CN204705386U - A kind of water level measurement system for boiler-steam dome - Google Patents
A kind of water level measurement system for boiler-steam dome Download PDFInfo
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- CN204705386U CN204705386U CN201520423824.XU CN201520423824U CN204705386U CN 204705386 U CN204705386 U CN 204705386U CN 201520423824 U CN201520423824 U CN 201520423824U CN 204705386 U CN204705386 U CN 204705386U
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Abstract
The utility model relates to a kind of water level measurement system for boiler-steam dome, comprises level measurement device, thermostat, all dasymeter, pressure samples door, pressure unit, temperature transmitter, differential pressure transmitter and omnidistance gauge glass; Vapour side door and the water side door of described level measurement device and boiler-steam dome are connected, and are connected with differential pressure transmitter by thermostat, are also connected with pressure unit by pressure samples door; Described thermostat is connected with equal dasymeter, is connected with temperature transmitter; Described pressure unit, temperature transmitter, differential pressure transmitter are all connected with omnidistance gauge glass.The condensate water that in the utility model, lateral steam tube door produces also flows into level measurement device, with the condensate water afflux common stream back-steam bag in device; Thermal loss is few, improves device bottom water temperature, improves measuring accuracy.The utility model device volume is little, lightweight, has reclaimed heat.
Description
Technical field
The utility model relates to boiler drum water level measurement field, specifically a kind of water level measurement system dynamically accurately can measuring water level in drum in real time.
Background technology
Drum level measurement technology, relate to thermodynamics, thermal conduction study, fluid mechanics, the mechanics of materials, thermal measurement technology, Error Theory etc. are multidisciplinary, be polygamma function, many independents variable, dynamically, in real time, the composite measurement process of the physical quantity of transition.In measuring process, mixed many uncertain additive errors, stochastic error be difficult to be separated.
Over the years, drum level measurement value, do not have " standard metering transmission ", steam water-level table does not have precision setting.Due to industrial needs, the gauge glass of various novel measuring principle constantly occurs, whole Yin Gaowen, high pressure, thermodynamic parameter working condition are severe, external influence factor is more, uncertain, the perishable leakiness of the water level error of indication, there is no continuous quantity, easily fault, easily stop using, maintenance is large, the life-span is short, easy radiation, high in cost of production reason could not be promoted.
Past level measuring many employings drum external hot jacket water level balance container or simple single chamber water level balance container.When gauge glass water level indicating value is unpunctual, namely adjust with the linear adjusting gear of differential pressure transmitter zero-bit, differential pressure transmitter proof test value is changed after adjustment, there is dead band in work differential pressure range, overflowing appears in range electricity, in maintenance verification, before differential pressure transmitter is adjusted, adjust rear reading not to be inconsistent, not only change the thermodynamic relation characteristic of water level and differential pressure, calibration tails was simultaneously lost efficacy.
Utility model content
The utility model object is to provide that one can adapt to pressure furnace, UHV (ultra-high voltage) stove steam water-level table open stove just accurate, non-maintaining, need not adjust, gauge glass runtime value conforms to gauge glass proof test value, and in sliding parameter operation, safety door course of action, normally can show the water level measurement system of water level value in drum.
The technical scheme that the utility model is adopted for achieving the above object is: a kind of water level measurement system for boiler-steam dome, comprises level measurement device, thermostat, all dasymeter, pressure samples door, pressure unit, temperature transmitter, differential pressure transmitter and omnidistance gauge glass; Vapour side door and the water side door of described level measurement device and boiler-steam dome are connected, and are connected with differential pressure transmitter by thermostat, are also connected with pressure unit by pressure samples door; Described thermostat is connected with equal dasymeter, and equal dasymeter is connected with temperature transmitter; Described pressure unit, temperature transmitter, differential pressure transmitter are all connected with omnidistance gauge glass.
Described level measurement device is concentric circles conjuncted structure, is provided with the pipe with its concentric bottom the cylindrical container of sealing, and pipe bottom leans out cylindrical container, and top is positioned at cylindrical container inside; Pipe Inner Constitution negative pressure chamber; Cylindrical container internal diameter and pipe external diameter form plemum; Described cylindrical container top is provided with into steam ports, is connected with the vapour side door of boiler-steam dome by lateral steam tube; The bottom of pipe is provided with water inlet, is connected with the water side door of boiler-steam dome by horizontally disposed water side pipe; The bottom of cylindrical container bottom and pipe is respectively equipped with malleation sample tap, sampling below atmospheric pressure mouth, is connected with thermostat.
The internal diameter of described pipe is 2 times of water side pipe internal diameter.
Described pipe top is equal with omnidistance gauge glass range to the vertical height in water side pipe axle center.
Described thermostat comprises positive-pressure constant-temperature device and negative pressure thermostat, and be closed container, top is provided with entrance, and bottom is provided with outlet; Positive-pressure constant-temperature device entrance is connected with cylindrical container malleation sample tap, exports and is connected with differential pressure transmitter by equal dasymeter; Negative pressure thermostat entrance is connected with the sampling below atmospheric pressure mouth of pipe, and outlet is connected with differential pressure transmitter.
Described equal dasymeter comprises four platinum resistance, to be evenly fixed on from top to bottom on steel pipe that positive-pressure constant-temperature device is connected with differential pressure transmitter and to be positioned at the vertical component in positive-pressure constant-temperature device exit; The platinum resistance series connection of two odd number orders, after forming parallel circuit, is connected with temperature transmitter with the platinum resistance of other two even number sequential series.
The positive and negative pressure input end of described differential pressure transmitter is connected with malleation gas collector and negative pressure gas collector respectively by positive-pressure door, negative pressure door; Described malleation gas collector and negative pressure gas collector are closed container, and top is provided with outlet, and bottom is provided with entrance; Described malleation gas collector is connected with positive-pressure constant-temperature device, negative pressure thermostat respectively with the entrance of negative pressure gas collector, and is connected with positive-pressure door, negative pressure door respectively, is also connected with malleation sewage door and negative pressure sewage door respectively; The outlet of described malleation gas collector and negative pressure gas collector is connected with exhaust valve respectively.
The utility model has following beneficial effect and advantage:
1. the utility model device structure is simple, because of being drum external, visual, can survey, and checks and facilitates; By checking whether the temperature of thermostat exceedes room temperature, can failure judgement fast: thermostat temperature exceedes room temperature, then can be judged as the pressure transmission piping leakage of water level measurement system at once, just can process in time.
2. the concentric circles conjuncted structure of level measurement device inside of the present utility model does not have weld bond, has eradicated interior leakage fault, the life-span same with boiler, and can realize failure-free operation.
3. in the utility model, lateral steam tube tilts to plemum direction, and the condensate water that lateral steam tube, door produce flows into level measurement device, jointly flows back to drum by water side pipe with the condensate water afflux in device; Thermal loss is few, improves device bottom water temperature, improves water level measurement accuracy.The utility model device volume is little, lightweight, has reclaimed heat.
4. the internal diameter of the utility model pipe used is 2 times of water side pipe internal diameter, makes measurement water-level fluctuation value < ± 5mm.
5. water level measurement system work is accurate, stable, reliable, reproducible, and equipment compatibility is strong, implement device data normalization.
6. drum external, verification door is installed in the conjuncted design of structure concentric circles, water side pipe additional, and achieving water level measurement system water level indicating value can full scale water column precision checking.And under blowing out overhaul, capital construction moderate condition, all can carry out system check to water level measurement system.
7. adopt this water level measurement system, many gauge glass water level indicating value differences of every platform boiler-steam dome are less than 30mm.
Accompanying drawing explanation
Fig. 1 is water level measurement system structural representation of the present utility model;
Wherein, 1 level measurement device, 2 positive-pressure constant-temperature devices, 3 negative pressure thermostats, 4 equal dasymeters, 5 malleation gas collectors, 6 negative pressure gas collectors, 7 verification doors, 8 pressure samples doors, 9 pressure units, 10 temperature transmitters, 11 differential pressure transmitters, 12 omnidistance gauge glasss, 13 temperature alarms;
Fig. 2 is the method for calibration schematic diagram of water level measurement system;
Fig. 3 is the Signal transmissions schematic diagram of CPU in omnidistance gauge glass.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
The utility model site test on 220t/h pressure furnace, 670t/h UHV (ultra-high voltage) stove has tried out this Drum Level Measurement System.Operating ambient temperature 5-90 degree.Water level measurement system comprises level measurement device 1, thermostat, all dasymeter 4, pressure samples door 8, pressure unit 9, temperature transmitter 10, differential pressure transmitter 11 and omnidistance gauge glass 12; Vapour side door and the water side door of described level measurement device 1 and boiler-steam dome are connected, and be connected, be also connected with pressure unit 9 by pressure samples door 8 by thermostat with differential pressure transmitter 11; Described thermostat is connected with equal dasymeter 4, is connected with temperature transmitter 10; Described pressure unit 9, temperature transmitter 10, differential pressure transmitter 11 are all connected with omnidistance gauge glass 12.As shown in Figure 1.
1, level measurement device is concentric circles conjoined structure, and airtight hollow circular cylinder container bottom is provided with the pipe with its concentric; Pipe Inner Constitution negative pressure chamber, top end opening is positioned at cylindrical container inside, and bottom leans out cylindrical container; Cylindrical container inwall and circular tube external wall form malleation (reference water) room.Cylindrical parts is inserted in cylindrical container, welds in cylindrical container outside with the junction of cylindrical container, ensures that plemum is inner without weld bond.
Level measurement device has two entrances, two outlets; Entrance be cylindrical container top be provided with enter steam ports, be connected with the vapour side door of boiler-steam dome by lateral steam tube, lateral steam tube tilts to plemum, and the condensate water be convenient in pipe flows to plemum; Another entrance is the water inlet of pipe bottom, is connected with the water side door of boiler-steam dome by water side pipe; When vapour side door and water side door are opened, level measurement device and drum constitute carbonated drink linker, can react the position, disengagement surface in drum normally.
Full water steel seal is carved with in cylindrical container outside, and the pipe top in steel seal and plemum is with high.To represent during normal work in plemum pipe periphery be full of water and in negative pressure chamber the water surface lower than overwater service in plemum.Circular tube external is carved with zero level steel seal, and in zero level steel seal and drum, zero level is with high.
Cylindrical container bottom is provided with outlet, is connected with positive-pressure constant-temperature device by S bend pipe.The outlet extension of S bend pipe and the corner, bottom of S bend pipe constitute horizontal tilt steel pipe, and tilt to positive-pressure constant-temperature device entrance, degree of tilt is 1:100; Horizontal tilt length of tube is about 400mm, 40mm place above the zero level steel seal of positive-pressure constant-temperature device inlet tube center line outside pipe.Adopt S forward voltage diode to reduce the height of plemum, in plemum, reference water-mass density heat dynamically delays reducing, and improves the changing sensitivity of malleation reference water-mass density, makes measured differential pressure value more accurate.
The bottom of pipe is also provided with water delivering orifice as sampling below atmospheric pressure mouth, is connected with negative pressure thermostat by the steel pipe of horizontal positioned.Axle center and the water side pipe axle center of this steel pipe are contour.
Large 2.5 times of plemum reference water-cooled area ratio heating surface (area) (HS, can obtain stable single-phase liquid reference water quality, namely can not there is boiling phenomenon in plemum reference water.
represent the volume of hypothesis without malleation indoor water during pipe,
represent volume shared by pipe in plemum, D and d represents plemum internal diameter and negative pressure chamber's external diameter respectively, and L ' is the height of water column in plemum.
Plemum reclaims condensate water and continuously flows into negative pressure chamber, improves negative pressure chamber's bottom reference coolant-temperature gage.Compare with thermal sleeve water level balance container and reduce level measurement device size, weight, reduce metal fever capacity, improve heat and dynamically delay characteristic, improve level measuring sensitivity, negative pressure chamber's internal diameter obtains expansion simultaneously, decreases water-level fluctuation.Eliminate thermal sleeve equalizing reservoir heating decline door and 10m downtake, eradicated decline door aperture difference and caused the operate miss that steam water-level indicating value is different.
In addition, negative pressure chamber's actual internal area equals 4 with the ratio of water side pipe actual internal area, and water level continuous oscillation ripple in the drum that effectively inhibit 4 cycle per seconds, serves damping filter action.
Negative pressure chamber latus rectum D=Ф 40mm; Water side pipe latus rectum d=Ф 20mm;
Section ratio K=π D
2/ 4 ÷ π d
2/ 4=D
2÷ d
2=Ф 40
2÷ Ф 20
2=1600 ÷ 400=4.
2, thermostat has two, and be closed hollow circular cylinder closed container, top is provided with entrance, and bottom is provided with outlet; Positive-pressure constant-temperature device entrance is connected with cylindrical container malleation sample tap by S malleation reference tube (S shape pipe): S malleation reference tube exports the pipe extending to form horizontal tilt, S malleation reference tube entrance is connected with cylindrical container malleation sample tap, and the outlet of horizontal tilt pipe is connected with positive-pressure constant-temperature device entrance; The outlet of positive-pressure constant-temperature device is connected with malleation gas collector and malleation sewage door by pressure tube; Negative pressure thermostat entrance is connected with the sampling below atmospheric pressure mouth of pipe, exports and is connected with negative pressure gas collector, negative pressure sewage door by another pressure tube.
3, temperature alarm is two, is located at thermostat top respectively, for reach when the temperature of reference water in thermostat temperature height report to the police setting value (as 80 degree) time, output contact signal be used for optoacoustic warning.
4, equal dasymeter: the pressure tube that positive-pressure constant-temperature device outlet place connects evenly is fixed with four platinum resistance (temperature sensor) from top to bottom with larynx hoop, this pressure tube one section of export at positive-pressure constant-temperature device be vertical setting.In parallel again after two series connection of odd number order, two series connection of even number order, the series connection direction of platinum resistance and the vertically parallel of pressure tube.When the pipeline internal upper part in positive-pressure constant-temperature device exit is different with the coolant-temperature gage of bottom, equally distributed like this platinum resistance can gather the water temperature of diverse location, after in parallel, the temperature value corresponding to resistance of gained is average temperature value, is input to the CPU in omnidistance gauge glass, for calculating water level in real time.
5, gas collector: the positive and negative pressure side pressure transmission pipeline peak of differential pressure transmitter installs gas collector additional, realizes automatically collecting air.Gas collector has two, and be hollow closed container, top is provided with outlet, and bottom is provided with entrance; Malleation gas collector is connected with positive-pressure constant-temperature device, negative pressure thermostat respectively with the entrance of negative pressure gas collector, and is connected with differential pressure transformer respectively by positive-pressure door, negative pressure door; Balance gate is connected with between the positive and negative pressure side of differential pressure transmitter; The outlet of malleation gas collector and negative pressure gas collector is connected with positive pressure ventilation door, negative pressure exhaust door (for differential pressure transmitter deaeration when to drop in front-seat exception pipeline air or safeguard) respectively.
When boiler water filling igniting, drum pressure are to 0.5Mpa, intrasystem gas collects emptying by gas collector, and to be drained dirt in pipeline by sewage door, after exhaust, blowdown, maintenance work terminates, and can drop into gauge glass measurement water level.
6, in level measurement device, the water inlet of pipe is connected with the water side door of boiler-steam dome by water side pipe; Other two can be connected by four-way and connect mouth Bonding pressure sampling gate and verification door respectively.Pressure samples door and verification door are and cut valve.Pressure samples door is connected with pressure unit, for directly measuring saturation pressure in drum, has eradicated the level measuring error that pressure pressure tube is introduced because of elevation difference; Verification door is for carrying out water level measurement system verification during shutdown maintenance or in capital construction.
7, water level measurement system checker: door place is connected with four-way in verification, and three-way interface is connected with respectively and adds water valve, wicket and glass tube in addition; Glass tube is vertically arranged, contour with water injecting tank.For carrying out Drum Level Measurement System verification.
For a water level measurement method for the water level measurement system of boiler-steam dome, specific as follows:
Water level measurement system principle of work is as follows:
Level measurement device and drum connect into vapour, water Communicating device, the absolute altitudes such as the water surface in drum are reflected in the negative pressure chamber of level measurement device, and fix the water surface with top plemum and carry out water surface differential pressure and compare, pressure differential (water column pressure) between the plemum water surface formed and negative pressure chamber's water surface, just from drum high static pressure Ρ
s=15.3MPa=1530000mmH
2be separated in O numerical value, and deliver to differential pressure transmitter and convert current signal directly proportional with water column micro-pressure to, namely complete drum (thick 100mm steel plate) interior water level, differential pressure, electrical measurement conversion work.
When in drum, working pressure reaches 15.3MPa, in saturation water, saturated vapor, drum, vapour side metallic surface temperature is all 344 DEG C, and saturated water density is 596kg/m
3, but ρ ' in differential pressure transmitter proof test value
20C=1000kg//m
3, be standard chamber proof test value.Saturated vapor density is 101kg//m
3, but ρ in differential pressure transmitter proof test value "
20C=0kg//m
3it is standard chamber proof test value.In dynamic operation, (ρ ', ρ ") changes with drum operating pressure; when drum pressure rises; saturated water density value declines with function curve, and saturated vapor density value rises with function curve, adds the complicacy of level measuring middle water level and difference pressure relationships.So saturation pressure, saturation temperature compensation must be carried out, namely by drum saturation pressure force value Ps, drum saturation temperature t to drum level measurement
simplement to compensate.
In fluid mechanics, water is liquid incompressible fluid.But in thermodynamics, water not still compressible fluid, maximum volume compression >-0.8%, be heated and also can produce very large thermal expansion, maximum volume swell value >+4.1%, the change of room temperature reference water-mass density, disturbs the single-valued relationship of steam water-level and differential pressure, needs to carry out pressure, temperature compensation to room temperature reference water-mass density.
When opening vapour, water side door, in drum, saturated vapor condenses into saturation water by vapour side door flows into level measurement device, malleation reference water surface self-assembling formation, in drum, saturation water flows into negative pressure chamber by water side door, negative pressure chamber's water surface is identical with the water surface in drum, the relation of water level and differential pressure starts to be formed, and when level measurement device each point temperature reaches steady-working state, relation and the proof test value of the differential pressure that level measurement device produces and water level are asymptotic.Gauge glass starts normally to show water level value in drum.
Differential pressure during by working to level measurement device, drum pressure, room temperature is measured, three amounts are input to the large scale integrated circuit CPU computing center in omnidistance gauge glass, computing is carried out with omnidistance water level compensation formula, level measurement device characteristic coefficient L is added in computing, complete testing laboratory to on-the-spot nominal parameter checking data and the seamless link running numerical value, eliminate additive error, uncertain error, stochastic error, eradicate service data dead angle, dead band, overflow defect, achieve and open stove just standard, disposable adjustment drops into, non-maintaining, adjustment is no longer needed in operation.
The water column differential pressure value that level measurement device produces, the i.e. differential pressure of the plemum water surface and negative pressure chamber's water surface, convert the directly proportional current signal with differential pressure to through differential pressure transmitter, convert directly proportional voltage signal (corresponding Δ P) to through current-to-voltage convertor, deliver to CPU;
In drum, saturation pressure converts the directly proportional current signal with pressure to through pressure unit, converts direct proportion voltage signal (corresponding Ps) to, deliver to CPU through current-to-voltage convertor;
Ambient temperature converts resistance signal to through platinum-resistance thermometer, through temperature transmitter the just proportional current signal of resistance signal conversion, converts directly proportional voltage signal (corresponding t to through current-to-voltage convertor
a), deliver to CPU;
As shown in Figure 3, three d. c. voltage signal Δs P, Ps, t
ainput computing machine to carry out real-time dynamic operation by water level compensation calculation formula and obtain real-time height of water level simultaneously.
Omnidistance water level compensation formula:
h＝[H
M(ρ
ta-ρ″)-L(ρ
ta-ρ′)-(q-H
M/2)(ρ
ta-ρ′)-ΔP]/(ρ′-ρ″)-B mm
Wherein, h is steam water-level height, H
mfor omnidistance gauge glass range, B is the setting constant of zero level point, i.e. 1/2 gauge glass range; Δ P is the differential pressure value that in the level measurement device measured of differential pressure transmitter, the positive and negative pressure chamber water surface produces, and q is gauge glass water level range choosing coefficient, is 0 ~ H
m; Room temperature reference water-mass density ρ
ta, saturated water density ρ ', saturated vapor density p is " all according to the ambient temperature value t that the saturation pressure force value Ps of pressure transmitter measurement and equal dasymeter measure
aobtained by inquiry steam parameter table; Wherein steam parameter table comprises in " water and steam nature parameters handbook ": the thermodynamics basic parameter of the thermodynamics basic parameter (pressing force arrangement) of saturation water and saturated vapour, water and superheated vapor.Therefore, by the saturation temperature t of saturation pressure force value Ps and correspondence thereof
simplement compensation to carry out tabling look-up obtaining ρ
ta, ρ ' and ρ ", substitute into omnidistance water level compensation formula, achieve the compensation of pressure and temperature.
L＝(2ρ
ta-ρ′-ρ″-ρ
20℃)/2(ρ
ta-ρ′)×H
M
In formula, L is level measurement device dynamic characteristic coefficients, ρ
20 DEG Cfor the density of water column 20 DEG C of water during testing laboratory's verification differential pressure transmitter, ρ
tathe room temperature reference water-mass density kg/m that the ambient temperature value measured for equal dasymeter is corresponding
3.
In addition, in h and L two formula, ρ
tacan adopt room temperature water density formula, eradicate the gradient error of list data, the room temperature water density accuracy that improve data seamless connection reaches ± 0.2kg/m
3; Room temperature water density formula is as follows:
ρ
ta＝1001.13+0.44(P+0.1)-0.0171×t
a 1 . 7kg/m
3
The scope of application: 1. saturation pressure scope: 0MPa<Ps<21.9MPa;
2. ambient temperature scope: 20 DEG C of <t
a<90 DEG C;
3. ρ
taformulae discovery precision: ± 0.2kg/m
3.
After omnidistance gauge glass computer chip CPU calculates, export 7 dynamically amounts in real time by omnidistance gauge glass, wherein:
1) 5 amounts are shown: water level value in h mm drum.Δ P mm H
2differential pressure value in O level measurement device.
P
ssaturation pressure force value in MPa drum.T
ssaturation temperature value in DEG C drum.
T
adEG C ambient temperature value.
2) steam water-level value: water level value in hmm Bar graphic display drum.
3) export and steam water-level directly proportional water level current signal Ih mA.
The built-in CPU of omnidistance gauge glass, for receiving differential pressure, pressure and temperature information that differential pressure transmitter, pressure unit and temperature transmitter are changed through current-to-voltage convertor, and by water level value in calculation process output drum etc., is shown by screen.Its level scale range value being provided with gauge glass equals the vertical height of full water steel seal to water side pipe axle center.
For the present embodiment, level scale range value (design load) H of omnidistance gauge glass
mfor ± 320mm, differential pressure transmitter range differential pressure value (proof test value) Δ P
mfor 640mmH
2o, level measurement device measurable process and full water steel seal are 640mm to the vertical height e in water side pipe axle center, and three Ge Liang units are different, but absolute value is equal, realizes checking data (H
m, Δ P
m, e) three value overlap.Data mapping table: Δ P, I
Δ P, V
Δ P, h, Ih (run differential pressure, differential pressure electric current, differential pressure voltage, level scale, output water level electric current).
Under atmospheric pressure, checking data (H
m, Δ P
m, e) three value overlap, checking data value five correspondence (Δ P, I
Δ P, V
Δ P, h, Ih) see the following form:
Table one
| ΔP mmH 2O | I ΔP mA | V ΔP V | h mm | Ih mA |
| 0 | 4 | 1 | +320 | 20 |
| 320 | 12 | 3 | 0 | 12 |
| 640 | 20 | 5 | -320 | 4 |
As shown in Figure 2, water level measurement system method of calibration:
In maintenance, capital construction, in drum, pressure is atmospheric pressure, and level measurement device possesses outer water filling condition, and the method for water level measurement system and available additional water filling, verifies water level measurement system.
Outer the injecting process:
Water injection equipment: water filling Plastic Drum 10L (liter), glass tube 1 is contour with water injecting tank.Four-way connects water filling door respectively, adds water valve, wicket, glass tube.Discharge water Plastic Drum 10L (liter).
1, the injecting process operation steps
1) close water side door, open vapour side door.
2) open verification door, close wicket.
3) open and add water valve, water filling in level measurement device.
4) when in glass tube, water surface rising reaches full water steel seal place outside plemum, plemum, negative pressure chamber's water surface also reach full water steel seal place, represent that now pressure reduction is zero; The pressure reduction of measurement is delivered to CPU by differential pressure transmitter, omnidistance gauge glass, if display full water (without differential pressure), then and water level rising verification succeeds; Otherwise, by the exhaust of positive and negative pressure side gas collector exhaust valve, as still unsuccessful, then carry out differential pressure transmitter verification, check electrical null position output difference current voltage I
Δ P mAtill initial value 4mA; Return step 4;
5) closedown adds water valve, open wicket, when in glass tube, water level decreasing is to zero level steel seal place, represent now pressure reduction be maximum differential pressure value 1/2 (in negative pressure chamber the water surface in plemum between the water surface and water side pipe center line pressure reduction 1/2, also namely range differential pressure value 1/2); The pressure reduction of measurement is delivered to CPU by differential pressure transmitter, if the water level range scale value of omnidistance gauge glass display 1/2 and zero level value, then water level decreasing first stage verification succeeds; Otherwise (if step does not carry out the gas collector exhaust of positive and negative pressure side in the past) is vented by positive and negative gas collector, as still unsuccessful, then carries out differential pressure transmitter verification, checks electrical null position, output difference current voltage I
Δ P mAtill initial value 4mA; Then step 5 is returned);
6) staying open wicket to make in glass tube water level decreasing to water side pipe centerline, now in negative pressure chamber the water surface also in water side pipe centerline; Differential pressure transmitter exports 20mA and the range maximum differential pressure of measurement is delivered to CPU, if display negative water level range scale value, then water level decreasing subordinate phase verification succeeds; Otherwise (if step does not carry out the gas collector exhaust of positive and negative pressure side in the past), by the exhaust of positive and negative pressure side gas collector, as still unsuccessful, then carries out differential pressure transmitter verification, checks electrical null position, output difference current voltage I
Δ P mAtill initial value 4mA; Then step 6 is returned).
7) water level rising verification, water level decreasing first stage School Affairs water level decreasing subordinate phase verification all successes, the verification of water level measurement system terminates.
After being noted that plemum fills water, the positive and negative pressure chamber water surface, all to full water steel seal place, now closes water filling door, need check that whether main equipment water side door is interior to leak, observe negative pressure chamber's water surface 20 minutes, as water level does not decline, then water level measurement system verifying work can start.As the water surface in glass tube declines, and positive and negative pressure pressure transmission piping No leakage, then should suspect in water side door and leak.When after water side door maintenance process, water level measurement system verification can be carried out.
Claims (7)
1. for a water level measurement system for boiler-steam dome, it is characterized in that: comprise level measurement device (1), thermostat, all dasymeter (4), pressure samples door (8), pressure unit (9), temperature transmitter (10), differential pressure transmitter (11) and omnidistance gauge glass (12); Vapour side door and the water side door of described level measurement device (1) and boiler-steam dome are connected, and are connected with differential pressure transmitter (11) by thermostat, are also connected with pressure unit (9) by pressure samples door (8); Described thermostat is connected with equal dasymeter (4), and equal dasymeter (4) is connected with temperature transmitter (10); Described pressure unit (9), temperature transmitter (10), differential pressure transmitter (11) are all connected with omnidistance gauge glass (12).
2. a kind of water level measurement system for boiler-steam dome according to claim 1, it is characterized in that described level measurement device is concentric circles conjuncted structure, the pipe with its concentric is provided with bottom the cylindrical container of sealing, pipe bottom leans out cylindrical container, and top is positioned at cylindrical container inside; Pipe Inner Constitution negative pressure chamber; Cylindrical container internal diameter and pipe external diameter form plemum; Described cylindrical container top is provided with into steam ports, is connected with the vapour side door of boiler-steam dome by lateral steam tube; The bottom of pipe is provided with water inlet, is connected with the water side door of boiler-steam dome by horizontally disposed water side pipe; The bottom of cylindrical container bottom and pipe is respectively equipped with malleation sample tap, sampling below atmospheric pressure mouth, is connected with thermostat.
3. a kind of water level measurement system for boiler-steam dome according to claim 2, is characterized in that the internal diameter of described pipe is 2 times of water side pipe internal diameter.
4. a kind of water level measurement system for boiler-steam dome according to claim 2, is characterized in that described pipe top is equal with omnidistance gauge glass range to the vertical height in water side pipe axle center.
5. a kind of water level measurement system for boiler-steam dome according to claim 1, it is characterized in that described thermostat comprises positive-pressure constant-temperature device (2) and negative pressure thermostat (3), be closed container, top is provided with entrance, and bottom is provided with outlet; Positive-pressure constant-temperature device (2) entrance is connected with cylindrical container malleation sample tap, exports and is connected with differential pressure transmitter (11) by equal dasymeter; Negative pressure thermostat (3) entrance is connected with the sampling below atmospheric pressure mouth of pipe, and outlet is connected with differential pressure transmitter (11).
6. a kind of water level measurement system for boiler-steam dome according to claim 1, it is characterized in that described equal dasymeter comprises four platinum resistance, to be evenly fixed on from top to bottom on steel pipe that positive-pressure constant-temperature device (2) is connected with differential pressure transmitter (11) and to be positioned at the vertical component in positive-pressure constant-temperature device (2) exit; The platinum resistance series connection of two odd number orders, after forming parallel circuit, is connected with temperature transmitter (10) with the platinum resistance of other two even number sequential series.
7. a kind of water level measurement system for boiler-steam dome according to claim 1, is characterized in that the positive and negative pressure input end of described differential pressure transmitter (11) is connected with malleation gas collector (5) and negative pressure gas collector (6) respectively by positive-pressure door, negative pressure door; Described malleation gas collector (5) and negative pressure gas collector (6) are closed container, and top is provided with outlet, and bottom is provided with entrance; Described malleation gas collector (5) is connected with positive-pressure constant-temperature device (2), negative pressure thermostat (3) respectively with the entrance of negative pressure gas collector (6), and be connected with positive-pressure door, negative pressure door respectively, be also connected with malleation sewage door and negative pressure sewage door respectively; The outlet of described malleation gas collector (5) and negative pressure gas collector (6) is connected with exhaust valve respectively.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520423824.XU CN204705386U (en) | 2015-06-18 | 2015-06-18 | A kind of water level measurement system for boiler-steam dome |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520423824.XU CN204705386U (en) | 2015-06-18 | 2015-06-18 | A kind of water level measurement system for boiler-steam dome |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104897235A (en) * | 2015-06-18 | 2015-09-09 | 郭春堂 | Water level measuring system for boiler drum and measuring and checking method thereof |
| CN113418582A (en) * | 2021-05-24 | 2021-09-21 | 杭州海芯达科技有限公司 | Automatic calibration device of boiler drum level gauge |
-
2015
- 2015-06-18 CN CN201520423824.XU patent/CN204705386U/en not_active Withdrawn - After Issue
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104897235A (en) * | 2015-06-18 | 2015-09-09 | 郭春堂 | Water level measuring system for boiler drum and measuring and checking method thereof |
| CN104897235B (en) * | 2015-06-18 | 2018-01-23 | 郭春堂 | It is a kind of for the water level measurement system of boiler-steam dome and its measurement and method of calibration |
| CN113418582A (en) * | 2021-05-24 | 2021-09-21 | 杭州海芯达科技有限公司 | Automatic calibration device of boiler drum level gauge |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20151014 Effective date of abandoning: 20180123 |