WO1985004470A2 - Installation pour l'echange de chaleur et le transfert de matiere entre deux ou plusieurs milieux pouvant s'ecouler - Google Patents

Installation pour l'echange de chaleur et le transfert de matiere entre deux ou plusieurs milieux pouvant s'ecouler Download PDF

Info

Publication number
WO1985004470A2
WO1985004470A2 PCT/DE1985/000095 DE8500095W WO8504470A2 WO 1985004470 A2 WO1985004470 A2 WO 1985004470A2 DE 8500095 W DE8500095 W DE 8500095W WO 8504470 A2 WO8504470 A2 WO 8504470A2
Authority
WO
WIPO (PCT)
Prior art keywords
tube
supply
inlet
inner tube
lines
Prior art date
Application number
PCT/DE1985/000095
Other languages
German (de)
English (en)
Other versions
WO1985004470A3 (fr
Inventor
Josef-Hubert Schick
Original Assignee
Schick Josef Hubert
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Schick Josef Hubert filed Critical Schick Josef Hubert
Publication of WO1985004470A2 publication Critical patent/WO1985004470A2/fr
Publication of WO1985004470A3 publication Critical patent/WO1985004470A3/fr

Links

Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
    • B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
    • B01D46/2407—Filter candles
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2457—Grouping of fuel cells, e.g. stacking of fuel cells with both reactants being gaseous or vaporised
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/04—Heat
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61L—METHODS OR APPARATUS FOR STERILISING MATERIALS OR OBJECTS IN GENERAL; DISINFECTION, STERILISATION OR DEODORISATION OF AIR; CHEMICAL ASPECTS OF BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES; MATERIALS FOR BANDAGES, DRESSINGS, ABSORBENT PADS OR SURGICAL ARTICLES
    • A61L2/00—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor
    • A61L2/02—Methods or apparatus for disinfecting or sterilising materials or objects other than foodstuffs or contact lenses; Accessories therefor using physical phenomena
    • A61L2/04—Heat
    • A61L2/06—Hot gas
    • A61L2/07—Steam
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/0011—Heating features
    • B01D1/0017—Use of electrical or wave energy
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/06—Evaporators with vertical tubes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D1/00—Evaporating
    • B01D1/06—Evaporators with vertical tubes
    • B01D1/065—Evaporators with vertical tubes by film evaporating
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D11/00—Solvent extraction
    • B01D11/04—Solvent extraction of solutions which are liquid
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D19/00—Degasification of liquids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/04—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping pipe stills
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D35/00—Filtering devices having features not specifically covered by groups B01D24/00 - B01D33/00, or for applications not specifically covered by groups B01D24/00 - B01D33/00; Auxiliary devices for filtration; Filter housing constructions
    • B01D35/18—Heating or cooling the filters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/42—Auxiliary equipment or operation thereof
    • B01D46/4263—Means for active heating or cooling
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/005—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by heat treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/18—Absorbing units; Liquid distributors therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14—Ultrafiltration; Microfiltration
    • B01D61/18—Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/06—Tubular membrane modules
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
    • B01D63/08—Flat membrane modules
    • B01D63/082—Flat membrane modules comprising a stack of flat membranes
    • B01D63/084—Flat membrane modules comprising a stack of flat membranes at least one flow duct intersecting the membranes
    • B01D63/085—Flat membrane modules comprising a stack of flat membranes at least one flow duct intersecting the membranes specially adapted for two fluids in mass exchange flow
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J47/00—Ion-exchange processes in general; Apparatus therefor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/06—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds in tube reactors; the solid particles being arranged in tubes
    • B01J8/067—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/70—Assemblies comprising two or more cells
    • C25B9/73—Assemblies comprising two or more cells of the filter-press type
    • 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
    • F28D21/0015—Heat and mass exchangers, e.g. with permeable walls
    • 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
    • F28D5/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation
    • F28D5/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, using the cooling effect of natural or forced evaporation in which the evaporating medium flows in a continuous film or trickles freely over the conduits
    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/103—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of more than two coaxial conduits or modules of more than two coaxial conduits
    • 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
    • F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/10—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically
    • F28D7/106—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged one within the other, e.g. concentrically consisting of two coaxial conduits or modules of two coaxial conduits
    • 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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • 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
    • F28F9/0243—Header boxes having a circular cross-section
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2459—Comprising electrode layers with interposed electrolyte compartment with possible electrolyte supply or circulation
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/2465—Details of groupings of fuel cells
    • H01M8/2483—Details of groupings of fuel cells characterised by internal manifolds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/22—Cooling or heating elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2313/00—Details relating to membrane modules or apparatus
    • B01D2313/22—Cooling or heating elements
    • B01D2313/221—Heat exchangers
    • 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
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
    • 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
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells
    • 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
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Definitions

  • the invention relates to a device for heat and material exchange between two or more flowable media for heat exchange or for initiating a reaction between the media with an inlet and an outlet for one and an inlet and an outlet for the other Medium and at least two surrounding tubes, one of which is connected to one and the other to the other inlet and outlet.
  • Heat exchangers are known in numerous designs.
  • two tubes are arranged concentrically to one another.
  • the cooling or heating medium is passed through the annular space between the two pipes.
  • the medium with a higher pressure is passed through the inner tube.
  • the inner tube is also provided with longitudinal ribs.
  • the mutual sealing of the spaces enclosed by the two tubes requires a great deal of effort in the known heat exchangers.
  • the object of the invention is to design a heat exchanger or generally a device of the type mentioned at the outset in such a way that the spaces through which the various media are carried out can be easily sealed off from one another.
  • a device is also created by means of which the media are not only carried out separately from one another, but in which they can also react with one another.
  • the solution to this problem according to the invention results from the fact that the inner tube is passed with its two ends through the outer tube and its ends protrude beyond it, the feed and Discharges run at a substantially right angle to the pipes, a pair of supply and discharge lines are placed on the ends of the inner pipe and a pair of supply and discharge lines are placed on the ends of the outer pipe, openings at the mounting points corresponding to the pipe diameters in the supply and discharge lines are provided and the pipes are connected to the supply and discharge lines and all lead-through and connection points are closed.
  • the inner tube runs through the outer tube in this construction. It passes through the supply and discharge lines placed on the outer pipe.
  • the spaces enclosed by the two pipes only have to be sealed off from one another at these passage or passage points.
  • the invention has the further advantage that the device has a simple geometric shape and has only a small space requirement with respect to the area over which the spaces enclosed by the two tubes are in contact with one another.
  • This enables the tubes arranged in the manner according to the invention to be arranged next to one another in a manner yet to be explained with the formation of registers and to be connected to one another in a variety of ways and in series.
  • the devices can also be arranged horizontally, vertically or also in an inclined position. Surprisingly, it has been shown that the device according to the invention can be used not only for heat exchange, but also for mass transfer between two or more media.
  • Group 1 double tube heat exchanger Finned tube heat exchanger; Triple and multiple heat exchangers; Plate heat exchangers.
  • Group 2 exhaust gas coolers; Air cooler; Cross tube cooler; Würz ⁇ cooling apparatus; Capacitors; Reflux condensers.
  • Group 3 evaporators; Steep tube evaporator; Multi-stage evaporator; Falling film evaporator; Evaporators for sensitive goods; Low pressure steam generator.
  • Group 4 Apparatus for: extraction, distillation, rectification, degassing.
  • Group 7 candle filters Ultrafiltration; Packed columns; Catalytic reactors; Ion exchanger; Low-pressure contact furnaces; Deodoriser.
  • Group 8 chlorate electrolysis; Perchlorate electrolysis; Gas separation; Thermal diffusion; Foreign gas diffusion; Isotope enrichment.
  • Group 9 air separation; Desalination.
  • Group 10 fuel cells; Differential pressure electrolysis; Bio-reactors.
  • Fig. 1 shows the basic form of the invention Device with an inner and an outer tube and the feed and discharge lines connected to them,
  • FIG. 3 shows the top view of a plurality of inner and outer tubes arranged next to one another and forming a register, this register forming a block together with others,
  • FIG. 4 shows a view along the section line 4 - 4 in FIG.
  • FIG. 7 shows a representation similar to FIG. 1 of more than two tubes lying one inside the other and forming a multiple heat exchanger
  • FIG. 11 shows a view, partly in section, of an electrolysis cell
  • 12 shows a section along the section line 12-12 in FIG. 11 through three registers arranged in the manner of a filter press
  • FIG. 13 shows a partial section through a frame with a special representation of a sleeve isolating the tubes from one another
  • FIG. 15 shows a representation, partly in section, of an electrolysis cell that can be used for water electrolysis
  • FIG. 16 shows a representation of the basic embodiment according to FIG. 1, the inner and the outer tube being formed by plates.
  • FIG. 19 shows a partial view of the device according to FIG. 18 on an enlarged scale
  • 21 shows the representation, partly in section, of a plurality of tubes lying one inside the other for use as a catalytic reactor and
  • FIG. 22 shows the representation of tubes lying one inside the other when used as a bioreactor.
  • 1 shows the principle of the device with the inner tube 30 and the outer tube 32 concentrically surrounding it.
  • the inner tube 30 projects beyond the outer tube 32. With its two ends, it is connected to supply or discharge lines 34.
  • the two ends of the outer tube 32 are connected to supply or discharge lines 36.
  • These supply and discharge lines 34 and 36 generally run at 90 ° to the inner and outer tubes 30 and 32. However, they can also include other angles with them.
  • the supply and discharge lines 36 are placed on the outer tube 32 at points 38. These attachment points 38 must be sealed. In general, it is sufficient to weld the supply and discharge lines 36 onto the ends of the outer tube 32.
  • the inner tube 30 is passed through openings 40 in the feed and discharge lines 36. These implementation points must also be sealed. Here too, weld seams are generally sufficient. 1 shows that the basic shape of the device is geometrically simple and even rotationally symmetrical and takes up little space. This enables the assembly
  • Fig. 2 shows different configurations of the two tubes, particularly when used in a heat exchanger.
  • the two tubes 30 and 32 are solid or impermeable.
  • Fig. 2 also shows an embodiment in which the inner tube 30 is porous. Such a tube is used for mass transfer, in carrying out reactions, for electrolysis and the like.
  • 2 further shows the arrangement of longitudinal ribs 42 on the inner tube 30. This improves the heat transfer.
  • FIG. 2 further shows the arrangement of spiral ribs 44 on the outer tube 32. Via these ribs 44, the entire device can be cooled with air supplied in cross flow if it is used for exothermic reactions.
  • the inner tube 30 additionally has longitudinal ribs 42. 2 further shows an embodiment.
  • the medium to be cooled can optionally be passed through the inner tube 30 or through the outer tube 32.
  • a cooling medium can additionally be introduced into the inner tube 30 or the intermediate space between the inner tube 30 and the outer tube 32. If several devices according to FIG. 1 are connected in series, cooling can also be carried out in countercurrent.
  • the medium to be cooled is first passed through the inner tube 30 and then through the annular space between the two tubes or vice versa. This is recommended if the medium to be cooled should only be cooled slowly for chemical or procedural reasons. The same applies if the medium is to be heated up slowly.
  • FIG. 1 The embodiment shown in FIG.
  • the medium to be filtered is introduced either through the inner or through the outer tube.
  • the outer tube 32 can be additionally heated or cooled.
  • the device then acts both as a filter and at the same time as a heat exchanger. It should also be mentioned that the two media can flow through the two tubes 30 and 32 both in the same direction and in the opposite direction. If the two tubes are arranged in a housing, a third medium can also participate in the heat exchange. This can be initiated in cocurrent, countercurrent or crossflow.
  • FIG. 3 shows a register composed of several embodiments according to FIG. 1.
  • a plurality of inner and outer pipes 30 and 32 are jointly connected to supply and discharge lines 34 and 36. These lead to collecting lines 46 and 48. These run perpendicular to the plane of the drawing.
  • a plurality of registers of the type shown in FIG. 3 can be arranged in series and on the same bus lines 46 and 48 be connected. This will be explained in the following.
  • Fig. 5 shows such a block.
  • Several registers are arranged next to each other and connected together to collecting lines 46 and 48. This results in blocks of any size. These can be arranged lying in two axes and standing in one axis. 6 shows the series connection of several registers.
  • FIG. 7 shows an embodiment with more than two tubes arranged concentrically around one another.
  • a further tube 52 with an additional feed and discharge line 54 is additionally arranged in the inner tube 30.
  • the outer tube 32 is surrounded by an additional further tube 52 with an additional further inlet and outlet 54.
  • This heat exchanger is also used for slow heating or cooling of sensitive media.
  • the supply and discharge lines 34, 36 and 54 are interconnected outside the register in such a way that the media flow through the pipes or registers either in cocurrent or in countercurrent.
  • the registers can also be interconnected so that the spaces between the individual tubes are flowed through from the inside to the outside or vice versa.
  • the inner tube 30 is a bit into the inlet and outlet 34. Strictly speaking, it is up to the level of the medium to be evaporated.
  • the upper end of the inner tube 30 can be equipped with liquid distributors.
  • the supplied to be evaporated and in the lower part of the inlet and outlet 34 medium passes over the upper edge of 'the inner tube 30 via and on the inside wall of down. This creates a falling film.
  • This can be heated by a heating medium passed through the outer tube 32.
  • the vapors collect in the upper part of the feed and discharge line 34. They can be fed to a register that works as a capacitor.
  • Fig. 9 shows a falling film evaporator with cooling.
  • a further additional tube 52 is passed through the inner tube 30. Its upper end opens into an inlet and outlet 54.
  • a heating medium can be passed through the outer tube 32.
  • a cooling medium is passed through the further tube 52. This allows a mixture of substances to be evaporated. Components with a higher boiling point are condensed in the vapor space 56 of the inner tube 30 and run back down the outer wall of the further tube 52.
  • This falling film evaporator with cooling enables various options for carrying out certain chemical reactions, evaporation or distillation processes *.
  • Fig. 10 shows an evaporator with return.
  • a heating medium is passed through the further tube 52.
  • the medium to be evaporated is fed through the inner tube 30. This has openings 58. So that the thick liquor overflows into the outer tube 32.
  • the vapors collect in the supply and discharge lines 36 and can be withdrawn from the side of the registers or fed to another register working as a capacitor.
  • 11 shows an embodiment working as an electrolysis cell.
  • the registers already described are cast in the form of a frame in the manner of filter press frames with plastic or inserted into a plastic frame 60.
  • the supply and discharge lines 34 and 36 are molded into this frame 60, and the electrolyte is supplied and discharged via these.
  • the inner and outer tubes 30 and 32 act as cathode and anode.
  • Either the outer walls of the inner tubes 30 or the inner walls of the outer tubes 32 can be coated with a catalyst, and a coolant is fed in via the manifolds 46.
  • the electrolyte is supplied via the collecting lines 48.
  • the electrodes are shown at 62 and 64.
  • Fig. 12 shows a section through three frames arranged like a filter press. The individual frames or registers are separated from one another by end walls 66. This results in a series connection of the individual registers. Without the end walls 66, the individual registers or electrolysis cells are connected in parallel. This circuit only affects electrolyte and coolant circuits. Alternatively, the electrolyte can be introduced in series and the coolant can be introduced in parallel or vice versa. This type of circuit is important for electrolysis processes in which a product is enriched.
  • a sleeve 68 consisting of an insulating material encloses the inner tube. 30. It insulates it from the inlet and outlet line 36 and the outer tube 32.
  • the inlet and outlet lines 34 and 36 are enclosed in a plastic frame 70.
  • the inner and outer tubes 30 and 32 are porous over part of their length.
  • Inner tube 30 forms the anode and outer tube 32 the cathode, via the space surrounding the outer tubes 32, oxygen or air is supplied.
  • the electrolyte is supplied via the feed or discharge line 36.
  • the fuel is introduced into the inner tubes 30 and flows out via the inlet or outlet line 34 shown.
  • the tubes 30 and 32 are insulated from one another via the sleeves 68.
  • the voltage is tapped off at electrodes 62 and 64. They are directly connected to the feed and discharge lines 34 and 36.
  • FIG. 15 shows a further embodiment of an electrolysis cell.
  • this is used for water electrolysis.
  • the two tubes 30 and 32 form the electrodes, and one is made of a porous material.
  • a jacket 74 projecting downward is fastened to the cuff 68. It dips into the electrolyte and prevents the electrolysis gases from mixing.
  • the inner tube 30 forms the anode and the outer tube 32 the cathode.
  • the electrolyte is introduced into the space between the two tubes 30 and 32 from below. It collects in the line 36 shown. Catholyte and hydrogen are separated outside the electrolysis cell.
  • a lower pressure is maintained in the inner tube 30 than in the outer tube 32. The pressure difference should be above the pressure loss created by the inner tube 30.
  • the oxygen produced at the anode can pass through the porous inner tube 30 and be discharged via the drawn-in line 34.
  • the anolyte can pass through the porous inner tube 30 and flow downwards.
  • the jacket 74 is immersed in the electrolyte and prevents the gases generated during the electrolysis from mixing.
  • FIG. 16 shows a modification of the basic form of the invention shown in FIG. 1.
  • the two pipes 30 and 32 no longer have a circular cross section, but are instead made of plates 76 and 78 formed. When used as a heat exchanger, this results in larger heat transfer areas.
  • FIG. 17 shows an embodiment in which several registers are connected in series with simple means.
  • any number of inner and outer “tubes are first arranged side by side and on their inflow and Ab ⁇ lines 34 and 36 connected together. This creates a single large register.
  • the supply line 34 for the inner tubes 30, which is at the bottom in FIG. 17, is now interrupted at one point.
  • the derivation 36 at the top in FIG. 17 for the outer tubes 32 is interrupted. The result of this is that the individual registers are placed in series and the media involved in the heat exchange flow through them in countercurrent. This is indicated by the arrows.
  • FIGS. 18 and 19 show an embodiment which is used as a reactor for carrying out chemical processes.
  • the inner tube 30 is filled with a fixed bed catalyst 82. This is held by a perforated support 80, which is arranged in the lower inlet and outlet 34.
  • the inner tube 30 can also be filled with an ion exchanger or packing.
  • the device can thus take over the functions of a reactor for catalytic processes, the function of an ion exchanger or a packed column. It is left to the respective reaction up to which height the inner tube 30 is filled.
  • a heating or cooling medium can be passed through the outer tube 32 to support the reactions.
  • the outer tube 32 can, as indicated in FIG. 18, enclose the inner tube only over a part of its length.
  • the filling mass 82 of the inner tube 30 is held by the support 80.
  • the filling compound 82 is entered through an opening in the upper inlet and outlet 34 and can through an opening in the lower feed and discharge line 34 can be taken out according to consumption. With a suitable connection of the supply and discharge lines 34, the filling compound 82 can be backwashed.
  • the inner tube 30 is porous and forms a candle filter. It is interchangeable and accessible from the outside.
  • the inner tube 30 is connected to the upper side of the lower inlet and outlet line 34 via a flange 84. It is completely passed through the upper inlet and outlet line 34, and is connected to the outside world via a flange 86.
  • the medium to be filtered is introduced into the lower inlet and outlet line 34, it flows through the flange 84 into the interior of the inner tube 30.
  • the medium to be filtered is introduced into the upper inlet and outlet line 34, it flows into the outer tube 32 and then passes through the porous inner tube 30 from the outside inwards. This results in filtration from the inside out or vice versa.
  • a cooling or heating medium can be passed through the further pipe 52. Heating is used for substances whose viscosity decreases with increasing temperature. Filtration is thereby facilitated.
  • the device thus acts simultaneously as a filter and heat exchanger. With a suitable connection of the supply and discharge lines 34, the filter, that is to say the porous inner tube 30, can be backwashed. When the porous inner tube 30 is replaced by a membrane placed on a support tube, the device can also be used for ultrafiltration.
  • the inner tube 30 is filled with catalyst mass 82. This is held by the support 80.
  • a liquid reactant is entered from above through the upper inlet and outlet 34.
  • a gaseous reactant is introduced into the lower inlet and outlet line 34 via a nozzle 88.
  • a cooling or heating medium is passed through tube 32.
  • the length and the diameter of the inner and outer tubes 30 and 32 depend on the reaction. The number of pipes connected to a register also depends on this.
  • the inner tubes 30 do not end in a lower inlet and outlet, but are bent in a hairpin shape to form arches 90 and are passed through the lower inlet and outlet 36 of the outer tubes 32.
  • Nozzles 88 are arranged in the ascending branches of the arches 90.
  • the medium to be gassed is introduced through the upper inlet and outlet 34 of the inner tubes 30. It flows down in the direction of the arrow.
  • the gas introduced through the nozzles 88 gives it buoyancy and flows upwards in the direction of the arrow.
  • Air, oxygen or another gaseous reactant for example, is introduced through the nozzles 88.
  • Several of the tubes shown in FIG. 22 can be combined to form a register. Such an arrangement allows continuous process control. A highly concentrated product can then be removed at the end of a register.
  • a cooling or heating medium is passed through the outer tubes 32.
  • a cooling medium is passed through in exothermic processes. In the case of endothermic processes or in the oxidation of substances which have a high viscosity at normal temperature and a viscosity which decreases with increasing temperature, a heating medium is passed through the outer tubes 32.
  • This embodiment finds particular application in the synthetic production of fatty acids, for example for the continuous oxidation of paraffins.
  • the first register can be affected by excessive temperatures (temperature shock) initiate the reaction.
  • the further registers can then be operated at lower temperatures.
  • the system can also be used for halogenating substances. It can also be used for continuous deodorization, for example of fats and oils,

Abstract

Dans son mode de réalisation de base, l'installation se compose de deux ou plusieurs tuyaux (30, 32) s'entourant concentriquement, les tuyaux intérieurs traversent les tuyaux extérieurs et dépassent ceux-ci par leurs extrémités. Les extrémités sont raccordées a des tuyaux formant des conduites d'alimentation et d'évacuation (34, 36). Plusieurs groupes de tuyaux s'entourant concentriquement peuvent être disposés les uns à côté des autres. De tels groupes de tuyaux peuvent être élargis pour former des registres. Il est possible de réaliser de nombreux types de réactions chimiques en rendant quelques tuyaux poreux, en remplissant les tuyaux de catalyseurs, etc.
PCT/DE1985/000095 1984-03-27 1985-03-26 Installation pour l'echange de chaleur et le transfert de matiere entre deux ou plusieurs milieux pouvant s'ecouler WO1985004470A2 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
DEP3411675.3 1984-03-27
DE8409717U DE8409717U1 (fr) 1984-03-27 1984-03-27
DE19843411675 DE3411675A1 (de) 1984-03-27 1984-03-27 Vorrichtung zum waerme- und stoffaustausch zwischen zwei oder mehr stroemungsfaehigen medien

Publications (2)

Publication Number Publication Date
WO1985004470A2 true WO1985004470A2 (fr) 1985-10-10
WO1985004470A3 WO1985004470A3 (fr) 1985-12-05

Family

ID=25819834

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/DE1985/000095 WO1985004470A2 (fr) 1984-03-27 1985-03-26 Installation pour l'echange de chaleur et le transfert de matiere entre deux ou plusieurs milieux pouvant s'ecouler

Country Status (5)

Country Link
EP (1) EP0177519A1 (fr)
JP (1) JPS61501523A (fr)
AU (1) AU4213785A (fr)
DE (2) DE8409717U1 (fr)
WO (1) WO1985004470A2 (fr)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0513230A1 (fr) * 1990-01-31 1992-11-19 Chen-Yen Cheng Panneau de transfert thermique prefabrique a double plaque renfermee et ses utilisations
EP0608439A1 (fr) * 1988-01-28 1994-08-03 Modine Manufacturing Company Evaporateur avec collection du condensat
WO1998008042A1 (fr) * 1996-08-19 1998-02-26 Chmelik Vaclav Echangeur thermique a tubes
WO2006097906A1 (fr) * 2005-03-17 2006-09-21 Sasol Technology (Proprietary) Limited Production de produits liquides et eventuellement gazeux a partir de reactifs gazeux
EP1736216A2 (fr) * 2005-06-17 2006-12-27 Basf Aktiengesellschaft Procédé et appareil pour vaporiser des matières sensibles à la chaleur
FR2941629A1 (fr) * 2009-02-04 2010-08-06 Roland Laruelle Dispositif de distillation avec recuperation de chaleur
CN108067164A (zh) * 2016-11-17 2018-05-25 中国石油化工股份有限公司 一种加氢反应器及加氢工艺
US11142467B2 (en) 2016-08-31 2021-10-12 VMACTEK Pty Ltd Evaporator

Families Citing this family (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2614686A1 (fr) * 1987-04-28 1988-11-04 Puicervert Luc Echangeur
JP3036835B2 (ja) * 1989-08-18 2000-04-24 イーブイアイ コーポレイション カテーテルアテロトーム
US5282484A (en) * 1989-08-18 1994-02-01 Endovascular Instruments, Inc. Method for performing a partial atherectomy
US5211651A (en) 1989-08-18 1993-05-18 Evi Corporation Catheter atherotome
US5178625A (en) * 1989-12-07 1993-01-12 Evi Corporation Catheter atherotome
US5160342A (en) 1990-08-16 1992-11-03 Evi Corp. Endovascular filter and method for use thereof
US5643297A (en) 1992-11-09 1997-07-01 Endovascular Instruments, Inc. Intra-artery obstruction clearing apparatus and methods
US5571122A (en) 1992-11-09 1996-11-05 Endovascular Instruments, Inc. Unitary removal of plaque
DE19957641C1 (de) 1999-11-30 2001-06-13 Membraflow Gmbh & Co Kg Filter Filtermembranmodul mit integriertem Wärmetauscher
DE102005001952A1 (de) * 2005-01-14 2006-07-27 Man Dwe Gmbh Rohrbündelreaktor zur Durchführung exothermer oder endothermer Gasphasenreaktionen
DE102007036066A1 (de) * 2007-08-01 2009-02-05 Georg Albersinger Verdampfer
JP5670672B2 (ja) * 2010-09-03 2015-02-18 シーアイ化成株式会社 熱交換器
DE102011078345A1 (de) * 2011-06-29 2013-01-03 Krones Aktiengesellschaft Sterilisation von Membranfiltern
US20140083666A1 (en) * 2012-09-27 2014-03-27 Tai-Her Yang Tri-Piece Thermal Energy Body Heat Exchanger Having Multi-Layer Pipeline and Transferring Heat to Exterior Through Outer Periphery of Pipeline
DE202013009357U1 (de) * 2013-06-27 2015-01-16 Dana Canada Corporation Integrierte Gasmanagementvorrichtung für ein Brennstoffzellensystem
CN107973763A (zh) * 2017-12-08 2018-05-01 河南心连心化肥有限公司 一种制备2-甲基呋喃的生产装置及方法
ES2785775B2 (es) * 2019-04-03 2021-03-26 H Inven Grup Xxi S L Dispositivo para electrolisis de agua electrolitica sumergido
DE102020007211A1 (de) 2019-12-17 2021-06-17 Silica Verfahrenstechnik Gmbh Adsorptionskältevorrichtung und Verfahren zum Erzeugen von Adsorptionskälte aus Wärme

Citations (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE38333C (de) * f. C. garbutt in Los Angeles, California, V. St. A Anordnung von Umlaufröhren bei Heizröhren-Dampfkesseln
BE430199A (fr) *
BE373876A (fr) *
GB279526A (en) * 1926-04-30 1927-10-31 Synthetic Ammonia & Nitrates Process for the utilisation of liquids for effecting transfer of energy or matter or like purposes
FR629047A (fr) * 1926-03-30 1927-11-03 Perfectionnements aux échangeurs de chaleur
US2042922A (en) * 1933-08-04 1936-06-02 Calco Chemical Co Inc Process and apparatus for vapor phase catalyses
FR979450A (fr) * 1942-04-20 1951-04-26 échangeur de chaleur
US2643863A (en) * 1948-09-09 1953-06-30 Hydrocarbon Research Inc Recuperative heat exchanger and process of producing same
US2925319A (en) * 1953-01-21 1960-02-16 Herbert P A Groll Process and apparatus for cooling exothermic reactions
FR1335975A (fr) * 1962-10-12 1963-08-23 Distillateur rapide
FR1341536A (fr) * 1962-08-02 1963-11-02 Paul Duclos S A Ets Perfectionnements aux installations ou appareils frigorifiques
US3162516A (en) * 1961-08-14 1964-12-22 Richard E Dwyer Method of filtering exhaust gases
FR1422447A (fr) * 1960-05-03 1965-12-24 Allied Breweries Uk Ltd Procédé et installation de fermentation en continu
FR1505393A (fr) * 1966-06-30 1967-12-15 échangeur de chaleur
FR1515860A (fr) * 1966-05-25 1968-03-08 Rhone Poulenc Sa Appareil de contact gaz-liquide
FR2091935A1 (en) * 1970-05-19 1971-01-21 Trepaud Georges Double tube heat exchanger - with double headers at both ends
DE1955346A1 (de) * 1969-11-04 1971-05-27 Siegener Ag Geisweid Doppelrohrregister fuer Waermeaustauscher
US3608730A (en) * 1969-10-02 1971-09-28 Selas Corp Of America Desalination apparatus
US3672953A (en) * 1970-02-09 1972-06-27 Mobil Oil Corp Process for growing cells of a microorganism on a carbon-containing liquid substrate
US3705622A (en) * 1970-07-07 1972-12-12 Dunham Bush Inc Cleanable tube within a tube heat exchanger and method of forming modular headers therefor
DE2614336A1 (de) * 1975-04-04 1976-10-21 Millipore Corp Rohrfoermiges filterelement und verfahren zu seiner herstellung
FR2308052A1 (fr) * 1975-04-18 1976-11-12 Commissariat Energie Atomique Echangeur de chaleur a tubes plongeurs
DE2644609A1 (de) * 1976-10-02 1978-04-06 Phillips Petroleum Co Verfahren und vorrichtung zum durchfuehren einer gaerung
GB2081114A (en) * 1980-07-11 1982-02-17 Bertrams Ag Improvements in or relating to methods of and apparatus for concentrating alkali solutions
DE3036935A1 (de) * 1980-09-30 1982-05-13 Klaus Esser Gmbh & Co Kg, 4040 Neuss Waermetauscher fuer ein waermetraegermedium
US4400277A (en) * 1981-06-25 1983-08-23 Filtertek, Inc. Low-profile inline filter

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US827479A (en) * 1905-12-26 1906-07-31 Harry W Hand Condenser.
FR488221A (fr) * 1917-03-31 1918-09-14 Societe E Barbet Et Fils & Cie Perfectionnements apportés aux appareils tubulaires d'évaporation ou de condensation-réfrigération permettant d'augmenter leur puissance
DE692836C (de) * 1938-04-24 1940-06-27 Fried Krupp Germaniawerft Akt r katalytischer Gasreaktionen
US2633338A (en) * 1947-02-19 1953-03-31 Continental Aviat & Engineerin Heat exchanger
CH449678A (de) * 1967-06-20 1968-01-15 Bertrams Ag Hch Röhrenwärmeaustauscher mit flüssigem Wärmeträger
JPS58136985A (ja) * 1982-02-08 1983-08-15 Mitsubishi Electric Corp 熱交換器

Patent Citations (26)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE38333C (de) * f. C. garbutt in Los Angeles, California, V. St. A Anordnung von Umlaufröhren bei Heizröhren-Dampfkesseln
BE430199A (fr) *
BE373876A (fr) *
FR629047A (fr) * 1926-03-30 1927-11-03 Perfectionnements aux échangeurs de chaleur
GB279526A (en) * 1926-04-30 1927-10-31 Synthetic Ammonia & Nitrates Process for the utilisation of liquids for effecting transfer of energy or matter or like purposes
US2042922A (en) * 1933-08-04 1936-06-02 Calco Chemical Co Inc Process and apparatus for vapor phase catalyses
FR979450A (fr) * 1942-04-20 1951-04-26 échangeur de chaleur
US2643863A (en) * 1948-09-09 1953-06-30 Hydrocarbon Research Inc Recuperative heat exchanger and process of producing same
US2925319A (en) * 1953-01-21 1960-02-16 Herbert P A Groll Process and apparatus for cooling exothermic reactions
FR1422447A (fr) * 1960-05-03 1965-12-24 Allied Breweries Uk Ltd Procédé et installation de fermentation en continu
US3162516A (en) * 1961-08-14 1964-12-22 Richard E Dwyer Method of filtering exhaust gases
FR1341536A (fr) * 1962-08-02 1963-11-02 Paul Duclos S A Ets Perfectionnements aux installations ou appareils frigorifiques
FR1335975A (fr) * 1962-10-12 1963-08-23 Distillateur rapide
FR1515860A (fr) * 1966-05-25 1968-03-08 Rhone Poulenc Sa Appareil de contact gaz-liquide
FR1505393A (fr) * 1966-06-30 1967-12-15 échangeur de chaleur
US3608730A (en) * 1969-10-02 1971-09-28 Selas Corp Of America Desalination apparatus
DE1955346A1 (de) * 1969-11-04 1971-05-27 Siegener Ag Geisweid Doppelrohrregister fuer Waermeaustauscher
US3672953A (en) * 1970-02-09 1972-06-27 Mobil Oil Corp Process for growing cells of a microorganism on a carbon-containing liquid substrate
FR2091935A1 (en) * 1970-05-19 1971-01-21 Trepaud Georges Double tube heat exchanger - with double headers at both ends
US3705622A (en) * 1970-07-07 1972-12-12 Dunham Bush Inc Cleanable tube within a tube heat exchanger and method of forming modular headers therefor
DE2614336A1 (de) * 1975-04-04 1976-10-21 Millipore Corp Rohrfoermiges filterelement und verfahren zu seiner herstellung
FR2308052A1 (fr) * 1975-04-18 1976-11-12 Commissariat Energie Atomique Echangeur de chaleur a tubes plongeurs
DE2644609A1 (de) * 1976-10-02 1978-04-06 Phillips Petroleum Co Verfahren und vorrichtung zum durchfuehren einer gaerung
GB2081114A (en) * 1980-07-11 1982-02-17 Bertrams Ag Improvements in or relating to methods of and apparatus for concentrating alkali solutions
DE3036935A1 (de) * 1980-09-30 1982-05-13 Klaus Esser Gmbh & Co Kg, 4040 Neuss Waermetauscher fuer ein waermetraegermedium
US4400277A (en) * 1981-06-25 1983-08-23 Filtertek, Inc. Low-profile inline filter

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
PATENTS ABSTRACTS OF JAPAN, Band 7, Nr. 254, 11 November 1983, (M-255)(1399), & JP - A - 58 136 985 (MITSUBISHI DENKI K.K.) 15 August 1983 *

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0608439A1 (fr) * 1988-01-28 1994-08-03 Modine Manufacturing Company Evaporateur avec collection du condensat
EP0513230A1 (fr) * 1990-01-31 1992-11-19 Chen-Yen Cheng Panneau de transfert thermique prefabrique a double plaque renfermee et ses utilisations
EP0513230A4 (en) * 1990-01-31 1993-02-10 Chen-Yen Cheng Prefabricated enclosed double plate heat transfer panel and its use
WO1998008042A1 (fr) * 1996-08-19 1998-02-26 Chmelik Vaclav Echangeur thermique a tubes
GB2438814A (en) * 2005-03-17 2007-12-05 Sasol Technology Production of liquid and, optionally gaseous products form gaseous reactants
WO2006097906A1 (fr) * 2005-03-17 2006-09-21 Sasol Technology (Proprietary) Limited Production de produits liquides et eventuellement gazeux a partir de reactifs gazeux
GB2438814B (en) * 2005-03-17 2009-01-07 Sasol Technology Production of liquid and, optionally gaseous products form gaseous reactants
EP1736216A2 (fr) * 2005-06-17 2006-12-27 Basf Aktiengesellschaft Procédé et appareil pour vaporiser des matières sensibles à la chaleur
EP1736216A3 (fr) * 2005-06-17 2008-06-25 Basf Se Procédé et appareil pour vaporiser des matières sensibles à la chaleur
FR2941629A1 (fr) * 2009-02-04 2010-08-06 Roland Laruelle Dispositif de distillation avec recuperation de chaleur
WO2010089478A1 (fr) * 2009-02-04 2010-08-12 Roland Laruelle Dispositif de distillation avec récupération de chaleur au moyen de tubes concentriques
US11142467B2 (en) 2016-08-31 2021-10-12 VMACTEK Pty Ltd Evaporator
CN108067164A (zh) * 2016-11-17 2018-05-25 中国石油化工股份有限公司 一种加氢反应器及加氢工艺
CN108067164B (zh) * 2016-11-17 2020-12-08 中国石油化工股份有限公司 一种加氢反应器及加氢工艺

Also Published As

Publication number Publication date
AU4213785A (en) 1985-11-01
DE3411675A1 (de) 1985-10-10
JPS61501523A (ja) 1986-07-24
WO1985004470A3 (fr) 1985-12-05
EP0177519A1 (fr) 1986-04-16
DE8409717U1 (fr) 1986-11-20

Similar Documents

Publication Publication Date Title
WO1985004470A2 (fr) Installation pour l'echange de chaleur et le transfert de matiere entre deux ou plusieurs milieux pouvant s'ecouler
DE3334775C2 (fr)
EP2427263B1 (fr) Système d'écoulement modulaire
DE3229286C2 (fr)
DE60310876T2 (de) Getauchter verdampfer mit integriertem wärmeaustauscher
EP2780093B1 (fr) Plateau pour une colonne de transfert de masse
WO2006053727A9 (fr) Dispositif pour realiser une reaction chimique
EP0131270A1 (fr) Absorbeur utilisant une matière solide pour un cycle d'absorption
EP3585509B1 (fr) Échangeur de chaleur et réacteur
DE102005039299A1 (de) Kondensator-Separator und Verfahren zum Separieren
DE19947803A1 (de) Reaktor mit Wärmeübertragerstruktur
DE1941005A1 (de) Dampferzeuger,insbesondere fuer einen Betrieb mit fluessigem Metall oder geschmolzenen Salzen als Heizmedium
EP0329747A1 (fr) Dispositif pour deshydrater des hydrures liquides
DE60102135T2 (de) Elektrochemischer Reaktor
EP2379978B1 (fr) Distributeur de fluides a symetrie de rotation
DE60313250T2 (de) Wärmeintegrierte Destillationskolonne
DE3026954A1 (de) Waerme- und stoff-austauschapparat
WO2000015550A1 (fr) Procede permettant de conduire des reactions gaz-liquide et reacteur a ecoulement correspondant
EP0484534A1 (fr) Appareil de traitement catalytique dans un lit fluidise
DE2534032B2 (de) Hochfrequenzozonisator
DE60019328T2 (de) Verdampfer-kondensator und luftzerlegungsanlage
DE60106212T2 (de) Chemischer reaktor mit wärmetauscher
DE202016104687U1 (de) Kondensator
EP3894062A1 (fr) Cascade de réacteurs et procédé pour faire fonctionner une cascade de réacteurs
DD269792A5 (de) Katalytischer reaktor

Legal Events

Date Code Title Description
AK Designated states

Designated state(s): AU BR DK FI JP NO SU US

AL Designated countries for regional patents

Designated state(s): AT BE CH DE FR GB LU NL SE

WWE Wipo information: entry into national phase

Ref document number: 1985901371

Country of ref document: EP

AK Designated states

Designated state(s): AU BR DK FI JP NO SU US

AL Designated countries for regional patents

Designated state(s): AT BE CH DE FR GB LU NL SE

WWW Wipo information: withdrawn in national office

Ref document number: 1985901371

Country of ref document: EP

WWP Wipo information: published in national office

Ref document number: 1985901371

Country of ref document: EP