WO2002095316A1 - Arrangement for connecting a pipe to a heat exchanger - Google Patents

Arrangement for connecting a pipe to a heat exchanger Download PDF

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Publication number
WO2002095316A1
WO2002095316A1 PCT/SE2002/000959 SE0200959W WO02095316A1 WO 2002095316 A1 WO2002095316 A1 WO 2002095316A1 SE 0200959 W SE0200959 W SE 0200959W WO 02095316 A1 WO02095316 A1 WO 02095316A1
Authority
WO
WIPO (PCT)
Prior art keywords
pipe
section
heat
deformable
heat exchangers
Prior art date
Application number
PCT/SE2002/000959
Other languages
French (fr)
Inventor
Max Xie
Original Assignee
Rekuperator Svenska Ab
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 Rekuperator Svenska Ab filed Critical Rekuperator Svenska Ab
Priority to EP02733715A priority Critical patent/EP1389297A1/en
Publication of WO2002095316A1 publication Critical patent/WO2002095316A1/en
Priority to US10/707,125 priority patent/US20040104009A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0246Arrangements for connecting header boxes with flow lines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F9/00Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
    • F28F9/02Header boxes; End plates
    • F28F9/0236Header boxes; End plates floating elements
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • F28D21/0003Recuperative heat exchangers the heat being recuperated from exhaust gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/26Safety or protection arrangements; Arrangements for preventing malfunction for allowing differential expansion between elements

Definitions

  • the present invention relates to an arrangement in a pipe joint for a heat exchanger - also termed a recuperator - that is adapted for use with a gas turbine for stationary use in a small scale combined power and heating plant or for mobile use in a vehicle.
  • a heat exchanger of the said type may be used in, for example, a combined power and heating plant, for mobile use or in a reserve power station.
  • the recuperator may for instance be made up of a plate heat exchanger comprising a number of plates manufactured from very thin sheet metal, generally having a thickness of about 0,1 mm.
  • the plates are provided with corrugations in a known manner, whereby they are stabilised relative to each other in a wave shaped pattern. Spaces between the corrugations will then form flow channels for a heat emitting medium and a heat-absorbing medium. If a gas turbine is used, the heat-emitting medium is combusted gases leaving the turbine, while the heat-absorbing medium is usually air.
  • FIG. 2 shows an inlet pipe connection 2 for conducting a heat emitting medium 6 to the heat exchanger.
  • the combusted exhaust gas at a temperature of about 650°C and a pressure of about 1 ,1 bar, is conducted from a gas turbine to the inlet pipe connection 2 and into the heat exchanger.
  • a heat absorbing medium 7, such as air, is heated by the exhaust gases, whereby the air leaves the heat exchanger through the outlet pipe connection 3, at a temperature of about 610°C and a pressure of 4 bar.
  • the lower end A of the inlet pipe connection 2 is mounted with a force fit onto a corresponding recess in a flange on the heat exchanger.
  • the lower end A can be provided with a number of radial grooves C around its periphery, in order to increase the contact pressure between said end and the recess B.
  • the grooves C may also be provided with sealing devices of some kind. Thermal loading caused by, for instance, axial expansion of the inlet pipe connection must be absorbed by the joint, whereby the component parts are movable relative to each other.
  • the arrangement may also have a certain leakage flow LF between the inlet and outlet parts.
  • the leakage flow is partly due to the pressure difference and partly due to poor fitting and relative movement between the component parts.
  • Such a leakage will lower the efficiency of the heat exchanger.
  • one problem is to achieve a pipe joint that can be deformed in order to absorb thermal loads without being damaged.
  • it may have to absorb movement in both axial and radial direction, in relation to the main axis of the pipe joint.
  • a further problem fit such a pipe joint between two fixed points, where variations in fit and tolerance between the component parts of the heat exchanger may sometimes occur. In such cases it is also desirable to have a pipe joint that is deformable in several directions.
  • the purpose of the current invention is to eliminate the problems described in relation to the prior art, thereby fulfilling the desired objectives of an improved pipe arrangement for a heat exchanger, as well as providing a simple and inexpensive embodiment for this purpose.
  • an outgoing collection channel for said heat-absorbing medium is arranged on the same side of the heat exchanger and has an outlet section connected to said inlet and outlet pipe.
  • the inlet pipe comprises a deformable first pipe section, arranged to absorb thermal and mechanical movements in both axial and radial directions, and at least one further pipe section.
  • the deformable section is preferably, but not necessarily, elastically deformable.
  • the heat exchanger may co-operate with a gas turbine, whereby its combusted exhaust gases is used as the heat-emitting medium.
  • the inlet pipe connection has a deformable first pipe section made up of a substantially cylindrical pipe, with walls having a corrugated cross-section in the axial direction of the pipe.
  • a deformable first pipe section made up of a substantially cylindrical pipe, with walls having a corrugated cross-section in the axial direction of the pipe.
  • the average diameter that is the average of the inner and outer diameters of the corrugations, should be larger than the inner diameter of the adjoining second pipe section.
  • the inner diameter of the deformable first pipe section corresponding to the smallest diameter of the corrugated section, is equal to the inner diameter of the second pipe section.
  • the cross-section of the corrugated section may be varied depending on the size and direction of the thermal movements to be absorbed.
  • a suitable shape is a sinusoidal cross-section, where the amplitude and wavelength can be varied to give the desired properties with respect to deformability in the axial and radial directions.
  • the first pipe section is preferably elastically deformable.
  • the inlet and outlet pipe joints are arranged concentrically, it is further possible to distribute the flow losses between inlet and outlet.
  • the average diameter of the corrugated section that is the average of the inner and outer diameters of the corrugations, can be equal to the inner diameter of the adjoining second pipe section.
  • a corrugated section as described above can be manufactured, for instance, by means of rolling, for metallic materials, injection moulding, for plastic materials, or winding, for composite material.
  • the resistance to deformation of the first pipe section is decided by the relative axial distance and radial amplitude of the corrugations, as well as the material thickness.
  • the corrugated section may have a material thickness of 0,3-0,6 mm.
  • the selected thicknesses and the relation between these is of course dependent on the size of the thermal movements, the dimensions of the pipes, the pressure of the flowing media and other factors.
  • the second pipe section of the inlet pipe has a cylindrical basic shape.
  • the deformable section may be attached to the cylindrical pipe section upstream or downstream in the direction of flow. If the deformable section is placed downstream of the cylindrical section, then it is directly attached, preferably welded, to the collection channel going into the heat exchanger. If the pipe assembly includes a further, third cylindrical pipe section, then the deformable section may be attached in-between the second and the third pipe section.
  • the second pipe section has a conical basic shape.
  • the deformable section may be attached to the conical pipe section upstream or downstream in the direction of flow. If the deformable section is placed downstream of the conical section, then it is directly attached, preferably welded, to the collection channel going into the heat exchanger.
  • the conical pipe section is arranged to diverge in the direction of flow, whereby the diameter of the respective inlet and outlet is selected with respect to the flow rate, pressure or outlet velocity of the flow, or some other desired parameter.
  • the combined inlet and outlet pipe joint is made up of two concentric pipes.
  • the outer pipe joint may either have a cylindrical or conical cross-section. Both these embodiments of the outer pipe joint can be combined with any one of the embodiments of the inner pipe joint described above. In these cases the average diameter of the corrugated section, as defined above, is preferably equal to the diameters of the adjoining pipe sections.
  • the material used for the pipe arrangement is best chosen with respect to the field of application of the heat exchanger, that is the type of heat emitting and absorbing medium, and the temperatures and pressure that the pipe arrangement will be subjected to.
  • High temperatures and pressures will preferably require metallic materials, such as steel or aluminium of suitable thickness and quality, while lower temperatures and pressures may allow the use of plastic pipes. Corrosive media may require particularly resistant materials. Joining of metallic pipes is preferably done by welding or soldering, while plastic materials and composites may be joined by welding, melting or gluing. Mechanical connections, such as threaded connections, are also possible, but will at the same time give a more space consuming, complex and therefore more expensive solution.
  • FIG. 1 shows a schematic drawing of a recuperator, provided with a combined inlet and outlet pipe joint according to the invention
  • Figure 2 shows a prior art pipe connection
  • Figure 3 shows an alternative embodiment of the invention
  • Figure 4 shows a further alternative embodiment of the invention.
  • FIG. 1 shows a schematic representation of a recuperator comprising a heat exchanger packet 1 with a combined inlet and outlet pipe joint 2, 3, and a outgoing, first collection channel 4 with a pipe connection 5 between the collection channel and the outlet pipe joint 3.
  • the combined inlet and outlet pipe joint 2, 3 comprises two concentric pipes forming channels for heat transporting media.
  • the inner inlet pipe joint 2 is connected to a source of heat emitting medium, which in this case is combusted exhaust gas from a gas turbine (not shown).
  • the mass flow of heat emitting medium 6 flows through the heat exchanger in which a large portion of its heat energy is emitted to a heat absorbing medium, which in this case is air.
  • the heat- absorbing medium is collected in the outgoing, first collection channel 4, whereby the flow 7 is directed out through a pipe connection 5 to the outlet pipe joint 3 towards the gas turbine.
  • the combined inlet and outlet joint comprises two concentric, partially conical channels.
  • the inner pipe section, or the inlet pipe joint 2 is welded to an incoming , second collection channel 8 in the form of a diverging section or flange, which in turn is attached to an upper casing 9 on the heat exchanger 1.
  • the upper casing 9 conducts the heat-emitting medium in the direction of the flow channels (not shown) of the heat exchanger.
  • a deformable pipe section 10 is attached to the inlet of the inner pipe section 2 and will be described in further detail in connection with Figure 4 below.
  • the outer pipe section 3 is attached to the flange 8 at its inlet end, facing the heat exchanger, and to a not shown casing surrounding the gas turbine at its opposite end.
  • Figure 3 shows an alternative embodiment of a pipe connection.
  • the combined inlet and outlet joint comprises a pair of concentric, cylindrical inner and outer pipe sections 2, 3.
  • the inlet pipe joint 2 includes a deformable, substantially cylindrical, first pipe section 10, attached between a cylindrical second pipe section 2a and a cylindrical third pipe section 2b.
  • the cylindrical second pipe section 2a is provided with a flange 11 for connecting it to a heat source, in this case a gas turbine (not shown), while the cylindrical third pipe section 2b is welded to the flange 8.
  • the deformable first pipe section has an inner diameter D-i, corresponding to the smallest diameter of the corrugated section 10, which is equal to the inner diameter D 2 of the second section.
  • the first pipe section 10 is provided with flanges 10a, 10b on either side of the corrugated section, which flanges are in contact with and welded to the outer periphery of the second and third section 2a, 2b respectively.
  • the outer pipe joint 3 has a cylindrical basic shape along its outer periphery. However, it is slightly conical along its inner periphery, as the inner surface is coated with an insulating material 12 with a gradually increasing thickness. The reason for this is to minimise heat loss from the medium flowing in the direction of the gas turbine.
  • the conical shape will also give certain flow-related advantages, which will not be described in further detail.
  • FIG. 3 shows a deformable section 10 having a cylindrical section 2a, 2b on either side. It is however possible to eliminate one of these cylindrical sections, whereby the deformable section is placed at one end of a cylindrical pipe section.
  • Figure 4 shows a further alternative embodiment in the form of a pipe connection.
  • the combined inlet and outlet pipe joint comprises a pair of conical inner and outer pipe sections 2, 3.
  • the inner pipe section is provided with a deformable, substantially cylindrical first pipe section 10 attached to a cylindrical second pipe section.
  • the cylindrical first pipe section is provided with a flange 11 for connection to a heat source, in this case a gas turbine (not shown), while the conical second pipe section is attached to the flange 8.
  • the deformable first pipe section has an inner diameter Di, corresponding to the smallest inner diameter of the corrugated section, which is equal to the inner diameter D 2 of the adjoining second section.
  • the first pipe section 10 is provided with flanges 10a, 10b on either side of the corrugated section, which flanges are in contact with and welded to the outer periphery of the second pipe section 2 and the flange 11 , respectively.
  • the inner surface of the outer pipe section is coated with an insulating material with a gradually increasing thickness, for reasons stated above (cf. Fig. 3).
  • both the inner and the outer periphery of the outer pipe section has a conical shape.
  • the diameter of the inlet of the outer section is selected with respect to the flow rate, pressure or outlet velocity of the flow, or some other desired parameter thereof.

Abstract

Pipe connection for heat exchangers (1), where said heat exchanger comprises a number of corrugated plates, where each plate has a first edge part opposite a second edge part and a third edge part opposite a fourth edge part, between which corrugated plates there are provided first and second flow channels, where a heat emitting medium (6) flows through every other alternate channel, and where a collecting channel (8) with a diverging cross-section for said heat emimtting medium (6) is placed at one side of the heat exchanger and connected to an inlet section a combined inlet and outlet pipe joint (2, 3) for said heat emitting and heat absorbing media, and an outgoing collection channel (4) for said heat absorbing medium (7) arranged on the same side of the heat exchanger and connected to an outlet section of said inlet and outlet pipe joint (2, 3). The inlet pipe joint (2) comprises a deformable first pipe section (10), arranged to absorb thermal and mechanical loading in both axial and radial directions, and at least one further, second pipe section (2a, 2b).

Description

Arrangement for connecting a pipe to a heat exchanger
TECHNICAL FIELD
The present invention relates to an arrangement in a pipe joint for a heat exchanger - also termed a recuperator - that is adapted for use with a gas turbine for stationary use in a small scale combined power and heating plant or for mobile use in a vehicle.
BACKGROUND ART A heat exchanger of the said type may be used in, for example, a combined power and heating plant, for mobile use or in a reserve power station. For many such applications it is of vital importance that the recuperator is designed in such a way that is as efficient as possible, while minimising weight and dimensions. The recuperator may for instance be made up of a plate heat exchanger comprising a number of plates manufactured from very thin sheet metal, generally having a thickness of about 0,1 mm. The plates are provided with corrugations in a known manner, whereby they are stabilised relative to each other in a wave shaped pattern. Spaces between the corrugations will then form flow channels for a heat emitting medium and a heat-absorbing medium. If a gas turbine is used, the heat-emitting medium is combusted gases leaving the turbine, while the heat-absorbing medium is usually air.
As the heat emitting and absorbing media may have a relatively high temperature, problems may arise in tubing and pipe joints of such systems. When starting a plant using a gas turbine, the temperature in the component parts will rise from ambient temperature, for example 20°C, to temperatures in excess of 600°C. This usually entails large thermal loading due to heat expansion . in different parts of the system. In operation the variations in temperature between different parts of the plant are less, but may still cause problems. . A pipe joint between two sections of a heat exchanger, or between a source of heat and the heat exchanger, for instance between a gas turbine having exhaust gases requiring cooling, it is therefore necessary to absorb forces that arise due to the fact that the heat exchanger packet and the pipe joint are very likely to have different coefficients heat expansion. For this reason, welded or soldered joints in pipe systems without the capability of absorbing thermal loading are totally unsuitable, as repeated thermal loading would quickly give rise to cracks and leaks. Corresponding problems will also arise should mechanical joints, such as bolted connections, be used. A known solution be seen in Figure 2, that shows an inlet pipe connection 2 for conducting a heat emitting medium 6 to the heat exchanger. According to this example, the combusted exhaust gas, at a temperature of about 650°C and a pressure of about 1 ,1 bar, is conducted from a gas turbine to the inlet pipe connection 2 and into the heat exchanger. In the heat exchanger a heat absorbing medium 7, such as air, is heated by the exhaust gases, whereby the air leaves the heat exchanger through the outlet pipe connection 3, at a temperature of about 610°C and a pressure of 4 bar. The lower end A of the inlet pipe connection 2 is mounted with a force fit onto a corresponding recess in a flange on the heat exchanger. The lower end A can be provided with a number of radial grooves C around its periphery, in order to increase the contact pressure between said end and the recess B. The grooves C may also be provided with sealing devices of some kind. Thermal loading caused by, for instance, axial expansion of the inlet pipe connection must be absorbed by the joint, whereby the component parts are movable relative to each other.
In addition to its sensitivity to uneven loading, both during and after assembly, the arrangement may also have a certain leakage flow LF between the inlet and outlet parts. The leakage flow is partly due to the pressure difference and partly due to poor fitting and relative movement between the component parts. Such a leakage will lower the efficiency of the heat exchanger. Hence one problem is to achieve a pipe joint that can be deformed in order to absorb thermal loads without being damaged. Depending on the positioning and assembly of the pipe joint, it may have to absorb movement in both axial and radial direction, in relation to the main axis of the pipe joint. A further problem fit such a pipe joint between two fixed points, where variations in fit and tolerance between the component parts of the heat exchanger may sometimes occur. In such cases it is also desirable to have a pipe joint that is deformable in several directions.
DISCLOSURE OF INVENTION The purpose of the current invention is to eliminate the problems described in relation to the prior art, thereby fulfilling the desired objectives of an improved pipe arrangement for a heat exchanger, as well as providing a simple and inexpensive embodiment for this purpose.
The above purpose is achieved by means of a pipe arrangement for heat exchangers as described above, wherein its characterising parts are described in claim 1 below relating to a pipe joint for a heat exchanger comprising a number of corrugated plates. Each plate has a first edge part opposite a second edge part and a third edge part opposite a fourth edge part. Between said corrugated plates there are provided first and second flow channels, where a heat emitting medium flows through every alternate channel and a heat absorbing medium flows through every other alternate channel. A collecting channel for heat emitting medium, which channel has a diverging cross-section is placed at one side of the heat exchanger and is provided with an inlet section connected to a combined inlet and outlet pipe connection for said heat emitting and heat absorbing media. In addition, an outgoing collection channel for said heat-absorbing medium is arranged on the same side of the heat exchanger and has an outlet section connected to said inlet and outlet pipe. The inlet pipe comprises a deformable first pipe section, arranged to absorb thermal and mechanical movements in both axial and radial directions, and at least one further pipe section. The deformable section is preferably, but not necessarily, elastically deformable. According to one embodiment the heat exchanger may co-operate with a gas turbine, whereby its combusted exhaust gases is used as the heat-emitting medium.
According to a first embodiment the inlet pipe connection has a deformable first pipe section made up of a substantially cylindrical pipe, with walls having a corrugated cross-section in the axial direction of the pipe. Such an embodiment can as a rule entail certain flow losses. In order not to limit or disturb the flow through the pipe joint the average diameter, that is the average of the inner and outer diameters of the corrugations, should be larger than the inner diameter of the adjoining second pipe section. Preferably, the inner diameter of the deformable first pipe section, corresponding to the smallest diameter of the corrugated section, is equal to the inner diameter of the second pipe section. The cross-section of the corrugated section may be varied depending on the size and direction of the thermal movements to be absorbed. One example of a suitable shape is a sinusoidal cross-section, where the amplitude and wavelength can be varied to give the desired properties with respect to deformability in the axial and radial directions. The first pipe section is preferably elastically deformable.
According to an alternative embodiment, where the inlet and outlet pipe joints are arranged concentrically, it is further possible to distribute the flow losses between inlet and outlet. In this case the average diameter of the corrugated section, that is the average of the inner and outer diameters of the corrugations, can be equal to the inner diameter of the adjoining second pipe section. A corrugated section as described above can be manufactured, for instance, by means of rolling, for metallic materials, injection moulding, for plastic materials, or winding, for composite material. Apart from the choice of material, the resistance to deformation of the first pipe section is decided by the relative axial distance and radial amplitude of the corrugations, as well as the material thickness. These variables are selected with respect to the desired diameter of the pipes, the maximum deformation caused by thermal loading, and the temperatures and pressures to be handled by the pipes. Deformation of the corrugated section in its axial direction will mainly occur during changes of temperature in connection with start-up and operation of the plant, while deformation in its radial direction will mainly occur during assembly and fitting of the pipe joint. By making the pipe section elastically deformable it will be able to absorb movements in the same way as a spring. Hence the section will absorb movements between the pipes without transmitting forces to any greater extent. In order to enable the said deformations the material thickness of the deformable first pipe section should be equal to or less than the thickness of the other pipe sections. If the said sections have a material thickness of 1 mm, the corrugated section may have a material thickness of 0,3-0,6 mm. The selected thicknesses and the relation between these is of course dependent on the size of the thermal movements, the dimensions of the pipes, the pressure of the flowing media and other factors.
According to a further embodiment the second pipe section of the inlet pipe has a cylindrical basic shape. The deformable section may be attached to the cylindrical pipe section upstream or downstream in the direction of flow. If the deformable section is placed downstream of the cylindrical section, then it is directly attached, preferably welded, to the collection channel going into the heat exchanger. If the pipe assembly includes a further, third cylindrical pipe section, then the deformable section may be attached in-between the second and the third pipe section.
According to a further embodiment the second pipe section has a conical basic shape. The deformable section may be attached to the conical pipe section upstream or downstream in the direction of flow. If the deformable section is placed downstream of the conical section, then it is directly attached, preferably welded, to the collection channel going into the heat exchanger. The conical pipe section is arranged to diverge in the direction of flow, whereby the diameter of the respective inlet and outlet is selected with respect to the flow rate, pressure or outlet velocity of the flow, or some other desired parameter.
According to a further embodiment, the combined inlet and outlet pipe joint is made up of two concentric pipes. In this case, the outer pipe joint may either have a cylindrical or conical cross-section. Both these embodiments of the outer pipe joint can be combined with any one of the embodiments of the inner pipe joint described above. In these cases the average diameter of the corrugated section, as defined above, is preferably equal to the diameters of the adjoining pipe sections. The material used for the pipe arrangement is best chosen with respect to the field of application of the heat exchanger, that is the type of heat emitting and absorbing medium, and the temperatures and pressure that the pipe arrangement will be subjected to. High temperatures and pressures will preferably require metallic materials, such as steel or aluminium of suitable thickness and quality, while lower temperatures and pressures may allow the use of plastic pipes. Corrosive media may require particularly resistant materials. Joining of metallic pipes is preferably done by welding or soldering, while plastic materials and composites may be joined by welding, melting or gluing. Mechanical connections, such as threaded connections, are also possible, but will at the same time give a more space consuming, complex and therefore more expensive solution.
BRIEF DESCRIPTION OF DRAWINGS
In the following text the invention will be described with reference to a number of preferred embodiments and the attached schematic drawings, where;
Figure 1 shows a schematic drawing of a recuperator, provided with a combined inlet and outlet pipe joint according to the invention, Figure 2 shows a prior art pipe connection, Figure 3 shows an alternative embodiment of the invention, Figure 4 shows a further alternative embodiment of the invention. MODES FOR CARRYING OUT THE INVENTION
Figure 1 shows a schematic representation of a recuperator comprising a heat exchanger packet 1 with a combined inlet and outlet pipe joint 2, 3, and a outgoing, first collection channel 4 with a pipe connection 5 between the collection channel and the outlet pipe joint 3. The combined inlet and outlet pipe joint 2, 3 comprises two concentric pipes forming channels for heat transporting media. The inner inlet pipe joint 2 is connected to a source of heat emitting medium, which in this case is combusted exhaust gas from a gas turbine (not shown). The mass flow of heat emitting medium 6 flows through the heat exchanger in which a large portion of its heat energy is emitted to a heat absorbing medium, which in this case is air. The heat- absorbing medium is collected in the outgoing, first collection channel 4, whereby the flow 7 is directed out through a pipe connection 5 to the outlet pipe joint 3 towards the gas turbine. According to this embodiment, the combined inlet and outlet joint comprises two concentric, partially conical channels. The inner pipe section, or the inlet pipe joint 2, is welded to an incoming , second collection channel 8 in the form of a diverging section or flange, which in turn is attached to an upper casing 9 on the heat exchanger 1. The upper casing 9 conducts the heat-emitting medium in the direction of the flow channels (not shown) of the heat exchanger. A deformable pipe section 10 is attached to the inlet of the inner pipe section 2 and will be described in further detail in connection with Figure 4 below. The outer pipe section 3 is attached to the flange 8 at its inlet end, facing the heat exchanger, and to a not shown casing surrounding the gas turbine at its opposite end.
Figure 3 shows an alternative embodiment of a pipe connection. According to this embodiment the combined inlet and outlet joint comprises a pair of concentric, cylindrical inner and outer pipe sections 2, 3. The inlet pipe joint 2 includes a deformable, substantially cylindrical, first pipe section 10, attached between a cylindrical second pipe section 2a and a cylindrical third pipe section 2b. The cylindrical second pipe section 2a is provided with a flange 11 for connecting it to a heat source, in this case a gas turbine (not shown), while the cylindrical third pipe section 2b is welded to the flange 8.
The deformable first pipe section has an inner diameter D-i, corresponding to the smallest diameter of the corrugated section 10, which is equal to the inner diameter D2 of the second section. Hence, in this case the average diameter D of the corrugated section is larger than the inner diameters of the pipe sections. The first pipe section 10 is provided with flanges 10a, 10b on either side of the corrugated section, which flanges are in contact with and welded to the outer periphery of the second and third section 2a, 2b respectively. During start-up of the plant the temperature of the pipe joint will rise from a relatively low temperature, such as 20°C, to an operating temperature in excess of 600°C. The axial movement of the inner pipe section in connection with thermal expansion of the material, to the extent it differs from that of the outer pipe section, will be taken up by the deformable pipe section 10.
As can be seen from Figure 3, the outer pipe joint 3 has a cylindrical basic shape along its outer periphery. However, it is slightly conical along its inner periphery, as the inner surface is coated with an insulating material 12 with a gradually increasing thickness. The reason for this is to minimise heat loss from the medium flowing in the direction of the gas turbine. The conical shape will also give certain flow-related advantages, which will not be described in further detail.
The embodiment of Figure 3 shows a deformable section 10 having a cylindrical section 2a, 2b on either side. It is however possible to eliminate one of these cylindrical sections, whereby the deformable section is placed at one end of a cylindrical pipe section.
Figure 4 shows a further alternative embodiment in the form of a pipe connection. According to this embodiment the combined inlet and outlet pipe joint comprises a pair of conical inner and outer pipe sections 2, 3. The inner pipe section is provided with a deformable, substantially cylindrical first pipe section 10 attached to a cylindrical second pipe section. The cylindrical first pipe section is provided with a flange 11 for connection to a heat source, in this case a gas turbine (not shown), while the conical second pipe section is attached to the flange 8. The deformable first pipe section has an inner diameter Di, corresponding to the smallest inner diameter of the corrugated section, which is equal to the inner diameter D2 of the adjoining second section. The first pipe section 10 is provided with flanges 10a, 10b on either side of the corrugated section, which flanges are in contact with and welded to the outer periphery of the second pipe section 2 and the flange 11 , respectively. As can be seen from Figure 4, the inner surface of the outer pipe section is coated with an insulating material with a gradually increasing thickness, for reasons stated above (cf. Fig. 3). In this case both the inner and the outer periphery of the outer pipe section has a conical shape. As in the case of the inlet pipe joint, the diameter of the inlet of the outer section is selected with respect to the flow rate, pressure or outlet velocity of the flow, or some other desired parameter thereof.
According to a further alternative embodiment it is also possible to position the deformable first pipe section 10 between the conical second pipe section 2 and the flange 8. Although the diameter Di of the pipe section 10 will be larger, such a positioning below the level of the inlet from the pipe connection 5 will cause less disturbance of the flow through the outlet pipe joint 3 as it passes the corrugations.
In addition, it is theoretically possible to position the deformable pipe section 10 between two conical pipe sections 2, in a way corresponding to that of Figure 3. However, due to differences in pressure between the different channels, as well as forces caused by thermal movements, the deformable section would be subjected to large stresses. Hence the embodiments described above are preferable.

Claims

1. Pipe connection for heat exchangers (1), where said heat exchanger comprises a number of corrugated plates, where each plate has a first edge part opposite a second edge part and a third edge part opposite a fourth edge part, between which corrugated plates there are provided first and second flow channels, where a heat emitting medium (6) flows through every alternate channel and a heat absorbing medium (7) flows through every other alternate channel, and where a collecting channel (8) with a diverging cross-section for said heat emitting medium (6) is placed at one side of the heat exchanger and connected to an inlet section a combined inlet and outlet pipe joint (2, 3) for said heat emitting and heat absorbing media, and an outgoing collection channel (4) for said heat absorbing medium (7) arranged on the same side of the heat exchanger and connected to an outlet section of said inlet and outlet pipe joint (2, 3), characterized in that the inlet pipe joint (2) comprises a deformable first pipe section (10), arranged to absorb thermal and mechanical loading in both axial and radial directions, and at least one further, second pipe section (2a, 2b).
2. Pipe connection for heat exchangers according to claim 1, c h a r a c t e r i z e d i n that the deformable first pipe section (10) comprises a substantially cylindrical pipe having a corrugated cross- section in the axial direction of the pipe.
3. Pipe connection for heat exchangers according to claim 2, characterized in that the deformable first pipe section (10) has an inner diameter (Di) corresponding to the smallest diameter of the corrugated section, equal to the inner diameter (D2) of the adjoining second section (2).
4. Pipe connection for heat exchangers according to any one of claims 1-3, characterized in that the deformable first pipe section (10) has a material thickness that is less than the thickness of the second pipe section. Pipe connection for heat exchangers according to any one of claims 1-3, characterized in that the second pipe section (2) has a cylindrical basic shape. Pipe connection for heat exchangers according to claim 5, characterized in that the deformable first pipe section (10) is attached to the cylindrical pipe section (2) upstream in the direction of flow. Pipe connection for heat exchangers according to claim 5, characterized in that the deformable first pipe section (10) is attached to the cylindrical pipe section (2) downstream in the direction of flow. Pipe connection for heat exchangers according to claim 5, characterized in that the deformable first pipe section (10) is attached between the second, cylindrical pipe section (2a) and a third, cylindrical pipe section (2b). Pipe connection for heat exchangers according to any one of claims 1-3, characterized in that the second pipe section (2) has a conical basic shape. Pipe connection for heat exchangers according to claim 9, characterized in that the deformable first pipe section (10) is attached to the conical pipe section (2) upstream in the direction of flow. Pipe connection for heat exchangers according to claim 9, characterized in that the deformable first pipe section (10) is attached to the conical pipe section (2) downstream in the direction of flow.
12. Pipe connection for heat exchangers according to any of the above claims, characterized in that the combined inlet and outlet pipe joint comprises two substantially concentric pipes (2, 3).
13. Pipe connection for heat exchangers according to claim 12, characterized in that the deformable first pipe section (10) has an inner diameter (D-i) corresponding to the smallest diameter of the corrugated section, equal to the inner diameter (D2) of the adjoining second section (2).
14. Pipe connection for heat exchangers according to claims 12 or 13, characterized in that the outer pipe joint (3) has a conical basic shape.
15. Pipe connection for heat exchangers according to any of the above claims, characterized in that the inlet pipe joint is welded to the incoming collection channel (8). 16. Pipe connection for heat exchangers according to any one of claims 1 -14, characterized in that the deformable section (10) is welded to the incoming collection channel (8).
PCT/SE2002/000959 2001-05-21 2002-05-17 Arrangement for connecting a pipe to a heat exchanger WO2002095316A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP02733715A EP1389297A1 (en) 2001-05-21 2002-05-17 Arrangement for connecting a pipe to a heat exchanger
US10/707,125 US20040104009A1 (en) 2001-05-21 2003-11-21 Arrangement in a pipe joint for a heat exchanger

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE0101797-9 2001-05-21
SE0101797A SE519051C2 (en) 2001-05-21 2001-05-21 Device for pipe connection for heat exchanger

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US10/707,125 Continuation US20040104009A1 (en) 2001-05-21 2003-11-21 Arrangement in a pipe joint for a heat exchanger

Publications (1)

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WO2002095316A1 true WO2002095316A1 (en) 2002-11-28

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ID=20284195

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Application Number Title Priority Date Filing Date
PCT/SE2002/000959 WO2002095316A1 (en) 2001-05-21 2002-05-17 Arrangement for connecting a pipe to a heat exchanger

Country Status (4)

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US (1) US20040104009A1 (en)
EP (1) EP1389297A1 (en)
SE (1) SE519051C2 (en)
WO (1) WO2002095316A1 (en)

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DE202012102759U1 (en) * 2012-07-23 2013-07-24 Krones Aktiengesellschaft folding
CA2925508A1 (en) 2013-09-30 2015-04-02 Dana Canada Corporation Heat exchanger with integrated co-axial inlet/outlet tube
CN112781405B (en) * 2021-01-25 2023-03-24 四川空分设备(集团)有限责任公司 High-efficient compact heat exchanger of multichannel formula

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US4216821A (en) * 1977-02-04 1980-08-12 Commissariat A L'energie Atomique Pump/heat exchanger

Also Published As

Publication number Publication date
SE519051C2 (en) 2003-01-07
SE0101797D0 (en) 2001-05-21
US20040104009A1 (en) 2004-06-03
SE0101797L (en) 2002-11-22
EP1389297A1 (en) 2004-02-18

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