• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:
    A bubbling fluidized bed combustion device (1) comprising a fluidization vessel (2), a fluidized sand bed (3) arranged in the fluidization vessel and an arrangement for monitoring the fluidized sand bed. The arrangement comprises at least one radar level gauge (4) arranged to repeatedly measure a distance (D) in the fluidization vessel from a reference point (5) to at least one portion (6) of the top surface of (7) the fluidized sand bed, and to provide a measurement signal (S) representative of the distance. The invention also relates to a method for monitoring a fluidized bed in a bubbling fluidized bed combustion device.(Fig. 1)
    公开号:SE1550364A1
    申请号:SE1550364
    申请日:2015-03-25
    公开日:2016-09-26
    发明作者:Badiei Shahriar
    申请人:Vattenfall Ab；
    IPC主号:
    专利说明:

    BUBBLING FLUIDIZED BED COMBUSTION DEVICE AND METHOD FORMONITORING THE FLUIDIZED BED IN SUCH A COMBUSTION DEVICE Field of the inventionThe invention relates to the field of bubbling fluidized bed combustion devices, and in particular monitoring of the fluidized bed in such a device.
    Background Bubbling fluidized bed combustion devices (BFB combustion devices) are well knownin the art. BFB combustion devices may be used for example to provide water steam,and is then often termed a BFB boiler. A BFB combustion device is based on theprinciple that combustion takes place in a fluidized bed of solid particles. The bed isfluidized by penetrating the bed by fluid flowing vertically upwards with sufficientvelocity to break up the bed. Fluidization of the bed is a central aspect of the combustion process in a BFB combustion device.
    Consumption of bed material in bio fuel driven BFB combustion devices is often high,in some real world cases the entire bed is exchanged within two days. The bedmaterial is exchanged at such rapid rate to be certain to avoid de-fluidization of thebed due to agglomeration of bed particles. This leads to high costs and highenvironmental impact. Sintering of the bed is another problem which may lead tosubstantial costs due to unwanted stops of the combustion device. Local sinteringand agglomeration in the bed may further influence the flow of combustion airthrough the bed. Uneven distribution of the combustion air may lead to locallyincreased temperature which further increases sintering, and may also lead toincreased NOx and CO emissions.
    Devices for monitoring the fluidized bed are known. One such device involves measuring pressure difference over the bed height. The pressure difference is usedtogether with other parameters to roughly estimate the bed height. This method hasseveral disadvantages however. Besides being somewhat unreliable, rapid changesand oscillations in the bed are not detected, and the estimated bed height is only an average value for the whole bed.
    Thus, there is a need for an improved system for monitoring the fluidized bed whichis more accurate and is able to detect rapid changes.
    JP2000042513 discloses a fluidized bed gasifying device comprising an uitrasoundlevel detector arranged in the top of the furnace. The uitrasound detector is arrangedto measure the distance to a stainless steel ball arranged on the surface of thefluidized bed. The ball moves in a vertical tube to maintain the ball at the correct position.
    Although this system offers advantages over measurement devices based on thepressure difference principle, it will not be very accurate in a combustion deviceapplication due to the high temperature gradients therein which causes greatvariations of the speed sound and therefore inaccurate level measurements. Further,the steel ball and the vertical tube add complexity to the system and may suffer fromreliability issues due to moving parts being in direct contact with the bed, possibly leading to jamming.
    Summary An object of the present invention is to provide a bubbling fluidized bed combustiondevice having means for monitoring the fluidized bed, and also a method formonitoring the fluidized bed, which overcomes at least some of the disadvantagesassociated with the prior art described above.
    These and other objects are achieved by the present invention by means of abubbling fluidized bed combustion device and a method for monitoring a fluidized bedin a bubbling fluidized bed combustion device according to the independent claims.
    Preferred embodiments are defined in the dependent claims.
    According to a first aspect of the invention, there is provided a bubbling fluidized bedcombustion device comprising a fluidization vessel, a fluidized sand bed arranged in the fluidization vessel and an arrangement for monitoring the fluidized sand bed. Thearrangement comprises at least one radar level gauge arranged to repeatedly measure a distance in the fluidization vessel from a reference point to at least one portion of the top surface of the fluidized sand bed, and to provide a measurementsignal representative of the distance. ln other words, the bubbling fluidized bed combustion device is provided with at leastone radar level gauge arranged in or at the fluidization vessel, for example throughon opening in a top or side wall of the fluidization vessel. The at least one radar levelgauge is arranged to measure the distance from a reference point, for example aposition in said radar level gauge where microwave pulses are emitted, to at leastone surface portion of the top surface of the fluidized sand bed. The distance may bemeasured vertically or essentially vertically, but may also be measured in any otherdirection provided that the radar level gauge has a free or undisrupted path to the topsurface of the bed. The micro wave pulses transmitted from the radar level gauge arepreferably reflected directly on the upper or top surface of the fluidized bed, i.e. nointermediate element is required to provide a sufficient reflection of the wave. The atleast one radar level gauge is configured to provide a measurement signalrepresentative of the distance, for example an analogue signal which scales with thedistance between the reference point and the bed surface. The at least one radarlevel gauge is configured to measure the distance repeatedly, i.e. at more than oneinstance, for example measure the distance continuously or with one or morepredetermined time intervals, such as 6 times per minute, or with a predetermined rate.
    The invention is based on the insight that a radar level gauge may advantageouslybe used to monitor the fluidized bed in a bubbling fluidized bed combustion device,and in particular that such a radar level gauge may detect rapid changes in thefluidized bed. The invention is further based on the insight that a radar level gaugemay measure a distance to the fluidized bed directly onto the top surface of the bedwithout any additional means for increasing the reflection on the bed surface, e.g. anintermediate member such as a ball arranged on the bed surface. lt is understood that radar level gauge refers to a microwave distance sensor whichpreferably is of the non-contact type provided with an antenna. Such a sensor can bearranged in or extending into the fluidization vessel at any suitable position, as longas the sensor has a free or undisrupted path to the top or upper surface of the fluidized bed. lt is also understood that bubbling fluidized bed refers to a bed of sandor solid particles which is fluidized by being penetrated by a fluid which flows at orslightly above the minimum velocity required to break up or fluidize the bed, therebyforming bubbles in the bed but still maintaining a stable bed.
    According to an embodiment of the device according to the first aspect of theinvention, the arrangement further comprises evaluation means configured torepeatedly, e.g. continuously or with predetermined time interval(s) or with apredetermined rate, determine a bed state parameter based on the signal, the stateparameter being one or at least one of the distance, a level of the fluidized sand bedor a height of the fluidized sand bed. The level (of the top surface of the bed) and theheight of the bed may be determined based on the signal and known geometricproperties of the fluidization vessel.
    The evaluation means may furthermore be configured to repeatedly, e.g.continuously or with predetermined time interval(s) or with a predetermined rate,determine a variation of the bed state parameter including determining an amplitudeand/or a frequency of the variation based on current and previously determined bed state parameter values.
    The evaluation means may furthermore be configured to repeatedly, e.g.continuously or with predetermined time interval(s) or with a predetermined rate,store data in a memory, the data including at least one of the determined bed stateparameter, the determined amplitude and the determined frequency. The abovedescribed determination of a variation of the bed state parameter may be based at least partly on bed state parameter values stored in said memory.
    The evaluation means may furthermore be configured to repeatedly, e.g.continuously or with predetermined time interval(s) or with a predetermined rate,apply a diagnostic algorithm to at least a sub set the stored data to determine if thefluidized sand bed comprises agglomerated or sintered sand particles. The diagnosticalgorithm may include determining if the determined frequency is changing over time(based on stored frequency values), and if so indicate that the fluidized sand bed comprises agglomerated or sintered sand particles. ln particular, the diagnostic algorithm may include determining if the determined frequency is decreasing overtime, and if so indicate that the fluidized sand bed comprises agglomerated or sintered sand particles.
    The bubbling fluidized bed combustion device may in embodiments furthermorecomprise gas supply means arranged to supply gas to fluidize the sand bed, fuelsupply means arranged to supply fuel to the sand bed, and feedback control means.The feedback control means are arranged to control the gas supply means and/orthe fuel supply means based on at least one of the determined bed state parameter,the determined frequency and the determined amplitude in order to control combustion in the sand bed.
    According to a second aspect of the invention, there is provided a method formonitoring a fluidized bed in a bubbling fluidized bed combustion device comprising afluidization vessel, a fluidized sand bed arranged in the fluidization vessel. Themethod comprises providing at least one radar level gauge in or at the fluidizationvessel, and repeatedly measuring a distance in the fluidization vessel from areference point to at least one portion of the top surface of the fluidized sand bed using the radar level gauge.
    The above comments regarding the first aspect of the invention and embodiments thereof apply analogously to the second aspect of the invention. ln an embodiment of the method according to the second aspect of the invention, themethod further comprises repeatedly, e.g. continuously or with predetermined timeinterval(s) or with a predetermined rate, determining a bed state parameter based ona measurement signal from the radar level gauge being representative of thedistance, the state parameter being one or at least one of the distance, a level of thefluidized sand bed or a height of the fluidized sand bed.
    The method may further comprise repeatedly, e.g. continuously or withpredetermined time interval(s) or with a predetermined rate, determining a variationof the bed state parameter including determining an amplitude and/or a frequency ofthe variation based on current and previously determined bed state parameter values. The method may further comprise repeatedly, e.g. continuously or with predetermined time interva|(s) or with a predetermined rate, storing data in amemory, the data including at least one of the determined bed state parameter, thedetermined amplitude and the determined frequency. The above describeddetermining of a variation of the bed state parameter may be based at least partly on bed state parameter values stored in said memory.
    The method may further comprise applying a diagnostic algorithm to at least a subset the stored data to determine if the fluidized sand bed comprises agglomerated orsintered sand particles. The diagnostic algorithm may include determining if thedetermined frequency is changing over time (based on stored frequency values), andif so indicate that the fluidized sand bed comprises agglomerated or sintered sandparticles. ln particular, the diagnostic algorithm may include determining if thedetermined frequency is decreasing over time, and if so indicate that the fluidized sand bed comprises agglomerated or sintered sand particles.
    Brief description of the drawingsThese and other aspects of the present invention will now be described in more detailwith reference to the appended drawings, which show presently preferredembodiments of the invention, wherein: fig. 1 shows a schematic illustration of an embodiment of a bubbling fluidizedbed combustion device according to the first aspect of the invention, and fig. 2 shows a flow chart of an embodiment of a method according to the second aspect of the invention.
    Detailed description Figure 1 shows a schematic illustration of an embodiment of a bubbling fluidized bedcombustion device 1 according the first aspect of the invention. The bubblingfluidized bed combustion device 1 comprises a fluidization vessel 2, a fluidized sandbed 3 arranged in the fluidization vessel, and an arrangement for monitoring thefluidized sand bed. The arrangement comprises a radar level gauge 4 and evaluation means 8.
    The fluidization vessel 2 is a cylindrical container and is provided with a gas inlet orgas supply means 10 configured to communicate gas from below to the bed 3 at a sufficient velocity such that the bed is fluidized. The bed 3 comprises solid particlesor sand, which may be silicate sand. ln the figure, the gas supply means is connectedto the interior of the fluidization vesse| through a bottom end or surface thereof, butmay in other embodiments have different physical shapes and positions, as long asthe desired effect is achieved, i.e. to fluidize the bed 3.
    The fluidization vesse| is also provided with an exhaust gas outlet 11 arranged toevacuate exhaust gas from the fluidization vesse| generated from combustion in thebed 3. ln the figure, the exhaust gas outlet is connected to the interior of thefluidization vesse| 2 through an upper end or surface 2a thereof, but may in otherembodiments have different physical shapes and positions, as long as the desiredeffect is achieved, i.e. to evacuate generated exhaust gas.
    The fluidization vesse| is furthermore provided with fuel supply means 9 configured tocommunicate fuel to the fluidized bed 3. The fuel supply means 9 is arranged abovethe upper surface 7 of the bed, such that fuel is added to the bed from above. ln thefigure, the fuel supply means is connected to the interior of the fluidization vesse|through a side surface thereof, but may in other embodiments have different physicalshapes and positions, as long as the desired effect is achieved, i.e. to provide fuel tothe fluidized bed.
    A water heating conduit 12 is provided in the fluidization vesse| 2 above the bed 3,and is provided with an inlet 12a for water and an outlet 12b for heated water orwater steam. The water heating conduit 12 functions as a heat exchanger whereinwater entering the conduit is heated or evaporated by heat from hot exhaust gas(originating from combustion in the bed 3) which rises upwards towards the exhaustgas outlet 11. The bubbling fluidized bed combustion device in figure 1 may thus bereferred to as a bubbling fluidized bed boiler.
    The radar level gauge 4 is arranged through the upper end surface 2a of thefluidization vesse|, and is arranged to measure a distance D in the fluidization vesse|from a reference point 5 to at least one surface portion 6 of the top surface 7 of thefluidized sand bed. The radar level gauge is provided with an antenna, for example ofthe parabolic type, directed downwards towards the bed. The surface portion 6 is typically only a few square centimeters of size. The radar level gauge has a smallangle of dispersion, for example 4 degrees. To provide a better measure of thefluidization of the entire bed, several radar level gauges may be used arranged tomeasure distance to different surface portions of the top surface of the bed. ln otherembodiments, the radar level gauge 4 may be arranged through a side wall orsurface of the fluidization vessel.
    The radar level gauge 4 provides a measurement signal S representative of thedistance D. The radar level gauge is electrically connected to the evaluation means 8to communicate the measurement signal S thereto. When the radar level gaugeperforms a measurement, pulses containing microwaves of electromagnetic radiationare transmitted from the radar level gauge in a direction towards the bed 3 and arereflected on the top surface 7 of the bed back to the antenna. ln the figure, the pathof the pulses is illustrated by the vertical dotted line shown in the figure, but it isunderstood that the measurements do not have to be performed vertically. Thereference point in this embodiment is the position in the radar level gauge where the microwave pulses are emitted (or received).
    As will be discussed below in more detail with reference to figure 2, the radar levelgauge 4 is configured to measure the distance repeatedly, i.e. at more than oneinstance, for example measure the distance continuously or with one or morepredetermined time intervals, or with a predetermined rate, such as 6 times perminute. The evaluation means 8 is configured to repeatedly, e.g. continuously or withpredetermined time interval(s) or with a predetermined rate, process the signal S anddetermine a bed state parameter, an amplitude and a frequency of a variation thereofand apply a diagnostic algorithm. This will also be discussed in more detail below with reference to figure 2. ln another embodiment of the device, which comprises all features of theembodiment described above with reference to figure 1, the device furthermorecomprises feedback control means arranged to control said gas supply means 10and/or said fuel supply means 9 based on at least one of the determined bed stateparameter, the determined frequency and the determined amplitude in order tocontrol combustion in said sand bed. For this purpose, the gas supply means may further include an electrically controllable blower or the like which allows the gas flowto be adjusted, and the fuel supply means may further include an electricallycontrollable pump or the like which allows the fuel flow to be adjusted. Alternatively,the gas supply means and fuel supply means may be provided with valves orthrottles which allow respective incoming flows to be throttled. The feedback controlmeans may be a separate physical unit, for example an electronic control unit (ECU),or may be implemented in the evaluating means or in another existing processing unit in or at the device.
    Figure 2 shows a flow chart of an embodiment of a method according to the secondaspect of the invention. The method is for monitoring a fluidized bed in a bubblingfluidized bed combustion device comprising a fluidization vessel, a fluidized sand bedarranged in the fluidization vessel, for example according to the embodiment shown in figure 1.
    The first step 101 of the method comprises providing at least one radar level gauge inor at the fluidization vessel. ln step 102, a distance in the fluidization vessel from a reference point to at least oneportion of the top surface of the fluidized sand bed is measured using the radar levelgauge. ln step 103, a bed state parameter is determined based on a measurement signalfrom the radar level gauge being representative of the distance. The bed stateparameter being determined is one of the distance, a level of the fluidized sand bedor a height of the fluidized sand bed. ln step 104, a variation of the bed state parameter is determined based on the bedstate parameter value determined in step 103 and at least one previously determinedbed state parameter value. The at least one previously determined bed stateparameter value has, in a previous iteration of the method loop, been stored in amemory in step 105, see below. ln step 105, data is stored in a memory. The data includes the determined bed state parameter, the determined amplitude and the determined frequency. ln step 106, a diagnostic algorithm is applied to at least a sub set the data stored inthe memory to determine if the fluidized sand bed comprises agglomerated orsintered sand particles. The diagnostic algorithm includes determining if thedetermined frequency is changing over time (based on stored frequency values).
    After step 106, the method returns to step 102 to once again measure the distance.ln this manner, the method steps 102-106 are repeated with predetermined timeinterval(s) or with a predetermined rate. The memory will thus contain time resolvedvalues of the bed state parameter, the amplitude and the frequency, i.e. values determined at each instant the method steps 102-106 are performed.
    The description above and the appended drawings are to be considered as non-limiting examples of the invention. The person skilled in the art realizes that severalchanges and modifications may be made within the scope of the invention. Forexample the fluidization vessel does not necessarily have to be cylindrical, and theevaluation means may be separate from the actual bubbling fluidized bed combustion device or may be included as software in another processing means. The scope of protection is determined by the appended patent claims.
    权利要求:
    Claims (14)
    [1] 1. Bubbling fluidized bed combustion device (1) comprising - a fluidization vessel (2); - a fluidized sand bed (3) arranged in said fluidization vessel; and - an arrangement for monitoring said fluidized sand bed, said arrangementcomprising at least one radar level gauge (4) arranged to repeatedly measurea distance (D) in said fluidization vessel from a reference point (5) to at leastone portion (6) of the top surface (7) of the fluidized sand bed, and to provide a measurement signal (S) representative of said distance.
    [2] 2. Bubbling fluidized bed combustion device according to claim 1, wherein saidarrangement further comprises evaluation means (8) configured to repeatedlydetermine a bed state parameter based on said signal, said state parameter beingone of said distance (D), a level of said fluidized sand bed (L) or a height (H) of saidfluidized sand bed.
    [3] 3. Bubbling fluidized bed combustion device according to claim 2, wherein saidevaluation means (8) is configured to repeatedly determine a variation of said bedstate parameter including determining an amplitude and/or a frequency of saidvariation based on current and previously determined bed state parameter values.
    [4] 4. Bubbling fluidized bed combustion device according to claim 3, wherein saidevaluation means (8) is configured to repeatedly store data in a memory, said dataincluding at least one of the determined bed state parameter, the determined amplitude and the determined frequency.
    [5] 5. Bubbling fluidized bed combustion device according to claim 4, wherein saidevaluation means (8) is configured to apply a diagnostic algorithm to at least a subset of said stored data to determine if said fluidized sand bed comprises agglomerated or sintered sand particles.
    [6] 6. Bubbling fluidized bed combustion device according to claim 5, wherein said diagnostic algorithm includes determining if said determined frequency is changing 12 over time, and if so indicate that said fluidized sand bed comprises agglomerated or sintered sand particles.
    [7] 7. Bubbling fluidized bed combustion device according to any one of claims 3-6,further comprising:- gas supply means (9) arranged to supply gas to fluidize said sand bed;-fuel supply means (10) arranged to supply fuel to said sand bed; and-feedback control means arranged to control said gas supply means and/or saidfuel supply means based on at least one of the determined bed stateparameter, the determined frequency and the determined amplitude in order to control combustion in said sand bed.
    [8] 8. Method for monitoring a fluidized bed (3) in a bubbling fluidized bed combustiondevice (1) comprising a fluidization vessel (2) and a fluidized sand bed (3) arranged in said fluidization vessel, said method comprising - providing at least one radar level gauge (4) in or at said fluidization vessel; and- repeatedly measuring a distance (D) in said fluidization vessel from areference point (5) to at least one portion (6) of the top surface (7) of the fluidized sand bed using said radar level gauge.
    [9] 9. Method according to claim 8, further comprising repeatedly determining a bedstate parameter based on a measurement signal from said radar level gauge (4)being representative of said distance (D), said state parameter being one of saiddistance, a level of said fluidized sand bed or a height of said fluidized sand bed.
    [10] 10. Method according to claim 9, further comprising repeatedly determining avariation of said bed state parameter including determining an amplitude and/or afrequency of said variation based on current and previously determined bed state parameter values.
    [11] 11. Method according to claim 10, further comprising repeatedly storing data in amemory, said data including at least one of the determined bed state parameter, the determined amplitude and the determined frequency. 13
    [12] 12. Method according to claim 11, further comprising applying a diagnostic algorithmto at least a sub set of said stored data to determine if said fluidized sand bed comprises agglomerated or sintered sand particles.
    [13] 13. Method according to claim 12, said diagnostic algorithm including determining ifsaid determined frequency is changing over time, and if so indicating that saidfluidized sand bed comprises agglomerated or sintered sand particles.
    [14] 14. Method according to any one of claims 10-13, wherein said bubbling fluidized bedcombustion device (1) further comprises gas supply means (9) arranged to supplygas to fluidize said sand bed and fuel supply means (10) arranged to supply fuel tosaid sand bed, said method further comprising controlling combustion in saidfluidized sand bed by controlling said gas supply means and/or said fuel supplymeans based on at least one of the determined bed state parameter, the determined frequency and the determined amplitude.
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    同族专利:
    公开号 | 公开日
    EP3274630A1|2018-01-31|
    US20180106475A1|2018-04-19|
    SE541321C2|2019-07-02|
    EP3274630A4|2018-12-05|
    CA2979522A1|2016-09-29|
    US10801719B2|2020-10-13|
    ES2870025T3|2021-10-26|
    KR20180014686A|2018-02-09|
    PL3274630T3|2021-07-05|
    WO2016153419A1|2016-09-29|
    EP3274630B1|2021-02-17|
    KR102239529B1|2021-04-12|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    SE1550364A|SE541321C2|2015-03-25|2015-03-25|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|SE1550364A| SE541321C2|2015-03-25|2015-03-25|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    PL16769174T| PL3274630T3|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    DK16769174.0T| DK3274630T3|2015-03-25|2016-03-23|Bubble fluidized bed incinerator and method of monitoring the fluidized bed in such an incinerator|
    US15/560,705| US10801719B2|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    ES16769174T| ES2870025T3|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method of monitoring the fluidized bed in such combustion device|
    PCT/SE2016/050242| WO2016153419A1|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    CA2979522A| CA2979522A1|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    EP16769174.0A| EP3274630B1|2015-03-25|2016-03-23|Bubbling fluidized bed combustion device and method for monitoring the fluidized bed in such a combustion device|
    KR1020177030767A| KR102239529B1|2015-03-25|2016-03-23|Bubble fluidized bed combustion device and method of fluidized bed monitoring of such combustion device|
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