EP0463041A1 - Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung. - Google Patents
Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung.Info
- Publication number
- EP0463041A1 EP0463041A1 EP90904824A EP90904824A EP0463041A1 EP 0463041 A1 EP0463041 A1 EP 0463041A1 EP 90904824 A EP90904824 A EP 90904824A EP 90904824 A EP90904824 A EP 90904824A EP 0463041 A1 EP0463041 A1 EP 0463041A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- liquid
- gas
- gas mixture
- designed
- reaction product
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
- B01F25/102—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components wherein the vortex is created by two or more jets introduced tangentially in separate mixing chambers or consecutively in the same mixing chamber
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/10—Mixing by creating a vortex flow, e.g. by tangential introduction of flow components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
- B01F25/51—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle in which the mixture is circulated through a set of tubes, e.g. with gradual introduction of a component into the circulating flow
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
- B01F2025/91—Direction of flow or arrangement of feed and discharge openings
- B01F2025/919—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings
- B01F2025/9191—Direction of flow or arrangement of feed and discharge openings characterised by the disposition of the feed and discharge openings characterised by the arrangement of the feed openings for one or more flows, e.g. for the mainflow and the flow of an additional component
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
- B01F23/20—Mixing gases with liquids
- B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
Definitions
- the invention relates to the use of a reaction product consisting of a gas and a liquid, the gas being present under normal conditions in an activated form and in an amount which is at least 30% above the saturation amount corresponding to the normal conditions for the solution of the gas in the Liquid, and which contains at least water and oxygen; further a method for producing such a reaction product according to the preamble of claims 2 to 4; and a device for carrying out the method according to the preamble of claim 7 and claim 12.
- reaction product in particular from gas and water
- EP-A1-0314015 Such a reaction product, in particular from gas and water, is known from EP-A1-0314015. This document describes that this reaction product of oxygen and water has been shown to be successful in the treatment of Candida albicans and Congelatio cutis. When this reaction product was taken orally, a significant reduction in the - previously increased - blood alcohol content was found. The uses described for therapeutic treatment purposes are, however, only a small part of a much broader field of application.
- the reaction product of oxygen and water is suitable for the production of medicaments for the therapeutic and / or prophylactic treatment of a wide variety of pathological changes.
- the effectiveness of loosely ionizing radiation is two to three times greater with good oxygen supply to the tissue than with complete anoxia. This oxygen effect depends exclusively on the oxygen conditions at the time of the irradiation. Supportive oral application of the water-oxygen reaction product shows a satisfactory effectiveness of the radiation.
- the therapeutically effective water-oxygen reaction product in which the oxygen becomes active beyond the reactivity achieved in dissolved form, remains without special measures, such as e.g. Storage under elevated pressure or temperature, stable for a long time, and the half-life is at least one month, usually even a year.
- a helical flow can be maintained in a reaction vessel if the feed is introduced tangentially into the reaction space at one or more points.
- Such devices are also known as cyclones or centrifugal separators; they serve to separate solid substances from gases or from liquids.
- DE-C-967943 uses this flow phenomenon for intensive mixing of the reaction participants when carrying out endothermic, chemical reactions.
- a similar device is known as a Hilsch tube, in which, when gases are blown in, a vortex which is cold on the inside and warm on the outside is produced about the tube axis. All of these methods are not suitable for introducing gas into liquid in the form and amount desired for the use according to the invention.
- EP-A1-0314015 describes a method in which a gas is "bound" in water, and in particular above the saturation value under the corresponding normal conditions.
- the gas is introduced into the water via a vortex thread.
- a container is provided, hereinafter referred to as the perturbator, which is connected in a closed circuit via hose lines to a reaction chamber, hereinafter referred to as converter, a liquid-demanding pump being provided in this circuit.
- the method according to the invention uses the known, vortex-generating mode of operation of a cyclone, combined with additional process steps including a smooth flow path and, as a result of an uninterrupted, expanded, preferably repeated, cycle, the effect potentiated, as in the characterizing features of claim 2 or claims 3 or 4.
- Advantageous developments of the method are described in the features of claims 5 and 6.
- the reaction chamber or the converter of EP-A1-0314015 is only suitable to a very limited extent, due to the shape described, to ensure a uniform, rotating flow movement.
- the channels leading into the interior of the converter do allow an approximately tangential inflow direction.
- the channels should on the one hand be additionally inclined against the closed apex of the converter interior and on the other hand their mouth openings on the inside should still be below the largest diameter of the converter interior if possible (seen in relation to the flow direction).
- 5a to c show schematic arrangement variants for carrying out the method according to the invention.
- the special measures consist in introducing a gas into a liquid in a multi-part device, preferably consisting of three, partly cyclone-like devices, which are referred to as perturbators 1, spinners 2 and converters 3, these intermixings being continuously circulated over several Hours, preferably at least 36 hours (Fig.1).
- Perturbator 1, spinner 2 and converter 3 are connected by means of hose lines 6 to form a closed circuit.
- the perturbator 1 consists of an approximately pear-shaped container 7 with a volume of e.g. 20 liters. Its spatial shape can be composed of a hollow spherical cap with a diameter of approx. 40 cm and a cone or (Fig. 2) a hyperboloid, which is created by the rotation of a hyperbola 29 around the axis of symmetry 24 of the container 7. If this spatial shape also proves to be particularly suitable for the course of the process, good process results are achieved, in particular even if the rotary body is designed differently but always in a funnel shape (e.g. dashed lines).
- the tube extension 21 is preferably inserted obliquely into the wall of the perturbator 1, in such a way that its axis 36 points obliquely from bottom to top, by approximately 15 ° against the equatorial plane BB of the perturbator 1 - preferably below it mouth - is inclined and encloses an angle of approximately 45 ° with the plane passing through the axis of rotation 24 and the pipe hub center 30.
- the container 7 is filled with a liquid up to a filling height 9, specifically via a filling opening 10 with an inner diameter of approximately 30 mm, which sits gas-tight on the top of the container 7 and can be shut off in the operating state (see also FIG. 4).
- a gas inlet 12 with a clear width of 8 mm, which can be shut off by means of a valve 8, and a connection 13 for measuring devices (not shown).
- a gas space 14 into which gas, for example pure oxygen, has been introduced via the gas inlet 12.
- the perturbator 1 is connected via a hose line 6b, any intermediate units 4 and a hose line 6c to the spinner 2, which is designed as a cyclone-like mixing device for the liquid-gas mixture. It serves as an auxiliary unit between the perturbator 1 and the converter 3 and is still in front of the pump 5.
- the spatial shape of the spinner 2 corresponds to a hollow egg which is drawn out too funnel-shaped and opens into the hose line 6d to the pump 5 via an outflow opening 18 .
- the supplying hose line 6c opens into the spinner 2 via a tube part 16, the axis 37 of which is inclined from bottom to top at an angle of approximately 10 ° to the equatorial plane FF of the spinner 2, possibly opening above it, and at an angle of about 45 ° against a plane determined by the axis of symmetry 17 of the spinner 2 and the center of the inlet opening 31.
- the spinner 2 has at its equatorial plane FF a diameter which is at least twice the diameter of the supplying hose line 6c.
- the outflow opening 18 of the spinner 2 is connected via a hose 6d to a preferably magnetically coupled pump 5, which has a minimum output of preferably 25 liters / min for the 20 liter perturbator system. From the pump 5 leads a hose line 6e, the cross section of which is approximately 10 to 15 mm smaller than the cross section of all other hose lines which are dimensioned 20 mm, to the lower inlet 19 of the converter 3.
- the "heart” of the converter consists of a preferably egg-shaped hollow body 25 (length about 7 cm, diameter about 3.5 cm), in the wall of which several obliquely in a plane parallel to the equatorial plane DD of the hollow body 25 channels 11 running below open tangentially.
- the axes of the channels 11 are inclined by preferably 45 ° to the equatorial plane D-D and to the axis of symmetry of the hollow body 25. If the mouth ends of the channels 11 in the interior of the hollow body 25 lie below the equatorial plane D-D, an optimal, cyclone-like functioning of the hollow body 25 is ensured.
- This egg-shaped hollow body 25 is introduced into an outer hollow body 39 and is firmly and seamlessly connected to it, in such a way that the egg-shaped hollow body 25 is held in a ring shape above the channels 11.
- This holder 27, which surrounds the upper part of the egg-shaped hollow body 25, is broken through in a channel-like manner in its center, and thus also at the apex of the egg-shaped hollow body 25.
- the device shown in FIG. 1, which consists of a perturbator 1, a spinner 2 and a converter 3. represents a variant to carry out the method. If the process with only a Perturbator 1 and a converter 3 is performed, such as in EP-A1-0314015 be ⁇ written / there is a prolongation of the process time.
- a plurality, possibly up to ten, of them can be connected in series in an analogous manner.
- one (or more) perturbator (s) 1 can also be provided.
- the position of the individual devices in relation to one another and in space is not necessarily fixed.
- the axes 17 and 38 of spinner 2 and converter 3 can lie obliquely or even horizontally, so that the designation used in the description from “above” and “below” for different parts of the device is only relative with reference to the drawing understand.
- the perturbator 1, as a liquid-absorbing device must of course be positioned vertically, preferably in such a way that no other part of the device comes to lie above the level determined by the fill level 9 for the liquid.
- the entire system In the operating state, the entire system, with the exception of the gas space 14, is filled with liquid, in particular water.
- liquid is conveyed in the direction of the arrows 22, a vortex being created by the tangential inflow of the water into the container 7.
- the surface of the water In the container 7, the surface of the water is changed from its rest position 9 into the funnel position 23, shown in broken lines, oxygen being sucked into the liquid from the gas space 14 in the form of bubbles and being conveyed or sucked further in the system according to the arrows 22 and is pressed.
- a gas space is formed during the course of the method, which contains the cavities 25 and 40 largely filled out.
- the liquid-gas mixture flows, corresponding to the arrows 22, tangentially into the hollow body 25 via the channels 11, a liquid-gas jacket rotating on the inner wall is formed there, which with increasing rotational speed at the lower end of the hollow body 25 reverses and swirls along the axis 38 in the form of a rapidly rotating vortex filament against the outlet nozzle 28, where it breaks off into the smallest liquid-gas mixture droplets and with suitable dimensions and forms a vortex system behind the nozzle edge.
- the expanded upper hollow body 40, into which the liquid-gas mixture is injected, acts like a diffuser.
- the particles of the liquid-gas mixture should have a maximum diameter of approximately 0.01 ⁇ m with suitable dimensioning of all components and suitably selected pump output.
- the gas bubbles are distributed more and more finely by the treatment in the various apparatuses.
- the mixture thus formed is drawn off via an outlet valve 33, for example arranged in the hose line 6b.
- the process runs over several hours, preferably for at least 36 hours, the gas apparently attaching itself to the liquid molecules or impressing the liquid with an activated structure that is stable over a long period of time.
- cooling is also provided which keeps the circulating mixture at only 15 to 18 ° C. In terms of energy consumption and the desired result, this means a rationalization of the process.
- the mixture enters the bottom of the coil, which is located in a pot through which the cooling medium flows.
- the spatial shapes of the perturbator 1 described in FIGS. 1 and 2a are possible design variants.
- the one shown in Fig. 2b is characterized by particularly good results.
- you can think of the spatial shape as being composed of two half-hyperboloids, which have the axis of symmetry 24 "as the axis of rotation. These hyperboloids are connected to each other by a flat, barrel-like middle piece without kinks.
- This spatial shape variant like that in Fig. 2a, has The spatial shape presented, the advantageous property of assigning an ever smaller diameter to the vortex formed during the method, and thus increasing the speed of rotation of the vortex funnel.
- the container 7 of the perturbator 1 is also possible, which is designed to correspond to an inverted, wide bottle with an approximately funnel-shaped neck.
- the upper part 7 "or 7b is cylindrical, spherical cap, cone-shaped or hyperboloid-shaped, the lower part 7 'or 7a conical or hyperboloid-shaped, the corresponding ver binding central part 35 is barrel-shaped or cylindrical, it is shown in all these cases to be additionally process-promoting if the height h of the lower container part 7 'or 7a is as large as possible with respect to the radius r of the perturbator container 7 (Fig. 2b), the swirl thread 26 important for the method is then longer and therefore more effective.
- the process was described using an approximately 20 liter per turbulator 1. Larger and also smaller embodiments are conceivable, but in the case of reduced dimensions (for example for a perturbator 1 with a capacity of approximately 5 1), a variant corresponding to FIG. 3 has proven to be advantageous for the converter 3.
- the channels II 1 are not in the wall of the egg-shaped hollow body 25 ', the wall thickness of which would be too thin for this.
- the ring-shaped holder 27 ' is here extended downwards in a ring-like manner, so that the channels 11' lie in this ring part. Access to the channels 11 'here is via guide channels 32 which are attached in the holder 27'.
- FIG. 4 shows a compact arrangement of the components spinner 2, perturbator 1, converter 3, pump 5 and coil 4 within a device cabinet 41, which at the same time takes over the function of the cooling unit.
- This arrangement which can be implemented, for example, as a 20 1, 10 1, or also 5 1 system, based on the liquid content, could prove itself for use in medical practices, therapy centers, health centers, and others.
- the combination of the components shown in FIG. 4 is only an exemplary possibility; all other possibilities described above and also below are conceivable.
- the liquid is poured in via a filling opening 10, which here can be closed with a standard ground cone 43 which has a tap which is closed at the end of the gassing.
- the fill level 9 for the liquid can be checked via a fill level indicator 42.
- a viewing window can simply be provided in the equipment cabinet 41; however, it is also possible to display the tubes communicating with one another, the connection to the perturbator 1 or the filling vessel being prevented after the filling level 9 has been reached.
- a gas reservoir 46 is filled from a gas bottle 45 and feeds the system with gas via the gas inlet opening.
- a plug contact 47 is provided for connecting the portable compact device to the mains.
- the perturbator 1 is fastened in an annular holder 48, for example, spinner 2, and converters 3 are arranged around the perturbator 1.
- a manometer 52 should advantageously be connected to the connection 13 provided for this purpose, in order to be able to determine any leaks that may occur in the system or functional defects.
- 5a to 5c schematically show arrangement variants for carrying out the method according to the invention, in which neither a perturbator 1 nor a converter 3 is required. Since this latter component in particular has a relatively complicated structure, it will be replaced to be preferred due to components which are simpler and therefore cheaper to produce.
- the perturbator 1 other devices can be used, by means of which gas can be introduced into liquid in a manner known per se. The effectiveness of the gas uptake is increased by passage through a plurality of spinners 2, through one or more coils 4 and by continuous passage and repetition of the same cycle.
- 5a, b and c show the fairly wide freedom in the number and choice of components that can be used (for the sake of clarity, cooling units have not been shown).
- FIG. 5 a provides a gas introduction device in the form of a vibrator 49, gas being introduced into the liquid from a gas space in a known manner via a vibrating membrane provided with fine holes. This arrangement is provided instead of the perturbator. This introduction of gas should take place throughout the process. When running through the circuit, the liquid-gas mixture flows through the mixing tank of the vibrator again and again, and there is always the possibility of introducing additional gas into the gas-liquid mixture.
- a suction device 50 for the gas from a gas reservoir 46a is provided, the mode of operation of which corresponds to the principle of a water jet pump.
- the device in FIG. 5c instead includes an atomizer 51, which brings liquid into the gas-filled container, which is finely atomized, and which is provided instead of the perturbator.
- the liquid-gas mixture passes through the circuit in the manner described above, but in addition to increasing the effectiveness, it can be repeatedly applied via the atomizing device, which is in the form of a nozzle or a centrifugal device.
- atomizer can be formed into the gas atmosphere.
- a variant of this consists in atomizing the liquid in an atomizer 51 and supplying it pulsatingly with gas via a pressure wave generator 53.
- a fundamentally different way of letting the process run is to introduce gas into a liquid under increased pressure and / or reduced temperature, i.e. thus to dissolve in it and to subject this gas-liquid mixture, for example, to a cycle corresponding to FIGS. 5 a to c, the pressure being gradually reduced and / or the temperature being increased continuously, until normal pressure or normal temperature are reached.
- a pressure vessel would have to be provided instead of the perturbator, which regulates the pressure in the vessel and thus also in the circuit via compensating valves;
- the entire circuit should advantageously run in a thermostat-controlled environment (housing).
- the mouth is rinsed by the doctor in a known manner. Afterwards, the patients rinsed the oxygen-water reaction product extremely intensively at home approximately every hour. The last rinse was carried out around 4:00 p.m., as the mucous membrane absorbed beers, and small amounts can be swallowed, so that sensitive patients could have difficulty falling asleep or sleeping through. After a week, all patients were symptom-free.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Description
Claims
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP93116950A EP0595177A1 (de) | 1989-03-17 | 1990-03-18 | Verfahren und Vorrichtung zur Herstellung eines Reaktionsprodukts aus einem Gas und einer Flüssigkeit |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CH1005/89 | 1989-03-17 | ||
CH100589 | 1989-03-17 | ||
PCT/EP1990/000444 WO1990011082A1 (de) | 1989-03-17 | 1990-03-18 | Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP93116950.2 Division-Into | 1993-10-20 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0463041A1 true EP0463041A1 (de) | 1992-01-02 |
EP0463041B1 EP0463041B1 (de) | 1994-06-22 |
Family
ID=4200236
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP90904824A Expired - Lifetime EP0463041B1 (de) | 1989-03-17 | 1990-03-18 | Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung |
EP93116950A Withdrawn EP0595177A1 (de) | 1989-03-17 | 1990-03-18 | Verfahren und Vorrichtung zur Herstellung eines Reaktionsprodukts aus einem Gas und einer Flüssigkeit |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP93116950A Withdrawn EP0595177A1 (de) | 1989-03-17 | 1990-03-18 | Verfahren und Vorrichtung zur Herstellung eines Reaktionsprodukts aus einem Gas und einer Flüssigkeit |
Country Status (4)
Country | Link |
---|---|
EP (2) | EP0463041B1 (de) |
AT (1) | ATE107511T1 (de) |
DE (1) | DE59006242D1 (de) |
WO (1) | WO1990011082A1 (de) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19615065A1 (de) * | 1996-04-17 | 1997-10-23 | Walter Kasanmascheff | Vorrichtung und Verfahren zum Anreichern von Flüssigkeiten |
DE102004007727A1 (de) * | 2004-02-16 | 2005-09-01 | Margret Spiegel | Herkömmliche Karbonatorsysteme oder Imprägniersysteme zusätzlich mindestens ein Hohlkörper-Inlineimprägnierer befüllt mit Schüttgut um schon karbonisierte oder imprägnierte Flüssigkeiten nachzukarbonisieren oder imprägnieren |
DE102013013200B4 (de) | 2013-08-09 | 2019-02-14 | Christian Sandkühler | Vorrichtung und Verfahren zur Ver- und/oder Bearbeitung mindestens eines Mediums, insbesondere zum Mischen mindestens zweier Medien |
DE202013007107U1 (de) | 2013-08-09 | 2013-10-10 | Christian Sandkühler | Vorrichtung zur Ver- und/oder Bearbeitung mindestens eines Mediums, insbesondere zum Mischen mindestens zweier Medien |
CZ309707B6 (cs) * | 2021-09-30 | 2023-08-09 | NUTRISTAMINA s.r.o | Generátor kapaliny sycené plynem |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1874209A (en) * | 1925-08-22 | 1932-08-30 | Pyrene Minimax Corp | Process of producing foam from foam developing substances |
NL75390C (de) * | 1950-10-13 | 1900-01-01 | ||
DE2741243A1 (de) * | 1977-09-14 | 1979-03-22 | Werner Anliker | Verfahren und vorrichtung zur durchmischung zweier medien |
EP0134890B1 (de) * | 1983-07-19 | 1990-09-12 | Wilfried Hacheney | Vorrichtung zum Herstellen hochwertiger Feststoff-Flüssigkeits-Gemische bis zum kolloiden System oder bis zur Koagulation, zur Wasseraufbereitung oder zum Einbringen von Gasen in Flüssigkeiten |
JPS6396129A (ja) * | 1986-10-14 | 1988-04-27 | Yukiaki Matsuo | 創傷用治療水 |
JPS63112521A (ja) * | 1986-10-28 | 1988-05-17 | Yoshiaki Matsuo | 消化器粘膜疾患および角結膜炎の治療水 |
DE3779242D1 (de) * | 1986-10-08 | 1992-06-25 | Zugol Ag | Verfahren und geraet zur erzeugung einer wasser-in-oel-emulsion. |
US4781676A (en) * | 1987-02-20 | 1988-11-01 | Air Products And Chemicals, Inc. | Interstitial administration of perfluorochemical emulsions for reoxygenation of hypoxic tumor cells |
IL88116A (en) * | 1987-10-23 | 1992-11-15 | Techno Bio Kk | Method for introducing and bonding gas into water,apparatus for carrying out the method,and water produced by the method |
EP0312642A1 (de) * | 1987-10-23 | 1989-04-26 | "Harrier" Gmbh Gesellschaft Für Den Vertrieb Medizinischer Und Technischer Geräte | Verfahren zum Einführen eines Gases in Wasser in Supergleichgewichtsquantität, Apparat zum Ausführen dieses Verfahrens und so erhaltenes Wasser |
CH676801A5 (en) * | 1988-11-17 | 1991-03-15 | Akozepta Ag | Prodn. of clathrate - by enclosing guest particles in liq. host polymer, used for disposing of sensitive cpds., toxic gases, etc. |
DE8905075U1 (de) * | 1989-04-21 | 1989-08-24 | "Harrier" GmbH Gesellschaft für den Vertrieb medizinischer und technischer Geräte, 8000 München | Mischvorrichtung für Strömungsmedien |
DE3923480A1 (de) * | 1989-07-15 | 1991-01-24 | Weickert Hans Joachim Dipl Ing | Verfahren und vorrichtung zum anreichern von fluessigkeiten mit gas |
-
1990
- 1990-03-18 AT AT90904824T patent/ATE107511T1/de not_active IP Right Cessation
- 1990-03-18 WO PCT/EP1990/000444 patent/WO1990011082A1/de active IP Right Grant
- 1990-03-18 EP EP90904824A patent/EP0463041B1/de not_active Expired - Lifetime
- 1990-03-18 EP EP93116950A patent/EP0595177A1/de not_active Withdrawn
- 1990-03-18 DE DE59006242T patent/DE59006242D1/de not_active Expired - Fee Related
Non-Patent Citations (1)
Title |
---|
See references of WO9011082A1 * |
Also Published As
Publication number | Publication date |
---|---|
WO1990011082A1 (de) | 1990-10-04 |
ATE107511T1 (de) | 1994-07-15 |
EP0595177A1 (de) | 1994-05-04 |
DE59006242D1 (de) | 1994-07-28 |
EP0463041B1 (de) | 1994-06-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
DE3850552T2 (de) | Verfahren zum Einführen und Binden eines Gases im Wasser, Apparat zum Ausführen dieses Verfahrens und so bekommenes Wasser. | |
DE3872059T2 (de) | Verfahren und vorrichtungen, um duftstoffe zu verteilen. | |
US7347944B2 (en) | Method for making and conditioning super-oxygenated and structured water | |
WO1992005792A1 (de) | Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung | |
DE69215722T3 (de) | Verstärker zur Ultraschalltherapie von Erkrankungen sowie diesen enthaltende flüssige Arzneimittelzusammensetzungen | |
DE202014004509U1 (de) | Gasgenerator für den Gesundheitsgebrauch | |
DE69913275T2 (de) | Verfahren und Vorrichtung zur positiven Beeinflussung des menschlichen Körpers | |
DE69029575T2 (de) | Ozongas verwendende medizinische behandlungsvorrichtung | |
CN109806148A (zh) | 一种便于调节升降高度的脚裸关节熏蒸护理装置 | |
EP0463041A1 (de) | Verwendung eines reaktionsproduktes aus einem gas und einer flüssigkeit, sowie verfahren und vorrichtung zu seiner herstellung. | |
US20060272989A1 (en) | System for oxygenating water | |
EP1728519A2 (de) | Polares Unterstützungs- und Breitbandresonatorpräparat | |
DE2432126C3 (de) | Automatisches Therapiegerät zur Behandlung durch Flüssigkeitsstrahlen | |
EP0331782A1 (de) | Duschvorrichtung | |
DE2909938A1 (de) | Fussbrause | |
DE202004018646U1 (de) | Vorrichtung zur Bereitstellung einer CO2-Gasatmosphäre | |
DE1808201A1 (de) | Einrichtung zur Behandlung des menschlichen Koerpers | |
DD297774A5 (de) | Verfahren zum einfuehren und binden von gas in wasser, vorrichtung zum ausfuehren des verfahrens und nach dem verfahren hergestelltes wasser | |
CN110151539A (zh) | 一种经络负离子药炙疗法 | |
DE68911274T2 (de) | Therapeutisches verdampftes Gemisch und Methode zu seiner Herstellung und Anwendung. | |
US1659085A (en) | Method and apparatus for charging fluids and other substances with ultraviolet rays | |
DE4022114A1 (de) | Therapiewanne | |
BE1029508B1 (de) | Menschliche akupunkturpunkte magnetothermische komposit-fitnessschnalle und herstellungsmethode und verwendungsmethode | |
RU2191558C2 (ru) | Способ лечения облысения и устройство для его осуществления | |
WO2021181296A1 (de) | Verwendung von cannabinoiden in therapie- und wellnessgeräten |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19910914 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE DK ES FR GB IT LI LU NL SE |
|
17Q | First examination report despatched |
Effective date: 19921106 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH DE DK ES FR GB IT LI LU NL SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRE;WARNING: LAPSES OF ITALIAN PATENTS WITH EFFECTIVE DATE BEFORE 2007 MAY HAVE OCCURRED AT ANY TIME BEFORE 2007. THE CORRECT EFFECTIVE DATE MAY BE DIFFERENT FROM THE ONE RECORDED.SCRIBED TIME-LIMIT Effective date: 19940622 Ref country code: ES Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY Effective date: 19940622 Ref country code: DK Effective date: 19940622 |
|
REF | Corresponds to: |
Ref document number: 107511 Country of ref document: AT Date of ref document: 19940715 Kind code of ref document: T |
|
REF | Corresponds to: |
Ref document number: 59006242 Country of ref document: DE Date of ref document: 19940728 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Effective date: 19940922 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 19940926 |
|
ET | Fr: translation filed | ||
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19950331 |
|
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed | ||
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 19980223 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 19980311 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 19980319 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 19980327 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: NL Payment date: 19980331 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 19980429 Year of fee payment: 9 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 19980528 Year of fee payment: 9 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19990318 Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19990318 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19990331 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19990331 Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19990331 |
|
BERE | Be: lapsed |
Owner name: BUCHHOLZ KLAUS L. Effective date: 19990331 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19991001 |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 19990318 |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 19991130 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 19991001 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20000101 |