flow and the probe, kg/m
3
Temperature was identical before and after gas was inhaled into, and the inside and outside gas density of probe equates ρ
0=ρ, the static pressure outside static pressure in the sampling probe and probe is equal, i.e. p
0=p
nThe time, can get w by following formula
0=w, promptly suction velocity equates with speed of incoming flow, can realize the isokinetic sampling.Germany import AKOMA isokinetic sample of pulverized coal device promptly adopts top sampling theorem.
But in fact only keep inside and outside static pressure to equate often not reach isokinetic sampling's purpose, reason is that actual airflow all has viscosity, to interior baroport one segment distance, there is every drag losses from the sampling import, though the absolute value of drag losses is very little, be enough to influence isokinetic sampling's accuracy.After considering drag effects, bernoulli's equation becomes:
The every drag losses sum of ∑ Δ p-in the formula, Pa;
Drag overall loss ∑ Δ p is for probe entrance friction loss, along journey fricting resistance loss and the speed loss sum that distributes again.The drag overall loss can take measures suitably to reduce, but inevitable.
Because p is worked as in the existence of drag losses
0=p
nThe time, can get w by following formula
0＞w, promptly suction velocity is less than speed of incoming flow, and its relative variable speed degree has departed from isokinetic sampling's operating mode out and away up to-25.1～-29.5%, causes sampling inaccurate.Only at p
0＞p
nShi Caineng reaches the requirement of constant speed.
For the sampling error that reduces to cause because of drag losses, can reduce flow velocity by increasing the method for probe inlet circulation area, increase static pressure, automatically the drag overall loss of compensation probe inducer.Fig. 2 is the structural drawing of compensation static balance formula isokinetic sampling probe, and then is a diffuser behind inducer, the static pressure p in diffuser
2Static pressure p during greater than no diffuser
n, when the static pressure that increases equals the drag losses of import between static opening, just can realize static pressure zero-bit isokinetic sampling, i.e. p
2-p
0=0 o'clock, w
1=w
0More than analyzing all is to carry out under the condition of gas single-phase flow, but when carrying out the coal dust sampling, actual gas is Dual-Phrase Distribution of Gas olid.Under the Dual-Phrase Distribution of Gas olid state, flow state is very complicated, and it is very difficult wanting to accurately calculate every drag losses and designing corresponding sonde configuration.Even therefore adopt compensation static pressure zero-bit probe, can not guarantee to realize the isokinetic sampling.
In fact, according to formula (2),, promptly guarantee p as long as make the differential pressure imbalance
0-p
n=∑ Δ p just can make w=w
0Thereby, realize the uneven isokinetic sampling of static pressure, but wherein have two key issues to solve:
The one, the accurate numerical value of ∑ Δ p.Out-of-date at pure airflow, can calculate the size that drag overall is lost according to resistance calculation formulae, test findings shows that in normal primary air velocity scope, under the different in flow rate condition, drag overall loss value changes little.When sampling probe was flowed through in actual Dual-Phrase Distribution of Gas olid, drag overall loss ∑ Δ p was different during with pure air, wanted to calculate under the Dual-Phrase Distribution of Gas olid state that drag overall is lost in is very difficult in theory.
The 2nd, how to guarantee that differential pressure keeps identical with drag overall loss all the time.Fact proved, can't meet the demands to have only and adopt advanced control technology and method just can meet the demands by manual shift.
The utility model content
The purpose of this utility model is exactly for addressing the above problem, a kind of two uneven isokinetic sample of pulverized coal of static pressure system that regulates is provided, it is simple in structure, easy to use, can really realize automatic isokinetic sampling, greatly improve the accuracy of coal dust sampling, obtain the test data of true and reliable coal powder density and fineness of pulverized coal, it is with good grounds that the burning adjustment of boiler is accomplished, avoids blindly adjusting.
For achieving the above object, the utility model adopts following technical scheme:
A kind of two uneven isokinetic sample of pulverized coal of static pressure system that regulates, it comprises the static pressure sampler, the static pressure sampler is connected with the electrical heating separation equipment with sample valve by the electrical heating sampling line, and the electrical heating separation equipment is connected with double-adjustment device, and double-adjustment device is connected with compressed gas source; Compressed gas source also is connected with the static pressure sampler by the differential pressure deriving means simultaneously; Controller is controlled double-adjustment device and differential pressure deriving means respectively.
Described differential pressure control device comprises a pair of pressure tube, and compressed gas source is communicated with two pressure tubes by solenoid valve A, solenoid valve B respectively; Two pressure tubes also are connected with the two ends of solenoid valve E by solenoid valve C, solenoid valve D respectively simultaneously, and the two ends of solenoid valve E also are connected with differential pressure transmitter, and differential pressure transmitter is connected with controller.
Described double-adjustment device comprises variable valve A, variable valve B and the air ejector of emanating, and variable valve A links to each other with the air ejector air entry of emanating by sampling line, and variable valve B links to each other with the air ejector inlet of emanating; Variable valve A is connected with controller respectively with variable valve B simultaneously.
A kind of two uneven isokinetic sample of pulverized coal method of static pressure of regulating, its step is:
The 1st step, before the coal dust sampling, electrical heating separation equipment and electrical heating sampling line are carried out electrical heating, keep temperature constant after being heated to design temperature;
The 2nd step fed pressurized air with the static pressure sampler, and pressurized air produces negative pressure after by the air ejector of emanating, and closes sample valve, checks the vacuum of electrical heating separation equipment, prevents that air from leaking;
The 3rd step, after the vacuum inspection finishes, the static pressure sampler is put into the airduct road one time, prepare sampling;
The 4th step, by the needed differential pressure definite value of controller input sampling, open sample valve then, controller begins sampling;
The 5th step, to the baroport purging of pressure tube and static pressure sampler, differential pressure transmitter is imported differential pressure make zero, then static pressure static pressure that sampler is surveyed input differential pressure transmitter is measured; Again purge after the measurement, repeat this process and finish until sampling;
Controller compares transmitter differential pressure signal and input differential pressure definite value, and adopts two differential pressure control modes of regulating:
If the actual measurement differential pressure value shows static pressure sampler pumping velocity less than pipe flow speed greater than the differential pressure definite value, controller sends signal, opens big variable valve A and variable valve B simultaneously, pumping velocity is increased, until returning to the differential pressure definite value;
If the actual measurement differential pressure value shows static pressure sampler pumping velocity greater than pipe flow speed less than the differential pressure definite value, controller sends signal, turns down variable valve A and variable valve B simultaneously, and pumping velocity is reduced, until returning to the differential pressure definite value;
In the 6th step, after the sample time that arrival is set, sampling can stop automatically, and all motorized valves will no longer move; The static pressure sampler is taken out from pipeline, open the electrical heating separation equipment, coal dust is taken out weigh and sieve, finish once complete coal dust sampling work.
In described the 5th step, after the aperture of variable valve A exceeds its range of linearity,, change compressed air pressure, make variable valve A come back to the range of linearity by changing the aperture of variable valve B; After the aperture of variable valve B exceeds its range of linearity, by changing the aperture of variable valve A, change compressed air pressure, make variable valve B come back to the range of linearity.
In described the 5th step, the differential pressure measurement process is: at first close solenoid valve C and solenoid valve D, open solenoid valve A and solenoid valve B purges the baroport on pressure tube and the sampling probe, close solenoid valve A and solenoid valve B after several seconds, open solenoid valve E then, making differential pressure transmitter input differential pressure is zero, closes solenoid valve E then; Open solenoid valve C and solenoid valve D, institute is surveyed static pressure input differential pressure transmitter measure, after tens seconds, close solenoid valve C and solenoid valve D, stop to measure; Open solenoid valve A then and solenoid valve B purges again, repeat said process and finish until sampling.
Coal fines sampling apparatus of the present utility model mainly is made up of coal dust sampling gun, electrical heating stopple coupon, sample valve, electrical heating separation equipment, the air ejector of emanating, pressure tube, differential pressure transmitter, controller, variable valve A, variable valve B, solenoid valve A, solenoid valve B, solenoid valve C, solenoid valve D, solenoid valve E.
The coal dust sampling gun effect be that pulverized coal particle is extracted from Dual-Phrase Distribution of Gas olid on the one hand, be to measure differential pressure signals on the other hand by two baroports of sampling probe.The effect of electrical heating stopple coupon is that coal dust sampling gun and electrical heating separation equipment are coupled together.The effect of sample valve is to open or close sampling line.The effect of electrical heating separation equipment is that pulverized coal particle is separated from Dual-Phrase Distribution of Gas olid.The effect of air ejector of emanating is can produce enough big negative pressure when pressurized air flows through, and the wind powder air-flow in the powder feeding pipes is pumped out and enters atmosphere after pressurized air mixes.The effect of pressure tube is with coal dust static pressure signal that sampling gun is surveyed input differential pressure transmitter.The effect of differential pressure transmitter is that coal dust sampling gun institute error of measurement is pressed conversion of signals is to import controller behind the standard electric signal.The effect of controller is to realize that the differential pressure of coal fines sampling apparatus is controlled automatically and the sequential control of electromagnetic valve group.The effect of variable valve A is a size of accepting controller output signal bleeding regulating amount.The effect of variable valve B is to accept controller output signal to regulate the preceding compressed air pressure size of the air ejector of emanating.The effect of solenoid valve A and solenoid valve B is that pressure tube and baroport are purged, and prevents the pipeline accumulated powder.The effect of solenoid valve C and solenoid valve D is to close with protection differential pressure transmitter outrange to damage when pipeline purges, and opens after purging end, and pipeline is measured in connection normally measures differential pressure transmitter.The effect of electromagnetism E is to measure front opening at differential pressure transmitter to make the both sides static balance at every turn.
The utility model course of work and principle are as described below: before the coal dust sampling, coal dust separation equipment and sampling line are carried out electrical heating, keep temperature constant after being heated to design temperature.Sampler is fed pressurized air, and pressurized air can produce negative pressure after by the air ejector of emanating, and closes sample valve, checks the vacuum of electrical heating coal dust separation equipment, prevents that air from leaking.After the vacuum inspection finishes, the coal dust sampling gun is put into the airduct road one time, prepare sampling.The controller energized by the needed differential pressure definite value of controller picture input isokinetic sampling, is opened sample valve then, begins sample button by controller and begins formal sampling.Controller work mainly comprises sequential control and control automatically.Sequence control procedure is as follows: at first close solenoid valve C and solenoid valve D, open solenoid valve A and solenoid valve B purges the baroport on pressure tube and the sampling probe, close solenoid valve A and solenoid valve B after several seconds, open solenoid valve E then, making differential pressure transmitter input differential pressure is zero, closes solenoid valve E then.Open solenoid valve C and solenoid valve D, institute is surveyed static pressure input differential pressure transmitter measure, after tens seconds, close solenoid valve C and solenoid valve D, stop to measure.Open solenoid valve A then and solenoid valve B purges again, repeat said process and finish until sampling.Automatic control process is as follows: in normal measuring phases, controller is compared transmitter differential pressure signal value with input differential pressure definite value.If the actual measurement differential pressure value, shows sampling gun probe pumping velocity greater than the differential pressure definite value less than pipe flow speed, controller sends signal, opens big variable valve A and variable valve B simultaneously, and pumping velocity is increased, and the actual measurement differential pressure value can diminish gradually until returning to the differential pressure definite value; If the actual measurement differential pressure value, shows sampling gun probe pumping velocity less than the differential pressure definite value greater than pipe flow speed, controller sends signal, turns down variable valve A and variable valve B simultaneously, and pumping velocity is reduced, and the actual measurement differential pressure value can become gradually greatly until returning to the differential pressure definite value.The differential pressure definite value is generally very little, and it is very big accurately to control difficulty, has therefore adopted two adjusting differential pressure control modes, i.e. while regulating and controlling valve A and variable valve B.After the aperture of variable valve A exceeds its range of linearity, can change compressed air pressure by changing the aperture of variable valve B, make variable valve A come back to the range of linearity, so just greatly improved the differential pressure control accuracy.After setting fixed sample time, sampling can stop automatically, and all motorized valves will no longer move.The coal dust sampling gun is taken out from pipeline, open the electrical heating separation equipment, coal dust is taken out weigh and sieve, just finished once complete coal dust sampling work.
The beneficial effects of the utility model are:
1 has proposed the uneven isokinetic sampling's new method of static pressure, has broken through the limitation that traditional static balance isokinetic sampling method exists, and has solved the big problem of sampling error that traditional sampling method causes because of drag losses, has greatly improved sampling precision.
2 by two differential pressure control technologys of regulating, and have improved the differential pressure control accuracy, have satisfied the requirement of the uneven isokinetic sampling of static pressure to differential pressure control, and have developed the new coal powder automatic sampling device, have filled up domestic blank on this device.
3 new type auto coal dust automatic sampling device control function are comprehensive, are easy to expand applied range.Applicable to the sampling of static balance formula single-point coal dust, prediction type single-point and the sampling of multiple spot coal dust; Applicable to the coal fines sampling apparatus that adopts different separate modes such as bag-type dust and cyclonic separation dedusting.
4 control modes are flexible, regulate parameter and can artificially regulate.For a change regulate parameter by the people, can be optimized, can be used as the standard device of other type coal dust sample apparatus of verification control mode.
5 automatic control sections and sampling part are arranged apart, have alleviated the volume and weight of coal dust sample apparatus greatly, have alleviated operating personnel's working strength.
6 can satisfy the requirement of the uneven isokinetic sampling's method of static pressure to differential pressure control.When carrying out the coal dust sampling at the scene,, guarantee that the control differential pressure for demarcating the drag overall loss that draws, can realize the isokinetic sampling by the uneven sampler of two adjusting static pressure.
Description of drawings
Fig. 1 is a static balance formula sampling probe;
Fig. 2 is compensation static balance probe;
Fig. 3 is two uneven isokinetic sampling's system schematic of static pressure of regulating.
Wherein, 1 static pressure sampling gun, 2 electrical heating sampling lines, 3 sample valves, 4 electrical heating separation equipments, 5 variable valve A, 6 air ejectors of emanating, 7 variable valve B, 8 controllers, 9 differential pressure transmitters, 10 solenoid valve A, 11 solenoid valve B, 12 solenoid valve C, 13 solenoid valve D, 14 solenoid valve E, 15 pressure tubes, 16 airduct roads.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
Among Fig. 3, it comprises static pressure sampling gun 1, and static pressure sampling gun 1 is connected with electrical heating separation equipment 4 with sample valve 3 by electrical heating sampling line 2, and electrical heating separation equipment 4 is connected with double-adjustment device by sampling line, and the double-adjustment device inlet is connected with compressed gas source; Compressed gas source also is connected with static pressure sampling gun 1 by the differential pressure deriving means simultaneously; Controller 8 is controlled double-adjustment device and differential pressure deriving means respectively.
Described differential pressure deriving means comprises a pair of pressure tube 15, and compressed gas source is communicated with two pressure tubes 15 by solenoid valve A10, solenoid valve B11 respectively; Two pressure tubes 15 also are connected with the two ends of solenoid valve E14 by solenoid valve C12, solenoid valve D13 respectively simultaneously, and the two ends of solenoid valve R14 also are connected with differential pressure transmitter 9, and differential pressure transmitter 9 is connected with controller 8.
Described double-adjustment device comprises variable valve A5, variable valve B7 and the air ejector 6 of emanating, and variable valve A5 links to each other with air ejector 6 air entries of emanating by sampling line, and variable valve B7 links to each other with air ejector 6 inlets of emanating; Variable valve A5 is connected with controller 8 respectively with variable valve B7 simultaneously.
A kind of two uneven isokinetic sample of pulverized coal method of static pressure of regulating, its step is:
The 1st step, before the coal dust sampling, electrical heating separation equipment 4 and electrical heating sampling line 2 are carried out electrical heating, keep temperature constant after being heated to design temperature;
The 2nd step fed pressurized air with static pressure sampling gun 1, and pressurized air produces negative pressure by air ejector 6 backs of emanating, and closes sample valve 3, checks the vacuum of electrical heating separation equipment 4, prevents that air from leaking;
The 3rd step, after the vacuum inspection finishes, static pressure sampling gun 1 is put into airduct road 16 one time, prepare sampling;
The 4th step, by the needed differential pressure definite value of controller 8 input samplings, open sample valve 3 then, controller 8 begins sampling;
The 5th step, to the baroport purging of pressure tube 15 and static pressure sampling gun 1, differential pressure transmitter 9 input differential pressures are made zero, then static pressure sampling gun 1 static pressure of surveying input differential pressure transmitter 9 is measured; Again purge after the measurement, repeat this process and finish until sampling;
Controller 8 compares transmitter differential pressure signal and input differential pressure definite value, and adopts two differential pressure control modes of regulating:
If the actual measurement differential pressure value shows static pressure sampling gun 1 pumping velocity less than pipe flow speed greater than the differential pressure definite value, controller 8 sends signal, opens big variable valve A5 and variable valve B7 simultaneously, pumping velocity is increased, until returning to the differential pressure definite value;
If the actual measurement differential pressure value shows static pressure sampling gun 1 pumping velocity greater than pipe flow speed less than the differential pressure definite value, controller 8 sends signal, turns down variable valve A5 and variable valve B7 simultaneously, and pumping velocity is reduced, until returning to the differential pressure definite value;
In the 6th step, after the sample time that arrival is set, sampling can stop automatically, and all motorized valves will no longer move; Static pressure sampling gun 1 is taken out from pipeline, open electrical heating separation equipment 4, coal dust is taken out weigh and sieve, finish once complete coal dust sampling work.
In described the 5th step, after the aperture of variable valve A5 exceeds its range of linearity,, change compressed air pressure, make variable valve A5 come back to the range of linearity by changing the aperture of variable valve B7; After the aperture of variable valve B7 exceeds its range of linearity, by changing the aperture of variable valve A5, change compressed air pressure, make variable valve B7 come back to the range of linearity.
In described the 5th step, the differential pressure measurement process is: at first close solenoid valve C12 and solenoid valve D13, opening solenoid valve A10 and solenoid valve B11 purges the baroport on pressure tube 15 and the static pressure sampling gun 1, close solenoid valve A10 and solenoid valve b11 after several seconds, open solenoid valve E14 then, making differential pressure transmitter 9 input differential pressures is zero, closes solenoid valve E14 then; Open solenoid valve C12 and solenoid valve D13, institute is surveyed static pressure input differential pressure transmitter 9 measure, after tens seconds, close solenoid valve C12 and solenoid valve D13, stop to measure; Open solenoid valve A10 then and solenoid valve B11 purges again, repeat said process and finish until sampling.
The differential pressure definite value can adopt the way head it off that test is demarcated in the step 4: promptly allow the pulverized coal particle of the known fineness air pipe line of flowing through a time, carry out coal dust sampling and analytic sample fineness under different differential pressures, the differential pressure under sample fineness and the immediate operating mode of raw sample fineness is drag overall loss ∑ Δ p under the Dual-Phrase Distribution of Gas olid state.
Claims (3)
1. regulate the uneven isokinetic sample of pulverized coal of static pressure system for one kind pair, it is characterized in that, it comprises the static pressure sampler, the static pressure sampler is connected with the electrical heating separation equipment with sample valve by the electrical heating sampling line, the electrical heating separation equipment is connected with double-adjustment device, and double-adjustment device is connected with compressed gas source; Compressed gas source also is connected with the static pressure sampler by the differential pressure deriving means simultaneously; Controller is controlled double-adjustment device and differential pressure deriving means respectively.
2. the two uneven isokinetic sample of pulverized coal of static pressure system that regulates as claimed in claim 1 is characterized in that described differential pressure deriving means comprises a pair of pressure tube, and compressed gas source is communicated with two pressure tubes by solenoid valve A, solenoid valve B respectively; Two pressure tubes also are connected with the two ends of solenoid valve E by solenoid valve C, solenoid valve D respectively simultaneously, and the two ends of solenoid valve E also are connected with differential pressure transmitter, and differential pressure transmitter is connected with controller.
3. the two uneven isokinetic sample of pulverized coal of static pressure system that regulates as claimed in claim 1, it is characterized in that, described double-adjustment device comprises variable valve A, variable valve B and the air ejector of emanating, and variable valve A links to each other with the air ejector air entry of emanating by sampling line, and variable valve B links to each other with the air ejector inlet of emanating; Variable valve A is connected with controller respectively with variable valve B simultaneously.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206170732U CN201852724U (en) | 2010-11-22 | 2010-11-22 | Double-regulating static and unbalanced constant-speed coal dust sampling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206170732U CN201852724U (en) | 2010-11-22 | 2010-11-22 | Double-regulating static and unbalanced constant-speed coal dust sampling system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201852724U true CN201852724U (en) | 2011-06-01 |
Family
ID=44095113
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010206170732U Expired - Fee Related CN201852724U (en) | 2010-11-22 | 2010-11-22 | Double-regulating static and unbalanced constant-speed coal dust sampling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201852724U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102564502A (en) * | 2012-01-12 | 2012-07-11 | 山东电力研究院 | Method and device for measurement of concentration and flow of pulverized coal |
-
2010
- 2010-11-22 CN CN2010206170732U patent/CN201852724U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102564502A (en) * | 2012-01-12 | 2012-07-11 | 山东电力研究院 | Method and device for measurement of concentration and flow of pulverized coal |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102095605B (en) | Double-regulation static pressure unbalanced coal dust constant-speed sampling system and method of system | |
| CN202033058U (en) | Real-time measuring device for air supply flow of boiler | |
| CN201434784Y (en) | Novel automatic coal powder constant-speed sampling device | |
| CN201555612U (en) | Self-deashing rectifier type cross section air quantity and air speed measuring device | |
| CN105510625A (en) | Wind speed measurement system and method of pulverized-coal-included airflow of pulverized coal feeding pipe of coal-fired boiler | |
| CN110487508A (en) | A kind of experimental provision for research level pipe gas-liquid two-phase spiral flow | |
| CN112763388A (en) | Online monitoring system and method for concentration deviation between coal mill powder conveying pipelines | |
| CN109539248A (en) | A kind of burner air distribution device and air distribution method | |
| CN113607227A (en) | Non-uniform flow field gas flow measurement method and system | |
| CN201828487U (en) | Dynamic performance testing device of filtering materials at high temperature | |
| CN103807852B (en) | The secondary-wind distributing device of pulverized-coal fired boiler and Secondary Air air distribution method | |
| CN205607744U (en) | Flue gas mixing arrangement and flue gas measurement system | |
| CN201852724U (en) | Double-regulating static and unbalanced constant-speed coal dust sampling system | |
| CN206876433U (en) | The portable anti-blocking coal dust constant-speed sampling device of non-transformer | |
| CN107664588A (en) | Isokinetic sample of pulverized coal method and sampler | |
| CN2911458Y (en) | Secondary air on-line monitoring system for boiler of power station | |
| CN203672406U (en) | Wind-pulverized coal on-line monitoring system used for boiler | |
| CN113760018A (en) | Power station boiler balanced combustion optimization method based on data driving | |
| CN201716216U (en) | Portable type pulverized coal sampling device | |
| CN207336148U (en) | Isokinetic sample of pulverized coal device | |
| CN103822669A (en) | Pulverized coal online monitoring method of boiler | |
| CN202304962U (en) | Air tunnel type speed-area-method air flow calibration device | |
| CN107192846A (en) | A kind of anti-blocking resistant wear wind speed and wind system for measuring quantity | |
| CN201876379U (en) | Fully-automatic coal dust sampler | |
| CN205156965U (en) | Wind powder blending transportation medium concentration, online static measurement system of velocity of flow |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: STATE ELECTRIC NET CROP. Effective date: 20130311 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20130311 Address after: 250002 Ji'nan City Central District, Shandong, No. 2 South Road, No. 500 Patentee after: Shandong Research Inst. of Electric Power Patentee after: State Grid Corporation of China Address before: 250002 Ji'nan City Central District, Shandong, No. 2 South Road, No. 500 Patentee before: Shandong Research Inst. of Electric Power |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110601 Termination date: 20191122 |