EP3670027A1 - Heat capturing device - Google Patents
Heat capturing device Download PDFInfo
- Publication number
- EP3670027A1 EP3670027A1 EP18382964.7A EP18382964A EP3670027A1 EP 3670027 A1 EP3670027 A1 EP 3670027A1 EP 18382964 A EP18382964 A EP 18382964A EP 3670027 A1 EP3670027 A1 EP 3670027A1
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- EP
- European Patent Office
- Prior art keywords
- energy
- heat
- capturing
- tubes
- layer
- 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.)
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D21/00—Arrangements of monitoring devices; Arrangements of safety devices
- F27D21/0014—Devices for monitoring temperature
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F13/00—Arrangements for modifying heat-transfer, e.g. increasing, decreasing
- F28F13/18—Arrangements for modifying heat-transfer, e.g. increasing, decreasing by applying coatings, e.g. radiation-absorbing, radiation-reflecting; by surface treatment, e.g. polishing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D19/00—Arrangements of controlling devices
- F27D2019/0006—Monitoring the characteristics (composition, quantities, temperature, pressure) of at least one of the gases of the kiln atmosphere and using it as a controlling value
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0028—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for cooling heat generating elements, e.g. for cooling electronic components or electric devices
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0077—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for tempering, e.g. with cooling or heating circuits for temperature control of elements
- F28D2021/0078—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for tempering, e.g. with cooling or heating circuits for temperature control of elements in the form of cooling walls
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2245/00—Coatings; Surface treatments
- F28F2245/06—Coatings; Surface treatments having particular radiating, reflecting or absorbing features, e.g. for improving heat transfer by radiation
Definitions
- the present invention relates to the field of radiant energy or heat collector assemblies. More particularly, it refers to methods and systems for recovering or capturing heat in the form of radiant energy and using the recovered energy for further purposes such as heating of buildings, electricity production or steam generation.
- the heat capturing device can be applied in industries such as in steel mills, metallurgy, furnaces or glass production or any other energy intensive industry with high radiant emissions.
- the European patent application EP2403668 (A2 ) discloses a heat retrieving system in which heat is retrieved via conduction and convection. This patent application uses the transportation rollers as heat exchangers.
- the patent application DE3019714 (A1 ) discloses a heat collection arrangement comprising water containing tubes. The prior art is silent on heat collection devices especially configured for capturing heat transferred by radiation. It is therefore required a technical arrangement recovering radiant energy or heat from an object or objects being at temperature higher than 500° C.
- the present application overcomes the drawbacks of the prior art and allows higher energy or heat retrieval of the heat or energy radiated by an object or group of objects.
- the described heat capturing device comprises an upper side and lateral sides connected to the upper side, said connected sides defining an energy capturing space.
- the device further comprises an energy insulating layer, an intermediate energy reflecting layer and an inner energy capturing layer capturing energy from at least a radiation emitting object (hereinafter referred to as "object") located at least partly in the energy capturing space.
- the inner energy capturing layer comprises at least one material containing structure.
- the material may be a heat transfer fluid (hereinafter referred to as fluid), for example a liquid such as silicon based thermal oil, for capturing energy.
- the material containing structure may be at least a tube having preferably a circular cross-section.
- the dimensions of the inner energy capturing layer are based, at least, on the dimensions of the at least an object in the energy capturing space and based on at least a further parameter.
- Said further parameter may be at least one of: at least one further parameter of said at least an object or at least one parameter of the inner energy capturing layer or at least one parameter of the energy capturing space or a combination of said further parameters.
- Said further parameter or parameters of the inner energy capturing layer may be intrinsic parameters of the surface of the inner energy capturing layer defining the energy capturing space.
- the energy insulating layer may entirely cover the intermediate energy reflecting layer, and the intermediate energy reflecting layer may entirely cover the inner energy capturing layer.
- a further plate or plates may be located at the entrance or exit of the energy capturing space for better retaining and/or reflecting the radiant heat or energy of the object or objects inside the energy capturing space.
- the plate or plates located at the entrance and/or exit of the energy capturing space may be made of a heat or energy reflecting material.
- the energy insulating layer may be covered with an outer casing or outer cover for protecting and encapsulating the heat capturing device.
- the described layers may be different layers which may be separated from each other.
- the heat capturing device may be connected to a bottom layer or plate or surface made of either reflecting or insulating heat material.
- the parameter or parameters defining the width and the height of the inner energy capturing layer may be, for example, at least one of: the convection coefficient of the air inside the energy capturing space, the emissivity and absorptivity of at least one of the surfaces of the object, the emissivity and absorptivity of at least one of the surfaces of the inner energy capturing layer or a combination of said parameters.
- the emissivity and absorptivity of a surface are magnitudes indicating its effectiveness in emitting or absorbing (respectively) thermal radiation. Quantitatively, they are described as the ratio between the thermal radiation emitted/absorbed by a surface compared to the radiation emitted/absorbed by an ideal black body at the same temperature (which is maximum).
- the parameter or parameters defining the height and width of the heat capturing device may be based on some intrinsic properties of the objects which are to be received in the energy capturing space or transported through the energy capturing space.
- the objects can be for example a slab, billet or beam resulting from a production process such as a metallurgic production process or preferably a piece of hot glass (e.g. bottle shaped glass) produced by a glass production factory. Said production processes may serially produce objects such as slabs or hot pieces of glass, and some properties of said serially produced objects or pieces are known.
- the objects may be solid or partly solid objects.
- the objects are preferably at a temperature higher than 500° C.
- the fact that the heat capturing device of the present application allows a modular construction permits the customization of the size or dimensions of the heat capturing device or tailoring the size of the heat capturing device according to the properties of the objects, thus allowing to capture the radiated heat from the objects when the objects are partly or completely in the energy capturing space or even slightly outside the energy capturing space.
- the width and the height of the inner energy capturing layer can be selected based on said properties of the object, which implies that the width and height of the heat capturing device as a whole is selected based on at least the properties of the objects or parameters taking into consideration the properties of the object.
- the heat capturing device and its size may be configured before the production process of the objects start.
- the modularity of the heat capturing device permits the heat capturing device to be assembled and/or remove parts of the heat capturing device easily.
- the inner energy capturing layer for example a tube bundle, may cover an inner surface of a tunnel-shaped surface defined by the energy capturing space or may have a tunnel-shaped arrangement, and the diameter of the tubes of the bundle may be the same or similar.
- the dimensions or the size of the tube bundle are defined in such a way that the heat captured by the heat capturing device is maximized, mainly the heat transmitted by radiation.
- the arrangement of the tube bundle may be perpendicular or parallel to the direction of movement of the objects being transported (e.g. objects entering, leaving or being transported through the energy capturing space or objects remaining for some time in the energy capturing space). Heat losses due to convection and radiation of the surfaces of the heat capturing device (e.g. the tubes of the bundle) are minimized using insulating materials.
- the heat capturing device, and more particularly the inner energy capturing layer may be designed to operate with the fluid flowing through the tubes at a medium fluid temperature around 350° C.
- the fluid may be at a temperature that satisfies a heat demand with temperatures between 600 and 140° C. In some other examples, the fluid may be at a temperature that satisfies a heat demand with temperatures between 140 and 40° C.
- the tubes of the bundle may be separated from each other. More preferably, the distance between the center of two consecutive tubes may be between 1,25 and 2 times the external diameter of a tube of the bundle.
- the bundle of tubes may be connected, e.g. welded, to at least two headers.
- the headers may be to feed the fluid to the inner energy capturing layer with the fluid being at a first temperature, to distribute the fluid through the inner energy capturing layer such the fluid may increase its temperature from the first temperature to a second temperature by absorbing heat from the object or objects, and to remove the fluid from the inner energy capturing layer with the fluid at the second temperature.
- the second temperature may be higher than the first temperature.
- the headers may transport the fluid from/to a fluid storage or to any other device that may reuse the recovered energy for similar or different purposes such as heating of buildings, electricity production or steam generation.
- the external surface of the bundle of tubes i.e., the surface of the bundle of tubes facing the object, may be covered with a high absorptivity coating or with a high absorptivity paint.
- the paint may have as much absorptivity as possible in near and mid-infrared spectrum, and at least higher than the corresponding values of the base material of the inner capturing layer.
- the paint may have an absorptivity around 0,97 for a wavelength between 2-3 microns.
- the intermediate energy reflecting layer may have a flat structure such as a plate or a corrugated shaped structure or surface or layer behind the bundle of tubes.
- the corrugated shaped structure may be a sinus shaped surface or sinus shaped structure.
- the convex part of the corrugated shaped structure is located in correspondence with at least one of the tubes of the bundle and the concave part of the corrugated shaped structure is located in correspondence with at least one of the separations between the tubes.
- the corrugated or wavy or sinus shaped structure is designed to better focus the reflected heat towards the rear part of the tubes for allowing better heat or energy absorption of the reflected heat, thus allowing an enhanced heat exchange with the rear part of the tubes.
- the heat capturing device may comprise an energy insulating layer surrounding the intermediate energy reflecting layer.
- the energy insulating layer may be made of ceramic fiber.
- the insulating layer may be a separate layer from the other layers.
- the heat capturing device may further comprise an outer casing covering the energy insulating layer.
- the outer casing that may be made of metal, contains and protects the heat capturing device.
- the heat capturing device may comprise one or several sensors.
- the sensors may be of the same type or may be a combination of different types of sensors.
- the sensors may be: one or more sensors for measuring the temperature of the object or objects, one or more sensors for measuring the temperature of the energy capturing space, one or more sensors for measuring the temperature inside the tubes or the temperature of the fluid within the tubes, one or more sensors for detecting the object either entering into, or exiting out of or remaining in the energy capturing space or any combination of said sensors.
- the sensors may be connected to control means, such as a controller or processor or group of processors for processing the information received from the sensors.
- the control means may process the data received form the sensors and may issue instructions or control data based on the sensed data as provided by one or more of said sensors, based on the processed data or based in a combination of the data as received and the data after being processed.
- the heat capturing device may comprise transport means for moving the object or objects relative to the energy capturing space.
- the transport means may be managed by control means, the control means configured to control the transport of the object from or to the energy capturing space.
- the heat capturing device automatically transports the object to or from the energy capturing space based on a certain temperature captured by at least one or more sensors exceeding or being below a predetermined threshold. Said threshold may define a temperature threshold.
- the transport means may transport the object through the energy capturing space or may leave the object in the energy capturing space for a predetermined time interval so that the inner energy capturing layer captures heat from the object.
- the transport means transport the object or objects through the energy capturing space in case the tunnel-shaped heat capturing device or tunnel-shaped inner energy capturing layer is open on both sides, that means no plate or door is placed at the entry and exit of the tunnel-shaped heat capturing device. In case a plate or door is located at the exit of the tunnel-shaped heat capturing device, the transport means use the open entry for entering and removing the object or objects to/from the energy capturing space.
- the device may comprise further control means, wherein the control means are configured for controlling the quantity of fluid and/or the speed of the fluid circulating in the bundle of tubes, wherein the control means automatically control said quantity and/or speed of fluid based on the data captured by at least one of the sensors.
- the control means may process the data received from the sensors and based on said processing, the control means may issue instructions or control data.
- the instructions may control the transport means such as its speed, start and stop functions, may control the quantity of fluid circulating in the bundle of tubes, may control the quantity of fluid in the headers and may control the speed of fluid circulating in the tubes or in the bundle of tubes.
- the transport means are preferably controlled for transporting the object or objects such that the objects or objects are symmetrically placed or located inside the energy capturing space or symmetrically placed or located while being transported through the energy capturing space.
- the control means may control the transport means and the speed of transport of the object or objects entering or leaving the energy capturing space. This may be useful in cases in which the object or objects are transported through the energy capturing space.
- the control means may control the time period an object or objects remain the energy capturing space and it can be implemented by the control means controlling the transport means for stopping and starting the transport means.
- the instructions of the control means may control the transport means and all devices regulating the flow and/or temperature of fluid in the tubes or headers.
- the distance of the respective lateral sides of the object to the respective corresponding closest surface or sides of the inner energy capturing layer is preferably the same, or equal or almost the same, while the object (or objects) is in the energy capturing space.
- a method for capturing energy as indicated by the heat capturing device may be implemented.
- a heat capturing system is further described.
- Said heat capturing system comprises a heat capturing device as previously described and at least one object located at least partly in the energy capturing space.
- the heat capturing device is configured to capture heat from the at least one object that is inserted into the energy capturing space defined by the upper side and lateral sides connected to the upper side of the heat capturing device.
- the at least one object is cooled by capturing the heat irradiated from the object by the inner energy capturing layer of the heat capturing device.
- the heat capturing device's geometry (see figure 1 ), in particular the width (A) and the height (B) of the inner energy capturing layer; the object's (or objects') geometry, in particular the height (C) and the width (D) of the object, considering that the object or objects are assimilated to a parallelepiped of smaller volume that can contain them; and the spatial relationship between the heat capturing device and the at least one object, in particular, the height of the position of the heat capturing device relative to the at least one object, influence the thermal behavior of the heat capturing device.
- the length (L) is the length to be covered in the process with one or more heat capturing devices lined up next to each other (not the length of an individual heat capturing device).
- F 12 _ 22 G 12 _ 22 x 12 _ 22 2 ⁇ x 12 _ 22 1 ⁇ y 12 _ 22 2 ⁇ y 12 _ 22 1
- F 21 A 1 A 2 ⁇ F 12
- F 23 A 3 A 2 ⁇ F 32
- a 1 2 ⁇ C i ⁇ L + D i ⁇ L
- a 2 A i ⁇ L + 2 ⁇ B i ⁇ L
- a 3 2 ⁇ L ⁇ A i ⁇ D i 2 2 + Hzl 2
- the optimal geometry of the heat capturing device is the one that maximizes the amount of net heat reaching the heat capturing device.
- Figure 9 shows the different heat fluxes considered.
- the heat capturing device is assumed to be perfectly insulated from the back.
- the object 1 and the heat capturing device 2 are considered as grey bodies (a body that emits radiation at each wavelength in a constant ratio less than unity to that emitted by a black body at the same temperature) and the surface 3 is considered a black body (a body that absorbs all incident electromagnetic radiation, regardless of frequency or angle of incidence, an ideal emitter that at every frequency emits as much or more thermal radiative energy as any other body at the same temperature).
- the next step is to calculate the energy transferred to the internal ambient through convection (Qnet_convection).
- Q net_convection h conv ⁇ A 2 ⁇ T 2 ⁇ T 3 ;
- the value of the convection heat transfer coefficient (h conv ) may be introduced by the user.
- the optimal design is obtained by solving an optimization problem. This is formulated as the maximization of the total heat transferred between the piece (object) and the heat capturing device (more particularly the bundle of tubes of the inner energy capturing layer), subject to the physical and manufacturing constraints.
- the minimum width and height that the heat capturing device can have are also input parameter.
- the model-based optimization approach was used to formulate the design optimization problem.
- the supporting model was developed in Python 3.6 based on physics equations.
- the proposed solution is based on the L-BFGS-B algorithm implemented in the Scipy (v1.1.0) optimization package.
- Figures 10-12 show a graphical representation of the listed cases 1-8 mentioned in the following Table 1.
- Figures 10-12 show a schematic representation of the size ratio between the object and the heat capturing device (named as collector in the figures for clarity purposes).
- Case 1 has been selected as a reference case where the optimal solution for the heat capturing device geometry matches with the minimal dimensions defined for it. As can be seen in cases 1 to 6 (see Table 1) with the same minimum values for the dimensions of the heat capturing device the optimal solution is affected by:
- Figure 13 shows a perspective view of an example tunnel shaped heat capturing device 30 wherein the inner energy capturing layer comprises a bundle of tubes 31.
- the tubes 31 may have preferably a circular cross section.
- the heat capturing device 30 may be implemented using tubes 31 having other cross sections such as square or elliptical cross sections.
- the tubes 31 are connected to the represented headers 32.
- the tubes 31 of the bundle may be welded to the headers 32.
- the inner energy capturing layer 31 is covered by an intermediate energy reflecting layer 33 that in turn is covered by an energy insulating layer 34, preferably made of ceramic fiber with low thermal conductivity.
- the energy insulating layer 34 is covered by an outer casing 35, preferably made of a metal.
- the headers 32 transport the heat captured by the fluid inside the tubes of the heat capturing device 30 to either a heating station or to a heat exchanger (not shown).
- the heat capturing device 30 comprises control means which may control the flow of fluid in the tubes 31 of the bundle and may control at least one pump, cooling means and/or valves (not shown).
- the control means of the heat capturing device 30 may control the cooling means or control one or more heat exchangers for regulating the temperature of the fluid flowing in the tubes 31.
- the control of the pump and/or valves by the control means allow to control the quantity or volume of fluid circulating in the tubes 31.
- the fluid circulating in the tubes 31 of the bundle may be water, an organic thermal oil or silicone based thermal oil.
- the objects introduced in the energy capturing space 36 are at high temperatures, such as typically greater than 500°C.
- the heat capturing device is designed to operate with medium temperatures in the fluid around 350° C.
- Figure 14 shows a cross-sectional cut of the heat capturing device 30 of figure 13 .
- all layers namely the outer casing 35, the energy insulating layer 34, the intermediate energy reflecting layer 33 and the inner energy capturing layer 31 (e.g. the tubes) have a tunnel shape as shown which indicates that said layers also define the ceiling and the sides of the tunnel shape arrangement. All said layers may also be at least partly disposed in the floor of said tunnel shaped structure, such that the tubes 31 are also able to capture heat or energy from the floor side of the structure.
- the outer casing 35 may be disregarded, and it is not installed.
- the tubes 31 are not in direct contact with the intermediate energy reflecting layer 33 or reflecting plate, i.e., the inner energy capturing layer 31 (e.g. tubes) and the intermediate energy reflecting layer 33 are separated by air or some gas.
- the inner energy capturing layer 31 may contact the intermediate energy reflecting layer 33.
- the intermediate energy reflecting layer 33 may be in direct contact with the energy insulating layer 34, or both layers (intermediate energy reflecting layer 33 and energy insulating layer 34) may be separated by a chamber of air or gas or insulating fluid.
- the energy insulating layer 34 may be in contact with the outer casing 35 or may be separated by air.
- the outer casing 35 may be made of steel or other metal or may be made of refractory material or heat resistant material.
- Figure 15 shows a perspective view of another example tunnel-shaped heat capturing device 40 with the tubes 41 being positioned substantially parallel to the direction of displacement of the two objects 47 relative to the energy capturing space 46 defined by the tunnel-shaped heat capturing device 40. While Figure 15 shows two identical objects placed parallel to each other, any number of objects with any different shape and spatial relationship to each other could be placed in the energy capturing space 46.
- the tubes 41 of the bundle may have preferably a circular cross section although any other cross sections such as square or elliptical cross sections may be implemented.
- the tubes 41 are connected to the represented headers 42 (not shown in this figure).
- the headers may be positioned at both openings of the tunnel such that their geometry corresponds to the geometry of the openings.
- the intermediate energy reflecting layer 43 is attached to the inner surface of the outer energy insulating layer 44.
- the energy insulating layer 44 is located between the intermediate energy reflecting layer 43 and the outer casing 45.
- the energy insulating layer 44 may be made of ceramic fiber with low thermal conductivity.
- Figure 16 shows a cross-sectional representation of the tunnel-shaped heat capturing device and the further layers of the device of figure 15 .
- Figure 17 shows a perspective view of an example inner energy capturing layer 50.
- the inner energy capturing layer 50 is formed by a bundle of tubes 51 for circulating the heat transfer fluid, a first header 52 and a second header 53.
- the tubes 51 are placed in parallel to each other and have the same diameter. Besides, the distance between two consecutives tubes 51 is the same along the entire inner energy capturing layer 50.
- the fluid 54 ingress in the tubes 51 via the first header 52 through a first opening 55.
- the first header 52 is divided in sections 56 wherein each section is communicated to a set of tubes 51 but isolated from the contiguous sections 56 within the first header 52.
- the second header 53 is divided in sections 57 wherein each section is communicated to a set of tubes 51 but isolated from the contiguous sections 57 within the first header 53.
- the fluid 54 that enters into the first section 56a of the first header 52 circulates through the tubes 51 connected to this first section 56a until the first section 57a of the second header 53, which in turn is connected to other tubes for keeping circulating the fluid towards a second section 56 b of the first header, and so on, until the fluid reaches the last section of the first header 53 through which the fluid 54 exits the inner energy capturing layer 50 via a second opening (not shown in this figure).
- Figure 18 shows a representation of an example architecture of some tubes of the tube bundle forming the inner energy capturing layer and a representation of the corrugated intermediate energy reflecting layer.
- the distance (d1) between the centers of two consecutive tubes is 1.25 times the outside diameter of one of the tubes. All tubes have the same diameter.
- the minimal distance (d2) between the outer surfaces of two consecutives tubes is 0.25 times the diameter of one of the tubes. Due to the particular pattern of the corrugated intermediate energy reflecting layer the radiation going through the existing space between tube is reflected in the reflective corrugated surface and directed back to the collecting tubes.
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Abstract
Description
- The present invention relates to the field of radiant energy or heat collector assemblies. More particularly, it refers to methods and systems for recovering or capturing heat in the form of radiant energy and using the recovered energy for further purposes such as heating of buildings, electricity production or steam generation. The heat capturing device can be applied in industries such as in steel mills, metallurgy, furnaces or glass production or any other energy intensive industry with high radiant emissions.
- The European patent application
EP2403668 (A2 ) discloses a heat retrieving system in which heat is retrieved via conduction and convection. This patent application uses the transportation rollers as heat exchangers. The patent applicationDE3019714 (A1 ) discloses a heat collection arrangement comprising water containing tubes. The prior art is silent on heat collection devices especially configured for capturing heat transferred by radiation. It is therefore required a technical arrangement recovering radiant energy or heat from an object or objects being at temperature higher than 500° C. - There is the general belief that optimal dimensions of the heat capturing device collecting energy tend to be minimum. However, the present application proves it is not necessarily the case because the dimensions or the size of a device collecting more energy than the known devices or systems depend on several factors. The present application achieves the unexpected technical effect of finding which are the dimensions of the heat capturing device that enable collecting more energy from an object at high temperature than the systems or devices in the prior art.
- The present application overcomes the drawbacks of the prior art and allows higher energy or heat retrieval of the heat or energy radiated by an object or group of objects.
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Claim 1 discloses the scope of the present realization. Preferred realizations are disclosed in claims 2-16. The described heat capturing device comprises an upper side and lateral sides connected to the upper side, said connected sides defining an energy capturing space. The device further comprises an energy insulating layer, an intermediate energy reflecting layer and an inner energy capturing layer capturing energy from at least a radiation emitting object (hereinafter referred to as "object") located at least partly in the energy capturing space. The inner energy capturing layer comprises at least one material containing structure. The material may be a heat transfer fluid (hereinafter referred to as fluid), for example a liquid such as silicon based thermal oil, for capturing energy. The material containing structure may be at least a tube having preferably a circular cross-section. The dimensions of the inner energy capturing layer (width and height of the inner energy capturing layer), and thus, the dimensions of the heat capturing device as a whole including the intermediate energy reflecting layer, the energy insulating layer and the energy capturing space defined, are based, at least, on the dimensions of the at least an object in the energy capturing space and based on at least a further parameter. Said further parameter may be at least one of: at least one further parameter of said at least an object or at least one parameter of the inner energy capturing layer or at least one parameter of the energy capturing space or a combination of said further parameters. Said further parameter or parameters of the inner energy capturing layer may be intrinsic parameters of the surface of the inner energy capturing layer defining the energy capturing space. - In the heat capturing device, the energy insulating layer may entirely cover the intermediate energy reflecting layer, and the intermediate energy reflecting layer may entirely cover the inner energy capturing layer.
- A further plate or plates may be located at the entrance or exit of the energy capturing space for better retaining and/or reflecting the radiant heat or energy of the object or objects inside the energy capturing space. The plate or plates located at the entrance and/or exit of the energy capturing space may be made of a heat or energy reflecting material. The energy insulating layer may be covered with an outer casing or outer cover for protecting and encapsulating the heat capturing device. The described layers may be different layers which may be separated from each other. The heat capturing device may be connected to a bottom layer or plate or surface made of either reflecting or insulating heat material.
- The parameter or parameters defining the width and the height of the inner energy capturing layer may be, for example, at least one of: the convection coefficient of the air inside the energy capturing space, the emissivity and absorptivity of at least one of the surfaces of the object, the emissivity and absorptivity of at least one of the surfaces of the inner energy capturing layer or a combination of said parameters. The emissivity and absorptivity of a surface are magnitudes indicating its effectiveness in emitting or absorbing (respectively) thermal radiation. Quantitatively, they are described as the ratio between the thermal radiation emitted/absorbed by a surface compared to the radiation emitted/absorbed by an ideal black body at the same temperature (which is maximum).
- The parameter or parameters defining the height and width of the heat capturing device may be based on some intrinsic properties of the objects which are to be received in the energy capturing space or transported through the energy capturing space. The objects can be for example a slab, billet or beam resulting from a production process such as a metallurgic production process or preferably a piece of hot glass (e.g. bottle shaped glass) produced by a glass production factory. Said production processes may serially produce objects such as slabs or hot pieces of glass, and some properties of said serially produced objects or pieces are known. The objects may be solid or partly solid objects. The objects are preferably at a temperature higher than 500° C. The fact that the characteristics of the production of the object or objects are known in advance, means that the properties of the product after the production process and before entering the energy capturing space are known. The fact that the heat capturing device of the present application allows a modular construction permits the customization of the size or dimensions of the heat capturing device or tailoring the size of the heat capturing device according to the properties of the objects, thus allowing to capture the radiated heat from the objects when the objects are partly or completely in the energy capturing space or even slightly outside the energy capturing space. The width and the height of the inner energy capturing layer can be selected based on said properties of the object, which implies that the width and height of the heat capturing device as a whole is selected based on at least the properties of the objects or parameters taking into consideration the properties of the object. The heat capturing device and its size may be configured before the production process of the objects start. The modularity of the heat capturing device permits the heat capturing device to be assembled and/or remove parts of the heat capturing device easily.
- The inner energy capturing layer, for example a tube bundle, may cover an inner surface of a tunnel-shaped surface defined by the energy capturing space or may have a tunnel-shaped arrangement, and the diameter of the tubes of the bundle may be the same or similar. The dimensions or the size of the tube bundle are defined in such a way that the heat captured by the heat capturing device is maximized, mainly the heat transmitted by radiation. The arrangement of the tube bundle may be perpendicular or parallel to the direction of movement of the objects being transported (e.g. objects entering, leaving or being transported through the energy capturing space or objects remaining for some time in the energy capturing space). Heat losses due to convection and radiation of the surfaces of the heat capturing device (e.g. the tubes of the bundle) are minimized using insulating materials. The heat capturing device, and more particularly the inner energy capturing layer may be designed to operate with the fluid flowing through the tubes at a medium fluid temperature around 350° C. In some examples and depending on the temperature of the objects from which radiated heat is going to be captured, the fluid may be at a temperature that satisfies a heat demand with temperatures between 600 and 140° C. In some other examples, the fluid may be at a temperature that satisfies a heat demand with temperatures between 140 and 40° C.
- The tubes of the bundle may be separated from each other. More preferably, the distance between the center of two consecutive tubes may be between 1,25 and 2 times the external diameter of a tube of the bundle.
- The bundle of tubes may be connected, e.g. welded, to at least two headers. The headers may be to feed the fluid to the inner energy capturing layer with the fluid being at a first temperature, to distribute the fluid through the inner energy capturing layer such the fluid may increase its temperature from the first temperature to a second temperature by absorbing heat from the object or objects, and to remove the fluid from the inner energy capturing layer with the fluid at the second temperature. In some examples, the second temperature may be higher than the first temperature. The headers may transport the fluid from/to a fluid storage or to any other device that may reuse the recovered energy for similar or different purposes such as heating of buildings, electricity production or steam generation.
- The external surface of the bundle of tubes, i.e., the surface of the bundle of tubes facing the object, may be covered with a high absorptivity coating or with a high absorptivity paint. The paint may have as much absorptivity as possible in near and mid-infrared spectrum, and at least higher than the corresponding values of the base material of the inner capturing layer. For example, the paint may have an absorptivity around 0,97 for a wavelength between 2-3 microns.
- The intermediate energy reflecting layer may have a flat structure such as a plate or a corrugated shaped structure or surface or layer behind the bundle of tubes. The corrugated shaped structure may be a sinus shaped surface or sinus shaped structure. The convex part of the corrugated shaped structure is located in correspondence with at least one of the tubes of the bundle and the concave part of the corrugated shaped structure is located in correspondence with at least one of the separations between the tubes. The corrugated or wavy or sinus shaped structure is designed to better focus the reflected heat towards the rear part of the tubes for allowing better heat or energy absorption of the reflected heat, thus allowing an enhanced heat exchange with the rear part of the tubes.
- The heat capturing device may comprise an energy insulating layer surrounding the intermediate energy reflecting layer. The energy insulating layer may be made of ceramic fiber. The insulating layer may be a separate layer from the other layers.
- The heat capturing device may further comprise an outer casing covering the energy insulating layer. The outer casing, that may be made of metal, contains and protects the heat capturing device.
- The heat capturing device may comprise one or several sensors. The sensors may be of the same type or may be a combination of different types of sensors. The sensors may be: one or more sensors for measuring the temperature of the object or objects, one or more sensors for measuring the temperature of the energy capturing space, one or more sensors for measuring the temperature inside the tubes or the temperature of the fluid within the tubes, one or more sensors for detecting the object either entering into, or exiting out of or remaining in the energy capturing space or any combination of said sensors. The sensors may be connected to control means, such as a controller or processor or group of processors for processing the information received from the sensors. The control means may process the data received form the sensors and may issue instructions or control data based on the sensed data as provided by one or more of said sensors, based on the processed data or based in a combination of the data as received and the data after being processed.
- The heat capturing device may comprise transport means for moving the object or objects relative to the energy capturing space. The transport means may be managed by control means, the control means configured to control the transport of the object from or to the energy capturing space. The heat capturing device automatically transports the object to or from the energy capturing space based on a certain temperature captured by at least one or more sensors exceeding or being below a predetermined threshold. Said threshold may define a temperature threshold. The transport means may transport the object through the energy capturing space or may leave the object in the energy capturing space for a predetermined time interval so that the inner energy capturing layer captures heat from the object. The transport means transport the object or objects through the energy capturing space in case the tunnel-shaped heat capturing device or tunnel-shaped inner energy capturing layer is open on both sides, that means no plate or door is placed at the entry and exit of the tunnel-shaped heat capturing device. In case a plate or door is located at the exit of the tunnel-shaped heat capturing device, the transport means use the open entry for entering and removing the object or objects to/from the energy capturing space.
- The device may comprise further control means, wherein the control means are configured for controlling the quantity of fluid and/or the speed of the fluid circulating in the bundle of tubes, wherein the control means automatically control said quantity and/or speed of fluid based on the data captured by at least one of the sensors. The control means may process the data received from the sensors and based on said processing, the control means may issue instructions or control data. The instructions may control the transport means such as its speed, start and stop functions, may control the quantity of fluid circulating in the bundle of tubes, may control the quantity of fluid in the headers and may control the speed of fluid circulating in the tubes or in the bundle of tubes. The transport means are preferably controlled for transporting the object or objects such that the objects or objects are symmetrically placed or located inside the energy capturing space or symmetrically placed or located while being transported through the energy capturing space. The control means may control the transport means and the speed of transport of the object or objects entering or leaving the energy capturing space. This may be useful in cases in which the object or objects are transported through the energy capturing space. Moreover, the control means may control the time period an object or objects remain the energy capturing space and it can be implemented by the control means controlling the transport means for stopping and starting the transport means.
- The instructions of the control means may control the transport means and all devices regulating the flow and/or temperature of fluid in the tubes or headers.
- The distance of the respective lateral sides of the object to the respective corresponding closest surface or sides of the inner energy capturing layer (e.g. bundle of tubes) is preferably the same, or equal or almost the same, while the object (or objects) is in the energy capturing space.
- A method for capturing energy as indicated by the heat capturing device may be implemented.
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- Wherein the nomenclature is the following:
- Fij View factor from surface "i" to surface "j" (according to
figure 4 ). - Ai Area of the different surfaces.
- Ti Temperature of the different surfaces.
- εi Emissivity of the different surfaces.
- αi Absorptivity of the different surfaces.
- σ Stefan-
Boltzman constant 5,67.10-8 W/m2K4. - hconv Convection coefficient of the air inside the energy capturing space (tunnel).
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- 1 Object.
- 2 Inner energy capturing layer or heat capturing device.
- 3 Surface that closes the energy capturing space.
- A heat capturing system is further described. Said heat capturing system comprises a heat capturing device as previously described and at least one object located at least partly in the energy capturing space. In such system, the heat capturing device is configured to capture heat from the at least one object that is inserted into the energy capturing space defined by the upper side and lateral sides connected to the upper side of the heat capturing device. The at least one object is cooled by capturing the heat irradiated from the object by the inner energy capturing layer of the heat capturing device.
- Additional advantages and features of the invention will become apparent from the detailed description that follows and will be particularly pointed out in the appended claims.
- To complete the description and in order to provide for a better understanding of the invention, a set of drawings is provided. Said drawings form an integral part of the description and illustrate an embodiment of the invention, which should not be interpreted as restricting the scope of the invention, but just as an example of how the invention can be carried out. The drawings comprise the following figures:
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Figure 1 shows a schematic representation of a system for carrying out the method of the invention. -
Figure 2 shows a rectangle to rectangle in a perpendicular plane; all boundaries are parallel or perpendicular to x and ξ boundaries. -
Figure 3 shows a rectangle to rectangle in a parallel plane; all boundaries are parallel or perpendicular to x and ξ boundaries. -
Figure 4 shows a rectangular heat capturing device's and object's surfaces listed. -
Figure 5 shows a view factor of the object's wall to heat capturing device's roof. -
Figure 6 shows a view factor of the object's wall to heat capturing device's wall. -
Figure 7 shows a view factor of the object's top wall to heat capturing device's wall. -
Figure 8 shows a view factor of the object's top wall to heat capturing device's roof. -
Figure 9 shows all heat transfer phenomena in the energy capturing space. -
Figures 10-12 show a graphical representation of the listed cases 1-8 mentioned in the following Table 1, in which the heat capturing device and the object in the heat capturing device are represented. The representation may be considered as a proportional representation of the dimensions of the heat capturing device relative to the dimensions of the object. -
Figure 13 shows a perspective view of an example tunnel-shaped heat capturing device using the tubes and the energy insulating layer, the tubes being positioned substantially perpendicular to the direction of displacement of the at least one object relative to the tunnel-shaped heat capturing device. -
Figure 14 shows a cross-sectional representation of the tunnel-shaped heat capturing device and the further layers of the tunnel-shaped heat capturing device offigure 13 . -
Figure 15 shows a perspective view of another example tunnel-shaped heat capturing device using the tubes and the energy insulating layer, the tubes being positioned substantially parallel to the direction of displacement of the at least one object relative to the tunnel-shaped heat capturing device. -
Figure 16 shows a cross-sectional representation of the tunnel-shaped heat capturing device and the further layers of the device offigure 15 . -
Figure 17 shows a perspective view of an example inner energy capturing layer. -
Figure 18 shows a representation of an example architecture of some tubes of the tube bundle forming the inner energy capturing layer and a representation of the corrugated intermediate energy reflecting layer. - The present description represents exemplary embodiments on how to carry out the present invention.
- The heat capturing device's geometry (see
figure 1 ), in particular the width (A) and the height (B) of the inner energy capturing layer; the object's (or objects') geometry, in particular the height (C) and the width (D) of the object, considering that the object or objects are assimilated to a parallelepiped of smaller volume that can contain them; and the spatial relationship between the heat capturing device and the at least one object, in particular, the height of the position of the heat capturing device relative to the at least one object, influence the thermal behavior of the heat capturing device. The length (L) is the length to be covered in the process with one or more heat capturing devices lined up next to each other (not the length of an individual heat capturing device). - In the following lines it is explained the procedure carried out to reach an equation that gives the optimal geometry of the inner energy capturing layer, and thus of the heat capturing device as a whole, for some given conditions. This optimal geometry will maximize the heat flow absorbed by the inner energy capturing layer of the heat capturing device.
- To obtain the equation some assumptions may be considered (see
Figure 1 ): - In the calculation of the view factors, the
heat capturing device 2 and the at least anobject 1 have been considered as 3D bodies, where they have a finite length (L). This has been done as the heat capturing device could, in some cases, have a length short enough to make considerable the radiation that is lost at the ends; - The heat capturing device is in a symmetrical position to the centre of the at least an object;
- For the heat balance equation, it has been considered that the heat capturing device is perfectly insulated from behind (face not exposed to the radiation from the at least one object) due to the intermediate energy reflecting layer and the energy insulating layer included in the heat capturing device design;
- It may have to be specified:
- ∘ the average temperatures (T) of the objects' surface (the surface and the kernel temperature of the object are different), the heat capturing device and the ambient inside the energy capturing space (in the space between the piece and the heat capturing device);
- ∘ the optical properties of the at least one object surfaces and heat capturing device surfaces;
- ∘ the dimensions of the objects considered as the parallelepiped of smaller volume that can contain them (C and D);
- ∘ the height (Hzl) of the position of the heat capturing device relative to the lower surface of the piece (or object) (in case there is any restriction that avoids that both systems are over the same plane);
- ∘ the length (L) to be covered in the process with one or more heat capturing devices;
- ∘ the maximum and minimum dimensions (height and width) the heat capturing device could have due to process constraints;
- ∘ the estimated convection heat transfer coefficient (hconv) of the air between the objects and the heat capturing device.
- Other parameters used in the following calculation are Ai (area of the different surfaces) and α (absorptivity of different surfaces), Ti (temperature of the different surfaces), εi (Emissivity of the different surfaces), αi (aabsorptivity of the different surfaces), σ (Stefan-
Boltzman constant 5,67.10-8 W/m2K4) and hconv (convection coefficient of the air inside the energy capturing space (tunnel).Sub-index 1 refers to the object,sub-index 2 refers to the heat capturing device andsub-index 3 refers to the surface that closes the energy capturing space (seefigure 4 ). - Based on the equations from the book Thermal Radiation Heat Transfer by Howell, J. R., Mengüç, M. P.& Siegel, R. for "Rectangle to rectangle in a perpendicular plane; all boundaries are parallel or perpendicular to x and ξ boundaries" and "Rectangle to rectangle in a parallel plane; all boundaries are parallel or perpendicular to x and ξ boundaries" and using the properties of the view factors the final view factor between the surfaces have been obtained (See
Figures 2 and 3 ). - Using these equations, the view factor between the heat capturing device and the object has been calculated. During the procedure the nomenclature from
Figure 4 has been used. -
- The coordinates x, y, a and b are represented graphically in the
Figures 5-8 . -
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Figure 9 shows the different heat fluxes considered. The heat capturing device is assumed to be perfectly insulated from the back. - For the calculation of the net heat flux transferred through radiation the
object 1 and theheat capturing device 2 are considered as grey bodies (a body that emits radiation at each wavelength in a constant ratio less than unity to that emitted by a black body at the same temperature) and thesurface 3 is considered a black body (a body that absorbs all incident electromagnetic radiation, regardless of frequency or angle of incidence, an ideal emitter that at every frequency emits as much or more thermal radiative energy as any other body at the same temperature). -
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- The value of the convection heat transfer coefficient (hconv) may be introduced by the user.
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- The optimal design is obtained by solving an optimization problem. This is formulated as the maximization of the total heat transferred between the piece (object) and the heat capturing device (more particularly the bundle of tubes of the inner energy capturing layer), subject to the physical and manufacturing constraints.
- It should be noted that the minimum width and height that the heat capturing device can have (since in real processes these dimensions must leave a safety margin) are also input parameter.
- The model-based optimization approach was used to formulate the design optimization problem. The supporting model was developed in Python 3.6 based on physics equations. Regarding the optimizer, the proposed solution is based on the L-BFGS-B algorithm implemented in the Scipy (v1.1.0) optimization package.
- The following table presents different cases in which the input parameters of the system have been varied. Depending on the value of these, the optimum geometry of the heat capturing device varies.
Table 1 Case 1Case 2Case 3Case 4Case 5Case 6Case 7Case 8 A minimum 0.255 0.255 0.255 0.255 0.255 0.255 0.255 0.455 B minimum 0.255 0.255 0.255 0.255 0.255 0.255 0.455 0.255 C 0.155 0.155 0.155 0.155 0.155 0.155 0.355 0.155 D 0.155 0.155 0.155 0.155 0.155 0.155 0.155 0.355 H 0 0 0 0 0 0 0 0 L 5 5 5 5 5 5 5 5 ε1 0.8 0.8 0.8 0.8 0.95 0.65 0.8 0.65 ε2 0.96687 0.96687 0.7 0.7 0.7 0.7 0.7 0.7 α1 0.8 0.8 0.8 0.8 0.95 0.65 0.8 0.65 α2 0.9664 0.9664 0.7 0.7 0.7 0.7 0.7 0.7 T1 900 900 900 900 900 900 900 900 T2 400 400 400 400 400 400 400 400 T3 24 24 24 24 24 24 24 24 hconv 10 0 10 5 10 10 10 10 A optimum 0.255 0.255 0.255 0.255 0.255 0.255 0.255 0.455 B optimum 0.255 0.73581 0.36354 0.59339 0.44862 0.27763 0.81044 0.32206 -
Figures 10-12 show a graphical representation of the listed cases 1-8 mentioned in the following Table 1. In particular such figures show a schematic representation of the size ratio between the object and the heat capturing device (named as collector in the figures for clarity purposes). - Case 1 (see Table 1) has been selected as a reference case where the optimal solution for the heat capturing device geometry matches with the minimal dimensions defined for it. As can be seen in
cases 1 to 6 (see Table 1) with the same minimum values for the dimensions of the heat capturing device the optimal solution is affected by: - the operating conditions:
case 2 andcase 4 with lower convection losses; - the absorptivity and emissivity of the inner surfaces of the heat capturing device:
case reference case 1; - the absorptivity and emissivity of the object:
case 5 has high values (such as the ones corresponding to glass pieces) andcase 6 has lower values; and -
cases reference Case 1. - As can be seen although intuitively it might seem that the optimal dimensions of the heat capturing device will always tend to be the minimum, the results show how this is not so. This is a surprising and unexpected technical effect achieved by the claimed scope.
- As seen in the previous section, with the optimization procedure it is possible to obtain the best geometric solution for the heat capturing device in many situations. These situations can be extrapolated to many industrial processes that produce high temperature pieces from which emitted radiation is captured for the heat capturing device herein described.
-
Figure 13 shows a perspective view of an example tunnel shapedheat capturing device 30 wherein the inner energy capturing layer comprises a bundle oftubes 31. Thetubes 31 may have preferably a circular cross section. Theheat capturing device 30 may be implemented usingtubes 31 having other cross sections such as square or elliptical cross sections. Thetubes 31 are connected to the representedheaders 32. Thetubes 31 of the bundle may be welded to theheaders 32. The innerenergy capturing layer 31 is covered by an intermediateenergy reflecting layer 33 that in turn is covered by anenergy insulating layer 34, preferably made of ceramic fiber with low thermal conductivity. Theenergy insulating layer 34 is covered by anouter casing 35, preferably made of a metal. Theheaders 32 transport the heat captured by the fluid inside the tubes of theheat capturing device 30 to either a heating station or to a heat exchanger (not shown). Theheat capturing device 30 comprises control means which may control the flow of fluid in thetubes 31 of the bundle and may control at least one pump, cooling means and/or valves (not shown). The control means of theheat capturing device 30 may control the cooling means or control one or more heat exchangers for regulating the temperature of the fluid flowing in thetubes 31. The control of the pump and/or valves by the control means allow to control the quantity or volume of fluid circulating in thetubes 31. The fluid circulating in thetubes 31 of the bundle may be water, an organic thermal oil or silicone based thermal oil. - The objects introduced in the
energy capturing space 36 are at high temperatures, such as typically greater than 500°C. The heat capturing device is designed to operate with medium temperatures in the fluid around 350° C. -
Figure 14 shows a cross-sectional cut of theheat capturing device 30 offigure 13 . It can be appreciated that all layers, namely theouter casing 35, theenergy insulating layer 34, the intermediateenergy reflecting layer 33 and the inner energy capturing layer 31 (e.g. the tubes) have a tunnel shape as shown which indicates that said layers also define the ceiling and the sides of the tunnel shape arrangement. All said layers may also be at least partly disposed in the floor of said tunnel shaped structure, such that thetubes 31 are also able to capture heat or energy from the floor side of the structure. - In some embodiments, the
outer casing 35 may be disregarded, and it is not installed. - Preferably, the
tubes 31 are not in direct contact with the intermediateenergy reflecting layer 33 or reflecting plate, i.e., the inner energy capturing layer 31 (e.g. tubes) and the intermediateenergy reflecting layer 33 are separated by air or some gas. In some embodiments the innerenergy capturing layer 31 may contact the intermediateenergy reflecting layer 33. The intermediateenergy reflecting layer 33 may be in direct contact with theenergy insulating layer 34, or both layers (intermediateenergy reflecting layer 33 and energy insulating layer 34) may be separated by a chamber of air or gas or insulating fluid. Theenergy insulating layer 34 may be in contact with theouter casing 35 or may be separated by air. - The
outer casing 35 may be made of steel or other metal or may be made of refractory material or heat resistant material. -
Figure 15 shows a perspective view of another example tunnel-shapedheat capturing device 40 with thetubes 41 being positioned substantially parallel to the direction of displacement of the twoobjects 47 relative to theenergy capturing space 46 defined by the tunnel-shapedheat capturing device 40. WhileFigure 15 shows two identical objects placed parallel to each other, any number of objects with any different shape and spatial relationship to each other could be placed in theenergy capturing space 46. - In such example, the
tubes 41 of the bundle may have preferably a circular cross section although any other cross sections such as square or elliptical cross sections may be implemented. Thetubes 41 are connected to the represented headers 42 (not shown in this figure). The headers may be positioned at both openings of the tunnel such that their geometry corresponds to the geometry of the openings. - In such example, the intermediate
energy reflecting layer 43 is attached to the inner surface of the outerenergy insulating layer 44. Theenergy insulating layer 44 is located between the intermediateenergy reflecting layer 43 and theouter casing 45. Theenergy insulating layer 44 may be made of ceramic fiber with low thermal conductivity. -
Figure 16 shows a cross-sectional representation of the tunnel-shaped heat capturing device and the further layers of the device offigure 15 . -
Figure 17 shows a perspective view of an example innerenergy capturing layer 50. In such example, the innerenergy capturing layer 50 is formed by a bundle oftubes 51 for circulating the heat transfer fluid, afirst header 52 and asecond header 53. Thetubes 51 are placed in parallel to each other and have the same diameter. Besides, the distance between twoconsecutives tubes 51 is the same along the entire innerenergy capturing layer 50. The fluid 54 ingress in thetubes 51 via thefirst header 52 through afirst opening 55. Thefirst header 52 is divided in sections 56 wherein each section is communicated to a set oftubes 51 but isolated from the contiguous sections 56 within thefirst header 52. Thesecond header 53 is divided in sections 57 wherein each section is communicated to a set oftubes 51 but isolated from the contiguous sections 57 within thefirst header 53. In such example, the fluid 54 that enters into thefirst section 56a of thefirst header 52 circulates through thetubes 51 connected to thisfirst section 56a until thefirst section 57a of thesecond header 53, which in turn is connected to other tubes for keeping circulating the fluid towards asecond section 56 b of the first header, and so on, until the fluid reaches the last section of thefirst header 53 through which the fluid 54 exits the innerenergy capturing layer 50 via a second opening (not shown in this figure). -
Figure 18 shows a representation of an example architecture of some tubes of the tube bundle forming the inner energy capturing layer and a representation of the corrugated intermediate energy reflecting layer. - In such example, the distance (d1) between the centers of two consecutive tubes is 1.25 times the outside diameter of one of the tubes. All tubes have the same diameter. The minimal distance (d2) between the outer surfaces of two consecutives tubes is 0.25 times the diameter of one of the tubes. Due to the particular pattern of the corrugated intermediate energy reflecting layer the radiation going through the existing space between tube is reflected in the reflective corrugated surface and directed back to the collecting tubes.
- The invention is obviously not limited to the specific embodiments described herein, but also encompasses any variations that may be considered by any person skilled in the art (for example, as regards the choice of materials, dimensions, components, configuration, etc.), within the general scope of the invention as defined in the claims.
Claims (15)
- Heat capturing device comprising:an upper side and lateral sides connected to the upper side, said connected sides define an energy capturing space, the device further comprising:an energy insulating layer;an intermediate energy reflecting layer; andan inner energy capturing layer capturing energy from at least one object located at least partly in the energy capturing space;wherein the dimensions of the inner energy capturing layer are based on the dimensions of the at least one object and based on a further parameter, said further parameter being at least one of: at least a second parameter of the at least one object, at least one parameter of the inner energy capturing layer, at least one parameter of the energy capturing space and any combination thereof.
- The device according to claim 1, wherein the second parameter of said at least one object is selected from a group comprising the emissivity of at least one or more of the surfaces of the at least one object, the absorptivity of at least one or more of the surfaces of the at least one object and a combination thereof, said second parameter of said at least one object defining the width of the inner energy capturing layer.
- The device according to any one of claims 1-2, wherein the further parameter defines the weight and the height of the inner energy capturing layer, said further parameter being at least one of: the convection coefficient of the air inside the energy capturing space, the emissivity of at least one of the surfaces of the object, the absorptivity of at least one of the surfaces of the object, the emissivity of at least one of the surfaces of the inner energy capturing layer, the absorptivity of at least one of the surfaces of the inner energy capturing layer and any combination thereof.
- The device according to any one of claims 1-3, wherein the inner energy capturing layer is a bundle of tubes, the bundle of tubes covers a tunnel-shaped surface, wherein at least of one or more of the tubes of the bundle comprises a heat transfer fluid.
- The device according to claim 4, wherein the distance between the center of two consecutive tubes is between 1,25 and 2 times the external diameter of a tube of the bundle.
- The device according to any one of claims 4-5, wherein the bundle of tubes is connected to at least two headers to distribute the heat transfer fluid through the bundle of tubes and wherein the heat transfer fluid is feed to the bundle of tubes at a first temperature and removed at a second temperature, the second temperature being higher than the first temperature.
- The device according to any of claims 4-6, wherein the external surface of the bundle of tubes is covered with high absorptivity coatings or high absorptivity paint.
- The device according to any of claims 1-7, wherein the energy absorbed is heat and the heat absorbed by the inner energy capturing layer is defined as follows:Ai Area of the different surfacesTi Temperature of the different surfaces, wherein T1 is the temperature of the object, T2 is the temperature of the fluid circulating through the heat capturing device, T3 is the ambient temperature in the energy capturing spaceεi Emissivity of the different surfacesαi Absorptivity of the different surfaceshconv Convection coefficient of the air inside the tunnel.Fij View factor from surface i to surface j (according to figure 4).σ Stefan-Boltzman constant 5,67.10-8 W/m2K4.Subscripts/Sub-index:1 Object2 Inner energy capturing layer3 Surface that closes the energy capturing space
- The device according to any one of claims 4-8, wherein the intermediate energy reflecting layer comprises a corrugated shaped surface behind the bundle of tubes, wherein the convex part of corrugated shaped surface is located in correspondence with at least one of the tubes of the bundle and the concave part of said surface is located in correspondence with at least one of the separations between the tubes.
- The device according to any one of claims 4-9, wherein the device comprises at least one sensor for measuring the temperature of the at least one object, or at least one sensor for measuring the temperature of the energy capturing space, or at least one sensor for measuring the temperature inside the tube or the temperature of the fluid within the tube, or at least one sensor for detecting the object either entering into, or exiting out of or remaining in the energy capturing space or a combination of said sensors.
- The device according to any one of claims 1-10, wherein the energy insulating layer covers the intermediate energy reflecting layer, and the intermediate energy reflecting layer covers the inner energy capturing layer, and wherein the device further comprises an outer casing covering the energy insulating layer.
- The device according to any one of claims 1-11, wherein the device comprises transport means and control means, the control means configured to control the transport of the object from or to the energy capturing space, wherein the device automatically transporting the object to or from the energy capturing space based on a certain captured temperature measured by at least one or more said sensors, said certain temperature exceeding or being below a predetermined threshold.
- The device according to any one of claims 11 or 12, wherein the control means are configured for controlling the quantity of fluid and/or the speed of the fluid circulating inside the bundle of tubes, wherein the control means automatically control said quantity and/or speed of fluid based on the data measured by at least one of the sensors.
- The device according to any one of claims 1-13, wherein the device comprises a modular structure permitting to add parts to the device or remove parts from the device.
- A heat capturing system comprising:a heat capturing device according to any one of claims 1 to 14; andat least one object located at least partly in the energy capturing space;wherein the heat capturing device is configured to capture radiated heat from the at least one object by the inner energy capturing layer.
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Citations (8)
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JPS56131906U (en) * | 1980-02-29 | 1981-10-06 | ||
DE3019714A1 (en) | 1980-05-23 | 1981-12-10 | Mannesmann AG, 4000 Düsseldorf | Steel billet heat recovery equipment - comprises tunnel containing rollers conveyor with water pipes between rollers |
US20110049773A1 (en) * | 2009-08-27 | 2011-03-03 | Kiefer Bruce V | Heat retention tunnel for processing coils of hot rolled bar and rod products |
EP2403668A2 (en) | 2009-03-02 | 2012-01-11 | SMS Siemag AG | Energy recovery in hot strip mills by converting the cooling heat of the continuous casting plant and the residual heat of slabs and coils into electrical energy or otherwise utilizing the captured process heat |
DE102011107685A1 (en) * | 2011-07-13 | 2013-01-17 | Werner Luz | Method and apparatus for recovering heat energy from coils |
EP2861771A1 (en) * | 2012-06-15 | 2015-04-22 | G.A.P. S.p.A. | Device for recovering heat and fumes from slag resulting from the steel production cycle |
WO2016178641A1 (en) * | 2015-05-06 | 2016-11-10 | Topal Ömer Ali | Waste heat exchanger for produced hot metal parts |
US20180050406A1 (en) * | 2015-04-24 | 2018-02-22 | Semikron Elektronik Gmbh & Co. Kg | Device, method, and system for cooling a flat object in a nonhomogeneous manner |
-
2018
- 2018-12-20 EP EP18382964.7A patent/EP3670027A1/en not_active Withdrawn
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
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JPS56131906U (en) * | 1980-02-29 | 1981-10-06 | ||
DE3019714A1 (en) | 1980-05-23 | 1981-12-10 | Mannesmann AG, 4000 Düsseldorf | Steel billet heat recovery equipment - comprises tunnel containing rollers conveyor with water pipes between rollers |
EP2403668A2 (en) | 2009-03-02 | 2012-01-11 | SMS Siemag AG | Energy recovery in hot strip mills by converting the cooling heat of the continuous casting plant and the residual heat of slabs and coils into electrical energy or otherwise utilizing the captured process heat |
US20110049773A1 (en) * | 2009-08-27 | 2011-03-03 | Kiefer Bruce V | Heat retention tunnel for processing coils of hot rolled bar and rod products |
DE102011107685A1 (en) * | 2011-07-13 | 2013-01-17 | Werner Luz | Method and apparatus for recovering heat energy from coils |
EP2861771A1 (en) * | 2012-06-15 | 2015-04-22 | G.A.P. S.p.A. | Device for recovering heat and fumes from slag resulting from the steel production cycle |
US20180050406A1 (en) * | 2015-04-24 | 2018-02-22 | Semikron Elektronik Gmbh & Co. Kg | Device, method, and system for cooling a flat object in a nonhomogeneous manner |
WO2016178641A1 (en) * | 2015-05-06 | 2016-11-10 | Topal Ömer Ali | Waste heat exchanger for produced hot metal parts |
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