FR2639652A1 - Adsorbent for uranium comprising bacterial cells - Google Patents
Adsorbent for uranium comprising bacterial cells Download PDFInfo
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- FR2639652A1 FR2639652A1 FR8914071A FR8914071A FR2639652A1 FR 2639652 A1 FR2639652 A1 FR 2639652A1 FR 8914071 A FR8914071 A FR 8914071A FR 8914071 A FR8914071 A FR 8914071A FR 2639652 A1 FR2639652 A1 FR 2639652A1
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- Prior art keywords
- uranium
- cells
- adsorbent
- bacterial cells
- bacteria
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- 229910052770 Uranium Inorganic materials 0.000 title claims abstract description 45
- JFALSRSLKYAFGM-UHFFFAOYSA-N uranium(0) Chemical compound [U] JFALSRSLKYAFGM-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 239000003463 adsorbent Substances 0.000 title claims abstract description 11
- 230000001580 bacterial effect Effects 0.000 title abstract description 3
- 238000000855 fermentation Methods 0.000 claims abstract description 12
- 230000004151 fermentation Effects 0.000 claims abstract description 12
- 150000001413 amino acids Chemical class 0.000 claims abstract description 7
- 241000186146 Brevibacterium Species 0.000 claims abstract description 5
- 241000186216 Corynebacterium Species 0.000 claims abstract description 3
- 241000894006 Bacteria Species 0.000 claims description 12
- 239000003758 nuclear fuel Substances 0.000 abstract description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 238000000605 extraction Methods 0.000 abstract description 4
- 210000004027 cell Anatomy 0.000 description 27
- 239000007788 liquid Substances 0.000 description 9
- 238000001179 sorption measurement Methods 0.000 description 8
- 239000002699 waste material Substances 0.000 description 8
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- 241000319304 [Brevibacterium] flavum Species 0.000 description 5
- 235000001014 amino acid Nutrition 0.000 description 5
- 229910021645 metal ion Inorganic materials 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 244000063299 Bacillus subtilis Species 0.000 description 4
- 235000014469 Bacillus subtilis Nutrition 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 241000186361 Actinobacteria <class> Species 0.000 description 3
- 239000010949 copper Substances 0.000 description 3
- 244000005700 microbiome Species 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- ZSLUVFAKFWKJRC-IGMARMGPSA-N 232Th Chemical compound [232Th] ZSLUVFAKFWKJRC-IGMARMGPSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 241000186226 Corynebacterium glutamicum Species 0.000 description 2
- 241000195493 Cryptophyta Species 0.000 description 2
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 229910052776 Thorium Inorganic materials 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- YKYOUMDCQGMQQO-UHFFFAOYSA-L cadmium dichloride Chemical compound Cl[Cd]Cl YKYOUMDCQGMQQO-UHFFFAOYSA-L 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 235000013922 glutamic acid Nutrition 0.000 description 2
- 239000004220 glutamic acid Substances 0.000 description 2
- 210000001822 immobilized cell Anatomy 0.000 description 2
- 238000009616 inductively coupled plasma Methods 0.000 description 2
- -1 lornithine Chemical compound 0.000 description 2
- 239000011572 manganese Substances 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 description 2
- 239000004475 Arginine Substances 0.000 description 1
- 241000193830 Bacillus <bacterium> Species 0.000 description 1
- 241000588724 Escherichia coli Species 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- QNAYBMKLOCPYGJ-REOHCLBHSA-N L-alanine Chemical compound C[C@H](N)C(O)=O QNAYBMKLOCPYGJ-REOHCLBHSA-N 0.000 description 1
- ODKSFYDXXFIFQN-BYPYZUCNSA-P L-argininium(2+) Chemical compound NC(=[NH2+])NCCC[C@H]([NH3+])C(O)=O ODKSFYDXXFIFQN-BYPYZUCNSA-P 0.000 description 1
- CKLJMWTZIZZHCS-REOHCLBHSA-N L-aspartic acid Chemical compound OC(=O)[C@@H](N)CC(O)=O CKLJMWTZIZZHCS-REOHCLBHSA-N 0.000 description 1
- RHGKLRLOHDJJDR-BYPYZUCNSA-N L-citrulline Chemical compound NC(=O)NCCC[C@H]([NH3+])C([O-])=O RHGKLRLOHDJJDR-BYPYZUCNSA-N 0.000 description 1
- ZDXPYRJPNDTMRX-VKHMYHEASA-N L-glutamine Chemical compound OC(=O)[C@@H](N)CCC(N)=O ZDXPYRJPNDTMRX-VKHMYHEASA-N 0.000 description 1
- HNDVDQJCIGZPNO-YFKPBYRVSA-N L-histidine Chemical compound OC(=O)[C@@H](N)CC1=CN=CN1 HNDVDQJCIGZPNO-YFKPBYRVSA-N 0.000 description 1
- AYFVYJQAPQTCCC-GBXIJSLDSA-N L-threonine Chemical compound C[C@@H](O)[C@H](N)C(O)=O AYFVYJQAPQTCCC-GBXIJSLDSA-N 0.000 description 1
- 239000004472 Lysine Substances 0.000 description 1
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910021380 Manganese Chloride Inorganic materials 0.000 description 1
- GLFNIEUTAYBVOC-UHFFFAOYSA-L Manganese chloride Chemical compound Cl[Mn]Cl GLFNIEUTAYBVOC-UHFFFAOYSA-L 0.000 description 1
- RHGKLRLOHDJJDR-UHFFFAOYSA-N Ndelta-carbamoyl-DL-ornithine Natural products OC(=O)C(N)CCCNC(N)=O RHGKLRLOHDJJDR-UHFFFAOYSA-N 0.000 description 1
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- AYFVYJQAPQTCCC-UHFFFAOYSA-N Threonine Natural products CC(O)C(N)C(O)=O AYFVYJQAPQTCCC-UHFFFAOYSA-N 0.000 description 1
- 239000004473 Threonine Substances 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 235000004279 alanine Nutrition 0.000 description 1
- ODKSFYDXXFIFQN-UHFFFAOYSA-N arginine Natural products OC(=O)C(N)CCCNC(N)=N ODKSFYDXXFIFQN-UHFFFAOYSA-N 0.000 description 1
- 235000003704 aspartic acid Nutrition 0.000 description 1
- OQFSQFPPLPISGP-UHFFFAOYSA-N beta-carboxyaspartic acid Natural products OC(=O)C(N)C(C(O)=O)C(O)=O OQFSQFPPLPISGP-UHFFFAOYSA-N 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 235000013477 citrulline Nutrition 0.000 description 1
- 229960002173 citrulline Drugs 0.000 description 1
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000012228 culture supernatant Substances 0.000 description 1
- 229960003280 cupric chloride Drugs 0.000 description 1
- VANPZBANAIIRJW-UHFFFAOYSA-N diuranium Chemical compound [U]#[U] VANPZBANAIIRJW-UHFFFAOYSA-N 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 238000010828 elution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- ZDXPYRJPNDTMRX-UHFFFAOYSA-N glutamine Natural products OC(=O)C(N)CCC(N)=O ZDXPYRJPNDTMRX-UHFFFAOYSA-N 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- HNDVDQJCIGZPNO-UHFFFAOYSA-N histidine Natural products OC(=O)C(N)CC1=CN=CN1 HNDVDQJCIGZPNO-UHFFFAOYSA-N 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- 239000011565 manganese chloride Substances 0.000 description 1
- 235000002867 manganese chloride Nutrition 0.000 description 1
- 229940099607 manganese chloride Drugs 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 description 1
- 239000010452 phosphate Substances 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002901 radioactive waste Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 235000008521 threonine Nutrition 0.000 description 1
- 229910002007 uranyl nitrate Inorganic materials 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
- 239000011592 zinc chloride Substances 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
Classifications
-
- G—PHYSICS
- G21—NUCLEAR PHYSICS; NUCLEAR ENGINEERING
- G21C—NUCLEAR REACTORS
- G21C19/00—Arrangements for treating, for handling, or for facilitating the handling of, fuel or other materials which are used within the reactor, e.g. within its pressure vessel
- G21C19/42—Reprocessing of irradiated fuel
- G21C19/44—Reprocessing of irradiated fuel of irradiated solid fuel
- G21C19/46—Aqueous processes, e.g. by using organic extraction means, including the regeneration of these means
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B60/00—Obtaining metals of atomic number 87 or higher, i.e. radioactive metals
- C22B60/02—Obtaining thorium, uranium, or other actinides
- C22B60/0204—Obtaining thorium, uranium, or other actinides obtaining uranium
- C22B60/0217—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes
- C22B60/0252—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries
- C22B60/0256—Obtaining thorium, uranium, or other actinides obtaining uranium by wet processes treatment or purification of solutions or of liquors or of slurries using biological agents, e.g. microorganisms or algae
-
- 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
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
-
- 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
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Plasma & Fusion (AREA)
- Biotechnology (AREA)
- Microbiology (AREA)
- Molecular Biology (AREA)
- High Energy & Nuclear Physics (AREA)
- Environmental & Geological Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Liquids With Adsorbents In General (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Description
La présente invention concerne des adsorbants de l'ura- nium utilisant des cellules de bactéries de fermentation des acides aminés. The present invention relates to uranium adsorbents using amino acid fermentation bacteria cells.
Des progrès constants ont été réalisés en vue d'utiliser
L'uranium et le thorium comme sources d'énergie nucléaire. On prévoit que l'énergie nucléaire sera prépondérante dans tes années à venir.Constant progress has been made towards using
Uranium and thorium as sources of nuclear energy. Nuclear power is expected to dominate in the years to come.
Les ressources terrestres en uranium sont estimées à 5 mitlions de tonnes sur Les continents, tandis que des ressources énormes en uranium, qui s'élèvent à 4 milliards de tonnes, sont dissoutes dans L'eau de mer. Terrestrial uranium resources are estimated at 5 million tonnes on continents, while huge uranium resources, which amount to 4 billion tonnes, are dissolved in seawater.
Par tailleurs, avec les progrès de l'industrie nucléaire, est apparu le problème urgent et sérieux du traitement et de la récupération de L'eau contenant des déchets radio-actifs libérée au cours de L'extraction et de L'enrichissement des éléments combustibles nucléaires tels que L'uranium, Le thorium, etc., qui va de pair avec la mise en va leur de ces éléments sur te plan énergétique. En outre, il est essentiel pour l'utilisation de l'énergie nucléaire de récupérer et régénérer les combustibles nucléaires utilisés et,pour ce faire, il est souhaitable de disposer d'un procédé plus sûr et plus économique. In addition, with the progress of the nuclear industry, the urgent and serious problem of treating and recovering water containing radioactive waste released during the extraction and enrichment of fuel elements has appeared. nuclear such as uranium, thorium, etc., which goes hand in hand with the energizing of these elements. In addition, it is essential for the use of nuclear energy to recover and regenerate the nuclear fuels used and, to do this, it is desirable to have a safer and more economical process.
La présente invention permet d'adsorber et de récupérer
L'uranium provenant de L'eau contenant de L'uranium libérée au cours d'une série de processus d'extraction des éléments combustibLes nucléaires afin de récupérer et réutiliser L'uranium de façon sure et économique.The present invention makes it possible to adsorb and recover
Uranium from Water containing Uranium released during a series of nuclear fuel element extraction processes to recover and reuse Uranium safely and economically.
Comme procédé d'adsorption de L'uranium à L'aide de micro-organismes, on connait un procédé utilisant des algues (demande de brevet japonais ouverte à l'inspection publique nO 50-73810). As a process for adsorbing uranium using microorganisms, there is known a process using algae (Japanese patent application open to public inspection No. 50-73810).
En outre, on a étudié les actinomycètes, les bactéries, les Levures et les champignons en ce qui concerne leur capacité d'adsorption de L'uranium (Marine Chemistry, 15 (11), 681-686, 1983). Au cours de L'essai de sélection, on a étudié des bactéries appartenant au genre Bacillus et au genre E. coli. Parmi les 4 types de micro-organismes mentionnés ci-dessus, les actinomycètes se sont révélés présenter une excellente aptitude à condenser L'uranium. In addition, actinomycetes, bacteria, yeasts and fungi have been studied for their uranium adsorption capacity (Marine Chemistry, 15 (11), 681-686, 1983). In the course of the selection test, bacteria belonging to the genus Bacillus and to the genus E. coli were studied. Among the 4 types of microorganisms mentioned above, actinomycetes have been shown to have an excellent ability to condense uranium.
Outre L'uranium, les algues ou cellules de microorganismes mentionnées ci-dessus teLs que les actinomycètes, les bactéries, etc., adsorbent toutes largement les métaux lourds tels que Le cadmium, le cobalt, Le nickel, Le cuivre, etc. De ce fait, on a cherché à développer de façon sélective des adsorbants peu coûteux pour L'uranium. On a cherché aussi à développer des adsorbants présentant une meilLeure capacité d'adsorption de luranium
Pour répondre à ce souhait, la présente invention propose des adsorbants de L'uranium et a été réalisée sur la base de la constatation que les cellules de bactéries adsorber de fermentation des acides aminés déterminées peuvent adsorber L'uranium de façon séLective avec une exceLlente capacite d'adsorption.In addition to uranium, the algae or cells of microorganisms mentioned above such as actinomycetes, bacteria, etc., all largely adsorb heavy metals such as cadmium, cobalt, nickel, copper, etc. As a result, attempts have been made to selectively develop inexpensive adsorbents for uranium. Attempts have also been made to develop adsorbents having a better adsorption capacity for uranium.
To meet this desire, the present invention provides uranium adsorbents and was carried out on the basis of the observation that bacteria cells adsorbing fermentation of determined amino acids can adsorb uranium selectively with an excellent capacity. adsorption.
PLus précisément, La présente invention concerne des adsorbants de L'uranium caractérisés en ce qu'ils comprennent des cellules de bactéries de fermentation des acides aminés appartenant au genre Brevibacterium ou au genre Corynebacterium. More specifically, the present invention relates to uranium adsorbents characterized in that they comprise bacteria bacteria for fermentation of amino acids belonging to the genus Brevibacterium or to the genus Corynebacterium.
IL n'existe pas de Limitation particuLière en ce qui concerne les types de bactéries de fermentation des acides aminés, mais on peut utiliser largement les bactéries utilisées pour La fermentation de L'acide glutamique et de La lysine et Les bactéries utilisées autrement pour La fermentation de L'arginine, de l'histi- dine, de La glutamine, de l'alanine, de ltornithine, de L'acide aspartique, de la citrulline, de ta thréonine, etc. Des exemples de bactéries de fermentation comprennent Brevibacterium flavum,
Brevibacterium lactofermentam, Corynebacterium glutamicum, etc.On peut cultiver ces cellules bactériennes indépendamment en vue de les faire proLiférer, mais on préfère utiliser les cellules constituant des déchets Libérées au cours de ta fermentation des acides aminés étant donné qu'elles sont peu coûteuses et qu'elles sont utilisées de façon efficace. Le surnageant de culture peu ne pas etre compLétement éliminé des cellules. Pour isoler Les cellules on peut utiliser un procédé quelconque de centrifugation et de fittra- tion. Ou bien encore, on peut précipiter Les cellules au préalable en ajoutant un agent de précipitation ou analogue, avant l'isole- ment.Dans le cas de l'utilisation d'un adjuvant de filtration dans le procédé par filtration, on peut utiliser le système contenant
L'adjuvant de filtration pour adsorber L'uranium én l'état. Cependant, on préfère procéder par centrifugation car les contaminants sont présents en moins grande quantité. Si nécessaire et si on le souhaite, les cellules obtenues sont lavées à L'eau. There is no particular limitation with regard to the types of amino acid fermentation bacteria, but the bacteria used for the fermentation of glutamic acid and lysine can be widely used and the bacteria used otherwise for fermentation arginine, histidine, glutamine, alanine, lornithine, aspartic acid, citrulline, threonine, etc. Examples of fermentation bacteria include Brevibacterium flavum,
Brevibacterium lactofermentam, Corynebacterium glutamicum, etc. We can cultivate these bacterial cells independently in order to make them proliferate, but we prefer to use the cells constituting waste released during the fermentation of amino acids since they are inexpensive and because 'they are used effectively. The culture supernatant may not be completely eliminated from the cells. To isolate the cells, any method of centrifugation and filtration can be used. Alternatively, the cells can be precipitated beforehand by adding a precipitation agent or the like, before isolation. In the case of the use of a filter aid in the filtration process, the container system
The filter aid to adsorb the uranium in the state. However, it is preferred to proceed by centrifugation because the contaminants are present in less quantity. If necessary and if desired, the cells obtained are washed with water.
On peut utiliser les cellules comme adsorbant de l'ura- nium sous forme d'une suspension ou d'un gâteau. Par ailleurs, on peut également immobiliser Les cellules à L'aide d'un gel de polyacrylamide, etc., et on peut utiliser les cellules immobilisées. On peut réaliser L'adsorption au moyen d'un système discontinu dans lequel les cellules sont ajoutées à un liquide contenant de l'ura- nium. En outre, dans Le cas où t'on immobilise Les ceLLuLes, Les cellules immobilisées peuvent être introduites dans une colonne pour permettre un traitement en continu.Dans tous les cas, à l'échelle industrielle, il est souhaitable de mettre les déchets dans lesquels l'uranium a été récupéré par adsorption en contact avec des cellules fraiches pour ainsi augmenter le taux de récupération. Les cellules mises en contact avec Les déchets sont mises en contact avec un Liquide frais contenant de L'uranium pour faire croître la quantité d'uranium adsorbé. Puis, on élue L'uranium de celles-ci. The cells can be used as an uranium adsorbent in the form of a suspension or cake. Furthermore, the cells can also be immobilized using a polyacrylamide gel, etc., and the immobilized cells can be used. Adsorption can be carried out by means of a discontinuous system in which the cells are added to a uranium-containing liquid. In addition, in the case where the cells are immobilized, the immobilized cells can be introduced into a column to allow continuous treatment. In all cases, on an industrial scale, it is desirable to put the waste in which the uranium was recovered by adsorption in contact with fresh cells, thereby increasing the recovery rate. The cells brought into contact with the waste are brought into contact with a fresh liquid containing uranium to increase the amount of uranium adsorbed. Then, we elect uranium from them.
On peut realiser L'élution de L'uranium en mettant en contact les cellules avec un acide ou une base. L'acide ou la base peut etre sous forme d'une solution tampon. On peut citer le carbonate de sodium comme exemple -d'éluant. The elution of uranium can be achieved by bringing the cells into contact with an acid or a base. The acid or base can be in the form of a buffer solution. Mention may be made of sodium carbonate as an example of eluent.
Les cellules obtenues après L'éluvion de L'uranium peuvent être de nouveau utilisées pour L'adsorption de L'uranium. The cells obtained after uranium uranium can be used again for uranium adsorption.
Ou bien encore, on peut se débarrasser des cellules en les détruisant par Le feu.Or else, we can get rid of the cells by destroying them with fire.
Par ailleurs, Lorsque les cellules sont utilisées pour la purification d'un Liquide contenant des déchets, etc., sans être destinées à la récupération de L'uranium, elles peuvent être solidifiées à L'aide d'un béton, etc., sans en éluer L'uranium, et les cellules solidifiées peuvent être éliminées. Furthermore, when the cells are used for the purification of a liquid containing waste, etc., without being intended for the recovery of uranium, they can be solidified using concrete, etc., without Elute the uranium, and the solidified cells can be eliminated.
Il n'existe pas de limitation particulière en ce qui concerne le type du liquide contenant de L'uranium et celui-ci peut être, par exemple, un liquide contenant des déchets Libéré au cours du processus d'enrichissement d'un combustible nucléaire, un liquide contenant des déchets libéré au cours du traitement d'un combustible nucléaire, un liquide contenant des déchets d'extraction, un Liquide contenant du phosphate, l'eau de mer, etc. There is no particular limitation with regard to the type of liquid containing uranium and this can be, for example, a liquid containing waste released during the enrichment process of a nuclear fuel, a liquid containing waste released during the processing of a nuclear fuel, a liquid containing extraction waste, a liquid containing phosphate, sea water, etc.
D'autres avantages et caractéristiques de L'invention apparaîtront mieux dans Les exemples non limitatifs suivants. Other advantages and characteristics of the invention will appear better in the following nonlimiting examples.
Exemple 1
20 mg (poids sec) de cellules humides de Brevibacterium flavum (souche déposée le 9 septembre 1975 à L'institut japonais de o recherche sur les fermentations sous le n FERM-P 3247) qui sont des bactéries de fermentation de l'acide glutamique et 20 mg (poids sec) de cellules humides de Bacillus subtilis ont été ajoutés à 100 ml d'une solution aqueuse de U02(N03)2 ayant une concentration en uranium de 10 ppm, respectivement. Chaque mélange a été agité à 300C pendant 1 h. Ensuite, les cellules ont été séparées et la concentration en uranium du surnageant a été mesurée à L'aide d'un appareil à plasma à couplage inductif pour mesurer la concentration des ions métalliques (Quantometer ICPQ-100, Shimadzu Seisakusho) pour déterminer la quantité d'ions uranyle adsorbés.Les résultats obtenus sont présentés dans le tableau suivant
Taux d'adsorption de L'uranium
Brevibacterium flavum 99,2 X
Bacillus subtilis 97,3 X
Exemple 2
20 mg (poids sec) de Brevibacterium flavum (FERM-P nO 3247) ont été ajoutés à différentes quantités d'une solution aqueuse de U02(N03)2 ayant une concentration en uranium de 20 ppm, respectivement. Chaque mélange a été agité pendant 3O0C pendant 1 h. Puis, les cellules ont été séparées et la concentration en uranium du surnageant a été mesurée de la même façon que dans l'exemple 1.Les résultats obtenus sont présentés dans le tableau suivant
Solution aqueuse Taux d'adsorption Quantité d'uranium adsorbé d'uranium ~ de l'uranium dans les cellules
100 ml 98,5 X 99,2 mg/g
300 ml 69,2 X 209,1 mg/g
500 ml 47,3 X 238,2 mg/g
Exemple 3
20 mg (poids sec) de cellules humides de Brevibacterium
o flavum (FERM-P n 3247) et 20 mg (poids sec) de Bacillus subtilis ont été ajoutés à une solution aqueuse contenant 4 x 10 5 M de chacun des éléments suivants : cadmium (chlorure de cadmium), cobalt (chlorure de cobalt), cuivre (chlorure cuivrique), manganèse (chlorure de manganèse), nickel (chlorure de nickel), zinc (chlorure de zinc) et uranium (nitrate d'uranyle) et ayant un pH de 5.Example 1
20 mg (dry weight) of wet cells of Brevibacterium flavum (strain deposited on September 9, 1975 at the Japanese Institute for Research on Fermentations under the number FERM-P 3247) which are fermentation bacteria of glutamic acid and 20 mg (dry weight) of Bacillus subtilis wet cells were added to 100 ml of an aqueous solution of U02 (N03) 2 having a uranium concentration of 10 ppm, respectively. Each mixture was stirred at 300C for 1 h. Next, the cells were separated and the uranium concentration of the supernatant was measured using an inductively coupled plasma device to measure the concentration of metal ions (Quantometer ICPQ-100, Shimadzu Seisakusho) to determine the amount of adsorbed uranyl ions. The results obtained are presented in the following table
Uranium adsorption rate
Brevibacterium flavum 99.2 X
Bacillus subtilis 97.3 X
Example 2
20 mg (dry weight) of Brevibacterium flavum (FERM-P nO 3247) were added to different amounts of an aqueous solution of U02 (N03) 2 having a uranium concentration of 20 ppm, respectively. Each mixture was stirred for 30 ° C for 1 h. Then, the cells were separated and the uranium concentration of the supernatant was measured in the same way as in Example 1. The results obtained are presented in the following table
Aqueous solution Adsorption rate Amount of uranium adsorbed uranium ~ uranium in cells
100 ml 98.5 X 99.2 mg / g
300 ml 69.2 X 209.1 mg / g
500 ml 47.3 X 238.2 mg / g
Example 3
20 mg (dry weight) of Brevibacterium wet cells
o flavum (FERM-P n 3247) and 20 mg (dry weight) of Bacillus subtilis were added to an aqueous solution containing 4 x 10 5 M of each of the following: cadmium (cadmium chloride), cobalt (cobalt chloride ), copper (cupric chloride), manganese (manganese chloride), nickel (nickel chloride), zinc (zinc chloride) and uranium (uranyl nitrate) and having a pH of 5.
Chaque mélange a été agité à 300C pendant 1 h. Puis, les cellules ont été séparées et la concentration des ions métalliques dans le surnageant a été mesurée avec un appareil à plasma à couplage inductif pour mesurer la concentration des ions métalliques (Quantometer ICPQ-100, Shimadzu Seisakusho) pour déterminer la quantité de chacun des ions métalliques adsorbes. Les résultats obtenus sont présentés dans Le tableau suivant :
Brevibacterium flavum Bacillus subtilis
Cd 6,5 X 16,8 X
Co 3,3 7,8
Cu 33,5 63,3
Mn 2,5 9,3
Ni 4,3 90,5
Zn 3,5 9,5
U 93,5 60,8
ExempLe 4
On a déterminé la quantité de chacun des ions métalliques adsorbés sur Corynebacterium glutamicum (souche déposée le 9 septembre 1975 à L'institut japonais de recherche sur les fermen
o tations sous le n FERM-P 3250). On a obtenu des résultats sem- blables à ceux des exemples 1 à 3.Each mixture was stirred at 300C for 1 h. Then, the cells were separated and the concentration of metal ions in the supernatant was measured with an inductively coupled plasma device to measure the concentration of metal ions (Quantometer ICPQ-100, Shimadzu Seisakusho) to determine the amount of each adsorbed metal ions. The results obtained are presented in the following table:
Brevibacterium flavum Bacillus subtilis
CD 6.5 X 16.8 X
Co 3.3 7.8
Cu 33.5 63.3
Mn 2.5 9.3
Ni 4.3 90.5
Zn 3.5 9.5
U 93.5 60.8
EXAMPLE 4
The quantity of each of the metal ions adsorbed on Corynebacterium glutamicum (strain deposited on September 9, 1975 at the Japanese Institute for Research on Fermen was determined.
oations under FERM-P 3250). Results similar to those of Examples 1 to 3 were obtained.
On constate ainsi qu'en utilisant l'adsorbant selon la présente invention, on peut récupérer de façon sélective et efficace L'uranium contenu dans l'eau. Il en resulte que la présente invention permet non seulement d'extraire l'uranium de nouvelles sources telles que l'eau de mer, etc., mais aussi de traiter Les liquides renfermant des déchets contenant de L'uranium. It is thus found that by using the adsorbent according to the present invention, the uranium contained in water can be recovered selectively and efficiently. As a result, the present invention not only makes it possible to extract uranium from new sources such as sea water, etc., but also to treat liquids containing wastes containing uranium.
Différentes modifications peuvent être apportées à l'invention sans sortir de son cadre. Various modifications can be made to the invention without departing from its scope.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63268162A JPH02118035A (en) | 1988-10-26 | 1988-10-26 | Uranium adsorbent |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| FR2639652A1 true FR2639652A1 (en) | 1990-06-01 |
| FR2639652B1 FR2639652B1 (en) | 1992-08-07 |
Family
ID=17454767
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FR8914071A Expired - Lifetime FR2639652B1 (en) | 1988-10-26 | 1989-10-26 | URANIUM ADSORBENT COMPRISING BACTERIAL CELLS |
Country Status (4)
| Country | Link |
|---|---|
| JP (1) | JPH02118035A (en) |
| AU (1) | AU618416B2 (en) |
| CA (1) | CA2001413A1 (en) |
| FR (1) | FR2639652B1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102009015413A1 (en) | 2009-03-27 | 2010-09-30 | B.P.S. Engineering Gesellschaft für Umwelt und Automatisierungstechnik mbH | Adsorbent to remove heavy metals from contaminated water, comprises mesoporous material with homogeneous distribution containing metal oxides and high-molecular cationic polymers, which contain quaternary ammonium and/or phosphonium groups |
| DE102013207197A1 (en) * | 2013-04-22 | 2014-10-23 | Helmholtz-Zentrum Dresden - Rossendorf E.V. | Process and system for the separation of heavy metals |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20220162103A1 (en) * | 2020-11-23 | 2022-05-26 | Algignis, Inc. | Environmental remediation, heat recovery, water purification, biomaterials |
| CN116411187B (en) * | 2021-12-31 | 2025-10-17 | 新疆中核天山铀业有限公司 | U-shaped tower leaching process for fixed bed |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2243264A1 (en) * | 1973-09-08 | 1975-04-04 | Kernforschungsanlage Juelich |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| PT69331A (en) * | 1978-03-23 | 1979-04-01 | Interox Chemicals Ltd | Leaching of minerals |
| US4293333A (en) * | 1980-02-12 | 1981-10-06 | Engelhard Minerals & Chemicals Corporation | Microbiological recovery of metals |
| GB8418588D0 (en) * | 1984-07-20 | 1984-09-12 | Harmon Frances Ltd | Removing metals from aqueous solutions |
-
1988
- 1988-10-26 JP JP63268162A patent/JPH02118035A/en active Pending
-
1989
- 1989-10-20 AU AU43610/89A patent/AU618416B2/en not_active Ceased
- 1989-10-25 CA CA 2001413 patent/CA2001413A1/en not_active Abandoned
- 1989-10-26 FR FR8914071A patent/FR2639652B1/en not_active Expired - Lifetime
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2243264A1 (en) * | 1973-09-08 | 1975-04-04 | Kernforschungsanlage Juelich |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102009015413A1 (en) | 2009-03-27 | 2010-09-30 | B.P.S. Engineering Gesellschaft für Umwelt und Automatisierungstechnik mbH | Adsorbent to remove heavy metals from contaminated water, comprises mesoporous material with homogeneous distribution containing metal oxides and high-molecular cationic polymers, which contain quaternary ammonium and/or phosphonium groups |
| DE102013207197A1 (en) * | 2013-04-22 | 2014-10-23 | Helmholtz-Zentrum Dresden - Rossendorf E.V. | Process and system for the separation of heavy metals |
| DE102013207197B4 (en) | 2013-04-22 | 2019-05-02 | Helmholtz-Zentrum Dresden - Rossendorf E.V. | Process for the separation of heavy metals, use of the process and use of a system for the purification of heavy metals contaminated waters or for the detection of heavy metals in waters |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2639652B1 (en) | 1992-08-07 |
| JPH02118035A (en) | 1990-05-02 |
| AU618416B2 (en) | 1991-12-19 |
| AU4361089A (en) | 1990-05-03 |
| CA2001413A1 (en) | 1990-04-26 |
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