芬兰专利FI20185437A1 Detecting leakage in a soda recovery boiler

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专利摘要:
A method, system, and computer program (93) for detecting a boiler leak, wherein the recovery boiler automation system (90) receives an indication (11) of the automatic sequence start need and initiates (12) the automatic sequence by: (13) stopping the monitoring (15) the performance of the boiler water over the reporting period and drawing a conclusion (16) on the basis of said monitoring.
公开号:FI20185437A1
申请号:FI20185437
申请日:2018-05-11
公开日:2019-11-12
发明作者:Timo Karjunen
申请人:Varo Teollisuuspalvelut Oy；
IPC主号:

专利说明:

MAKING A MILITARY BOILER LEAK
20185437 prh 11 -05- 2018
FIELD OF THE INVENTION
The invention relates to monitoring the tightness of a recovery boiler.
BACKGROUND OF THE INVENTION
A central component of the forest industry's steam turbine power plants is the recovery boiler, which is designed to produce steam for the turbine. The heat transfer surfaces of the boiler are to a large extent composed of pipes carrying water and / or steam. If a small leak is detected in any of the pipes, the damage caused by the leak can usually be repaired relatively quickly and at low cost. If the leak is not detected, the leak can cause extensive damage, which is difficult and time-consuming to repair.
SUMMARY
To prevent widespread damage, the boiler tightness monitoring should be arranged so that leakage is detected even when it is relatively small.
In practice, the following methods can be used to check the leak-tightness of boilers:
- monitoring of the mass balance;
- monitoring of the chemical balance;
- monitoring of acoustic emissions.
Mass balance monitoring is accomplished by calculating the difference between water and steam flows into and out of the boiler. As a result of the leakage, the difference becomes larger than normal. An alarm limit can be set for the difference, whereby the alarm is activated when the difference increases above the alarm limit. The size of the alarm limit is influenced by the size of the boiler, the accuracy of the flow measurements and the noise of the flow measurements
20185437 prh 11 -05- 2018 filter method. By monitoring all flows affecting the balance sheet with moderately accurate flow measurements and effectively eliminating noise in the measurement data, the alarm limit can be set so low that relatively small leaks can be detected.
Chemical balance monitoring is accomplished using a tracer that does not exit the boiler with steam, which has four terms in the balance:
- tracer flow into the boiler with feed water during the reference period;
- Flow of tracer out of the boiler with blow-off during the reference period;
- Flow of tracer from boiler with leakage from boiler evaporator section during reference period; and
- change in tracer content (= change in concentration x boiler evaporator water content) over the boiler evaporator over the reference period.
By equipping the boiler with suitable measurements, the chemical balance can be constructed so that the only unknown in the balance is the tracer leakage from the evaporator portion of the boiler. The leakage flow can then be solved from the balance sheet.
In monitoring acoustic emissions, the leak is detected on the basis of the sound it emits. The air space or boiler (pressure) body of the boiler plant can be listened to with suitable sensors.
According to a first aspect of the invention, there is provided a method of detecting a boiler leak comprising:
receiving, in the boiler automation system, an indication of the need for automatic sequence activation;
initiating, in the automation system, an automatic sequence in response to receiving said indication 30 with the following operations:
- stopping metering of the tracer in boiler water in the event that the boiler comprises a separate metering of the tracer;
- stop the boiler water outflow;
20185437 prh 11 -05- 2018
- monitoring the boiler water property over the reporting period; and
- draw a conclusion on the leakage on the basis of that monitoring.
In some embodiments of the invention, the automatic sequence comprises stopping dosing of the tracer in boiler water. Dosing refers here to special dosing into the feed water.
In some alternative embodiments of the invention, the tracer itself is not metered, but the tracer is naturally present in the feed water, so that metering is not interrupted. Instead, to control the pH and / or other properties of the boiler water, the dosing of the chemical to be dosed is interrupted. Alternatively, to adjust the pH and / or other properties of the boiler water, the dosing of the chemical being dosed is not interrupted.
By automatic sequence herein is meant an automatic sequence (set of functions) performed without user intervention or significantly without user intervention (i.e., non-manual intervention). Boiler water refers to water circulating in boiler tubes. Boiler leakage in particular means leakage in the evaporator part of the boiler.
In some embodiments of the invention, said indication is received by automated means (i.e., without user intervention), for example from within the system. In other embodiments of the invention, the user (operator) may enter a start command into the automation system.
In some embodiments of the invention, the indication of the need for an automatic sequence start (i.e., a sequence start indication) is an indication of a potential leakage in the evaporator portion of the boiler.
In some embodiments of the invention, an increase in the feed-water-vapor difference is used as an indicator for sequence initiation. In some embodiments of the invention, an increase in the level of acoustic emission is used as an indication for sequence initiation. In some embodiments of the invention, a sequence
20185437 prh 11 -05- 2018 The starting indication is the increase in the revolution of the flue gas fans. In some embodiments of the invention, a sudden increase in furnace pressure is used as an indication for sequence initiation. In some embodiments of the invention, a sudden drop in the surface of the cylinder 5 is used as the sequence-triggering indication. In some embodiments of the invention, any other change in boiler measurements is used as the sequence trigger indication. In some embodiments of the invention, any combination of the above which may indicate a leak in the boiler is used as the sequence-triggering indication.
In some embodiments of the invention, said sequence is automatically initiated (i.e., without user intervention) in response to receiving said indication.
In some embodiments of the invention, the indication of the need for automatic sequence initiation is not an indication of a potential leak, but the indication may be, e.g., the fulfillment of a time-related condition. Said automated sequence can be started automatically in the automation system, for example, periodically (e.g., once a week).
In some embodiments of the invention, the command provided by the user serves as an indication received by the automation system of the need to trigger the automatic sequence. In these embodiments, the operator may manually issue a start command, for example, if there is a leak in the boiler. When the automation system receives an indication (start command), it starts the automatic sequence.
In some embodiments of the invention:
- return to tracer (normal) metering, if discontinued, and to 30 effluent streams at the end of the observation period.
Returning to tracer dosing and bleeding flow (restarting tracer dosing and bleeding stream) may include
20185437 prh 11 -05-2018 for automatic sequence functions. In some embodiments of the invention, the return is made after a predetermined time.
In some embodiments of the invention, to stop tracer dosing, the tracer dosing pump or pumps is stopped and / or the dosing line valve (s) are closed. The operations are carried out under the control of an automation system.
In some embodiments of the invention, the outlet line valve (s) is closed to stop the boiler water outflow flow. The operation is performed under the control of 10 automation systems.
In some embodiments of the invention, monitoring is performed and the conclusion is made with only one variable. In some embodiments of the invention, said boiler water property is a tracer concentration. In some embodiments of the invention, said boiler water has the property of boiling water conductivity.
In some embodiments of the invention, said boiler water has the cation-exchanged conductivity of boiler water. In some embodiments of the invention, an automation system alerts a leak if the property of the boiler water during the reference period behaves according to a predetermined criterion. If the aforementioned 20 features, for example, decreases (especially steadily) during the reference period, the automation system will alert the leak. In this case, the predetermined criterion is a certain change in the property (a fall, or in particular a steady fall) during the reference period.
In some embodiments of the invention, said predetermined criterion is selected from the group consisting of: a property change, a steady change in a property (e.g., must be greater than a predetermined threshold), a decline in a property, and bigger).
In some embodiments of the invention, more than one property of boiler water (e.g., two or three of the above) is monitored over a period of time.
20185437 prh 11 -05- 2018
In some embodiments of the invention, said property of boiler water is monitored by measuring a property of a boiler water pipe (e.g., a cylinder drainage pipe) where the boiler water continues to flow even though the outflow flow has been stopped. In these embodiments, in particular, not a boiler outlet line is used as the boiler water sample flow tube, but a thinner sample flow tube or, depending on the measurement method, a sample flow tubeless solution.
In some embodiments of the invention, stopping the tracer dosing and stopping the blow-off flow creates a tracer closed loop. Said property of boiler water is monitored by measuring the property of a boiler water pipe forming part of said closed circuit.
In some embodiments of the invention, sodium is used as a marker.
In some embodiments of the invention, phosphate is used as a marker.
The tracer can be administered as a compound in boiler water (feed water), e.g. in the form of sodium phosphate, whereby sodium, phosphate or both can be used as a tracer. In some embodiments of the invention, sodium is used as a tracer and is administered as saline. In some embodiments of the invention, sodium is used as a tracer and is administered in the form of lye (NaOH). In some embodiments of the invention, the label is sodium and is administered in the form of sodium sulfate. In some embodiments of the invention, the tracer is phosphate and is administered as a sodium-free phosphate compound. In some embodiments of the invention, another chemical is used as a marker. In some embodiments of the invention, a plurality of chemicals are used as the tracer and / or the tracer is administered in a combination of different chemicals. In still other embodiments of the invention, silicate (S1O2) naturally present in the feed water is used as a tracer.
In some embodiments of the invention, the automation system provides an estimate of leakage size based on a change in said property. In some embodiments of the invention, if said boiler water property changes or decreases steadily, the automation system provides a steady change in property
20185437 prh 11 -05-2018 or an estimate of the leak size based on a steady bill.
In some embodiments of the invention, tracer dispensing is first stopped, followed by a blow-off flow. In other embodiments of the invention, the blow-off flow is first stopped and then the tracer dosing is stopped.
In still other embodiments of the invention, tracer dosing and blow-off flow are simultaneously terminated.
In some embodiments of the invention, based on said monitoring, the location of the boiler leak is located. For example, if said feature of boiler water in some embodiments of the invention changes or decreases steadily, the leak is in the evaporator. Conversely, if the property remains the same, there is no leakage in the evaporator, so if there is a leak in the boiler, it is in superheaters or economizers.
In some embodiments of the invention, said blow-off flow is only closed with a delay after cessation of tracer dosing. In particular, if the tracer, e.g., nathumphosphate, is metered into the feed water line prior to economizers, the outflow flow may be terminated with a delay. In such an embodiment of tracer dosing, even after dosing is discontinued, the evaporator portion of the boiler is flushed with tracer water from economizers. It is preferable to wait until the Economizers have been filled with clean water before closing the outflow flow.
In some embodiments of the invention, the method is implemented as a top-level control.
According to another aspect of the invention, there is provided a system for detecting a boiler leak which is configured to receive an indication of the need for an automatic sequence to be triggered and to trigger an automatic sequence in response to receiving said indication by:
- stopping metering of the tracer in boiler water in the event that the boiler comprises a separate metering of the tracer;
- stop the boiler water outflow;
20185437 prh 11 -05- 2018
- monitoring the boiler water property over the reporting period; and
- draw a conclusion on the leakage on the basis of that monitoring.
According to a third aspect of the invention there is provided a computer program comprising program code executable in a recovery boiler automation system which causes the automation system to perform the following operations:
receiving, in the boiler automation system, an indication of the need for automatic sequence start;
- initiating, in the automation system, an automatic sequence in response to the receipt of said indication by the following operations:
• stopping the tracer metering in boiler water in the event that the boiler comprises a separate tracer metering;
• stopping the boiler water outflow;
· Monitoring the performance of boiler water over the reporting period; and • concluding the leak on the basis of said monitoring.
An automation system is a computerized system whereby a computer program can be executed on a processor or coin unit comprised in the system.
The computer program contains the program code executable on the computer.
According to a fourth aspect of the invention there is provided a computer program product comprising a computer program according to the third aspect.
According to a fifth aspect of the invention, a memory medium is implemented comprising a computer program or program code according to a third aspect stored thereon.
Aspects of various aspects and embodiments of the invention have been described above. The above-described embodiments illustrate exemplary embodiments that may be used in various embodiments of the invention. Various embodiments of the invention will be described or described in connection with some or some aspects of the invention. However, the corresponding embodiments are also applicable to other aspects and related embodiments. Embodiments or features thereof may be used alone or in combination with other embodiments.
BRIEF PRESENTATION OF THE PATTERNS
The invention will now be described, by way of example, with reference to the accompanying drawings, in which:
Fig. 1 is a flow chart illustrating a method according to an embodiment of the invention,
Figure 2 shows parts of a recovery boiler in connection with embodiments of the invention,
Figure 3 shows the recovery boiler of Figure 2 supplemented with an automation system in some embodiments of the invention; and
Figure 4 is a block diagram of a recovery boiler automation system according to an embodiment of the invention.
DETAILED EXPLANATION
It is to be noted that the figures shown are not to scale in their entirety and that their purpose is merely to illustrate embodiments of the invention.
In the method for detecting a boiler leak, the boiler automation system receives an indication of the need for automatic sequence activation and starts an automatic sequence in response to said
20185437 prh 11 -05- 2018 for indication.
Fig. 1 is a flow chart illustrating a method according to an embodiment of the invention. In the method automation system, in step 11, the recovery boiler indication of the need for automatic sequence start is received. In step 12, an automated sequence is initiated in the automation system in response to receiving said indication.
The automatic sequence includes the following functions:
stop adding tracer to boiler water (step 13)
20185437 prh 11 -05- 2018
- stop the boiler water outflow (step 14);
monitoring the boiler water property over the reporting period (step 15), and
- concluding the leakage on the basis of this monitoring (step 16).
Figure 2 shows parts of a recovery boiler in connection with embodiments of the invention. The feed water pump 22 pumps the feed water from the feed water tank 21 along the feed water line 25 to the feed water preheaters or economizers 36 from where the feed water passes to the cylinder 41. The boiler water drains from Typically, the cooking surface 67 of the boiler has a different drain from the cylinder 41 and a return pipe to the cylinder. Water vapor flows from cylinder 41 to superheaters 86 and thence to steam turbines (not shown). The feed water is dispensed from the chemical tank 31 by a chemical solution pump 32 along a chemical dispensing line 35, e.g. to adjust the pH of the boiler water.
The evaporator portion of the boiler includes a furnace 80, a cooking surface 67, a cylinder 41, and a drain pipe 45. From the evaporator portion (e.g., from cylinder 41), an outlet line 55 is discharged to the outlet vessel. The outflow flow is controlled by the outflow control valve 54.
In addition to the outlet line 55, a boiler water sample line 75 exits the evaporator section, from which a predetermined property of the boiler water is measured.
The feed water line 25, the chemical dosing line 35, the bleed line 55, and the steam lines 25 are provided with flow meters (flow meters). In the figure, reference numeral 23 denotes a feed water line flow meter, reference numeral 33 a chemical dosing line flow meter, reference numeral 53 an outflow line flow meter, and reference numeral 63 a steam line flow meter.
The boiler water sample line 75 has a measuring device 73 for measuring said boiler water property.
The water in the aforementioned pipes or lines may flow as either liquid, vapor or
20185437 prh 11 -05- 2018 as water vapor mixture.
The figure shows the recovery boiler of Figure 2 supplemented with an automation system in some embodiments of the invention. The automation system 90 communicates with 5 control, measurement and control devices such as 22-23, 32-33, 53-54, 63 and 73.
It controls the operation of the devices and receives data from the devices such as measurement data and status information.
The following describes the operation of the method in some embodiments of the invention.
Mass balance monitoring is accomplished by calculating the difference between water and steam flows into and out of the boiler. When this so-called. the feed-to-steam difference increases, it may be an indication of leakage in the boiler evaporator section. When the feedwater15 steam difference exceeds the alarm limit, the automation system alerts you of the increase in feedwater steam difference. In an automation system, this serves as a received (received) indication of the need for automatic sequence start.
The automation system 90 then initiates an automatic sequence in which:
a) Pump 32 which pumps a chemical (e.g. sodium phosphate) into the feed water stops
b) If the sodium phosphate solution is dispensed to the feed water line 25 before the economizers 36, a delay will occur in which the sodium phosphate-containing water in the economizers 36 will be exchanged with water which is free of sodium phosphate. If the sodium phosphate solution is metered directly into cylinder 41 or in a line between cylinder and economizer 36, no delay is required.
c) The outlet line valve 54 closes
d) After closing the outlet line valve 54, monitoring of the phosphate or sodium (= tracer) content of the boiler water 30 is initiated: if the value decreases steadily, the automation system will alert 90 leaks in the boiler evaporator section
e) The automation system 90 reports the phosphate or sodium content
20185437 prh 11 -05-2018 estimates the leakage rate and updates the result each time a measurement of the phosphate or sodium content in the boiler gives a new result.
Instead of increasing the feed-water-vapor difference, the sequence-triggering indication may be, for example, an increase in acoustic emission level, an increase in flue gas fan speed, a sudden increase in furnace pressure, a sudden drop in cylinder surface, or any other change in
The sequence both stops the delivery of the sodium phosphate to the boiler and interrupts the flow of sodium and phosphate out of the boiler.
The outflow is closed with a delay when the nathumphosphate is dispensed to the feed water line 25 before the economizers 36, since even after discontinuing the dosing, sodium phosphate-containing water flows from the economizers 36 into the boiler evaporator until the economizers 36 are filled with clean water. The length of the required delay depends on the volume of the economizers 36 and the feedwater flow.
Sodium and phosphate will only flow out of the evaporator portion of the boiler after the blow-off is closed only along sample line 75 with the boiler water sample flow. The sample flow rate is usually about 1 l / min = 0.06 m ³ / h. Boiler leaks typically start with a small crack so that the total initial leakage is 0.2 - 0.4 kg / s or 0.7 - 1.4 m ³ / h. Thus, from the outset, the leakage is at least an order of magnitude larger than the sample flow, so that the effect of the sample flow on the sodium and phosphate content of the boiler water is so small that it can be neglected.
With the supply of sodium phosphate shut off and the blowdown closed, there are now only two terms in the chemical balance from which the leak can be calculated.
The first term describes the amount of sodium or phosphate escaping from the boiler with the leak, and the second describes the change in the sodium or phosphate inventory of the boiler water during the period under review. Thus, for example, the equation for phosphate can be represented
20185437 prh 11 -05- 2018 format
CpO4 v leakage t = (CpO4, to - CpO4, tl) 'microstatic water (1) where
Cpo4 = mean phosphate content of the boiler water over the reference period (mg / kg or g / t) v leakage = mean leakage flow over the reference period (kg / s or t / h) t = length of the reference period (s or h)
Cpo4, to = value of the phosphate content of the boiler water at the beginning of the period (mg / kg or g / t)
Cpo4, ti = value of the phosphate content of the boiler water at the end of the period (mg / kg or g / t) sludge water = water mass (kg or t) of the boiler evaporator.
From equation (1), the leakage current can be solved
V leakage ^- ((CpO4, tO - CpO4, tl) 'boiler water) / (CpO4' t)
The above equation shows the leakage flow on the basis of two quantities, namely the phosphate content of the boiler water and the water mass of the evaporator portion of the boiler.
Phosphate concentration in the cataract can be monitored with a continuous phosphate analyzer (measuring device 73, Figures 2 and 3).
The water mass of the boiler evaporator section, in turn, can be estimated from the water volume of the boiler evaporator and the type of boiler. For example, in cylindrical boilers operating at 30 cycles, about half the volume of water is water and half is steam, so the first approximation is that the mass of water in the evaporator corresponds to half the volume of the evaporator. This estimate can be refined by testing how quickly the boiler water dilutes when
20185437 prh 11 -05-2018 Sodium phosphate metering is interrupted and water is drained from the evaporator via blowdown. The outflow flow is then the boiler leakage of equation (1), and its magnitude is known when the outflow flow is measured by the flow meter 53 of the outflow line 55. Then, the amount of water in the boiler 5 can be solved. This amount of water can then be used in the future as a boiler-specific constant for the boiler in question.
The method according to some embodiments of the invention is illustrated by the following example.
A boiler with a evaporator water mass of 100,000 kg receives a leakage of 1 kg / s. The boiler automation system 90 continuously monitors the feedwater / steam difference calculated from the flow measurements so that an increase in the difference is triggered when the difference exceeds 0.5 kg / s. As the leakage is above the alarm limit, there are now 15 alarms. The boiler staff (or operator) thus receives the first indication of a leak from the boiler, but the indication does not indicate in which part of the boiler the potential leak is. To detect a leak, an automatic sequence is initiated which stops the dosing of sodium phosphate and closes the purge line valve. If there is a leak in superheaters 86 or economizers 36, there is no significant change in the sodium and phosphate yields of the evaporator portion 20 of the boiler since no sodium phosphate enters the furnace and no significant amount of sodium or phosphate is removed from the boiler. Thus, the concentrations of the substances in question in the boiler water do not change. On the other hand, if there is a leak in the evaporator section, the concentrations of the substances in question begin to decrease steadily.
In the exemplary situation, the phosphate content drops from 3 mg / kg to 2.2 mg / kg in six hours and the evaporator has a water mass of 100,000 kg. The automation system 90 thus estimates the leak size as follows: v leakage ⁼ ((3 mg / kg - 2.2 mg / kg) 100,000 kg) / (2.6 mg / kg 6,300 s) v leakage = 1.07 kg / s.
20185437 prh 11 -05- 2018
The result corresponds well to the feed-water-vapor difference. case.
The automation system 90 has then provided the operator with two mutually supportive but completely independent indications of leakage in the boiler. Method 5 can also be utilized without calculating the size of the leak, since dilution of boiler water with the bleed closed and chemical dosing off is a clear indication of a leak in the evaporator portion of the boiler. This indication alone, without, for example, an increase in feed-water vapor separation, is a clear indication that water is leaking from the evaporator portion of the boiler, either through leaking valves or through 10 leaks in the pipeline, and as such sufficient to provide further action.
The method described above for detecting boiler leakage (or for monitoring boiler tightness) can be used in all boilers where non-vapor transport chemicals can be added to the boiler water. The outflow should be arranged so that sampling of the boiler evaporator does not take place from the outflow line, since no sample of boiler water for analyzing tracer concentration is obtained at the time of the sequence. Most commonly, the boiler water sample line is connected, for example, in cylindrical boilers to one of the downpipes through which the boiler water descends from the cylinder to manifolds below the bottom of the furnace. The change in sample line to the drain line from the blow line is a relatively small change, so even in boilers where the sample is collected from the blow line, the necessary changes to use the method described above can be easily accomplished.
As mentioned above, for example, phosphate or sodium may be used as tracers. These are suitable because continuous analyzers for monitoring phosphate and sodium in boiler water are commercially available from a variety of suppliers. In addition, for example, in most cylindrical boilers, the pH of the boiler water is adjusted with sodium phosphate or lye, so that the boiler water is relatively high in both sodium and phosphate, so it does not need to be dispensed solely to control boiler tightness.
20185437 prh 11 -05- 2018
The method may be applied using any other tracer provided that a continuous analyzer is available which can measure the concentration of the substance in boiler water and that the tracer has no adverse effect on boiler water chemistry or water quality.
In some embodiments of the invention, a substance that is naturally present in the feed water is used as a tracer. Because, for example, silicate (S1O2) is typically naturally present in the feed water, it does not need to be dispensed separately on the dispensing line. In some embodiments of the invention, the concentration of silicate in the boiler water is monitored by a continuous analyzer disposed, for example, in the aforementioned sample line 75 (Figures 2 and 3). In the disclosed method, the dispensing of boiler chemicals via the dispensing line 35 does not need to be interrupted, but it is sufficient to shut off the outflow flow. Because 15 silicates are constantly coming into the boiler water, closing the blow-off flow will result in a situation where the silicate content in the boiler water increases if the boiler is tight (i.e. no leakage in the boiler). Even in this embodiment, the leakage conclusion is based on the monitoring of the boiler water property (here: the monitoring of the silicate content). If the silicate content increases as expected during the monitoring period, this is an indication that there is no leakage in the boiler. If, on the other hand, the silicate content does not increase as expected, this is an indication that the boiler is leaking.
In boilers where the pH of the boiler water is not adjusted with sodium phosphate, the method can be utilized by dosing boiler water lye or a sodium salt, such as sodium sulfate, for a short time at the beginning of the sequence. A step is then added to the sequence in which a portion of boiler water is dispensed at the beginning of the sequence with lye or sodium sulfate. When the dose is dispensed, dosing is stopped and the bleed is closed. From now on, the sequence proceeds as normal. The arrangement requires a separate dosing pump and a reservoir for the tracer in question.
When the dispensing agent is alkaline, the same dispensing pump and reservoir can also be used in situations where the pH of the boiler water should be raised.
20185437 prh 11 -05- 2018
Measurement of tracer concentration can be replaced by measurement of conductivity or cation exchanged conductivity, subject to certain restrictions related to tracer concentration and water quality.
In boilers where sodium phosphate can be used with high concentrations of both sodium and phosphate in boiler water (eg 10 mg / l or more) and good water quality with no other conductivity impurities, the conductivity of the boiler water is almost directly dependent on these. 10 concentrations of chemicals in boiler water. The effect of chemicals supplied to the feed water on the conductivity of the boiler water is so small that it can be neglected. The equation for the leakage size can then be expressed as leaks = (Qohtokyto-conductivity) mkati water / Conductivity t = where conductivity to = boiler water conductivity at the beginning of the observation period (at time to) conductivity ti = boiler water conductivity at the end of average conductivity of boiler water over the period.
The difference in leakage currents calculated from the change in conductivity and the change in sodium or phosphate concentration is about 5-10% in cases, meaning insignificant for leak verification and location.
In boilers where the pH of the boiler water is adjusted with nathumphosphate, monitoring of the boiler leakage based on the conductivity of the boiler water can be enhanced by providing a cation exchanger for conductivity measurement of the boiler water. The cation exchanger filters out water, for example. cationic feedwater chemicals, so their error in estimating leakage size is reduced compared to direct conductivity determination.
Figure 4 is a block diagram illustrating an example of an automation system 90 that fits
20185437 prh 11 -05-2018 for implementing certain embodiments of the invention.
System 90 comprises at least one processor 91 for controlling system operation and at least one memory 92 comprising computer program / software 93. Computer software 93 includes instructions or program code for processor 91 to control system 90. Software 90 may typically comprise an operating system and various applications.
Said at least one processor 91 may be, for example, a central processing unit (CPU), a microprocessor, a digital signal processor (DSP) or the like. Figure 4 shows a single processor, but automation systems can typically have multiple processors.
Said at least one memory 92 may comprise, for example, read-only memory (ROM), programmable read-only memory,
PROM), EPAS (erasable programmable read-only memory), EEPROM (Electronically erasable programmable read-only memory), RAM (random access memory), flash memory, optical or magnetic memory and / or the like. System 90 may have multiple memories. The memory may be part of system 90 or it may be a separate module that can be connected to system 90.
The memory can only be used to store data or it can also be used for data processing.
System 90 includes a communication unit 95. The communication unit 95 provides an interface for internal communication of the system 25 using a suitable protocol. Particularly in some embodiments of the invention, communication with the boiler units is made via the communication unit. It sends commands to devices (e.g., measuring devices, valves, and pumps) and receives data from said devices.
To receive inputs from the user (boiler personnel / operator) and output to the user, system 90 comprises a user interface 96, which may comprise, for example, a display and a keyboard (not shown).
20185437 prh 11 -05- 2018
In addition to the elements shown in Figure 4, the system 90 may comprise other elements. Also, in some embodiments of the invention, said measuring devices, valves and pumps may be incorporated into the system.
The mass balance of the boiler can be represented in the form (see Figures 2 and 3)
F1 = F3 + F4 + Fv where
F1 = feed water flow
F3 = blow-off flow
F4 = vapor flow to the turbine, and
Fv = leakage current.
All quantities are over a sufficiently long time step so that changes in cylinder surface can be ignored (there may be other terms in the balance sheet, eg steam flow for scrubbers (on the right side of the balance sheet) and feedwater flow for steam temperature control (left side of the balance) feed water and said flow is taken from the feed water line prior to the feed water flow measurement, but these are not considered here).
The chemical balance can be represented as (all values averaged over a time step of 25 h, phosphate tracer) phosphate in = F2 phosphate content of dosing solution t phosphate out = (F3 + F _v ) phosphate in boiler water t change in phosphate inventory = phosphate out - phosphate out -
20185437 prh 11 -05-2018 Change in phosphate inventory = change in phosphate content of boiler water over time t mass of boiler water (kg)
In some embodiments of the invention, monitoring of mass and chemical balances is in a way combined. And it's done in a simple, easy and reliable way.
Without limiting the scope and interpretation of the claims, the following lists some technical effects of one or more of the embodiments shown. One technical effect is that a leak can be located in a vaporizer or superheaters / economizers by the mere presence of a boiler water sodium or phosphate analyzer or boiler water conductivity or cation exchanged conductivity. In other words, a leak can be detected and / or localized by observing only one variable. As there is only one measurement required, the method is reliable and reliable. Another technical effect is that the size of the evaporator leakage is determined by a single measurement variable (variable). Since the quantities needed for the calculation are minimal, the error related to the calculation is also minimal, ie the calculation works accurately. A third technical effect with respect to embodiments based on conductivity measurement is that the measurement is simple, maintenance-free, reliable and inexpensive compared to concentration measurements using e.g. sodium or phosphate analyzers.
The foregoing description provides non-limiting examples of some embodiments of the invention. It will be apparent to one skilled in the art that features presented in connection with only one or some embodiments may also be used in other embodiments. It will be apparent to one skilled in the art that the invention is not limited to the details set forth, but that the invention may be practiced in other equivalent ways. Throughout this document, the terms "comprising" and "containing" are open terms and are not intended to be limiting.
Some features of the embodiments shown may be utilized without the use of other features. The foregoing description is to be construed as merely describing the principles of the invention and not limiting it.
The scope of the invention is thus limited only by the appended claims.

权利要求:
Claims (19)
[1]
1. A method for detecting a boiler leak comprising:
receiving an indication in the boiler automation system
5 need for automatic sequence start;
triggering an automated sequence in the automation system in response to receiving said indication with the following operations:
- stopping metering of the tracer in boiler water in the event that the boiler comprises a separate metering of the tracer;
10 - stop the boiler water outflow;
- monitoring the boiler water property over the reporting period; and
- draw a conclusion on the leakage on the basis of that monitoring.
[2]
The method of claim 1, wherein said indication 15 is received by automatic methods.
[3]
The method of claim 1 or 2, wherein the sequence-triggered indication is an increase in the feed-water vapor difference.
20
[4]
The method according to any one of the preceding claims, wherein the sequence-triggering indication is one of the following: increase in feed-water vapor difference, rise in acoustic emission level, increase in flue gas fan speed, sudden increase in furnace pressure, sudden drop in cylinder surface.
[5]
The method of any preceding claim, wherein said sequence is automatically initiated in response to receiving said indication.
30
[6]
The method according to any one of the preceding claims, wherein the method:
return to tracer dosing, if discontinued, and to the effluent flow at the end of the observation period.
20185437 prh 11 -05- 2018
[7]
The method of any preceding claim, wherein the monitoring is performed and the conclusion is made with only one variable.
5
[8]
The method of any one of the preceding claims, wherein said property of boiler water is tracer concentration.
[9]
The method according to any one of the preceding claims, wherein said property of boiler water is the conductivity of boiler water or
[10]
10 cation exchanged conductivity.
The method of any preceding claim, wherein said property of boiler water is monitored by measuring the property of a boiler water pipe in which the boiler water continues to flow, even though
The 15 outflow flow has been stopped.
[11]
A method according to any one of the preceding claims, wherein stopping dosing and stopping the outflow flow creates a tracer closed loop and said boiler water
The 20 properties are monitored by measuring the property of the boiler water pipe forming part of said closed circuit.
[12]
The method of any one of the preceding claims, wherein the automation system alerts a leak if the boiler water property
For the 25 reference periods, behave according to a predetermined criterion.
[13]
The method of claim 11, wherein said criterion is selected from the group consisting of: property change, property change, property decline, and property decline.
[14]
A process according to any one of the preceding claims wherein the tracer is one or more of sodium, phosphate, and silicate.
[15]
15.
[16]
16.
[17]
17.
[18]
18.
[19]
19.
The method of any one of the preceding claims, wherein the automation system provides an estimate of the size of the leak based on a change in said property.
The method of any one of the preceding claims, wherein, based on said monitoring, the location of the boiler leak is located.
The method of any one of the preceding claims, wherein said blow-off flow is only closed with a delay after cessation of tracer dosing.
A system for detecting a boiler leak that is configured to receive an indication of the need for an automatic sequence to be triggered and to trigger an automatic sequence in response to receiving said indication by the following operations:
- stopping metering of the tracer in boiler water in the event that the boiler comprises a separate metering of the tracer;
- stop the boiler water outflow;
- monitoring the boiler water property over the reporting period; and
- draw a conclusion on the leakage on the basis of that monitoring.
20185437 prh 11 -05- 2018
A computer program comprising program code executable in a recovery boiler automation system that causes the automation system to perform the following operations:
- receiving in the boiler automation system the need for automatic sequence start;
- triggered in the automation system to receive an indication by automatic operation:
stopping metering of the tracer in the event that the boiler comprises metering;
in response to a sequence indication of said subsequent boiler water therein discontinuing the tracer • flow of boiler water;
• monitoring the boiler water property over the reporting period; and • concluding the leak on the basis of said monitoring.
20185437 prh 11 -05- 2018
An indication is received
12- ^ Starting the sequence
Stop dosing
14 -J ~ Stop bleeding
15-S ~ Tracking
20185437 prh 11 -05- 2018
Conclusion

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同族专利:

公开号 | 公开日

FI128387B|2020-04-15|

EP3567313A1|2019-11-13|

US11181264B2|2021-11-23|

US20190346131A1|2019-11-14|

EP3567313B1|2021-09-15|

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法律状态:
2020-04-15| FG| Patent granted|Ref document number: 128387 Country of ref document: FI Kind code of ref document: B |

2021-01-14| MD| Opposition filed|Opponent name: ANDRITZ OY |

优先权:

申请号 | 申请日 | 专利标题

FI20185437A|FI128387B|2018-05-11|2018-05-11|Detecting leakage in a soda recovery boiler|FI20185437A| FI128387B|2018-05-11|2018-05-11|Detecting leakage in a soda recovery boiler|

EP19172891.4A| EP3567313B1|2018-05-11|2019-05-07|Detection of leakage in recovery boiler|

US16/406,457| US11181264B2|2018-05-11|2019-05-08|Detection of leakage in recovery boiler|

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