EP2685201B1 - A heat exchanger with a silicon carbide set of tubes and tube plates in enamelled steel - Google Patents
A heat exchanger with a silicon carbide set of tubes and tube plates in enamelled steel Download PDFInfo
- Publication number
- EP2685201B1 EP2685201B1 EP13187710.2A EP13187710A EP2685201B1 EP 2685201 B1 EP2685201 B1 EP 2685201B1 EP 13187710 A EP13187710 A EP 13187710A EP 2685201 B1 EP2685201 B1 EP 2685201B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- tube
- tubes
- plate
- ring
- steel
- 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.)
- Expired - Lifetime
Links
- 229910000831 Steel Inorganic materials 0.000 title claims description 19
- 239000010959 steel Substances 0.000 title claims description 19
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 title description 9
- 229910010271 silicon carbide Inorganic materials 0.000 title description 7
- 239000012530 fluid Substances 0.000 claims description 12
- JUPQTSLXMOCDHR-UHFFFAOYSA-N benzene-1,4-diol;bis(4-fluorophenyl)methanone Chemical compound OC1=CC=C(O)C=C1.C1=CC(F)=CC=C1C(=O)C1=CC=C(F)C=C1 JUPQTSLXMOCDHR-UHFFFAOYSA-N 0.000 claims description 5
- 239000004696 Poly ether ether ketone Substances 0.000 claims description 4
- 229920002530 polyetherether ketone Polymers 0.000 claims description 4
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 22
- 239000004810 polytetrafluoroethylene Substances 0.000 description 22
- 239000011248 coating agent Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 7
- 239000000463 material Substances 0.000 description 6
- 239000011521 glass Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 5
- 238000007789 sealing Methods 0.000 description 4
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000013519 translation Methods 0.000 description 2
- 230000014616 translation Effects 0.000 description 2
- -1 PolyTetraFluoroEthylene Polymers 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 229920001973 fluoroelastomer Polymers 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 230000000750 progressive effect Effects 0.000 description 1
- 230000011664 signaling Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/04—Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/02—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/0229—Double end plates; Single end plates with hollow spaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/02—Header boxes; End plates
- F28F9/04—Arrangements for sealing elements into header boxes or end plates
- F28F9/06—Arrangements for sealing elements into header boxes or end plates by dismountable joints
- F28F9/10—Arrangements for sealing elements into header boxes or end plates by dismountable joints by screw-type connections, e.g. gland
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
- F28F2265/26—Safety or protection arrangements; Arrangements for preventing malfunction for allowing differential expansion between elements
Definitions
- the present invention relates to a heat with a set of tubes and tube plates and more particularly a heat exchanger suited for the treatment of highly corrosive fluids or the ones for which a high level of purity must be ensured.
- Heat exchanger are known for processing highly corrosive fluids or fluids with special purity requirements, wherein the tube plates are of a suitable material, such as solid PTFE.
- the tubes are sealed with the plate by means of threaded ring nuts, directly tightened in a threading provided in the PTFE.
- This solution presents drawbacks connected with the not satisfactory mechanical resistance of the plates, especially at high temperatures, which limits the possible applications of the exchanger and renders frequent maintenance necessary.
- a heat exchanger comprising a set of tubes consisting of SiC tubes mounted between two tube plates in enamelled steel by means of a pressure seal system on the outer surface of each tube, in which the tube can axially slide therein to compensate for thermal expansions.
- Fig.1 is briefly represented a heat exchanger according to the present invention, comprising a set of tubes in silicon carbide (SiC) (11) and tube plates in enamelled steel (12) as the essential members.
- SiC silicon carbide
- both the central shell (14) and the end distributors (13) may be provided in enamelled steel.
- a characteristic and original aspect of the heat exchanger according to the invention is represented by the enamelled tube plates substituting the traditional ones in PTFE (PolyTetraFluoroEthylene) see Fig. 2 reference 21 or the ones in PFTE-coated steel (see Fig.3 reference 31)
- PTFE PolyTetraFluoroEthylene
- Fig.4 shows the embodiment of the exchanger with a single tube plate (41), with enamelling on the shell side, in which the O ring seal gaskets (42) are locked by the threaded ring nut (43) by means of the intermediate bushing (44).
- the seal on the inner (by O ring reference 51) and the outer (by O ring reference 52) tube plate can be simultaneously achieved by a single locking of the threaded ring nut (53) by means of the intermediate bushing (54) in steel or in PEEK (phenylpolyetherketones of Du Pont), which is fitted with holes (55) for conveying possible fluid leakages to the outside.
- the two seals on the tube are separate.
- the seal is implemented by means of a double O ring gasket (62) pressed by an intermediate bushing in steel or in PEEK (64) by the screwing of a steel ring nut (63) in the corresponding thread provided in the tube plate.
- the required pressure for pressing the O ring seals has been provided by means of a special bushing in glass-filled PEEK or PTFE (66), being pressed by the tube plate.
- This pressure is applied during the coupling step of the two single plates by the locking of the screws located on an outer peripheral circumference of the enamelled area to avoid any point of discontinuity in the coating (see fig.7 reference 74).
- the type of seal is characterised by a high degree of elasticity in the axial direction made by means of a mechanical spring system or an adequate number of overlapping O ring gaskets (68), in addition to those provided for pressure seal.
- An underlying L-profile ring (69) ensures support to this elastic system regardless of the position of the underlying seal ring nut on the inner plate.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
- The present invention relates to a heat with a set of tubes and tube plates and more particularly a heat exchanger suited for the treatment of highly corrosive fluids or the ones for which a high level of purity must be ensured.
- Heat exchanger are known for processing highly corrosive fluids or fluids with special purity requirements, wherein the tube plates are of a suitable material, such as solid PTFE. The tubes are sealed with the plate by means of threaded ring nuts, directly tightened in a threading provided in the PTFE. This solution presents drawbacks connected with the not satisfactory mechanical resistance of the plates, especially at high temperatures, which limits the possible applications of the exchanger and renders frequent maintenance necessary.
- A possible alternative is the use of PTFE coated steel plates; the coating is necessarily thin, which renders it not always sufficiently impermeable, and unsuitable for providing a proper sealing for the tubes passing through the plate. This requires complicate construction for properly fixing and sealing the tubes, and a relevant danger of seepage of the circulating fluid is anyway present.
-
GB 1,112,265 US 5,630,470 provide related prior art discussing heat exchangers. - The above mentioned problems have been solved, according to the present invention, with a heat exchanger comprising a set of tubes consisting of SiC tubes mounted between two tube plates in enamelled steel by means of a pressure seal system on the outer surface of each tube, in which the tube can axially slide therein to compensate for thermal expansions. This invention is described in claim 1.
- In the attached figures are represented:
-
Figure 1 : overall view of the exchanger according to the invention where (11) is the set of tubes with silicon carbide tubes, (12) are the tube plates in enamelled steel, (14) is the central shell in enamelled steel, and (13) are the end distributors; -
Figure 2 : a detail of the tube plate in PTFE according to the prior art, double O ring seal (24), threaded ring nut (22) with threading (23) on the PTFE; -
Figure 3 : a detail of the double tube plate according to the prior art, in PTFE coated steel, where (32) is the coating in PTFE, (33) O ring seal, (34) locking through screw, (35) through holes; -
Figure 4 : a detail of the single tube plate (41) according to the invention, with O ring seal (42), threaded ring nut (43), and intermediate bushing (44); -
Figure 5 : a detail of the double tube plate, with O ring seal (51) on the inner plate and an O ring (52) on the outer plate, a single locking ring nut (53), intermediate bushing (54) hole (55) for the conveyance of possible fluid leakages; -
Figure 6 : a detail of the double tube plate, with O ring seal (62) on the inner plate (61), O ring seal (67) on the outer plate (65) locking bushing (66), steel ring nut (63), intermediate bushing (64), elastic seal system support L-profile (68); -
Figure 7 : a detail of the double tube plate with locking screw (74) of the two plates with gasket (73) between the plates. - In
Fig.1 is briefly represented a heat exchanger according to the present invention, comprising a set of tubes in silicon carbide (SiC) (11) and tube plates in enamelled steel (12) as the essential members. Depending on the plates which may be enamelled indifferently on one or both the two faces, both the central shell (14) and the end distributors (13) may be provided in enamelled steel. - A characteristic and original aspect of the heat exchanger according to the invention is represented by the enamelled tube plates substituting the traditional ones in PTFE (PolyTetraFluoroEthylene) see
Fig. 2 reference 21 or the ones in PFTE-coated steel (seeFig.3 reference 31) - Another original aspect is represented by the seal systems between the end of the SiC tube and the tube plate (see.
Fig. 4, 5, 6 ). These seal systems, especially studied for the various combinations of enamelled tube plates (enamelling only on the distributor side face, only on that of the shell side or on both), can also be adopted for traditional tube plates with tubes in SiC or in glass and represent an improvement with respect to the traditional solutions. - The improvement achieved with the present invention overcomes the drawbacks of the above mentioned prior art exchangers and in particular (with reference to
figure 2 for the plate in solid PTFE andfigure 3 for the plate in PTFE-coated steel): - The plate in solid PTFE (
Fig.2 , reference21), normally of the glass fiber filled type, can be used up to a maximum temperature of 165°C, beyond which a rapid decline in the mechanical resistance values of this material is observed. In addition, being PTFE essentially a plastic material, the tube plate may deform over time and bend under pressure, subjecting the ends of the SiC tubes (particularly the most exterior ones with respect to the set of tubes) to flexing stress beyond their ultimate stress. For this reason in practice they do not exceed φ 300 mm. - For sealing the tubes on the glass-filled solid PTFE tube plates threaded ring nuts (22) also in glass-filled PTFE are provided, which press a gasket generally of a double O ring type (24). The threading (23) on the PTFE (plastic material) tends to loosen with time the higher the temperature as well as the amplitude and the frequency of the thermal cycles. Accordingly, frequent inspections of the locking moment of the PTFE ring nuts are required to avoid leakages from the seating.
- The PTFE coated steel plates (
Fig.3 , reference 31) are not subjected to permanent progressive deformations. However, being the coating (32) necessarily thin, it has certain porosity and as a consequence is not completely impermeable. Furthermore, in this low thickness neither the threading required for the locking ring nuts of the O ring gasket nor the housings for the gaskets themselves can be formed, as it is however possible to do for the plates in solid PTFE. One must therefore resort to the solution represented by the double plate with O ring (33) in the intermediate area. To allow for the tightening of the O rings between the two plates through screws (34) passing through holes in the plate, are used and thus the PTFE coating is drilled accordingly. In correspondence of such holes (35) an appropriate seal system must be provided, which will however constitute a point of discontinuity in the coating with a danger of seepage of the circulating fluid. - With the enamelled tube plate the following advantages may be achieved:
- The coating is not porous, but perfectly impermeable and cleanable like glass;
- The high mechanical resistance of the steel plate allows the use of large-sized plates, well beyond 300 mm diameter;
- It is suitable to be easily implemented in a double embodiment with enamelling on one or on both faces and with an intermediate circuit for leakage collection (see
Fig.7 reference 71) delimited on the circumference of the O ring gasket reference 73 with a drainage hole (72) in the lower part, wherein an appropriate device for signalling the leakage itself may be screwed thereto (for example a manometer with min/max pressure contacts). In this way, the fluids are prevented from entering into contact with each other, an event to be avoided with chemically incompatible fluids or fluids which must not contaminate each another. The collected fluid allows for an immediate identification of whether the leakage is on the tube side or the shell side. - All the threaded couplings for the locking ring nuts are metallic and there fore much more reliable than those in PTFE.
- With the new sealing systems between the end of the SiC tube and the tube plate the basic needs are considered, which are however met by the traditional seal systems (generally made with fluoro-elastomer O ring gaskets of KalrezR and VitonR type or FEP-coated Silicone (C2F4/C3F6 copolymer), or other materials with high corrosion resistance), and that is:
- accomplish the pressure seal between tube and tube plate,
- prevent direct contact of the tube with the tube plate (both elements in rigid material) in such a way as to avoid breakage due to localised peaks of stress,
- allow the sliding of the tube (in the hole of the tube plate) for the automatic compensation of the different expansion between set of tubes and shell of the exchanger,
- prevent that the sum of subsequent translations of the tube, which may also occur always in the same direction, may cause the tube itself to unthread from the hole of the plate. This is achieved by a "translation limiter" consisting in the reduction in diameter of the ring nut head (reference 43, 53, 66), which prevents the tube from exiting beyond the ring nut itself.
-
Fig.4 shows the embodiment of the exchanger with a single tube plate (41), with enamelling on the shell side, in which the O ring seal gaskets (42) are locked by the threaded ring nut (43) by means of the intermediate bushing (44). - The following new prerogatives for the double tube plates are further added as examples.
- For the double tube plate enamelled only on the inner face (shell side)
Fig.5 , the seal on the inner (by O ring reference 51) and the outer (by O ring reference 52) tube plate can be simultaneously achieved by a single locking of the threaded ring nut (53) by means of the intermediate bushing (54) in steel or in PEEK (phenylpolyetherketones of Du Pont), which is fitted with holes (55) for conveying possible fluid leakages to the outside. - For the double tube plate enamelled on both sides (
Fig.6 ), the two seals on the tube are separate. For the inner plate (shell side) (61) the seal is implemented by means of a double O ring gasket (62) pressed by an intermediate bushing in steel or in PEEK (64) by the screwing of a steel ring nut (63) in the corresponding thread provided in the tube plate. - For the outer tube plate (distributor side) (65), the use of a ring nut for the locking of every single tube not being possible, the required pressure for pressing the O ring seals (67) has been provided by means of a special bushing in glass-filled PEEK or PTFE (66), being pressed by the tube plate. This pressure is applied during the coupling step of the two single plates by the locking of the screws located on an outer peripheral circumference of the enamelled area to avoid any point of discontinuity in the coating (see
fig.7 reference 74). The type of seal is characterised by a high degree of elasticity in the axial direction made by means of a mechanical spring system or an adequate number of overlapping O ring gaskets (68), in addition to those provided for pressure seal. - An underlying L-profile ring (69) ensures support to this elastic system regardless of the position of the underlying seal ring nut on the inner plate.
Claims (2)
- A heat exchanger comprising a set of tubes consisting of SiC tubes (11) mounted between two tube plates (41) in steel by means of a pressure seal system at the end of, and on the outer surface of each tube (11), in which the tube can axially slide therein to compensate for thermal expansions,
wherein each of the two tube plates (41) being a single plate (41) enamelled only on the inner face, which is the shell side thereof, and
wherein the seal between the ends of the tubes (11) and the tube plate (41) is obtained by a double O-ring gasket (42) pressed, by means of an intermediate bushing in steel or in PEEK (44), by screwing of a steel ring nut (43) in the corresponding threading provided on the distributor side of the tube plate. - The heat exchanger according to claim 1, in which the members of the seal system between tubes (11) and tube plate (41) are adapted for chemically and thermally resisting to the circulating fluids the normal operating conditions of the exchanger.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IT002449A ITMI20022449A1 (en) | 2002-11-19 | 2002-11-19 | HEAT EXCHANGER WITH SILICON CARBIDE TUBE BAND E |
EP03005976.0A EP1422488B2 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and double tube plates in enamelled steel |
Related Parent Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03005976.0A Division-Into EP1422488B2 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and double tube plates in enamelled steel |
EP03005976.0A Division EP1422488B2 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and double tube plates in enamelled steel |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2685201A2 EP2685201A2 (en) | 2014-01-15 |
EP2685201A3 EP2685201A3 (en) | 2014-02-26 |
EP2685201B1 true EP2685201B1 (en) | 2020-11-11 |
Family
ID=32211401
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03005976.0A Expired - Lifetime EP1422488B2 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and double tube plates in enamelled steel |
EP13187710.2A Expired - Lifetime EP2685201B1 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and tube plates in enamelled steel |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP03005976.0A Expired - Lifetime EP1422488B2 (en) | 2002-11-19 | 2003-03-18 | A heat exchanger with a silicon carbide set of tubes and double tube plates in enamelled steel |
Country Status (3)
Country | Link |
---|---|
EP (2) | EP1422488B2 (en) |
ES (1) | ES2835223T3 (en) |
IT (1) | ITMI20022449A1 (en) |
Families Citing this family (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8105649B1 (en) * | 2007-08-09 | 2012-01-31 | Imaging Systems Technology | Fabrication of silicon carbide shell |
CN105651099B (en) | 2010-05-06 | 2017-11-21 | 热矩阵集团有限公司 | Heat exchanger tube sheet, heat exchanger and the method for manufacturing heat exchanger tube sheet |
FR2960051B3 (en) * | 2010-05-12 | 2012-04-27 | Thermi Consult | DEVICE FOR PLATING TUBULAR PLATES FOR HEAT EXCHANGERS |
CN102278911A (en) * | 2011-05-27 | 2011-12-14 | 许昌东方化工有限公司 | Method for plugging graphite condenser for chloridizing kettle |
BE1021633B1 (en) * | 2013-03-20 | 2015-12-21 | Atlas Copco Airpower, Naamloze Vennootschap | HEAT EXCHANGER |
CN103837022A (en) * | 2013-06-19 | 2014-06-04 | 山东润银生物化工股份有限公司 | Heat exchanger |
CN106546120B (en) * | 2017-01-23 | 2019-01-01 | 上海金由氟材料股份有限公司 | A kind of interior cladding fastening seal structure of fluoroplastics pipe heat exchanger |
CN106546121B (en) * | 2017-01-23 | 2019-01-01 | 上海金由氟材料股份有限公司 | A kind of fluoroplastics coat sealing structure and encapsulating method entirely |
US10823515B2 (en) * | 2017-02-07 | 2020-11-03 | Caterpillar Inc. | Tube-to-header slip joint for air-to-air aftercooler |
DE102018001548A1 (en) | 2018-02-28 | 2019-08-29 | Sgl Carbon Se | Tube bundle heat exchanger and tube sheet and method for sealing the same |
DE102018112907A1 (en) * | 2018-05-30 | 2019-12-05 | Shengjun Feng | heat exchangers |
CN110274507A (en) * | 2019-06-18 | 2019-09-24 | 衢州佰强新材料科技有限公司 | A kind of heat exchanger that thermal stress is completely eliminated |
CN110243225B (en) * | 2019-07-17 | 2024-02-13 | 南通三圣石墨设备科技股份有限公司 | Round block hole type silicon carbide heat exchanger |
DE102019120096A1 (en) * | 2019-07-25 | 2021-01-28 | Kelvion Machine Cooling Systems Gmbh | Shell and tube heat exchanger |
CN110779358B (en) * | 2019-08-19 | 2022-04-08 | 四川奥格莱能源科技有限公司 | Loading and unloading type protection device for built-in tube type heat exchanger |
CN111678363A (en) * | 2020-07-10 | 2020-09-18 | 贵州兰鑫石墨机电设备制造有限公司 | Double-tube-plate silicon carbide heat exchanger with single-plate double-seal structure |
CN114427601B (en) * | 2020-09-16 | 2024-08-23 | 中国石油化工股份有限公司 | Sealing structure of enamel plate type preheater |
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GB273605A (en) * | 1926-02-12 | 1927-07-12 | Thornycroft John I & Co Ltd | Improvements in or relating to steam condensers |
FR650058A (en) * | 1928-02-09 | 1929-01-04 | Delas Condenseurs | Device to avoid mixing of fluids in tube bundle heat exchangers |
GB311245A (en) * | 1928-05-07 | 1930-01-02 | Egidio Torre | Improvements in surface condensers |
GB618236A (en) † | 1943-06-15 | 1949-02-18 | James Clarence Hobbs | Improvements in or relating to pressure sealing joint for pipes |
CH425850A (en) * | 1964-11-24 | 1966-12-15 | Schneider Fritz Ing Dr | Tubular heat exchanger |
DE2326365A1 (en) * | 1973-05-23 | 1974-12-19 | Qvf Glastech Gmbh | PIPE HEAT EXCHANGER WITH DOUBLE PIPE BOTTOMS |
US3923314A (en) * | 1973-12-06 | 1975-12-02 | Carborundum Co | Non-rigid seal for joining silicon carbide tubes and tube sheets in heat exchangers |
US4930568A (en) † | 1989-05-17 | 1990-06-05 | L And M Radiator, Inc. | Heat exchanger |
US5323849A (en) * | 1993-04-21 | 1994-06-28 | The United States Of America As Represented By The Secretary Of The Navy | Corrosion resistant shell and tube heat exchanger and a method of repairing the same |
US5515914A (en) * | 1994-04-29 | 1996-05-14 | Saint Gobain/Norton Industrial Ceramics Corp. | Ceramic heat exchanger design |
US5630470A (en) * | 1995-04-14 | 1997-05-20 | Sonic Environmental Systems, Inc. | Ceramic heat exchanger system |
DE19610501A1 (en) * | 1996-03-18 | 1997-09-25 | Siegfried Otte | Heat or matter exchange system with enamelled and perforated tube plate |
DE19714423C2 (en) * | 1997-04-08 | 2003-05-08 | Schnabel Gmbh & Co Kg Dr | Shell and tube heat exchangers |
-
2002
- 2002-11-19 IT IT002449A patent/ITMI20022449A1/en unknown
-
2003
- 2003-03-18 EP EP03005976.0A patent/EP1422488B2/en not_active Expired - Lifetime
- 2003-03-18 EP EP13187710.2A patent/EP2685201B1/en not_active Expired - Lifetime
- 2003-03-18 ES ES13187710T patent/ES2835223T3/en not_active Expired - Lifetime
Non-Patent Citations (1)
Title |
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None * |
Also Published As
Publication number | Publication date |
---|---|
EP1422488B2 (en) | 2017-01-25 |
ITMI20022449A1 (en) | 2004-05-20 |
EP1422488A3 (en) | 2011-12-14 |
ES2835223T3 (en) | 2021-06-22 |
EP1422488B1 (en) | 2014-02-26 |
EP2685201A2 (en) | 2014-01-15 |
EP2685201A3 (en) | 2014-02-26 |
EP1422488A2 (en) | 2004-05-26 |
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