EP2404147A1 - Arrangement for mounting a sensor in a heat exchanger wall - Google Patents

Arrangement for mounting a sensor in a heat exchanger wall

Info

Publication number
EP2404147A1
EP2404147A1 EP10748389A EP10748389A EP2404147A1 EP 2404147 A1 EP2404147 A1 EP 2404147A1 EP 10748389 A EP10748389 A EP 10748389A EP 10748389 A EP10748389 A EP 10748389A EP 2404147 A1 EP2404147 A1 EP 2404147A1
Authority
EP
European Patent Office
Prior art keywords
sensor
tube
wall
arrangement according
sensor element
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP10748389A
Other languages
German (de)
French (fr)
Other versions
EP2404147A4 (en
Inventor
Timo Leino
Markku Orjala
Jouko Aalto
Janne KÄRKI
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
VTT Technical Research Centre of Finland Ltd
Original Assignee
VTT Technical Research Centre of Finland Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by VTT Technical Research Centre of Finland Ltd filed Critical VTT Technical Research Centre of Finland Ltd
Publication of EP2404147A1 publication Critical patent/EP2404147A1/en
Publication of EP2404147A4 publication Critical patent/EP2404147A4/en
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F22STEAM GENERATION
    • F22BMETHODS OF STEAM GENERATION; STEAM BOILERS
    • F22B37/00Component parts or details of steam boilers
    • F22B37/02Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
    • F22B37/38Determining or indicating operating conditions in steam boilers, e.g. monitoring direction or rate of water flow through water tubes

Definitions

  • the present invention relates to an arrangement for mounting a sensor in a heat exchanger wall, which is formed of steel tubes, of a selected internal diameter and minimum wall thickness, welded next to each other with fin plates in between the tubes forming a membrane wall, which delimit the furnace, from which the heat flux is coming, which is arranged to heat a high-pressure medium travelling in the steel tubes, and in which the sensor chamber, and the conductor channel it requires for the sensor leads, are located on the furnace side, in a thickening of the wall of the steel tube, and in which a sensor element to be attached to some other tube wall is formed for the measurement sensor chamber, comprising at least one length of steel tube, in which the said wall thickening is formed.
  • Heat flux is measured using a heat-flux sensor, which is mounted in the tube wall.
  • a heat-flux sensor which is mounted in the tube wall.
  • Various solutions are known, by means of which the sensor can be installed without disturbing the flows on the furnace side.
  • Publication US 6,485,174 discloses a heat-flux measuring ar- rangement to be mounted on a fin plate.
  • the fin plate permits a much easier way of mounting the sensor than the external surface of a tube. If a more accurate measurement of heat flux is required through the tube wall, it is made from the tube itself.
  • a dent is made on the furnace side, to create a suitable chamber for the sensors and their leads. After creating the sensor chamber and channel the dent is welded over, when the surface becomes uniform with the rest of the heat exchanger surface. This solu- tion contains a considerable drawback. Inside the tube the flow is disturbed due to a dent in an indefinite way. Especially in a boiler with natural circulation, the flow can differ substantially in the measurement tube from the other tubes .
  • the present invention is intended to create an arrangement es- pecially for the measurement of the heat flux of an evaporator surface, which does not have the aforementioned drawbacks.
  • the arrangement according to the invention is characterized by what is stated in the characterizing portion of Claim 1.
  • the homogeneous structure of the steel piece, in which the tube itself, the sensor chamber, and the leads channel can be machined and created in casting in the controlled circumstances, achieves precisely predictable structural and thermo-technical properties.
  • the arrangement is also pre-eminently suitable for the measurement of other variables.
  • the measurement method is mounted permanently in the heat exchanger surface of the evaporator, so that the measurement results correspond very well to the real evaporator surface.
  • the thickening of the wall faces inwards and the furnace side of the mounted sensor element lies on the plane of the rest of the heat exchanger surfaces, so that the channel formed by the internal diameter is shaped as a gentle bend and the sensor chamber and channel for the leads will fit into the local enlargement of the tube wall thickness .
  • the arrangement according to the invention does not preclude the thickening being made as a very gently curved protrusion into the furnace, in which case the internal channel in the tube could be quite straight.
  • the sensor chamber and lead channel can be formed precisely in a wall thickening outside the minimum wall thickness.
  • the tube is drilled into a steel piece.
  • the sensor element is a cast piece, in which the medium channel is formed with the aid of a core. This can also be applied in the manufacture of the sensor chamber and conductor channel .
  • the sensor element includes not only a first tube containing the sensor chamber, but also at least one tube welded to it on the side of the said channel, in which case the field conditions need not particularly endanger the channel and leads possibly inside it.
  • This risk can be further reduced by forming shapes corresponding to the fin and welding in a homogeneous steel piece at least on the channel side, in which case the joint welding will be even further from the leads channel.
  • the sensor element formed in the homogeneous piece can also be corrosion coated with another material, for example, according to the requirements of a recovery boiler.
  • the sensor chamber can be under the surface or open out onto the surface, depending on the type of sensor in question.
  • a thermocouple suitable for measuring heat flux is placed under the surface, whereas a sensor measuring corrosion will be placed on the surface.
  • the method according to the invention permits the measurement of heat flux and corrosion from an evaporator surface.
  • Other benefits and embodiments of the invention are described here- inafter, in connection with an example application.
  • Figure 1 shows a cross-section of a sensor element according to the invention mounted on the wall of a boiler.
  • Figure 2 shows a top view of the sensor element of Figure 1, when separate.
  • Figure 3 shows a view from the furnace of the sensor element, when separate.
  • Figure 4 shows an alternative way of forming the tube of the sensor element.
  • the figures show a sensor element intended for the tubes of a boiler.
  • the boiler can be a hot water boiler or a steam- generating boiler.
  • the furnace is marked with the reference number 8, the tube equipped with a bend with the number 4, the parallel tubes with number 3, and the internal channel of the tubes with the reference number 18, 18', of which the latter is the internal channel 18 ' in the location of the bend.
  • a gentle bend do not disturb the flow of the medium 19, which is heated by the heat flux transferred from the furnace through the tube wall.
  • FIG 1 there is insulation 23 in the boiler wall on the boiler-room side of the tube wall and a skin plate 22 on the boiler-room side.
  • the leads 13 ( Figure 2) are run to the out- side of the wall in a conduit 14 and from there through a connector component 25 to a junction box 16.
  • the tube 14 is supported on angle supports 17 and it should have a sufficient length to reduce heat conduction, though it can turn through a 90° bend.
  • the tubes 3, 4 there is a common flow cross-sectional area, i.e. a channel, which is otherwise marked with the reference number 18, but at the bend location the channel is marked with the reference number 18 '.
  • the fin plate 11 is first welded to the homogeneous steel piece, i.e. tube 4 with welds 12 and 12". After that the conductor channel 5 is drilled from the boiler- room side. On the boiler-room side, the weld 12" can be thicker, in order to give this area heat-transfer conditions similar to those of the other tubes.
  • the weld 12 ' of the fin plate 11 in the vicinity of the channel 5 to the adjacent tube is quite critical and is best made in factory conditions.
  • the drill-hole direction 9 of the leads channel 5 is marked on the furnace side.
  • This drill hole 9 connects to a drill hole made from the other side.
  • the cavity is closed by welding, unless the sensor is left on the surface intentionally.
  • the leads 13 run on the hot side in the conductor channel 5.
  • the leads 13 can also be protected on the surface of the tube by welding on the channel 28 up to the connection conduit 14.
  • the sensor element 1 to be installed is very compact and can withstand installation without endangering the sensor in the sensor chamber 2 and its leads.
  • the sensor element, together with the sensors and leads, can be cali- brated prior to delivery to the installation site, where it can be welded on, using conventional work procedures.
  • a homogeneous piece makes possible the best durability of the sensor element in terms of pressure resistance, while also giving excellent measurement precision.
  • a homogeneous piece according to Figure 4 can comprise not only a tube 4, but also a fin 11 integrated with it, at least on the side of the conductor channel 5.
  • the fin 11 and the shapes corresponding to its welds are formed in same piece.
  • the heat flux for example, can be measured from the evaporator surface of a fluidized bed boiler.
  • additional information is obtained on the heat load of the evaporator at the measurement location, making it possible to investigate both excessive heat fluxes and fouling on the evaporator surface.
  • information on boiler's temperature distribution is obtained with different fuels.
  • additional information is obtained for the design of the boiler's evaporator and also information for the sootblowing.
  • Furnace corrosion measurements that have been developed earlier have been made with special probes, which are installed in the furnace through openings. Corresponding corrosion measurement methods do not exist.
  • Hot corrosion is a problem, especially on the evaporator and superheater surfaces of recovery and waste-incineration boilers.
  • the hot-corrosion sensor can itself operate in many different ways. The following are among the known types: Electrical Resistance (ER) , Electrochemical Noise (EN) , and Linear Polarization Resistance (LPR) .
  • ER Electrical Resistance
  • EN Electrochemical Noise
  • LPR Linear Polarization Resistance
  • Each technique has its own specific sensor type, which is fitted to the sensor element according to the invention.
  • the sensor is insulated from the steel tube by means of a suitable cast mass.
  • the corrosion monitoring can be used, for instance, to control the use of additives preventing corrosion (fuel, chemicals), as well as sootblowing as required, so that the material of the evaporator will last longer and the replacement interval will be lengthened. Based on the measurement results, addi- tional information is also obtained for the selection of the material of the boiler evaporator, as well as on the effects of different fuels on the corrosion of the evaporator surface.
  • hot corrosion can be measured from the evaporator surface of a power-plant boiler, without disturbing the flow of the furnace or steam.
  • the measurement method is mounted permanently on the heat exchanger surface of the evaporator, so that the measurement results correspond well with the real evaporator surface.
  • the shape of the sensor chamber can be any whatever and be designed according to the sensor or sensors at the time. It can be a simple drill hole, for example, if the sensor is an optical fibre extending to the surface, for optical observation of the furnace .
  • the arrangement according to the invention can be used in connection with nearly all types of sensor.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Measuring Temperature Or Quantity Of Heat (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The invention relates to an arrangement for mounting a sensor in a heat exchanger wall, which is formed of steel tubes (3, 4) welded next to each other with fin plates (11) in between the tubes forming a membrane wall. The sensor chamber (2) and the conductor channel (5) required by it for the sensor leads (13) are located on the furnace (8) side in a thickening (6) of the wall of the steel tube (4). A sensor element (1) to be attached to some other tube wall is formed for the measurement sensor chamber (2) as a homogeneous steel piece, comprising at least one length of steel tube (3, 4), in which the said wall thickening (6) is formed.

Description

ARRANGEMENT FOR MOUNTING A SENSOR IN A HEAT EXCHANGER WALL
The present invention relates to an arrangement for mounting a sensor in a heat exchanger wall, which is formed of steel tubes, of a selected internal diameter and minimum wall thickness, welded next to each other with fin plates in between the tubes forming a membrane wall, which delimit the furnace, from which the heat flux is coming, which is arranged to heat a high-pressure medium travelling in the steel tubes, and in which the sensor chamber, and the conductor channel it requires for the sensor leads, are located on the furnace side, in a thickening of the wall of the steel tube, and in which a sensor element to be attached to some other tube wall is formed for the measurement sensor chamber, comprising at least one length of steel tube, in which the said wall thickening is formed.
By means of the measurement of the heat flux, additional information is obtained on the temperature distribution of a steam boiler furnace, as well of the thermal load of. the e- vaporator, so that excessive heat fluxes and fouling of the evaporator surface can be measured.
Heat flux is measured using a heat-flux sensor, which is mounted in the tube wall. Various solutions are known, by means of which the sensor can be installed without disturbing the flows on the furnace side.
Publication US 6,485,174 discloses a heat-flux measuring ar- rangement to be mounted on a fin plate. Naturally, the fin plate permits a much easier way of mounting the sensor than the external surface of a tube. If a more accurate measurement of heat flux is required through the tube wall, it is made from the tube itself. In publication US 7,249,885, a dent is made on the furnace side, to create a suitable chamber for the sensors and their leads. After creating the sensor chamber and channel the dent is welded over, when the surface becomes uniform with the rest of the heat exchanger surface. This solu- tion contains a considerable drawback. Inside the tube the flow is disturbed due to a dent in an indefinite way. Especially in a boiler with natural circulation, the flow can differ substantially in the measurement tube from the other tubes .
In the article λThe measurement of radiant heat flux in large boiler furnaces-II. Development of flux measuring instruments', Neal, S. B. H. et al . , Int. J. Heat Mass Transfer, Vol. 23, pp. 1023 - 1031, a solution is also disclosed, in which the tube is bent inwards to form a bend and the cavity that arises is used as a mounting chamber, the cavity then being welded over evenly. In such a solution, the filler welding creates two kinds of problem. Firstly, its durability against bed material is questionable. Secondly, the extensive welding and non-homogeneous structure weaken the tube and create a particular stress state in it. Its structural durability is difficult to estimate.
The present invention is intended to create an arrangement es- pecially for the measurement of the heat flux of an evaporator surface, which does not have the aforementioned drawbacks. The arrangement according to the invention is characterized by what is stated in the characterizing portion of Claim 1. The homogeneous structure of the steel piece, in which the tube itself, the sensor chamber, and the leads channel can be machined and created in casting in the controlled circumstances, achieves precisely predictable structural and thermo-technical properties. The arrangement is also pre-eminently suitable for the measurement of other variables. By means of the arrangement that has been developed, heat flux in particular can be measured more precisely than previously from the evaporator surface of a fluidized bed boiler.
The measurement method is mounted permanently in the heat exchanger surface of the evaporator, so that the measurement results correspond very well to the real evaporator surface.
In one embodiment, the thickening of the wall faces inwards and the furnace side of the mounted sensor element lies on the plane of the rest of the heat exchanger surfaces, so that the channel formed by the internal diameter is shaped as a gentle bend and the sensor chamber and channel for the leads will fit into the local enlargement of the tube wall thickness . However, the arrangement according to the invention does not preclude the thickening being made as a very gently curved protrusion into the furnace, in which case the internal channel in the tube could be quite straight.
According to the invention, the sensor chamber and lead channel can be formed precisely in a wall thickening outside the minimum wall thickness.
In one embodiment, the tube is drilled into a steel piece. Alternatively, the sensor element is a cast piece, in which the medium channel is formed with the aid of a core. This can also be applied in the manufacture of the sensor chamber and conductor channel .
In one embodiment, the sensor element includes not only a first tube containing the sensor chamber, but also at least one tube welded to it on the side of the said channel, in which case the field conditions need not particularly endanger the channel and leads possibly inside it. This risk can be further reduced by forming shapes corresponding to the fin and welding in a homogeneous steel piece at least on the channel side, in which case the joint welding will be even further from the leads channel.
The sensor element formed in the homogeneous piece can also be corrosion coated with another material, for example, according to the requirements of a recovery boiler.
The sensor chamber can be under the surface or open out onto the surface, depending on the type of sensor in question. A thermocouple suitable for measuring heat flux is placed under the surface, whereas a sensor measuring corrosion will be placed on the surface.
The method according to the invention permits the measurement of heat flux and corrosion from an evaporator surface. Other benefits and embodiments of the invention are described here- inafter, in connection with an example application.
In the following, the invention is described with the aid of examples and with reference to the accompanying figures.
Figure 1 shows a cross-section of a sensor element according to the invention mounted on the wall of a boiler.
Figure 2 shows a top view of the sensor element of Figure 1, when separate. Figure 3 shows a view from the furnace of the sensor element, when separate.
Figure 4 shows an alternative way of forming the tube of the sensor element. The figures show a sensor element intended for the tubes of a boiler. The boiler can be a hot water boiler or a steam- generating boiler. In the figures, the furnace is marked with the reference number 8, the tube equipped with a bend with the number 4, the parallel tubes with number 3, and the internal channel of the tubes with the reference number 18, 18', of which the latter is the internal channel 18 ' in the location of the bend. A gentle bend do not disturb the flow of the medium 19, which is heated by the heat flux transferred from the furnace through the tube wall.
According to Figure 1, in the homogeneous structure of the tube 4 on the furnace 8 side there is a thickening 6, in which a sensor chamber 2 can be formed, and also a channel 5 (Figure 2) leading to it for the sensor leads.
In Figure 1, there is insulation 23 in the boiler wall on the boiler-room side of the tube wall and a skin plate 22 on the boiler-room side. The leads 13 (Figure 2) are run to the out- side of the wall in a conduit 14 and from there through a connector component 25 to a junction box 16. The tube 14 is supported on angle supports 17 and it should have a sufficient length to reduce heat conduction, though it can turn through a 90° bend. At the base of the junction box 16, there is a sili- con seal 26, in order to achieve steam tightness.
According to Figure 2, there are tubes 3 in the sensor element parallel to the special tube 4, attached to it by fin plates 11 and welding 12. In the tubes 3, 4, there is a common flow cross-sectional area, i.e. a channel, which is otherwise marked with the reference number 18, but at the bend location the channel is marked with the reference number 18 '. At the conductor channel 5, the fin plate 11 is first welded to the homogeneous steel piece, i.e. tube 4 with welds 12 and 12". After that the conductor channel 5 is drilled from the boiler- room side. On the boiler-room side, the weld 12" can be thicker, in order to give this area heat-transfer conditions similar to those of the other tubes.
The weld 12 ' of the fin plate 11 in the vicinity of the channel 5 to the adjacent tube is quite critical and is best made in factory conditions.
It is easy to see from this Figure 2 that it could be advantageous if the homogeneous piece also included in its shape the fin plate on the side of the channel 5, together with its welds. When the sensor element 1 is attached to the rest of the boiler's tube wall, the edge-most fin plates II1 are welded onto the adjacent tubes. Correspondingly, the bevelled joint ends 3' and 4' (Figure 3) of the tubes 3, 4 are welded endwise to the tubes of the wall.
In Figure 2, the drill-hole direction 9 of the leads channel 5 is marked on the furnace side. This drill hole 9 connects to a drill hole made from the other side. Instead of drill holes, it is possible to use other machining procedures, such as electro-discharge machining. After the machining of the sensor cavity and the installation of the sensor itself, the cavity is closed by welding, unless the sensor is left on the surface intentionally. The leads 13 run on the hot side in the conductor channel 5. On the other side, the leads 13 can also be protected on the surface of the tube by welding on the channel 28 up to the connection conduit 14.
According to Figure 3, the sensor element 1 to be installed is very compact and can withstand installation without endangering the sensor in the sensor chamber 2 and its leads. The sensor element, together with the sensors and leads, can be cali- brated prior to delivery to the installation site, where it can be welded on, using conventional work procedures.
A homogeneous piece makes possible the best durability of the sensor element in terms of pressure resistance, while also giving excellent measurement precision.
A homogeneous piece according to Figure 4 can comprise not only a tube 4, but also a fin 11 integrated with it, at least on the side of the conductor channel 5. In this case, the fin 11 and the shapes corresponding to its welds are formed in same piece.
By means of the arrangement according to the invention, the heat flux, for example, can be measured from the evaporator surface of a fluidized bed boiler. By means of measurement of the heat flux, additional information is obtained on the heat load of the evaporator at the measurement location, making it possible to investigate both excessive heat fluxes and fouling on the evaporator surface. In addition, information on boiler's temperature distribution is obtained with different fuels. On the basis of the measurement results, additional information is obtained for the design of the boiler's evaporator and also information for the sootblowing.
Furnace corrosion measurements that have been developed earlier have been made with special probes, which are installed in the furnace through openings. Corresponding corrosion measurement methods do not exist.
Hot corrosion is a problem, especially on the evaporator and superheater surfaces of recovery and waste-incineration boilers. Using the arrangement according to the invention, the state of corrosion on the evaporator surface can be monitored at the measurement location, without disturbing the flow properties. The hot-corrosion sensor can itself operate in many different ways. The following are among the known types: Electrical Resistance (ER) , Electrochemical Noise (EN) , and Linear Polarization Resistance (LPR) . Each technique has its own specific sensor type, which is fitted to the sensor element according to the invention. The sensor is insulated from the steel tube by means of a suitable cast mass.
The corrosion monitoring can be used, for instance, to control the use of additives preventing corrosion (fuel, chemicals), as well as sootblowing as required, so that the material of the evaporator will last longer and the replacement interval will be lengthened. Based on the measurement results, addi- tional information is also obtained for the selection of the material of the boiler evaporator, as well as on the effects of different fuels on the corrosion of the evaporator surface.
By means of corrosion measurement, additional information will be obtained on the hot corrosion of the furnace of a steam boiler. The information can be used, for instance, in the selection of fuel blend, in the use of additives, and in material selection. Using the measurement method developed, hot corrosion can be measured from the evaporator surface of a power-plant boiler, without disturbing the flow of the furnace or steam. The measurement method is mounted permanently on the heat exchanger surface of the evaporator, so that the measurement results correspond well with the real evaporator surface.
The shape of the sensor chamber can be any whatever and be designed according to the sensor or sensors at the time. It can be a simple drill hole, for example, if the sensor is an optical fibre extending to the surface, for optical observation of the furnace . The arrangement according to the invention can be used in connection with nearly all types of sensor.

Claims

1. Arrangement for mounting a sensor in a heat exchanger wall, which is formed of steel tubes (3, 4), of a selected internal diameter and minimum wall thickness, welded next to each other with fin plates in between the tubes (11) forming a membrane wall, which delimit the furnace, from which the heat flux is coming, which is arranged to heat a high-pressure medium travelling in the steel tubes (3, 4), and in which the sensor chamber (2) and the conductor channel (5) it requires for the sensor leads (13) are located on the furnace side (8), in a thickening (6) of the wall of the steel tube (4) , and in which a sensor element (1) to be attached to some other tube wall is formed for the measurement sensor chamber (2), comprising at least one length of steel tube (3, 4), in which the said wall thickening (6) is formed, characterized in that the sensor element (1) is essentially a homogeneous steel piece, in which a channel (18, 18'), corresponding in internal diameter to the rest of the tube wall, is formed.
2. Arrangement according to Claim 1, characterized, in that the said thickening (6) of the wall faces inwards and the furnace-side (8) part of the installed sensor element (1) lies on the plane of the rest of the heat exchanger surface, in which case the channel (18, 18') forming the internal diameter is shaped in a gentle inward curve.
3. Arrangement according to Claim 1 or 2 , characterized in that the said sensor chamber (2) and conductor channel (5) are formed in the wall thickening (6) outside the minimum wall thickness.
4. Arrangement according to any of Claims 1 - 3, characterized in that the tube (18, 18') is drilled in the steel piece.
5. Arrangement according to any of Claims 1 - 3, characterized in that the sensor element (1) is a cast piece, in which the tube (18, 18') is formed with the aid of a core.
6. Arrangement according to any of Claims 1 - 5, characterized in that the sensor element (1) includes not only a first tube (4) containing the sensor chamber, but also at least one tube (3) welded to it on the said channel side.
7. Arrangement according to any of Claims 1 - 6, characterized in that the sensor element (1) includes a corrosion coating on the side next to the furnace (8) .
8. Arrangement according to any of Claims 1 - 7, characterized in that the sensor element (1) includes a thermocouple fitted in the sensor chamber (2) .
9. Arrangement according to any of Claims 1 - 8, character- ized in that the sensor element (1) includes a corrosion sensor fitted in the sensor chamber (2) .
10. Arrangement according to any of Claims 1 - 9, characterized in that the sensor element (1) includes a channel tube (14) attached rigidly to one of the said tubes (3) .
11. Arrangement according to any of Claims 1 - 10, characterized in that the homogeneous steel piece includes an external shape, which corresponds to at least one fin together with its welds .
EP10748389.3A 2009-03-02 2010-03-02 Arrangement for mounting a sensor in a heat exchanger wall Withdrawn EP2404147A4 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FI20095206A FI20095206A0 (en) 2009-03-02 2009-03-02 Method for measuring from the evaporation surface
PCT/FI2010/050161 WO2010100335A1 (en) 2009-03-02 2010-03-02 Arrangement for mounting a sensor in a heat exchanger wall

Publications (2)

Publication Number Publication Date
EP2404147A1 true EP2404147A1 (en) 2012-01-11
EP2404147A4 EP2404147A4 (en) 2017-05-10

Family

ID=40510206

Family Applications (1)

Application Number Title Priority Date Filing Date
EP10748389.3A Withdrawn EP2404147A4 (en) 2009-03-02 2010-03-02 Arrangement for mounting a sensor in a heat exchanger wall

Country Status (4)

Country Link
EP (1) EP2404147A4 (en)
KR (1) KR101618394B1 (en)
FI (1) FI20095206A0 (en)
WO (1) WO2010100335A1 (en)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8870455B2 (en) 2011-09-15 2014-10-28 Jeffrey N. Daily Temperature sensing assembly for measuring temperature of a surface of a structure
BE1022051B1 (en) 2013-05-23 2016-02-10 Sa Cockerill Maintenance & Ingenierie THERMAL FLOW SENSOR
WO2017036997A1 (en) 2015-09-03 2017-03-09 Basf Se Process for formulating quantum dots
WO2017144401A1 (en) 2016-02-23 2017-08-31 Basf Se Luminescent particles
US20200348018A1 (en) * 2017-11-17 2020-11-05 Sandvik Intellectual Property Ab Boiler Tube and Boiler Tube Unit and Furnace
US11408779B2 (en) 2019-06-03 2022-08-09 Daily Thermetrics Corporation Temperature sensor and methods of use

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5826481B2 (en) * 1977-04-11 1983-06-03 三菱重工業株式会社 How to attach a thermocouple to a boiler tube
IT1164309B (en) * 1983-07-07 1987-04-08 Cise Spa INSTRUMENTED GROUP FOR THE SURVEY OF TEMPERATURES AND HEAT FLOWS IN EVAPORATIVE WALLS OF STEAM GENERATORS
GB9220856D0 (en) 1992-10-03 1992-11-18 Boiler Management Systems Limi Improvements in or relating to boiler wall cleaning
DE10248312A1 (en) * 2002-10-16 2004-04-29 Clyde Bergemann Gmbh Heat flow measuring device for pressure pipe and method for measuring heat flow through pressure pipes
US6848373B2 (en) * 2003-02-21 2005-02-01 Breen Energy Solutions Method of monitoring heat flux and controlling corrosion of furnace wall tubes
GB0508584D0 (en) * 2005-04-28 2005-06-01 Boiler Man Systems Internation A pipe assembly

Also Published As

Publication number Publication date
FI20095206A0 (en) 2009-03-02
KR20120007494A (en) 2012-01-20
EP2404147A4 (en) 2017-05-10
WO2010100335A1 (en) 2010-09-10
KR101618394B1 (en) 2016-05-04

Similar Documents

Publication Publication Date Title
WO2010100335A1 (en) Arrangement for mounting a sensor in a heat exchanger wall
CA2360217C (en) Attachable heat flux measuring device
US4527908A (en) Instrument unit for measuring temperatures and heat flux in evaporative walls of steam generators
US20090188645A1 (en) Tube fouling monitor
TWI823995B (en) Temperature sensor system
JP2013500456A (en) Heat exchange device and use thereof
JP5215750B2 (en) Sensor, liquid film measuring device
US4516425A (en) Device for measuring the speed of the fluid in the annular space of a steam generator
CN112629685A (en) Device and method for measuring temperature in boiler heating surface pipe
CA2572518A1 (en) Establishing a connection between steam generator heating surfaces and a collector and/or distributor
KR101926649B1 (en) Pressure Vessel for Heat Transfer and Flow Control Experiments of Reactor Building
CN109115355B (en) Method for measuring metal wall temperature of heating surface of boiler
CN115681945A (en) Online monitoring method for temperature of fire-facing side wall of supercritical carbon dioxide boiler hearth
GB2410558A (en) Heat flow measuring device for pressure pipes and method for measuring a heat flow penetrating pressure pipes
AU2014270734B2 (en) Heat flow sensor
CN100368779C (en) Boiler water circulation safety online monitor
JP2003287464A (en) Thermocouple well
CN111356877A (en) Boiler tube, boiler tube unit and melting furnace
WO1998054549A1 (en) Midloop ultrasonic instrument
CN206450332U (en) A kind of device that temperature survey is carried out to pipe for shell-and-tube exchanger journey fluid
JP2548392Y2 (en) Mounting structure of heat transfer tube temperature detector in thermal equipment
KR101961738B1 (en) Heat flux sensor installed boiler wall tube of thermal power plant
KR102006828B1 (en) Erosion and high-temperature corrosion monitoring apparatus using the bimetal
JP3252533U (en) Header structure and boiler
CN204281811U (en) A kind of Technique in Boiler Membrane Water Cooled Wall local post weld heat treatment device

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20110929

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR

DAX Request for extension of the european patent (deleted)
RA4 Supplementary search report drawn up and despatched (corrected)

Effective date: 20170406

RIC1 Information provided on ipc code assigned before grant

Ipc: G01K 17/20 20060101AFI20170401BHEP

Ipc: F22B 37/38 20060101ALI20170401BHEP

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20171107