CN100339318C - 从水流中除去砷的方法 - Google Patents

从水流中除去砷的方法 Download PDF

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CN100339318C
CN100339318C CNB2004800030181A CN200480003018A CN100339318C CN 100339318 C CN100339318 C CN 100339318C CN B2004800030181 A CNB2004800030181 A CN B2004800030181A CN 200480003018 A CN200480003018 A CN 200480003018A CN 100339318 C CN100339318 C CN 100339318C
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water
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CN1745038A (zh
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理查德·D·威瑟姆
爱德华·B·麦克纽
约翰·L·伯巴三世
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Molycorp Minerals LLC
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
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    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/28Treatment of water, waste water, or sewage by sorption
    • C02F1/281Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/52Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
    • C02F1/5236Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/58Treatment of water, waste water, or sewage by removing specified dissolved compounds
    • C02F1/62Heavy metal compounds
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    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/72Treatment of water, waste water, or sewage by oxidation
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    • C02F1/28Treatment of water, waste water, or sewage by sorption
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02F1/42Treatment of water, waste water, or sewage by ion-exchange
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2305/00Use of specific compounds during water treatment
    • C02F2305/12Inert solids used as ballast for improving sedimentation
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00Multistage treatment of water, waste water or sewage
    • YGENERAL 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
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    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S210/00Liquid purification or separation
    • Y10S210/902Materials removed
    • Y10S210/911Cumulative poison

Abstract

通过下述方法从水和其他含水物料中除去砷:(1)用含+4氧化态铈的化合物,优选二氧化铈处理物料,以将+3氧化态的砷氧化成+5氧化态的砷,和(2)通常通过使处理过的物料和氧化铝或含+3氧化态阳离子的其他沉淀剂接触,从水相中除去+5氧化态的砷。

Description

从水流中除去砷的方法
相关申请的交叉参考
本申请要求享有美国专利申请No.10/353,705(2003年1月29日提交)的优先权,并且成为美国部分连续(CIP)专利申请,其整体内容通过引用并入本文。
背景技术
本发明主要涉及从水流中除去砷的方法、组合物和装置,具体涉及使用+4氧化态铈使砷氧化以使其能够从水中沉淀出来,从而从地下水和饮用水中除去砷的方法、组合物和装置。
砷是以各种组合形式天然存在于地表的有毒元素。例如,其在天然水中的存在可以源自地球化学反应、工业废物排放和过去含砷杀虫剂的农业应用。由于高水平砷的存在会对生命体具有致癌作用和其他有害作用,因此美国环保局(EPA)和世界卫生组织已规定饮用水中砷的最大污染水平(MCL)为每10亿份中含10份(ppb)。废水、地下水、地表水和地热水中的砷浓度经常超过该水平。因此,当前的MCL和可低至2.0ppb的任何未来MCL的降低产生了对从饮用水、井水和工业用水中经济有效地除去砷的新技术的需求。
砷存在有四种氧化态或价态,即-3、0、+3和+5。在正常情况下,发现+3和+5氧化态的砷,通常以亚砷酸盐(AsO2 -1)和砷酸盐(AsO4 -3)的形式溶解于含水或水生体系中。通过混凝(coagulation)技术有效地除去砷需要砷为砷酸盐形式。砷以+3氧化态存在的亚砷酸盐仅能通过吸附混凝技术部分除去,这是因为其主要形式亚砷酸(HAsO2)是弱酸,在最有效发生吸附的pH5-pH8条件下它仍保持非离子化状态。
过去已使用了多种技术来从含水体系中除去砷。这些技术的实例包括在高表面积材料如氧化铝和活性碳上的吸附、使用阴离子交换树脂的离子交换、共沉淀和电渗析。但是,大多数除砷技术都由于除去亚砷酸盐的困难而受阻。已经用于大型市政供水的更成功技术对于住宅应用来说不实用,因为需要大的空间和使用危险化学品。用于住宅水处理的两种最常见的技术是反渗透和活化氧化铝。前一方法产生必须加以处理的含砷废水流,后一方法需要使用腐蚀性化学品。
结合上述事实和将MCL降低至2-10ppb的可能性,有必要开发从水和其他含水体系中除去砷的有效方法、组合物和装置。
发明内容
根据本发明,目前已发现通过下述方法可以高效地从水和其他含水物料中除去砷:用含+4氧化态铈的化合物,优选二氧化铈(CeO2)处理含砷的水物料,以将砷氧化,从而使其更易于通过沉淀法从处理过的含水物料中除去,从而生成砷浓度减小的净化含水液体。本文所用的“沉淀法”不仅包括除去不可溶物质形式的含砷离子,还包括将含砷离子固定在不溶性颗粒之上或内部。在本发明方法的一个实施方案中,使含有溶解的+3和+5氧化态砷的水或其他含水液体与二氧化铈接触,以将+3氧化态的砷氧化成+5氧化态的砷,并使该液体接触与+5氧化态的砷反应的沉淀剂,以产生不溶性砷化合物和砷含量减小的含水液体,从而从含水液体中除去+5氧化态的砷。
通常,氧化的砷为+5氧化态,以砷酸盐(AsO4 -3)的形式溶解于水或其他含水液体中。用于从含水液体中除去氧化的砷的沉淀剂可以是与砷酸盐或其他形式的氧化的砷反应产生不溶性砷化合物的任意物质。例如,沉淀剂可以是在+4氧化态铈被还原时的砷氧化步骤中产生的+3氧化态铈。作为选择,沉淀剂可以是含+3氧化态阳离子的任意颗粒固体,如氧化铝、铝硅酸盐、离子交换树脂和粘土。
氧化和沉淀步骤可以在同一或分隔的区中进行。如果这些步骤在同一区中进行,则含+4氧化态铈的化合物通常与沉淀剂混合。虽然该混合物可以通过将铈化合物负载在沉淀固体的表面上和/或微孔中而制造,但是通常优选的是将颗粒形式的铈化合物与沉淀剂颗粒物理混合。本发明的优选组合物包括二氧化铈和氧化铝的混合物。
在本发明方法的一个优选实施方案中,所述的处理所述含水物料和所述的除去所述氧化的砷都发生在所述的氧化区中,具体而言,使含砷酸盐和亚砷酸盐形式的溶解砷的含水液体与二氧化铈颗粒和氧化铝颗粒的混合物在氧化区中接触,从而使二氧化铈将亚砷酸盐氧化成砷酸盐,并使氧化铝与砷酸盐反应以形成吸附在氧化铝颗粒上的不溶性砷酸铝。流出氧化区的含水溶液所含砷的浓度大大减小,通常小于约2.0ppb。
具体实施方式
虽然本发明的方法主要设想用于从饮用水和地下水中除去溶解的砷,但是可以理解:该方法可以用来处理砷含量不合需要的任何含水液体物料。这些液体物料的实例尤其包括井水、地表水诸如来自湖泊、池塘和湿地的水、农业用水、来自工业生产过程的废水和地热流体。含砷物料还可以包含其他无机污染物,如硒、镉、铅和汞,以及某些有机污染物。通常,本发明的方法可用来处理砷含量大于2.0ppb的任何含水液体物料,并且可以有效地处理砷含量大于500ppb的物料。该方法可有效地将这些物料中的砷水平降至5.0ppb以下,通常是2.0ppb以下。
污染含水物料的砷通常溶解于水相,且通常以分别为亚砷酸盐(AsO2 -1)和砷酸盐(AsO4 -3)的+3和+5氧化态存在。除去砷酸盐的技术是现有的,并且是相当有效的,但是除去亚砷酸盐比较困难,这是因为用于此目的的现有技术都不是很有效。已经发现:通过用+4氧化态铈处理含水物料,可以容易地将基本上所有溶解的亚砷酸盐氧化成砷酸盐,所得的砷酸盐和原本就存在于含水物料中的砷酸盐一起从处理过的物料中沉淀出来,从而产生砷减少的含水液体。
在本发明的方法中,将被砷污染的含水物料在通常为使物料中的水保持为液态的环境温度和环境压力下,通过进口进入氧化容器。如果物料被颗粒固体污染,那么通常在进入氧化容器之前进行处理以除去该固体。可以采用诸如过滤、离心和水力旋流的任何液-固分离技术除去颗粒固体。
在氧化容器中,使含水物料与含+4氧化态铈(下文中称作铈+4)的化合物接触,其中Ce+4是极强的氧化剂,可以将任何亚砷酸盐或以+3氧化态存在的其他砷氧化成砷酸盐或含有+5氧化态砷的其他物质。然后通过将氧化的含水物料与沉淀剂接触,使所有含+5氧化态砷的砷物质从水相中沉淀出来。
氧化剂可以是含+4氧化态铈的任何固体或液体。虽然通常优选使用不溶于水、较耐磨的二氧化铈固体颗粒作为氧化剂,但也可使用水溶性的铈化合物。这些化合物的实例包括硝酸高铈铵、硫酸高铈铵、硫酸高铈和硝酸高铈。
与含+5氧化态砷的砷酸盐反应形成不溶性砷化合物的沉淀剂可以和铈4+化合物共存于氧化容器中,从而使沉淀和氧化基本上同时发生。作为选择,可将沉淀剂置于经处理的液体离开氧化容器后所进入的分离容器中。简单起见,铈化合物和沉淀剂通常都优选共存于氧化容器中。本发明的该实施方案不需要额外容器,因此降低了本发明方法的安装和操作成本。
虽然沉淀剂可以是与含+5氧化态砷的砷酸盐或其他物质反应形成不溶性砷化合物的任何固体或液体材料,,但通常是含有+3氧化态阳离子的颗粒固体,所述的阳离子与砷酸盐反应形成不溶性砷酸盐化合物。含+3氧化态阳离子的这些固体的实例包括氧化铝、γ-氧化铝、活化氧化铝、酸化氧化铝如经盐酸处理的氧化铝、含不稳定阴离子的金属氧化物如氯氧化铝、结晶铝硅酸盐如沸石、无定形二氧化硅-氧化铝、离子交换树脂、粘土如蒙脱土、硫酸铁、多孔陶瓷和含+3氧化态铈的铈化合物如碳酸铈。优选地,所述的砷沉淀剂包括颗粒固体,其含有选自氧化铝、离子交换树脂、结晶铝硅酸盐、粘土和多孔陶瓷的+3氧化态阳离子。虽然可以将氧化镧和其他稀土化合物用作沉淀剂,但在本发明方法中通常不采用这些材料(当然除铈化合物之外),这是因为优选使用具有比稀土化合物更小的Ksp的沉淀剂。因此,在本发明方法的一个优选实施方案中,所述的处理所述含水物料和所述的除去所述氧化的砷在基本不存在镧的条件下进行。
如上所述,通常优选的是,铈+4化合物和沉淀剂共存于氧化容器中,从而使砷的氧化和沉淀在同一容器中基本同时进行。虽然铈+4化合物和沉淀剂都可以是水溶性的,但通常优选铈+4化合物和沉淀剂都是不溶于水的颗粒固体,其在氧化容器中与含水物料形成悬浮液,或在氧化步骤期间一起物理混合在含水物料所流经的固定床中。在本发明的可供选择的实施方案中,铈+4化合物可以沉淀在固体沉淀剂的表面和/或微孔中。该实施方案通常并不优于物理混合物,因为将铈化合物负载在沉淀固体上或内部需要将铈化合物溶解于液体中,然后将所得溶液与负载固体混合,并干燥该湿固体。这些步骤明显增加了实施本发明方法的成本。因此,本发明还提供一种组合物,其包含二氧化铈CeO2和颗粒固体的混合物,其中所述的二氧化铈不负载在所述的颗粒固体上。在一个实施方案中,所述组合物基本不含镧。在另一个实施方案中,所述组合物基本不含铈以外的所有稀土元素。
通常,足量的铈+4化合物和颗粒沉淀剂一起存在于氧化容器中,从而使二者的混合物含有约8-60重量%的铈+4化合物,以氧化物计。优选的是,所述混合物含有约10-50重量%,更优选约20-30重量%的铈+4化合物,以氧化物计。但是,在某些情况下,会需要混合物含有40-45重量%以上的铈+4化合物,以氧化物计。
不论铈+4化合物是与颗粒沉淀剂一起混合在氧化容器中,或是负载在沉淀剂之上或内部,该固体的直径通常为约0.25-1.5毫米,优选为0.5-1.0毫米。当铈+4化合物和沉淀剂存在于作为固定床的氧化区时,通常优选颗粒为球形,以使含水物料经过床的流动均匀分布。但是,如果需要的话,颗粒可以是包括压出物形状的其他形状。这些压出物的长度通常为约0.2-约3.0毫米。
在本发明方法的氧化步骤中,含水物料中的亚砷酸盐根据下列方程式氧化成砷酸盐:
                Ce+4+AsO2 -1→Ce+3+AsO4 -3
当铈+4化合物氧化亚砷酸盐时,其自身被还原成+3氧化态的铈,然后与氧化步骤中形成的砷酸盐反应生成不溶性的砷酸铈,如下列方程式所示:
                Ce+3+AsO4 -3→CeAsO4(固体)
虽然理论上有足量的由铈+4还原形成的铈+3和氧化反应中形成的所有砷酸盐反应以沉淀砷酸盐,但通常优选存在额外的沉淀剂。使可以是含铈+3的化合物的沉淀剂与任何未反应的砷酸盐反应以形成不溶性的沉淀物,将该沉淀物从含水物料中除去,以产生所需的砷减少的含水液体。
发生在氧化容器中的氧化步骤通常在环境压力、约4℃-100℃、优选约5℃-40℃的温度下以及pH大于约3.0的条件下进行。含水物料在氧化容器中的停留时间通常为约2.0-约30分钟。当铈+4化合物和砷沉淀剂均为固体颗粒并一起作为氧化容器中的固定床存在时,沉淀的砷化合物将被沉淀剂的固体颗粒吸附,或通过其他方式与之结合,从而使流出氧化容器的含水液体基本不含固体并几乎不含砷,砷含量通常小于约10ppb,绝大多数情况下小于2.0ppb。如果沉淀剂不在氧化容器中,则使来自容器的流出物流到另一容器,在此单独用砷沉淀剂加以处理。最后,如果铈+4化合物和沉淀剂是与氧化容器中的含水物料形成悬浮液的颗粒固体,则通常处理来自容器的流出物以将固体从砷减少的液体中分离,所述的固体包括容器中形成的不溶性砷化合物。虽然分离可以在能够从液体中除去颗粒的任何类型装置中进行,但通常采用过滤系统进行。
如果本发明方法的含水物料含有除砷以外的必须除去以生成所需净化的含水产物的其他污染物,则这些污染物的去除通常在氧化步骤之前或之后进行。如果其他污染物干扰砷的氧化,则它们应该在氧化步骤之前除去。在某些情况下,本发明的方法对于从含水物料中除去砷和其他污染物或砷以外的其他污染物而言也是有效的。
在本发明的优选实施方案中,使用带有滤筒或滤器的砷净化装置来处理住宅饮用水。处理装置可以是带有含本发明组合物的过滤器装置或设计来配置在水槽下方的滤筒型装置的自立式容器。这些装置的安置应使进入家庭或商业场所的水在进入水槽龙头之前流经滤器或滤筒。该滤器和滤筒装置非常简单,包括入口,其与饮用水源相连;滤器或滤筒,其含有铈+4氧化剂,所述氧化剂通常为固定床形式并与砷沉淀剂形成混合物;和出口,其与水槽龙头相通,以将流出滤筒或滤器的砷减少的饮用水引向龙头的入口。作为选择,滤筒或滤器型装置可以设计来配置在龙头上,从而使流出龙头的水在使用之前流经滤筒或滤器装置。
在滤器或滤筒中,+3氧化态的砷被氧化成+5氧化态的砷,并且基本上所有存在的溶解的砷+5都与+3氧化态铈和砷沉淀剂反应,形成吸附到固定床固体上的不溶性砷化合物。沉淀剂优选为氧化铝或者离子交换树脂。流出固定床和滤筒或滤器装置出口的流出物的砷浓度通常小于约2.0ppb。在一个滤筒或滤器装置中的固定床被砷饱和后,将滤筒或滤器更换为具有相同或相似设计的新的滤筒或滤器。然后将用过的滤筒或滤器以法律上许可的方式加以处理。
在另一个实施方案中,本发明的方法用在社区水处理设施中,以在将水分配到当地家庭和商业区之前从饮用水中除去砷。对于这种应用,铈+4氧化剂通常以悬浮液形式或固定床形式存在于大型储水池中,从而可以以连续或间歇方式处理较大量的含砷水。砷沉淀剂可以和铈+4氧化剂共存于储水池中,或存在于由来自储水池的流出物进料的单独容器中。该过程流出的水的砷浓度通常小于约10ppb,一般小于5.0ppb,优选小于2.0ppb。
下面的实施例进一步说明了本发明的性质和目的,其只是说明性的,并不如权利要求书那样限定本发明。该实施例表明使用二氧化铈可以将+3和+5氧化态的砷从水中完全除去。
实施例
通过将检验合格的+3和+5氧化态砷标准溶液和不含砷的自来水混合,制备测试溶液来模拟含砷地下水。将20克氧化镧(La2O3)、20克二氧化铈(CeO2)和10克氧化镧与10克二氧化铈的混合物分别装入密封的100毫升玻璃容器中,并与约96毫升含100ppb砷+3、100ppb砷+5和均为50ppb的砷+3与砷+5的测试溶液形成悬浮液。将所得的悬浮液用具有Taflon涂层的磁力搅拌棒搅拌15分钟。搅拌后,通过Whatman#41滤纸过滤使自来水与固体分离,并将自来水密封在125毫升塑料样品瓶中。然后将该瓶送到合格的饮用水分析实验室,在那里通过石墨炉原子吸收光谱测定每个样品中的砷含量。测试结果如表1所示。
                                    表1
  测试号     测试前水中的砷   成浆材料百分数  测试后水中的砷ppb  除砷百分数
    ppbAs+3     ppbAs+5
    12345678     05050505010000     05050505001000     00100%La2O3100%CeO250%La2O350%CeO250%La2O350%CeO250%La2O350%CeO250%La2O350%CeO2     01004500000     NA055100100100100NA
表中测试3的数据表明:当只使用氧化镧时,只除去了掺杂砷的自来水中存在的55%的砷。由于含砷+5的砷酸镧的溶解性非常小,因此认为保留在溶液中的砷主要是亚砷酸盐形式的砷+3。另一方面,测试4的结果表明二氧化铈可以从水中除去所有的砷。这些结果的不一致是由于铈在二氧化铈中以+4氧化态存在,并且其是强氧化剂,而氧化镧中以+3氧化态存在的镧不是氧化剂。虽然镧+3与+5氧化态的砷反应,使之从水中沉淀,但是镧不与+3氧化态的砷反应。二氧化铈中的铈将砷+3氧化成砷+5,然后砷+5与铈+4还原所形成的铈+3反应从而沉淀所有溶解在水中的砷。测试5-7表明二氧化铈和氧化镧的等量混合物也可以从自来水中有效除去所有的砷。
本申请公开了通过下述方法从水和其他含水物料中除去砷:(1)用含+4氧化态铈的化合物,优选二氧化铈处理物料,以将+3氧化态砷氧化成+5氧化态砷,和(2)通常通过使处理过的物料与含+3氧化态阳离子的氧化铝或其他沉淀剂接触,从水相中除去+5氧化态的砷。
虽然本发明是参照本发明的几个实施方案进行描述的,但显然根据上文的描述进行许多更改、改进和变化对于本领域的技术人员来说是显而易见的。因此,本发明还包括在不背离所附权利要求的实质和范围的条件下所做的所有更改、改进和变化。
申请人现在或将来有权要求保护或不要求保护本文所公开的任意特征、特征组合或特征亚组合。
本发明中所列的所有数值和定量测定值(包括说明书、权利要求书、摘要、附图和任何附录中的)都是近似值。
在不存在本文未具体公开或要求保护的任何要素的情况下,可适合实施本文中说明性公开或要求保护的发明。因此,本发明可以包括本文公开或要求保护的要素,由本文公开或要求保护的要素组成或基本上由本文公开或要求保护的要素组成。
所附权利要求具有与本申请相一致的尽可能宽的范围。权利要求没有必要局限于优选的实施方案或实施例中所示的实施方案。
本申请中引用或参考的所有专利、优先提交的专利申请和任何其他文献和印刷物都整体通过引用并入本文。

Claims (44)

1.一种从含水物料中除去砷的方法,包括:
用含有足量铈的化合物处理所述含水物料,以氧化所述的砷;和
从所述处理过的含水物料中除去所述氧化的砷。
2.权利要求1所述的方法,其中所述足量的铈是+4氧化态,以氧化所述砷,从而将所述铈还原为+3氧化态;和其中所述的从所述处理过的含水物料中除去所述氧化的砷,是通过所述含水物料与颗粒状砷沉淀剂接触来形成与所述含水物料相比砷浓度减小的含水液体,所述砷沉淀剂含有与所述氧化的砷反应形成不溶性砷化合物的离子。
3.权利要求2所述的方法,其中所述含+4氧化态铈的化合物负载在所述颗粒状砷沉淀剂上。
4.权利要求2所述的方法,其中所述含+4氧化态铈的化合物与所述颗粒状砷沉淀剂混合。
5.权利要求2所述的方法,其中所述颗粒状砷沉淀剂包含氧化铝。
6.权利要求4所述的方法,其中所述含+4氧化态铈的化合物与所述颗粒状砷沉淀剂的组合包含作为氧化物计算的10重量%-50重量%的所述含+4氧化态铈的化合物。
7.一种从含水物料中除去砷的方法,包括下述步骤:
用含足量+4氧化态铈的化合物处理氧化区中的所述含水物料,以氧化所述砷,从而将所述铈还原为+3氧化态;和
从所述处理过的含水物料中通过沉淀法除去所述氧化的砷,以形成与所述含水物料相比砷浓度减小的净化含水液体。
8.权利要求7所述的方法,其中所述含水物料中的+3氧化态砷在所述的氧化区中被氧化成+5氧化态的砷。
9.权利要求8所述的方法,其中所述含水物料中的亚砷酸盐AsO2 -1在所述氧化区中被氧化成砷酸盐AsO4 -3
10.权利要求7所述的方法,其中所述的含铈化合物是颗粒固体。
11.权利要求10所述的方法,其中所述的含铈化合物包括二氧化铈CeO2
12.权利要求7所述的方法,其中所述的处理所述含水物料和所述的除去所述氧化的砷都发生在所述氧化区中。
13.权利要求9所述的方法,其中通过使所述的砷酸盐AsO4 -3与所述的+3氧化态铈反应产生不溶性的砷酸铈,而将所述砷酸盐从所述的含水物料中除去。
14.权利要求7所述的方法,其中通过使所述的含水物料和含有与所述氧化的砷反应形成不溶性砷化合物的离子的砷沉淀剂接触,而将所述氧化的砷从所述的含水物料中除去。
15.权利要求14所述的方法,其中所述的砷沉淀剂包括颗粒固体,其含有选自氧化铝、离子交换树脂、结晶铝硅酸盐、粘土和多孔陶瓷的+3氧化态阳离子。
16.权利要求15所述的方法,其中所述的处理所述含水物料和所述的除去所述氧化的砷都发生在所述的氧化区中。
17.权利要求14所述的方法,其中含+3氧化态阳离子的所述砷沉淀剂与含+4氧化态铈的所述铈化合物共存于所述的氧化区中。
18.权利要求7所述的方法,其中所述的处理所述含水物料和所述的除去所述氧化的砷在不存在镧的条件下进行。
19.权利要求7所述的方法,其中处理所述含水物料于5℃-40℃的温度下在所述氧化区中进行。
20.权利要求7所述的方法,其中所述的含水物料选自地下水、饮用水、工业废水、农业用水、湖水、湿地水和地热水。
21.权利要求7所述的方法,其中所述净化的含水液体中的砷浓度小于10ppb。
22.权利要求10所述的方法,其中所述的含铈颗粒固体以固定床或悬浮体的形式存在于所述的氧化区中。
23.一种从含水物料中除去砷的方法,包括下述步骤:
用二氧化铈CeO2在氧化区中处理所述的含水物料,以将氧化态小于+5的砷氧化成+5氧化态的砷;和
通过使所述氧化区中的所述处理过的物料和与所述+5氧化态砷反应形成不溶性砷化合物的颗粒固体接触,来从所述处理过的含水物料中除去+5氧化态砷,从而形成与所述含水物料相比砷浓度减小的净化含水液体。
24.权利要求23所述的方法,其中所述的二氧化铈CeO2负载在所述的颗粒固体上。
25.权利要求23所述的方法,其中所述的二氧化铈CeO2与所述的颗粒固体混合。
26.权利要求23所述的方法,其中亚砷酸盐AsO2 -1形式的+3氧化态砷在所述氧化区中被氧化成砷酸盐AsO4 -3形式的+5氧化态砷。
27.权利要求26所述的方法,其中所述的颗粒固体包含氧化铝。
28.权利要求23所述的方法,其中所述的处理所述含水物料和所述的除去砷在不存在镧的条件下进行。
29.权利要求25所述的方法,其中所述二氧化铈CeO2和所述颗粒固体的组合含有10重量%-50重量%的二氧化铈CeO2,以氧化物计。
30.权利要求23所述的方法,其中所述净化的含水液体中砷的浓度小于2.0ppb。
31.一种组合物,其包含二氧化铈CeO2和颗粒固体的混合物,其中所述的二氧化铈不负载在所述的颗粒固体上。
32.权利要求31所述的组合物,其中所述颗粒固体含有+3氧化态的阳离子。
33.权利要求32所述的组合物,其中所述的颗粒固体包含氧化铝。
34.权利要求33所述的组合物,其不含镧。
35.权利要求33所述的组合物,其不含铈以外的所有稀土元素。
36.权利要求33所述的组合物,其中所述混合物中的所述颗粒固体直径为0.5-1.0毫米。
37.一种从饮用水中除去砷的装置,包括:
入口,其与所述饮用水源相通;
容器,其含有二氧化铈CeO2,并与所述入口相通;和
出口,其与所述容器相通。
38.权利要求37所述的装置,其中所述含有二氧化铈CeO2的容器还包括:
入口部分和出口部分,所述的入口部分与所述入口相通;和
出口,其与所述容器的所述出口部分相通。
39.权利要求38所述的装置,其中所述的容器含有与颗粒固体结合的二氧化铈CeO2,所述的颗粒固体与+5氧化态砷反应形成不溶性砷化合物。
40.权利要求39所述的装置,其中所述的容器包括含所述二氧化铈CeO2的滤筒,并且所述的装置设计用来配置在水槽下面或龙头的出口之上。
41.权利要求39所述的装置,其中所述的容器包括含所述二氧化铈CeO2的槽。
42.权利要求41所述的装置,其中含有固体的容器包括含+4氧化态铈的化合物与颗粒状砷沉淀剂,所述颗粒状砷沉淀剂与+5氧化态的砷反应形成不溶性砷化合物,其中所述容器具有进口部分和出口部分并且所述进口部分与所述入口相通;和出口,其与所述容器的出口部分相通。
43.权利要求42所述的装置,其中所述含+4氧化态铈的化合物包含二氧化铈CeO2
44.权利要求43所述的装置,其中所述容器包含含有所述二氧化铈CeO2的筒或滤器,并且所述装置设计为装配在水槽下方或龙头出口上。
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