RECOVERY METHOD FOR A CONTINUOUS CALCIUM EXTRACTION AND PCC PRODUCTION
    21.
    发明申请
    RECOVERY METHOD FOR A CONTINUOUS CALCIUM EXTRACTION AND PCC PRODUCTION 审中-公开
    连续萃取和PCC生产的回收方法

    公开(公告)号:WO2013096764A1

    公开(公告)日:2013-06-27

    申请号:PCT/US2012/071238

    申请日:2012-12-21

    Abstract: A method of mineralizing calcium from industrial waste comprising extracting calcium ions from a suspension of calcium rich granular particles and aqueous ammonium nitrate to form a calcium-rich first fraction and a heavy second fraction. The heavy second fraction is separated from the first fraction and the calcium-rich first fraction is carbonated with a gas comprising carbon dioxide to form a suspension of precipitated calcium carbonate and aqueous ammonium nitrate. The precipitate is separated from the aqueous ammonium nitrate by centrifugal means and the separated heavy second fraction comprises an enriched weight percent of iron.

    Abstract translation: 从工业废物中使钙矿化的方法包括从富含钙的颗粒和硝酸铵水溶液的悬浮液中提取钙离子,形成富含钙的第一馏分和重的第二馏分。 将重的第二馏分与第一馏分分离,并将富含钙的第一馏分用包含二氧化碳的气体碳酸化以形成沉淀碳酸钙和硝酸铵水溶液的悬浮液。 通过离心方式将沉淀物与硝酸铵水溶液分离,分离的重质二级馏分包含铁的富含重量百分数。

    高純度カルシウムの製造方法
    22.
    发明申请
    高純度カルシウムの製造方法 审中-公开
    生产高纯度钙的方法

    公开(公告)号:WO2013084672A1

    公开(公告)日:2013-06-13

    申请号:PCT/JP2012/079320

    申请日:2012-11-13

    Inventor: 高畑 雅博

    Abstract: ガス成分を除く純度が4N以下であるカルシウムの原料を、昇華容器のルツボに装入し、これを750°C~800°Cに加熱して昇華させ、これを昇華容器内の側壁に付着(蒸着)させて第1回目の昇華精製を行い、次にこの第1回目で昇華精製したカルシウムを回収した後、このカルシウムを再度昇華容器のルツボに装入し、750°C~800°Cに加熱して第2回目の昇華精製を行い、同様に昇華容器内の側壁に付着(蒸着)させて純度4N5以上のカルシウムを回収することを特徴とする高純度カルシウムの製造方法。高純度ランタンの製造に使用できるだけでなく、他の希土類等の還元剤、金属の脱硫剤又は脱酸剤、高真空ポンプ用ゲッターとして使用するための、高純度化したカルシウムを安定して提供できる技術を提供することを課題とする。

    Abstract translation: 本发明是一种高纯度的钙的制造方法,其特征在于:通过将不含气体成分的纯度除外的4%以下的钙原料引入坩埚中进行第一次升华和纯化 的升华容器,通过加热至750℃至800℃使起始材料升华,并使产物沉积(蒸发)到升华容器的内壁上; 然后,一旦恢复了经过第一升华和纯化的钙,通过再次将回收的钙再次引入升华容器的坩埚进行第二次升华和纯化,将钙加热至750-800℃,并使产物 类似地在升华容器的内壁上沉积(蒸发),从而回收纯度为4N5或更高的钙。 本发明的目的是提供一种可以稳定地获得已经达到高纯度的钙的技术,以便用于制备高纯度的镧,并且被用作 用于其他稀土元素的还原剂,脱硫剂或金属脱氧剂,以及作为高真空泵的吸气剂。

    SELECTIVE LEACH RECOVERY OF MINERALS FROM COMPOSITE ORES
    23.
    发明申请
    SELECTIVE LEACH RECOVERY OF MINERALS FROM COMPOSITE ORES 审中-公开
    从复合矿石中选择性的矿物矿物回收

    公开(公告)号:WO2011020181A1

    公开(公告)日:2011-02-24

    申请号:PCT/CA2010/001263

    申请日:2010-08-17

    Abstract: Calcium (Ca), manganese (Mn) and magnesium (Mg) carbonate plus lead (Pb) and zinc (Zn) sulphide minerals in a permeable host, crushed ore, concentrates or as mine discharge tailing are selectively solution mined (in-situ or ex-situ) with a selected acid e.g. acetic acid to extract Ca, Mn, and Mg followed by multivalent oxidizing salts e.g. ferric salts to extract Pb and Zn sequentially. For in-situ leaching, an inter relationship has been identified between pressure, temperature, target depth and leachate concentration such that carbonate leaching is performed in a manner to prevent carbon dioxide gas (CO 2 ) discharge thereby plugging host rock permeability avenues to preclude further leaching. This requires controlling the rate of acetic acid leaching to be in step with availability of solution to dissolve the resulting discharged CO 2 . Sulphide leaching is subsequently conducted on the carbonate-depleted host. The two resulting leachates are chemically treated to selectively recover extracted minerals as value added industrially ready products. The in situ method is particularly advantageous in preparing the high purity manganese products necessary for lithium ion batteries because it prevents occurrence of very fine metallic particles in the products that may happen during conventional mining. Alternatively, the in situ carbonate recovery steps can be independently employed; all in an environmentally friendly manner.

    Abstract translation: 选择性地开采了可渗透的主体,粉碎的矿石,浓缩物或排矿尾矿中的钙(Ca),锰(Mn)和镁(Mg)碳酸盐加铅(Pb)和锌(Zn) 用选择的酸例如 乙酸提取Ca,Mn和Mg,然后是多价氧化盐,例如 铁盐依次提取Pb和Zn。 对于原位浸出,已经确定了压力,温度,目标深度和渗滤液浓度之间的相互关系,使得碳酸盐浸出以防止二氧化碳气体(CO 2)排放的方式进行,从而堵塞主体岩石渗透性通道以排除进一步浸出 。 这需要控制乙酸浸出的速度与溶液的可用性一致,以溶解所产生的排出的CO 2。 硫酸盐浸出随后在碳酸盐贫乏的主体上进行。 化学处理两种生成的浸出液,以选择性回收提取的矿物质作为工业增值产品。 原位法在制备锂离子电池所需的高纯度锰产品方面特别有利,因为它防止在常规采矿过程中可能发生的产品中发生非常细小的金属颗粒。 或者,可以独立地使用原位碳酸盐回收步骤; 都以环保的方式。

    ELECTROSTATICALLY ENHANCED TRIBOCHEMICAL METHODS AND APPARATUS
    24.
    发明申请
    ELECTROSTATICALLY ENHANCED TRIBOCHEMICAL METHODS AND APPARATUS 审中-公开
    静电增强三化学方法和装置

    公开(公告)号:WO2004018717A9

    公开(公告)日:2004-09-30

    申请号:PCT/US0326394

    申请日:2003-08-21

    Abstract: A milling apparatus is modified by electrically insulating the milling chamber to enhance the efficiency of tribochemical reactions between reactive compositions during milling. The enhanced level of tribochemical reactivity is attributed to the buildup of electrostatic charge in and on the milled chamber during mill operation. The insulated mills in accordance with the invention can be used in a wide variety of commercial applications generally involving tribomechanically induced redox chemistry, including ore extraction, precious metal extraction, production of ferrites and pigments, and waste processing.

    Abstract translation: 研磨设备通过电绝缘研磨室来改进,以提高在研磨期间反应性组合物之间的摩擦化学反应的效率。 增加的摩擦化学反应性水平归因于在研磨操作期间在磨碎室中和其上的静电电荷的累积。 根据本发明的绝缘磨机可以用于通常涉及三重力学诱导的氧化还原化学的各种商业应用,包括矿石提取,贵金属提取,铁素体和颜料的生产以及废物处理。

    A method for isolating and purifying 90y from 90strontium in multi-curie quantities
    26.
    发明申请
    A method for isolating and purifying 90y from 90strontium in multi-curie quantities 审中-公开
    分离和净化90 from从90锶多方位数量的方法

    公开(公告)号:WO0180251A3

    公开(公告)日:2002-04-25

    申请号:PCT/US0112116

    申请日:2001-04-13

    CPC classification number: G21F9/007

    Abstract: The invention relates to a process for separating and purifying multi-curie quantities 90Y of sufficient chemical and radiochemical purity suitable for use in medical applications without a series of 90Sr selective extraction chromatographic columns while minimizing loss of radioactive 90Sr parent and waste stream. The process includes dissolving a nitrate salt of an original 90Sr stock solution in H¿2?O creating a strontium nitrate solution; acidifying the strontium nitrate solution containing ?90¿Y with concentrated nitric acid; evaporating the strontium nitrate solution; filtering or centrifuging strontium nitrate solution to separate crystalline 90Sr nitrate salt from the solution; evaporating the remaining 90Y enriched supernate to dryness; dissolving the remaining 90Y enriched supernate in a strong acid; passing the solution through an yttrium selective extraction chromatographic column; rinsing the yttrium selective extraction chromatographic column with strong acid; and eluting yttrium from yttrium selective extraction column with strong acid.

    리튬 추출 방법
    28.
    发明申请

    公开(公告)号:WO2021145488A1

    公开(公告)日:2021-07-22

    申请号:PCT/KR2020/000856

    申请日:2020-01-17

    Applicant: 전웅

    Abstract: 리튬 추출 방법에 대한 것으로, 알칼리 토금속을 포함하는 리튬 함유 용액을 준비하는 단계; 상기 리튬 함유 용액 내 알칼리 토금속의 활동도를 제어하는 단계; 및 상기 리튬 함유 용액에 인 공급 물질을 투입하여 인산 리튬을 석출시키는 단계;를 포함하는 리튬 추출 방법을 제공한다.

    用仲酰胺/烷烃复合溶剂从含钙卤水中分离钙提取锂的萃取体系、萃取方法和其应用

    公开(公告)号:WO2021088290A1

    公开(公告)日:2021-05-14

    申请号:PCT/CN2020/079080

    申请日:2020-03-13

    Applicant: 湘潭大学

    Abstract: 一种用仲酰胺/烷烃复合溶剂从含钙卤水中分离钙提取锂的萃取体系、萃取方法和其应用。萃取体系中含有仲酰胺和烷烃分别由其单一化合物或两种以上的混合物组成,分子中碳原子总数分别为12~18和9~18,萃取体系的凝固点小于0℃。在有机相与卤水相体积比1~10∶1、卤水密度为1.30~1.56g/cm3卤水pH值1~7和温度0~50℃下进行单级或多级逆流萃取,反萃取得到低钙锂比水相,经过浓缩、除杂与制备,分别得到氯化锂、碳酸锂和氢氧化锂。本发明的优异效果:仲酰胺萃取剂分子结构简单,容易生产,烷烃改进复合溶剂的粘度等性质;Li+多级萃取率高,锂钙分离系数大,用水反萃取酸碱消耗大大减少;萃取分离工艺流程短,萃取体系溶损小,适合于油田卤水开发。

    用仲酰胺/烷基醇复合溶剂从含钙卤水中分离钙提取锂和硼的萃取体系、萃取方法和其应用

    公开(公告)号:WO2021088285A1

    公开(公告)日:2021-05-14

    申请号:PCT/CN2020/079075

    申请日:2020-03-13

    Applicant: 湘潭大学

    Abstract: 一种用仲酰胺/烷基醇复合溶剂从含钙卤水中分离钙提取锂和硼的萃取体系、萃取方法和其应用。萃取体系中含有仲酰胺和烷基醇分别作为萃取锂和硼的萃取剂由其单一化合物或两种以上的混合物组成,分子中碳原子总数分别为12~18和8~20,萃取体系的凝固点小于0℃。在有机相与卤水相体积比1~10∶1、卤水密度为1.30~1.56g/cm 3、卤水pH值0~7和温度0~50℃下进行单级或多级逆流萃取,反萃取得到低钙锂比水相,经过浓缩、除杂与制备,分别得到氯化锂、碳酸锂、氢氧化锂和硼酸。本发明的仲酰胺分子结构简单,由烷基醇改进的复合溶剂能同时萃取锂和硼;多级萃取率高,用水反萃取,酸碱消耗大大减少;萃取分离流程缩短,萃取体系溶损小,适合油田卤水开发。

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