WO2014007331A1 - アルカリ金属及び/又はアルカリ土類金属の抽出方法 - Google Patents
アルカリ金属及び/又はアルカリ土類金属の抽出方法 Download PDFInfo
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- WO2014007331A1 WO2014007331A1 PCT/JP2013/068376 JP2013068376W WO2014007331A1 WO 2014007331 A1 WO2014007331 A1 WO 2014007331A1 JP 2013068376 W JP2013068376 W JP 2013068376W WO 2014007331 A1 WO2014007331 A1 WO 2014007331A1
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- aqueous solution
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- 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
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
- C22B26/20—Obtaining alkaline earth metals or magnesium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
- B01D11/0288—Applications, solvents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/80—Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F11/00—Compounds of calcium, strontium, or barium
- C01F11/18—Carbonates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F5/00—Compounds of magnesium
- C01F5/24—Magnesium carbonates
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- 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
- C22B26/00—Obtaining alkali, alkaline earth metals or magnesium
-
- 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
- C22B3/00—Extraction of metal compounds from ores or concentrates by wet processes
- C22B3/04—Extraction of metal compounds from ores or concentrates by wet processes by leaching
- C22B3/16—Extraction of metal compounds from ores or concentrates by wet processes by leaching in organic solutions
- C22B3/1608—Leaching with acyclic or carbocyclic agents
- C22B3/1616—Leaching with acyclic or carbocyclic agents of a single type
- C22B3/165—Leaching with acyclic or carbocyclic agents of a single type with organic acids
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- 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
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/006—Wet processes
- C22B7/007—Wet processes by acid leaching
Definitions
- the present invention relates to a method for extracting the alkali metal and / or alkaline earth metal from a solid containing alkali metal and / or alkaline earth metal.
- Patent Document 1 As a conventional method for extracting the alkali metal and / or alkaline earth metal from a solid containing alkali metal and / or alkaline earth metal, for example, the method described in Patent Document 1 below is known. Yes.
- steel slag or the like is added to an aqueous solution containing formic acid or citric acid to elute magnesium and calcium, and then precipitated as carbonate (magnesium carbonate and calcium carbonate) by blowing carbon dioxide into the aqueous solution.
- a method for extracting magnesium and calcium from steel slag and the like is disclosed.
- An object of the present invention is to provide an alkali metal and / or alkaline earth metal extraction method that can repeatedly use an aqueous solution for extracting an alkali metal and / or alkaline earth metal from a solid, and is excellent in cost. There is.
- the present inventors have found that when extracting an alkali metal and / or alkaline earth metal from a solid, when an aqueous solution containing an amino acid is used, its extraction ability is not easily lowered even if it is repeatedly used.
- the present invention has been reached.
- the characteristic configuration of the method for extracting an alkali metal and / or alkaline earth metal according to the present invention is to extract the alkali metal and / or alkaline earth metal from a solid material containing the alkali metal and / or alkaline earth metal. It is a method, Comprising: It is a point including the elution process which adds the said solid substance to amino acid containing aqueous solution, and elutes the said alkali metal and / or alkaline-earth metal to said amino acid containing aqueous solution.
- the amino acid-containing aqueous solution has a high extraction capability for alkali metals and / or alkaline earth metals in solids, and the high extraction capability is maintained even after repeated use. Can be used repeatedly, and the cost can be reduced.
- characteristic configurations include, after the elution step, a precipitation step of bringing the amino acid-containing aqueous solution into contact with an acidic gas to precipitate the alkali metal and / or alkaline earth metal as a salt, and a recovery step of recovering the salt It is in the point including.
- the alkali metal and / or alkaline earth metal eluted in the elution step can be efficiently recovered as a salt by a simple operation of contacting the acid gas.
- the precipitation step includes a pH adjustment step of adding a pH adjuster to the amino acid-containing aqueous solution before or after contacting the acidic gas to make the pH higher than 7. .
- the pH of the amino acid-containing aqueous solution after the elution step may become acidic.
- the salt hardly precipitates.
- precipitation of alkali metal and / or alkaline earth metal salt is promoted by making the pH of the aqueous solution containing amino acid greater than 7 before or after contact with acidic gas to make it alkaline. Is efficient.
- Another feature is that another solid substance containing an alkali metal and / or alkaline earth metal is added to the amino acid-containing aqueous solution after the recovery step, and the alkali metal and / or alkaline earth metal is added to the amino acid-containing aqueous solution.
- the second elution step to be eluted is included.
- the amino acid-containing aqueous solution that has been used once can be reused to extract alkali metal and / or alkaline earth metal from another solid material, which is convenient.
- amino acid is aspartic acid.
- the aspartic acid-containing aqueous solution has a high extraction capability, and the extraction capability is stably maintained even after being used a relatively large number of times, so that the cost can be further reduced. Can do.
- FIG. 1 It is the schematic of the apparatus used in the Example. 1 is a flowchart according to Embodiment 1.
- FIG. It is a table
- throwing-in, and the elution rate of a calcium ion (Substance amount (mol) of CaO in cement: Substance amount (mol) of various added amino acids 1: 0. .1).
- FIG. 6 It is a graph which shows the elution rate (moL%) and precipitation rate (moL%) of a calcium ion when the amino acid containing aqueous solution which concerns on Example 2 is used repeatedly.
- the method for extracting an alkali metal and / or alkaline earth metal comprises adding a solid material containing an alkali metal and / or alkaline earth metal to an amino acid-containing aqueous solution, and the alkali metal and / or alkaline earth metal.
- An elution step of elution of the amino acid in an amino acid-containing aqueous solution comprises adding a solid material containing an alkali metal and / or alkaline earth metal to an amino acid-containing aqueous solution, and the alkali metal and / or alkaline earth metal.
- the solid material in the present invention is at least one selected from the group consisting of alkali metals such as lithium, sodium, potassium, rubidium and cesium, and alkaline earth metals such as magnesium, calcium, strontium, barium and radium. It means to include. Examples of such solids include natural minerals, waste materials, and by-products discharged in the manufacturing process.
- Examples of natural minerals include alkali metal carbonates, phosphates, silicates, aluminates, sulfates, hydroxides, chlorides, and the like, and alkaline earths. Examples include simple substances and hydrates of metal carbonates, phosphates, silicates, aluminates, sulfates, hydroxides, and chlorides. Specific examples of such natural minerals include at least one selected from the group consisting of calcium silicate, sodium silicate, sodium phosphate, magnesium silicate, calcium phosphate, magnesium phosphate, calcium aluminate, magnesium aluminate and the like. And rocks mainly composed of one or weathered or crushed material of the rocks.
- waste materials and by-products discharged in the manufacturing process include concrete solidified with cement hydrated solids, building waste containing the concrete, pulverized materials, and by-product steel slag discharged from the steel making process, cupola.
- waste materials and by-products discharged in the manufacturing process include concrete solidified with cement hydrated solids, building waste containing the concrete, pulverized materials, and by-product steel slag discharged from the steel making process, cupola.
- examples thereof include slag, soda lime glass, potash lime glass, fly ash generated by waste incineration or molten slag thereof, paper sludge generated in the papermaking process, municipal waste, or sludge.
- the solid material used in the present invention is pulverized so as to have a particle size of about 1 ⁇ m to 100 ⁇ m, the alkali metal and / or the alkaline earth metal is easily eluted.
- the amino acid-containing aqueous solution in the present invention means an aqueous solution containing at least a predetermined amount of amino acid, but may contain a carboxylic acid such as citric acid in addition to the amino acid.
- the amino acid in the present invention means all organic compounds having both amino group and carboxyl group functional groups.
- main amino acids that can be generally used 20 kinds of amino acids (isoleucine) constituting a protein in a living body are used.
- amino acid is mentioned as a particularly preferable amino acid for more stably and repeatedly using an amino acid-containing aqueous solution.
- the amino acid is not limited to the amino acids described above, and N-protected amino acids such as N-acetyl-DL-tryptophan and C-protected amino acids may be used.
- the amount of amino acid to be contained in the amino acid-containing aqueous solution depends on the amount of the solid matter added to the amino acid-containing aqueous solution and may be adjusted as appropriate by the operator.
- the alkali contained in the solid matter What is necessary is just to add about 0.01 times or more of the total number of moles of a metal and an alkaline-earth metal.
- an amino acid is added to water to prepare an amino acid-containing aqueous solution, and then a solid containing an alkali metal and / or alkaline earth metal is added, for example, left for a while or known stirring.
- the alkali metal and / or alkaline earth metal may be eluted into the amino acid-containing aqueous solution by stirring and mixing using an apparatus.
- the operator may appropriately adjust, for example, When the elution step is performed on about 2 g to 4 g of a solid using a stirrer, the amino acid-containing aqueous solution used is about 0.01 L, and the stirrer is stirred at a speed of about 300 rpm to 500 rpm.
- the temperature is preferably about 10 ° C. to 70 ° C., and the stirring time is preferably about 0.5 minutes or more.
- the present invention includes a precipitation step in which an acidic gas is brought into contact with the amino acid-containing aqueous solution after the elution step to precipitate an alkali metal and / or alkaline earth metal as a salt, and a recovery step in which the precipitated salt is recovered. There may be.
- the present invention adds a pH adjuster to the amino acid-containing aqueous solution before or after contacting the acid gas in the precipitation step, in order to precipitate the salt more efficiently in the precipitation step, and to adjust the pH. You may make it implement the pH adjustment process made larger than seven.
- the pH adjuster applicable at this time is not particularly limited, and examples thereof include sodium hydroxide (NaOH) and potassium hydroxide (KOH).
- CO 2 is not limited to pure carbon dioxide, and any gas containing carbon dioxide can be used.
- gaseous fuel such as liquefied natural gas (LNG) and liquefied petroleum gas (LP)
- liquid fuel such as gasoline and light oil
- combustion exhaust gas generated by burning solid fuel such as coal are used as carbon dioxide gas. it can.
- the method of bringing the acidic gas into contact with the amino acid-containing aqueous solution in the precipitation step can be performed by a known method and is not particularly limited.
- a method of bubbling (blowing) an acid gas into an amino acid-containing aqueous solution a method of shaking an amino acid-containing aqueous solution and an acidic gas enclosed in the same container, and the like can be mentioned.
- combustion exhaust gas etc. as acidic gas
- a precipitation process can be implemented at arbitrary temperature, since acidic gas becomes difficult to melt
- alkaline earth metal calcium ions or magnesium ions react with carbonic acid eluted from the solid, and carbonates such as calcium carbonate and magnesium carbonate are produced. Precipitate.
- the salt precipitated in the precipitation step can be recovered by a known method such as filtration in the subsequent recovery step.
- the recovered salt can be used as a filler in industries such as papermaking, pigments, paints, plastics, rubber, woven and knitted fabrics.
- the present invention adds another solid containing an alkali metal and / or alkaline earth metal to the amino acid-containing aqueous solution after the recovery step, and elutes the alkali metal and / or alkaline earth metal into the amino acid-containing aqueous solution.
- the second elution step to be performed may be performed, and then the second precipitation step and the recovery step may be performed. That is, in the present invention, the second elution step, the precipitation step, and the recovery step are performed using the amino acid-containing aqueous solution used in the first elution step, and further the third elution step, the precipitation step, and the recovery step are performed.
- a series of processes such as an elution step, a precipitation step, and a recovery step can be repeated for the same amino acid-containing aqueous solution.
- the solid substance added to the amino acid-containing aqueous solution may be the same or different from that used in the previous elution step, and is not particularly limited.
- Example 1 In order to confirm that an alkali metal and / or alkaline earth metal can be extracted from a solid with an amino acid-containing aqueous solution, an elution process according to the present invention was performed using the apparatus shown in FIG. As shown in FIG. 1, the apparatus includes a reaction vessel 1, a stirrer 2, a water bath 3 that adjusts the temperature of the solution in the reaction vessel 1, flow rate regulators 4 and 5, a mixing device 6, a meter 7, and a gas chromatograph. 8. A backflow prevention device 9 and a computer 10 are provided.
- an amino acid-containing aqueous solution (100 mL) containing each of nine types of amino acids was prepared, and solid (Corland Analysis Portland Cement, Cement Association, 211R Standard Sample for Chemical Analysis) was prepared as a solid. 2.40 g or 3.66 g of slag (blast furnace slag standard material, Japan Iron and Steel Federation Standardization Center, blast furnace slag No. 6) was added to prepare a mixed aqueous solution.
- the amount of calcium contained in each of the cement and slag was 64.2 wt% and 42 wt% in terms of CaO.
- the nine types of added amino acids and their weights, the types and weights of solids, and the molar ratio (the amount of CaO in the solid (mole): the amount of added amino acids (mole)) are shown in FIG. .
- the amount (mol) of various amino acids when the amount (mol) of CaO contained in each of cement and slag was set to 1 or 0.1. That is, in this example, 36 types of mixed aqueous solutions were prepared depending on the type of added amino acid, the type of solid, and the molar ratio.
- FIGS. 4 to 7 show the relationship between the pH of the mixed aqueous solution immediately after charging the solid material and the elution rate of calcium ions
- FIGS. 8 to 11 show the pH of the mixed aqueous solution 10 minutes after the solid material is charged. And the relationship between the elution rate of calcium ions.
- the pH of each mixed aqueous solution was approximately 11 to 12, which was biased toward the alkali side.
- the pH of each mixed aqueous solution was about 9 to 12, and it was biased toward the alkali side.
- the pH of each mixed aqueous solution was about 9 to 11, which was biased toward the alkali side.
- the pH of each mixed aqueous solution was about 4 to 11, and the pH range was slightly shifted to the alkali side.
- the pH of the mixed aqueous solution immediately after the solid is added to the amino acid-containing aqueous solution is determined by the equivalence point (pH) of various amino acids.
- acidic amino acids L-glutamic acid and L-
- the pH of the mixed aqueous solution containing aspartic acid, etc. is on the acidic side
- the pH of the mixed aqueous solution containing basic amino acids L-arginine, etc.
- it exhibits a wide range of pH.
- the alkali metal and / or alkaline earth metal can be extracted from the solid by using the amino acid-containing aqueous solution.
- the pH of the mixed aqueous solution after 10 minutes has elapsed from the addition of the solid is determined from the neutralization point (pH) of calcium ions eluted from the solid and the equivalence point (pH) of various amino acids. That is, in each of the mixed aqueous solutions shown in FIGS. 8 to 10, the substance amount (mol) of eluted calcium ions is higher than the substance amount (moles) of various amino acids, and the pH is mainly neutralized with calcium ions. It is considered that the pH range was narrowed because all the mixed aqueous solutions became alkaline as determined by (pH). On the other hand, in each of the mixed aqueous solutions shown in FIG.
- the substance amounts (moles) of various amino acids are substantially the same as the substance amount (moles) of the eluted calcium ions, or more than the substance amounts (moles) of the eluted calcium ions. It is considered that the pH range was increased because the pH was mainly determined from the equivalence point (pH) of various amino acids.
- the pH range is about 3 to 11 immediately after the cement is added, and becomes about 11 to 12 after 10 minutes.
- the pH range is about 3 to 11 immediately after the slag is charged, and becomes about 9 to 11 after 10 minutes. That is, when the amino acid concentration in the mixed aqueous solution is the same, the pH change from immediately after charging to 10 minutes after adding cement becomes larger when cement is added.
- acidic amino acids such as L-glutamic acid and L-aspartic acid have high extraction ability among the nine types of amino acids used in this example.
- Example 2 In order to confirm whether the extraction ability of alkali metal and / or alkaline earth metal of the amino acid-containing aqueous solution is maintained when the amino acid-containing aqueous solution is repeatedly used, the same apparatus is used as shown in FIG. A series of processes of an elution step, a precipitation step, and a recovery step according to the present invention were repeatedly performed on the amino acid-containing aqueous solution, and the elution rate and precipitation rate of calcium ions in each process were examined.
- an amino acid-containing aqueous solution 100 mL containing 2.40 g of L-aspartic acid as an amino acid was prepared, and a solid (Portland Cement for Chemical Analysis, Cement Association, 211R Chemical Analysis) was used as a solid.
- a solid Portableland Cement for Chemical Analysis, Cement Association, 211R Chemical Analysis
- 2.40 g was added to prepare a mixed aqueous solution, and the mixture was stirred for 10 minutes in the same manner as in Example 1 to elute calcium ions (elution step).
- the number of moles of CaO in the cement the number of moles of added L-aspartic acid was 1: 1.
- the calcium ion elution rate (Ca elution rate) was examined by measuring the pH, oxidation-reduction potential, and temperature of the mixed aqueous solution in the reaction vessel 1 with the measuring instrument 7.
- the simulated combustion exhaust gas As the simulated combustion exhaust gas, a mixed gas of carbon dioxide (CO 2 ) and nitrogen (N 2 ) gas was used.
- the simulated combustion exhaust gas was supplied by mixing carbon dioxide gas and nitrogen gas at a predetermined mixing ratio in the mixing device 6 while adjusting the flow rate with the flow rate adjusters 4 and 5, respectively.
- the composition of the simulated combustion exhaust gas was 10 vol% CO 2 +90 vol% N 2 and introduced at 1 liter / min for 90 minutes.
- the precipitated calcium carbonate was recovered by suction filtration, and the filtrate (amino acid-containing aqueous solution) was collected (recovery step).
- the recovered calcium carbonate was dried and weighed, and the precipitation rate of calcium ions (Ca precipitation rate: the ratio of calcium in calcium carbonate to the amount of calcium ions eluted in the elution step) was examined.
- the present invention can be suitably used to recover alkali metal and / or alkaline earth metal from industrial waste such as building waste including concrete and steelmaking slag.
Abstract
Description
この場合、酸性のアミノ酸含有水溶液に酸性ガスを接触させて、アルカリ金属及び/又はアルカリ土類金属と反応させても、塩が析出し難くなる。
そこで、本構成のごとく、酸性ガスと接触させる前又は接触させた後に、アミノ酸含有水溶液のpHを7より大きくしてアルカリ性にすれば、アルカリ金属及び/又はアルカリ土類金属の塩の析出が促進されるため効率が良い。
以下、本発明の実施形態を説明する。本発明に係るアルカリ金属及び/又はアルカリ土類金属の抽出方法は、アミノ酸含有水溶液に、アルカリ金属及び/又はアルカリ土類金属を含む固形物を添加して、アルカリ金属及び/又はアルカリ土類金属をアミノ酸含有水溶液に溶出させる溶出工程を含む。
本発明における固形物とは、リチウム、ナトリウム、カリウム、ルビジウム、セシウム等のアルカリ金属、及び、マグネシウム、カルシウム、ストロンチウム、バリウム、ラジウム等のアルカリ土類金属からなる群から選択される少なくとも一つを含むものを意味する。そのような固形物として、例えば、天然鉱物、廃材、製造工程で排出される副産物等が挙げられる。
本発明におけるアミノ酸含有水溶液とは、少なくとも所定量のアミノ酸を含む水溶液を意味するが、アミノ酸の他にクエン酸などのカルボン酸を含むようにしても良い。
また本発明におけるアミノ酸とは、アミノ基と、カルボキシル基の両方の官能基を持つ有機化合物全般を意味するが、通常使用できる主なアミノ酸としては、生体のタンパク質を構成する20種類のアミノ酸(イソロイシン、ロイシン、バリン、リシン、スレオニン、トリプトファン、メチオニン、フェニルアラニン、ヒスチジン、アルギニン、アスパラギン酸、アスパラギン、システィン、チロシン、アラニン、グルコサミン、グルタミン酸、グリシン、プロリン、セリン)が挙げられる。また、アミノ酸含有水溶液をより多く安定して繰り返し使用するのに特に好ましいアミノ酸としては、アスパラギン酸が挙げられる。なお、上述したアミノ酸に限定されず、N-アセチル-DL-トリプトファンなどのN保護アミノ酸やC保護アミノ酸を使用しても良い。
本発明に適用可能な酸性ガスとしては、例えば、CO2、NOx、SOx、硫化水素などを挙げることができる。特にCO2(炭酸ガス)は、純粋な炭酸ガスに限らず、炭酸ガスを含む気体であれば適用できる。例えば、液化天然ガス(LNG)・液化石油ガス(LP)等の気体燃料、ガソリン・軽油等の液体燃料、石炭等の固体燃料等を燃焼させて発生する燃焼排ガス等を炭酸ガスとして用いることができる。
アミノ酸含有水溶液によって、固形物からアルカリ金属及び/又はアルカリ土類金属を抽出できることを確認するため、図1に示す装置を用いて、本発明に係る溶出工程を実施した。図1に示すように、当該装置は、反応容器1、攪拌機2、反応容器1内の溶液の温度を調整する水浴槽3、流量調整器4,5、混合装置6、計測計7、ガスクロマトグラフ8、逆流防止装置9、計算機10を備えて構成される。
アミノ酸含有水溶液を繰り返して使用した場合に、そのアミノ酸含有水溶液のアルカリ金属及び/又はアルカリ土類金属の抽出能力が維持されるか否かを確認するため、図1に示す装置を用いて、同じアミノ酸含有水溶液に対して、本発明に係る溶出工程、析出工程、及び回収工程という一連のプロセスを繰り返し実施し、各プロセスにおけるカルシウムイオンの溶出率と析出率とを調べた。
2 攪拌機
3 水浴槽
4,5 流量調整器
6 混合装置
7 計測計
8 ガスクロマトグラフ
9 逆流防止装置
10 計算機
Claims (5)
- アルカリ金属及び/又はアルカリ土類金属を含む固形物から、前記アルカリ金属及び/又はアルカリ土類金属を抽出する方法であって、
アミノ酸含有水溶液に前記固形物を添加して、前記アルカリ金属及び/又はアルカリ土類金属を前記アミノ酸含有水溶液に溶出させる溶出工程を含む方法。 - 前記溶出工程の後、前記アミノ酸含有水溶液に酸性ガスを接触させて前記アルカリ金属及び/又はアルカリ土類金属を塩として析出させる析出工程と、前記塩を回収する回収工程とを含む請求項1に記載の方法。
- 前記析出工程において、前記酸性ガスを接触させる前又は接触させた後に、前記アミノ酸含有水溶液にpH調整剤を添加し、pHを7より大きくするpH調整工程を含む請求項2に記載の方法。
- 前記回収工程後のアミノ酸含有水溶液にアルカリ金属及び/又はアルカリ土類金属を含む別の固形物を添加して、当該アルカリ金属及び/又はアルカリ土類金属を前記アミノ酸含有水溶液に溶出させる第2溶出工程を含む請求項2又は3に記載の方法。
- 前記アミノ酸がアスパラギン酸である請求項1~4のいずれか1項に記載の方法。
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US14/409,723 US9631256B2 (en) | 2012-07-05 | 2013-07-04 | Alkali metal and/or alkali earth metal extraction method |
EP13813295.6A EP2870987B1 (en) | 2012-07-05 | 2013-07-04 | Alkali metal and/or alkali earth metal extraction method |
JP2014523786A JP6020565B2 (ja) | 2012-07-05 | 2013-07-04 | アルカリ金属及び/又はアルカリ土類金属の抽出方法 |
AU2013285917A AU2013285917B2 (en) | 2012-07-05 | 2013-07-04 | Alkali metal and/or alkali earth metal extraction method |
IN533DEN2015 IN2015DN00533A (ja) | 2012-07-05 | 2015-01-21 |
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---|---|---|---|---|
JP2020033263A (ja) * | 2014-04-28 | 2020-03-05 | リクシヴィア・インコーポレイテッドLixivia, Inc. | アルカリ土類炭酸塩の製造方法 |
JP2021191890A (ja) * | 2020-06-05 | 2021-12-16 | ▲ろん▼▲鉱▼▲環▼保科技(上海)有限公司Greenore Cleantech (Shanghai) Co., Ltd | 二酸化炭素に基づく湿式製錬の多段反応及び分離システム |
WO2023033039A1 (ja) * | 2021-08-31 | 2023-03-09 | 住友大阪セメント株式会社 | 炭酸カルシウム生成方法及びシステム |
JP7388633B2 (ja) | 2020-03-23 | 2023-11-29 | 国立大学法人山梨大学 | 高炉スラグからのカルシウムおよびケイ素の分離方法 |
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JP6013480B2 (ja) * | 2012-07-05 | 2016-10-25 | アイシン精機株式会社 | アルカリ金属及び/又はアルカリ土類金属の抽出方法 |
US20180223392A1 (en) * | 2017-02-09 | 2018-08-09 | Lixivia, Inc. | Compositions and methods for recovery of alkaline metals |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1072215A (ja) * | 1996-08-29 | 1998-03-17 | Maruo Calcium Co Ltd | 微細粒子炭酸カルシウムの製造方法 |
JP2006509787A (ja) * | 2002-12-05 | 2006-03-23 | エムディー バイオアルファ カンパニー リミテッド | アミノ酸キレートの調製方法 |
JP2007222713A (ja) | 2006-02-21 | 2007-09-06 | Tohoku Univ | 鉄鋼産業副生成物からのマグネシウム及びカルシウム除去回収とa型ゼオライト製造方法 |
Family Cites Families (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS493755B1 (ja) * | 1970-08-10 | 1974-01-28 | ||
US4237147A (en) * | 1974-01-04 | 1980-12-02 | Monsanto Company | Stabilized amorphous calcium carbonate |
JPS5742532A (en) | 1980-08-28 | 1982-03-10 | Nippon Kokan Kk <Nkk> | Treatment of smelting slag containing alkali metal compound |
US4760138A (en) * | 1984-12-13 | 1988-07-26 | Nestec S. A. | Carbonating agents and their preparation |
JPS621832A (ja) | 1985-02-07 | 1987-01-07 | Sumitomo Metal Ind Ltd | 溶銑処理スラグからのアルカリ金属回収方法 |
JPH01317531A (ja) | 1988-06-18 | 1989-12-22 | Hakuba Plast Kogyo Kk | 改良された石膏溶解剤 |
GB9815289D0 (en) * | 1998-07-14 | 1998-09-09 | Unilever Plc | Speroidal calcitic calcium carbonate |
JP2001121188A (ja) | 1999-10-28 | 2001-05-08 | Ajinomoto Co Inc | 新規なスケール防止剤 |
JP3962855B2 (ja) | 2001-07-19 | 2007-08-22 | 日立造船株式会社 | 飛灰からの重金属の回収方法 |
JP2003159583A (ja) | 2001-11-27 | 2003-06-03 | Kurita Water Ind Ltd | 重金属汚染土壌又は廃棄物の処理方法 |
JP3954009B2 (ja) | 2003-08-18 | 2007-08-08 | 財団法人地球環境産業技術研究機構 | 炭酸ガスの固定化方法 |
JP2005219013A (ja) | 2004-02-09 | 2005-08-18 | National Institute Of Advanced Industrial & Technology | 重金属汚染土壌浄化剤 |
JP4671646B2 (ja) | 2004-09-03 | 2011-04-20 | 柳 沢 幸 雄 | カルシウムを含む廃棄物からの高純度炭酸カルシウムの製造方法 |
JP2007056308A (ja) | 2005-08-24 | 2007-03-08 | Japan Science & Technology Agency | ペプチドを用いた貴金属の回収方法 |
JP5083748B2 (ja) | 2006-05-23 | 2012-11-28 | 独立行政法人物質・材料研究機構 | 炭酸カルシウム・ゼオライト系化合物複合体の製造方法 |
CN101293663B (zh) * | 2007-04-28 | 2011-05-25 | 北京紫光英力化工技术有限公司 | 微细碳酸钙制备工艺 |
JP5072090B2 (ja) | 2007-12-06 | 2012-11-14 | 日本コンクリート工業株式会社 | コンクリートスラッジ処理装置 |
CN101993104A (zh) * | 2009-08-21 | 2011-03-30 | 北京紫光英力化工技术有限公司 | 一种以电石渣为原料生产超微细碳酸钙的新方法 |
JP5630629B2 (ja) | 2009-09-29 | 2014-11-26 | アイシン精機株式会社 | 炭酸ガス処理装置及び炭酸ガスの処理方法 |
JP5523169B2 (ja) | 2010-03-31 | 2014-06-18 | 三井造船環境エンジニアリング株式会社 | メタン発酵システム |
-
2013
- 2013-07-04 WO PCT/JP2013/068376 patent/WO2014007331A1/ja active Application Filing
- 2013-07-04 US US14/409,723 patent/US9631256B2/en active Active
- 2013-07-04 EP EP13813295.6A patent/EP2870987B1/en active Active
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Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH1072215A (ja) * | 1996-08-29 | 1998-03-17 | Maruo Calcium Co Ltd | 微細粒子炭酸カルシウムの製造方法 |
JP2006509787A (ja) * | 2002-12-05 | 2006-03-23 | エムディー バイオアルファ カンパニー リミテッド | アミノ酸キレートの調製方法 |
JP2007222713A (ja) | 2006-02-21 | 2007-09-06 | Tohoku Univ | 鉄鋼産業副生成物からのマグネシウム及びカルシウム除去回収とa型ゼオライト製造方法 |
Non-Patent Citations (1)
Title |
---|
See also references of EP2870987A4 |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2020033263A (ja) * | 2014-04-28 | 2020-03-05 | リクシヴィア・インコーポレイテッドLixivia, Inc. | アルカリ土類炭酸塩の製造方法 |
JP7056959B2 (ja) | 2014-04-28 | 2022-04-19 | リクシヴィア・インコーポレイテッド | アルカリ土類炭酸塩の製造方法 |
JP7388633B2 (ja) | 2020-03-23 | 2023-11-29 | 国立大学法人山梨大学 | 高炉スラグからのカルシウムおよびケイ素の分離方法 |
JP2021191890A (ja) * | 2020-06-05 | 2021-12-16 | ▲ろん▼▲鉱▼▲環▼保科技(上海)有限公司Greenore Cleantech (Shanghai) Co., Ltd | 二酸化炭素に基づく湿式製錬の多段反応及び分離システム |
JP7018493B2 (ja) | 2020-06-05 | 2022-02-10 | ▲ろん▼▲鉱▼▲環▼保科技(上海)有限公司 | 二酸化炭素に基づく湿式製錬の多段反応及び分離システム |
WO2023033039A1 (ja) * | 2021-08-31 | 2023-03-09 | 住友大阪セメント株式会社 | 炭酸カルシウム生成方法及びシステム |
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EP2870987A1 (en) | 2015-05-13 |
AU2013285917A1 (en) | 2015-01-22 |
JPWO2014007331A1 (ja) | 2016-06-02 |
JP6020565B2 (ja) | 2016-11-02 |
EP2870987B1 (en) | 2020-01-08 |
IN2015DN00533A (ja) | 2015-06-26 |
US20150322547A1 (en) | 2015-11-12 |
US9631256B2 (en) | 2017-04-25 |
EP2870987A4 (en) | 2015-07-15 |
AU2013285917B2 (en) | 2015-11-26 |
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