Classifications

• • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
  • F24—HEATING; RANGES; VENTILATING
  • F24T—GEOTHERMAL COLLECTORS; GEOTHERMAL SYSTEMS
  • F24T10/00—Geothermal collectors
  • F24T10/10—Geothermal collectors with circulation of working fluids through underground channels, the working fluids not coming into direct contact with the ground
  • F24T10/13—Geothermal collectors with circulation of working fluids through underground channels, the working fluids not coming into direct contact with the ground using tube assemblies suitable for insertion into boreholes in the ground, e.g. geothermal probes
• • 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
  • F28F13/185—Heat-exchange surfaces provided with microstructures or with porous coatings
• • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
  • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
  • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
  • Y02E10/00—Energy generation through renewable energy sources
  • Y02E10/10—Geothermal energy

Definitions

• the invention relates to a downhole heat exchanger for recovering geothermal energy from a borehole.
• the recovery of geothermal energy from boreholes is carried out by extraction of thermal water from opened-up aquifers or by cooling of the earth along a borehole. Cooling of the earth is effected by means of various downhole heat exchangers. To extract heat from the earth, it is possible to use vaporizable refrigerants which recover the energy by boiling. Such direct boiling heat exchangers are being used to an increasing extent. Compared to brine heat exchangers, they offer a significantly higher degree of efficiency and in technical circles are considered to be the technology of the future. There are, for example, systems based on propane (R290), butane, ammonia (R717) or carbon dioxide (R744), with propane being preferred.
• Deep downhole heat exchangers with direct boilers are also referred to as heat pipes.
• the refrigerant is conveyed upward through a channel into the heat exchanger and through a second channel.
• Film vaporization is sought by means of a spiral track which has to be produced in a complicated manner.
• vaporization of the refrigerant over the entire length of the borehole and thus heat exchanger cannot be achieved using the arrangement described there, so that complete extraction of heat is not made possible.
• the utility model DE 20 2004 018 559 U1 describes a heat generator for recovering geothermal energy from a borehole, in which a condensate stream distributor is incorporated in a heat exchanger pipe. Although wetting on all sides is likewise said to be achieved, film vaporization cannot be realized.
• DE 10 2007 005 270 Al describes a downhole heat exchanger which contains a condensate stream distributor having condensate conveying devices arranged radially and/or tangentially to the wall of the heat exchanger pipe. A radially distributed condensate film is said to be produced in this way.
• EP 1 450 142 A2 describes a heat exchanger pipe consisting of a filler-containing polymer material.
• the pipe serves to convey air as heat transfer medium.
• WO 2008/113569 discloses a pipe arrangement for downhole heat exchangers, in which the pipes have at least one layer of a polymer molding composition which contains a filler or reinforcing material which increases the mechanical strength. Damage to the outer surface during installation and subsequent crack growth are said to be prevented in this way.
• the pipe arrangement is intended for transport of a liquid heat transfer medium.
• the roughness measurement is carried out by the tracer method in accordance with DIN EN ISO 4288.
• a tracer tip made of diamond is moved at constant speed over the surface of a specimen.
• the measurement profile is given by the vertical displacement of the tracer tip, which is generally measured by means of an inductive displacement measurement system.
• standardized roughness parameters are obtained from the measured profile.
• Ra is the arithmetic mean roughness from the absolute values of all profile values.
• Rz is the average of the five peak-to-valley heights from the five individual measurements.
• Rz1max is the greatest peak-to-valley height from the five individual measurements.
• the downhole heat exchanger comprises a heat exchanger pipe which is connected to the earth via a packing material, for example bentonite.
• a packing material for example bentonite.
• the vaporization of the refrigerant condensate occurs on the interior surface of the heat exchanger pipe.
• the upward transport of the vapor formed occurs in the center of the pipe.
• the internal diameter of the heat exchanger pipe is generally in the range from 15 to 80 mm, preferably in the range from 20 to 55 mm and particularly preferably in the range from 26 mm to 32 mm.
• the heat exchanger length is generally from 60 to 200 m, with greater or smaller lengths also being possible in individual cases.
• the heat exchanger is preferably from 80 to 120 m long.
• refrigerant use is made of, for example, propane (R290), butane, ammonia (R717) or carbon dioxide (R744).
• refrigerants are, for example, propene (R1270), tetrafluoroethane (R134a), difluoromethane (R32), pentafluoroethane (R125), a mixture of R32, R125 and R134a in a ratio of 23/25/52 (R407C) or a mixture of R32 and R125 in a ratio of 50:50 (R410A).
• the interior of the heat exchanger is therefore under relatively high pressure.
• the refrigerant vapor which has ascended is compressed in a compressor and thus liquefied.
• the heat exchanger pipe can, for example, consist of metal.
• the interior surface bears a rough coating.
• the exterior surface can also be coated here, for example for reasons of corrosion protection.
• the metal can be aluminum, an aluminum alloy, steel, for example stainless steel, or any other metal. Coating can be effected by powder coating or by coating with the melt of a further molding composition as described below, for example by means of extrusion coating.
• the pipe preferably consists of plastic and particularly preferably of a thermoplastic molding composition.
• Such pipes can be rolled up so that it is not necessary to join comparatively short pieces to one another, e.g. by welding, during installation.
• the molding composition used has to have sufficient stiffness for the wall thickness to be made thin for reasons of heat transfer.
• the plastic which forms the matrix of the molding composition has to be sufficiently resistant to the refrigerant and to the moisture in the earth. This means that the wall must not swell since this would be associated with undesirable length changes.
• Suitable plastics are, for example, fluoropolymers such as PVDF, PTFE or ETFE, polyarylene ether ketones such as PEEK, polyolefins such as polyethylene or polypropylene and polyamides.
• polyamides particular preference is given to those whose monomer units contain an arithmetic mean of at least 8, at least 9 or at least 10 carbon atoms.
• the monomer units can be derived from lactams or w-aminocarboxylic acids.
• the arithmetic mean of the carbon atoms of diamine and dicarboxylic acid has to be at least 8, at least 9 or at least 10.
• Suitable polyamides are, for example: PA610 (which can be prepared from hexamethylenediamine [6 carbon atoms] and sebacic acid [10 carbon atoms], and the mean number of carbon atoms in the monomer units is thus 8), PA88 (which can be prepared from octamethylenediamine and 1.8-octanedioic acid), PA8 (which can be prepared from caprylic lactam), PA612, PA810, PA108, PA9, PA613, PA614, PA812, PA128, PA1010, PA10, PA814, PA148, PA1012, PA11, PA1014, PA1212 and PA12.
• PA610 which can be prepared from hexamethylenediamine [6 carbon atoms] and sebacic acid [10 carbon atoms], and the mean number of carbon atoms in the monomer units is thus 8
• PA88 which can be prepared from octamethylenediamine and 1.8-octanedioic acid
• PA8 which
• copolyamides based thereon with monomers such as caprolactam also being used if desired.
• the thermoplastic molding composition can be filled with reinforcing fibers and/or fillers.
• the fibers or filler particles which project at the surface in this way produce the required roughness.
• the molding composition contains from 0.1 to 50% by weight, preferably from 0.5 to 20% by weight and particularly preferably from 3 to 10% by weight, of fillers and/or fibers.
• the molding composition contains only fibers.
• the molding composition contains only fillers.
• the molding composition contains a mixture of fibers and fillers.
• Suitable reinforcing fibers are, for example, glass fibers, basalt fibers, carbon fibers, aramid fibers and potassium titanate whiskers and also fibers composed of relatively high-melting polymers.
• Suitable fillers are, for example, titanium dioxide, zinc sulfide, silicates, chalk, aluminum oxide and glass spheres.
• the thermal conductivity of the heat exchanger walls can be increased by means of suitable reinforcing fibers or fillers.
• metal fibers can be used as fiber material or metal powders, carbon black, graphite, CNTs (carbon nanotubes), hexagonal boron nitride or combinations or mixtures of the various materials can be used as filler.
• the molding composition can additionally contain the customary auxiliaries and additives, for example impact modifiers, plasticizers, stabilizers and/or processing aids.
• the surface roughness is generated by compounding in a second polymer which is incompatible or only slightly compatible with the matrix polymer and is therefore dispersed only relatively coarsely.
• Suitable combinations of materials are, for example, polyamide/polypropylene and polyamide/ethylene-acrylic ester-acrylic acid copolymer/polypropylene.
• the heat exchanger pipe can, in one embodiment, be made up of a single layer and thus consist of one of the above-described molding compositions over the entire wall thickness.
• the heat exchanger pipe is made up of a plurality of layers, with the inner layer consisting of one of the above-described molding compositions and the other layers having functions which are not performed sufficiently by the layer of molding composition having a rough surface, for example flexibility, impact toughness or barrier action toward the refrigerant or the moisture in the earth. If the layers do not adhere to one another sufficiently well, bonding agents can be used as described in the prior art.
• Suitable layer sequences from the inside outward are, for example:
• Suitable bonding agents for the bonding of polyamide and polyolefins are, for example, polyolefins functionalized with maleic anhydride.
• Polyamides such as PA12 and EVOH can, for example, be joined to one another with the aid of polyolefins functionalized with maleic acid or by means of polyamide blends corresponding to EP 1 216 826 A2.
• Polyolefins functionalized with maleic acid are suitable as bonding agents for forming the bond between EVOH and polyolefins.
• Bonding agents for joining polyamides and fluoropolymers are known, for example, from EP 0 618 390 A1, while adhesion-modified fluoropolymers can be prepared, for example, by mixing in small amounts of polyglutarimide as described in EP 0 637 511 A1, by functionalization with maleic anhydride or by incorporation of carbonate groups as described in EP 0 992 518 A1.
• the heat exchanger pipe can additionally contain internals as are known from the prior art, for example DE 10 2007 005 270 A1.
• the invention results in the falling film having a uniform layer thickness over the circumference of the heat exchanger; streaming or separation of the film is prevented. Owing to the increased surface area, better heat exchange is made possible; at the same time, the flow velocity is decreased, which counters flooding of the lowermost part of the heat exchanger.

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• Engineering & Computer Science (AREA)
• Life Sciences & Earth Sciences (AREA)
• Mechanical Engineering (AREA)
• Chemical & Material Sciences (AREA)
• General Engineering & Computer Science (AREA)
• General Life Sciences & Earth Sciences (AREA)
• Sustainable Development (AREA)
• Sustainable Energy (AREA)
• Combustion & Propulsion (AREA)
• Thermal Sciences (AREA)
• Physics & Mathematics (AREA)
• Crystallography & Structural Chemistry (AREA)
• Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
• Rigid Pipes And Flexible Pipes (AREA)
• Laminated Bodies (AREA)
• Compositions Of Macromolecular Compounds (AREA)

Applications Claiming Priority (3)

Publications (1)

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Family Applications (1)

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Cited By (11)

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Citations (8)

Family Cites Families (14)

• 2009
  • 2009-10-21 DE DE102009045882A patent/DE102009045882A1/de not_active Withdrawn
• 2010
  • 2010-10-11 KR KR1020127010174A patent/KR20120099015A/ko not_active Application Discontinuation
  • 2010-10-11 EP EP10768913A patent/EP2491316A1/de not_active Withdrawn
  • 2010-10-11 CA CA2777344A patent/CA2777344A1/en not_active Abandoned
  • 2010-10-11 MX MX2012004571A patent/MX2012004571A/es not_active Application Discontinuation
  • 2010-10-11 US US13/502,767 patent/US20120199317A1/en not_active Abandoned
  • 2010-10-11 JP JP2012534621A patent/JP2013508658A/ja not_active Withdrawn
  • 2010-10-11 RU RU2012120569/06A patent/RU2012120569A/ru not_active Application Discontinuation
  • 2010-10-11 AU AU2010309960A patent/AU2010309960A1/en not_active Abandoned
  • 2010-10-11 WO PCT/EP2010/065162 patent/WO2011047979A1/de active Application Filing
  • 2010-10-11 CN CN2010800476893A patent/CN102713458A/zh active Pending
• 2012
  • 2012-04-19 ZA ZA2012/02872A patent/ZA201202872B/en unknown
  • 2012-04-20 CO CO12065762A patent/CO6531462A2/es not_active Application Discontinuation

Patent Citations (8)

Non-Patent Citations (1)

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