WO1996033129A1 - Procede chimique de production d'eau possedant une teneur limitee en deuterium - Google Patents
Procede chimique de production d'eau possedant une teneur limitee en deuterium Download PDFInfo
- Publication number
- WO1996033129A1 WO1996033129A1 PCT/HU1996/000019 HU9600019W WO9633129A1 WO 1996033129 A1 WO1996033129 A1 WO 1996033129A1 HU 9600019 W HU9600019 W HU 9600019W WO 9633129 A1 WO9633129 A1 WO 9633129A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- water
- hydrogen
- deuterium
- deuterium content
- low deuterium
- 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.)
- Ceased
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B4/00—Hydrogen isotopes; Inorganic compounds thereof prepared by isotope exchange, e.g. NH3 + D2 → NH2D + HD
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
- C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
- C01B3/06—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents
- C01B3/08—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of inorganic compounds containing electro-positively bound hydrogen, e.g. water, acids, bases, ammonia, with inorganic reducing agents with metals
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B5/00—Water
-
- 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
Definitions
- the subject of the present invention is a chemical process for the production of low deuterium content water.
- Natural water contains 130-160 ppm deuterium (in Hungary 150-154 ppm in average). According to recent discoveries water of lower deuterium content (0.1 - 130 ppm) is suitable for the prevention and treatment of several types of cancer (HU 208,084, FEBS Letters, 1993, 317 (1-2), (1-4).
- Water of reduced deuterium content is a side product of heavy water production.
- low deuterium water can be obtained in clean form, in the form of a solution or with varying deuterium content, during the enrichment process (US 2,137,430, GB 435,450, FR 789,822, US 2,044,704, SU
- light water or light hydrogen suitable to produce light water is formed as a side product of heavy water production in the following methods: isotopic exchange reaction between hydrogen and water (US 2,690,380, US 2,690,379, IT 493,492) isotopic exchange reaction between hydrogen-sulphide and water (US 2,787,526, GB 845, 501, FR 1,165, 257, FR 1,164,750, FR 1,169,140, FR 1,175,894, GB 870,036, CA 616,048,DE 1,047,753), exchange reactions between mercaptanes and water (US 2,741,543, GB 837, 730), isotopic exchange in the mixture of ammonia, hydrogen and water (DE 1,036,223, GB 867,736, FR 1,180,973), as well as exchange reactions between cyclohexane or benzene and hydrogen (US 2,690,380).
- the main disadvantage of these methods is that in addition to the serious equipment and technical support demand, in the first step - using natural water - the deuterium level decreases only slightly. Moreover, the light water produced has to be submitted to serious purification due to the use of poisonous materials e.g. hydrogen-sulphide, ammonia, etc, in order to make it suitable for human consumption. Disclosure of the invention
- the fractionation efficiency is three-fold, considering that the water to be fractinated contains 1/3 of the deuterium content of natural water used in the known processes; 4. the starting material applied is a side product;
- Burning of hydrogen can be carried out directly, in a flameless process,with or without catalyst, in the interaction of air, oxygen or a material containing oxygen.
- Specific examples of the invention are set forth below. In order that the invention described herein can be more fully understood, the following examples are to illustrate the invention process, however, the examples are for illustration purposes only, and are not to be construed as limiting this invention in any manner. Best mode for carrying out the invention Example 1
- Example 2 Proceeding as in Example 1 with a sodium-amalgam containing 3% sodium, the reaction mixture was not allowed to heat up (intense cooling) and practically the same result was obtained (51 ppm).
- Example 3 Proceeding as in Example 1 with a sodium-amalgam containing 3% sodium, the reaction mixture was not allowed to heat up (intense cooling) and practically the same result was obtained (51 ppm).
- Example 4 Proceeding as in Example 1 with the use of sodium-amalgams of 0.1, 0.5 and 1.0% sodium, the results were practically the same (53,56 and 60 ppm, respectively).
- Example 4
- Example 5 Proceeding as in Example 4, but using the hydrogen without deep cooling (the water content was not removed) and carrying out burning in a direct flame in air, the deuterium content of water after condensation was found to be 55 ppm.
- Example 6 Proceeding as in Example 4, the water vapour formed was introduced to liquid water to cool (without pre-cooling) in counter-current in a column packed with Rasching rings using the dripping method. In this way by mixing the condensed water (55 ppm) and the recycled dripping (cooling) water (154 ppm) in the right rations, water of 130 ppm deuterium content was obtained for use in the food industry.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- General Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
Abstract
L'eau possédant une teneur limitée en deutérium est utile pour prévenir ou soigner plusieurs types de cancers. Le procédé consiste à fractionner la vapeur d'eau obtenue par combustion directe ou catalytique d'hydrogène à basse teneur en deutérium ou par sa réaction avec des matériaux contenant de l'oxygène, afin d'obtenir de l'eau à teneur limitée en deutérium. L'hydrogène à basse teneur en deutérium s'obtient par mise en réaction d'un métal alcalin, de préférence, un amalgame de sodium obtenu par électrolyse d'alcalis et de chlorure, avec de l'eau naturelle et l'hydrogène généré par le procédé - possédant une teneur en deutérium d'environ 1/3 de celle de l'eau naturelle de départ - est utilisé pour produire de la vapeur d'eau.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU52855/96A AU5285596A (en) | 1995-04-20 | 1996-04-18 | A chemical procedure to produce water of reduced deuterium c ontent |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| HUP9501118 | 1995-04-20 | ||
| HU9501118A HU217418B (hu) | 1995-04-20 | 1995-04-20 | Kémiai eljárás alacsony deutériumtartalmú víz előállítására |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO1996033129A1 true WO1996033129A1 (fr) | 1996-10-24 |
| WO1996033129B1 WO1996033129B1 (fr) | 1996-11-28 |
Family
ID=10986734
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/HU1996/000019 Ceased WO1996033129A1 (fr) | 1995-04-20 | 1996-04-18 | Procede chimique de production d'eau possedant une teneur limitee en deuterium |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU5285596A (fr) |
| HU (1) | HU217418B (fr) |
| WO (1) | WO1996033129A1 (fr) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2011011877A1 (fr) * | 2009-07-29 | 2011-02-03 | Stuart Andrew T B | Systèmes au chlorate et au dioxyde de chlore conçus pour produire de l'eau enrichie en deutérium |
| US9297509B2 (en) | 2004-03-18 | 2016-03-29 | Brasscorp Limited | LED work light |
| WO2017001874A1 (fr) * | 2015-06-29 | 2017-01-05 | Erdős Elemér Antal | Procédé de production économique d'eau potable, en particulier d'eau potable appauvrie en deutérium, utilisée en médecine humaine et vétérinaire |
| RU2612667C1 (ru) * | 2015-10-13 | 2017-03-13 | Общество с ограниченной ответственностью "МТК Айсберг" | Устройство для получения воды с пониженным содержанием тяжелых молекул |
| US10370249B2 (en) * | 2014-05-26 | 2019-08-06 | Hongjian Liu | Method and system for producing deuterium depleted water |
| WO2019174659A1 (fr) | 2018-03-15 | 2019-09-19 | Karl Bau Gmbh | Procédé et ensemble servant à fabriquer de l'eau à teneur réduite en deutérium |
| CN112811559A (zh) * | 2020-12-30 | 2021-05-18 | 江苏奥特泉超轻水饮料有限公司 | 一种低氘氢水及其制备方法及应用 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3649486A (en) * | 1970-02-02 | 1972-03-14 | Bitterfeld Chemie | Method of acceleration of the decomposition of sodium-amalgam in decomposers of mercury-cells |
| US4058440A (en) * | 1975-10-17 | 1977-11-15 | Iowa State University Research Foundation, Inc. | Concurrent separation of lithium and hydrogen isotopes |
| EP0355349A2 (fr) * | 1988-07-08 | 1990-02-28 | Forschungszentrum Jülich Gmbh | Dispositif de sécurité pour éviter l'explosion d'un mélange tonnant |
| WO1993008794A1 (fr) * | 1991-10-31 | 1993-05-13 | Hyd Kutató-Fejlesztõ Kft. | Produits pharmaceutiques destines a guerir les maladies tumorales, et leur procede de preparation |
-
1995
- 1995-04-20 HU HU9501118A patent/HU217418B/hu not_active IP Right Cessation
-
1996
- 1996-04-18 WO PCT/HU1996/000019 patent/WO1996033129A1/fr not_active Ceased
- 1996-04-18 AU AU52855/96A patent/AU5285596A/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3649486A (en) * | 1970-02-02 | 1972-03-14 | Bitterfeld Chemie | Method of acceleration of the decomposition of sodium-amalgam in decomposers of mercury-cells |
| US4058440A (en) * | 1975-10-17 | 1977-11-15 | Iowa State University Research Foundation, Inc. | Concurrent separation of lithium and hydrogen isotopes |
| EP0355349A2 (fr) * | 1988-07-08 | 1990-02-28 | Forschungszentrum Jülich Gmbh | Dispositif de sécurité pour éviter l'explosion d'un mélange tonnant |
| WO1993008794A1 (fr) * | 1991-10-31 | 1993-05-13 | Hyd Kutató-Fejlesztõ Kft. | Produits pharmaceutiques destines a guerir les maladies tumorales, et leur procede de preparation |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9297509B2 (en) | 2004-03-18 | 2016-03-29 | Brasscorp Limited | LED work light |
| WO2011011877A1 (fr) * | 2009-07-29 | 2011-02-03 | Stuart Andrew T B | Systèmes au chlorate et au dioxyde de chlore conçus pour produire de l'eau enrichie en deutérium |
| US10370249B2 (en) * | 2014-05-26 | 2019-08-06 | Hongjian Liu | Method and system for producing deuterium depleted water |
| WO2017001874A1 (fr) * | 2015-06-29 | 2017-01-05 | Erdős Elemér Antal | Procédé de production économique d'eau potable, en particulier d'eau potable appauvrie en deutérium, utilisée en médecine humaine et vétérinaire |
| RU2612667C1 (ru) * | 2015-10-13 | 2017-03-13 | Общество с ограниченной ответственностью "МТК Айсберг" | Устройство для получения воды с пониженным содержанием тяжелых молекул |
| WO2017065647A1 (fr) * | 2015-10-13 | 2017-04-20 | Общество с ограниченной ответственностью "МТК Айсберг" | Procédé pour produire de l'eau à faible teneur en molécules lourdes |
| US10688436B2 (en) | 2015-10-13 | 2020-06-23 | Obschestvo S Ogranichennoj Otvetstvennostyu “Mtk Ajsberg” | Device for producing water having reduced heavy molecule content |
| WO2019174659A1 (fr) | 2018-03-15 | 2019-09-19 | Karl Bau Gmbh | Procédé et ensemble servant à fabriquer de l'eau à teneur réduite en deutérium |
| CN112811559A (zh) * | 2020-12-30 | 2021-05-18 | 江苏奥特泉超轻水饮料有限公司 | 一种低氘氢水及其制备方法及应用 |
Also Published As
| Publication number | Publication date |
|---|---|
| HUT75696A (en) | 1997-05-28 |
| HU9501118D0 (en) | 1995-06-28 |
| AU5285596A (en) | 1996-11-07 |
| HU217418B (hu) | 2000-01-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| SU988184A3 (ru) | Способ получени четыреххлористого кремни | |
| NO170787B (no) | Reflekterende ark | |
| Schlesinger et al. | Hydrides of Boron. XII. Symmetrical Dimethyldiborane and the Methyl Derivatives of Borine Trimethylammine | |
| GB855913A (en) | Improvements in or relating to the manufacture of silicon | |
| SK280897B6 (sk) | Spôsob odstránenia oxidu siričitého z odpadových plynov | |
| WO1996033129A1 (fr) | Procede chimique de production d'eau possedant une teneur limitee en deuterium | |
| US4010246A (en) | Process for preparing sulfur dioxide | |
| US2817580A (en) | Process for purifying hydrogen sulphide containing hydrogen cyanide | |
| GB1347884A (en) | Process for cracking sulphuric acid | |
| US4794204A (en) | Process for the removal of dimethyl ether in methyl chloride | |
| UA40622C2 (uk) | Спосіб безперервного одержання водних розчинів формальдегіду | |
| US1765688A (en) | Process of making sulphuryl chloride | |
| JPS61268635A (ja) | 二塩化エタンの製造方法 | |
| RU2166982C2 (ru) | Способ разделения изотопов углерода | |
| GB1125453A (en) | Electrolytic production of chlorine | |
| Haber et al. | The Production of Synthetic Ammonia. | |
| US3145079A (en) | Process for the preparation of purified hydrogen bromide gas by the use of activated arbon as catalyst | |
| US1311175A (en) | Herbert h | |
| RU2827098C1 (ru) | Способ получения бромистого водорода электронного класса и катализатор для его осуществления | |
| SU1680286A1 (ru) | Способ получения смеси хлористоводородной и фтористоводородной кислот из отходящих газов | |
| SU658122A1 (ru) | Способ получени четыреххлористого углерода | |
| RU2063261C1 (ru) | Способ разделения изотопов водорода | |
| US2081097A (en) | Manufacture of hydrogen peroxide | |
| US4115460A (en) | Method for producing hexachlorocyclobutene | |
| US1036224A (en) | Process of making penta- and hexa-chlorethanes. |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AK | Designated states |
Kind code of ref document: A1 Designated state(s): AL AM AU BB BG BR CA CN CZ EE FI GE IS JP KG KP KR LK LR LT LV MD MG MK MN MX NO NZ PL RO SG SI SK TR TT UA US UZ VN AM AZ BY KG KZ MD RU TJ TM |
|
| AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): KE LS MW SD SZ UG AT BE CH DE DK ES FI FR GB GR IE IT LU MC NL PT SE BF BJ CF CG CI CM GA GN ML MR NE SN TD TG |
|
| DFPE | Request for preliminary examination filed prior to expiration of 19th month from priority date (pct application filed before 20040101) | ||
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
| 122 | Ep: pct application non-entry in european phase | ||
| NENP | Non-entry into the national phase |
Ref country code: CA |