JP2007054818A - Method for treating water polluted with selenium and agent therefor - Google Patents
Method for treating water polluted with selenium and agent therefor Download PDFInfo
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本発明は、工場排水や下水、河川水など各種の汚染水に含まれるセレンを鉄粉等に接触させて還元し、析出除去する処理方法において、セレンの還元析出効果に優れており、処理後のセレン濃度を環境基準値以下に容易に低減することができるセレン含有汚染水の処理方法に関する。 The present invention is excellent in the reduction and precipitation effect of selenium in a treatment method in which selenium contained in various polluted water such as factory effluent, sewage and river water is brought into contact with iron powder to reduce and precipitate and is removed. The present invention relates to a method for treating selenium-containing contaminated water that can easily reduce the selenium concentration of the selenium to an environmental standard value or less.
セレンは環境汚染物質であり、従来から排水中のセレンを除去する方法が知られている。例えば、特開平07−2502号公報(特許文献1)には、セレンおよび(または)セレン化合物を含む排液を鉄または鉄系金属に接触させて、鉄または鉄系金属の表面にセレンを析出させて排液中のセレン濃度を低減するセレンおよび(または)セレン化合物含有排液の処理方法が記載されている。 Selenium is an environmental pollutant, and a method for removing selenium in wastewater has been conventionally known. For example, in Japanese Patent Application Laid-Open No. 07-2502 (Patent Document 1), selenium is deposited on the surface of iron or iron-based metal by contacting a drainage liquid containing selenium and / or a selenium compound with iron or iron-based metal. A method for treating selenium and / or selenium compound-containing effluents that reduces the selenium concentration in the effluents is described.
また、特願平09−47790号公報(特許文献2)には、排煙脱硫水を鉄、マンガン、ニッケル、および銅から選ばれた少なくとも1種の金属に接触させることによって、排水中の酸化性物質およびセレンを沈殿化して除去する処理方法が記載されている。
特許文献1の処理方法では、純鉄に限らず、鉄系金属としてクロム含有量が12.5%以下の鉄クロム合金を用いることが示されているが、その他の合金成分については記載されていない。また、特許文献2の処理方法では、鉄以外に、マンガン、ニッケル、および銅を用いることが記載されているが、その他の金属については言及されておらず、さらに、何れの処理方法においても、鉄に含有される他の金属成分の種類および含有量とセレンの除去効果との関係は知られていない。さらに、特許文献2の処理方法では排水の酸性が強いとマンガンやニッケル、銅が可溶化するので、これらの金属による汚染を生じる問題がある。 In the treatment method of Patent Document 1, it is shown that an iron-chromium alloy having a chromium content of 12.5% or less is used as an iron-based metal, not just pure iron, but other alloy components are described. Absent. Further, in the treatment method of Patent Document 2, it is described that manganese, nickel, and copper are used in addition to iron, but other metals are not mentioned, and in any treatment method, The relationship between the type and content of other metal components contained in iron and the effect of removing selenium is not known. Furthermore, in the treatment method of Patent Document 2, manganese, nickel, and copper are solubilized when the acidity of the wastewater is strong, so that there is a problem of causing contamination by these metals.
本発明は、工場排水や下水、河川水など各種の排水等に含まれているセレンを鉄粉等に接触させて還元析出させる処理方法において、使用する鉄粉等の成分に注目し、アルミニウム等を少量含有する鉄粉等のセレン除去効果が優れていることを見い出し、この知見に基づいてセレン含有水の処理効果を高めたものであり、マンガンやニッケル、銅などによる二次的な金属汚染を生じる懸念がなく、セレンの除去効果に優れた処理方法を提供する。 The present invention focuses on components such as iron powder to be used in a treatment method for reducing and precipitating selenium contained in various wastewaters such as factory wastewater, sewage, river water, etc. Based on this finding, it has been found that the effect of removing selenium such as iron powder containing a small amount of iron is excellent, and the effect of treating selenium-containing water has been enhanced. Secondary metal contamination by manganese, nickel, copper, etc. A processing method that is excellent in the effect of removing selenium is provided.
本発明は、以下の構成を有するセレン含有汚染水の処理方法に関する。
(1)汚染水を鉄粉微粒子に接触させて汚染水に含まれる重金属類を還元し析出させて除去する処理方法において、アルミニウム0.1重量%以上、カルシウム0.05重量%以上、およびチタン0.05重量%以上を含有する鉄粉微粒子を用い、この鉄粉微粒子にセレンを含有する汚染水を接触させてセレンを還元析出させて除去することを特徴とするセレン含有汚染水の処理方法。
(2)アルミニウム0.1重量%以上、カルシウム0.05重量%以上、およびチタン0.05重量%以上を含有する鉄粉微粒子に、密閉反応槽の非酸化性雰囲気下および弱酸性下で、セレンを含有する汚染水を接触させる上記(1)に記載するセレン含有汚染水の処理方法。
(3)処理前のセレン濃度0.05〜0.5mg/Lのセレン含有汚染水について、処理後のセレン濃度を環境基準値(0.01mg/L)以下に低減する上記(1)または上記(2)に記載するセレン含有汚染水の処理方法。
(4)アルミニウム0.1重量%以上、カルシウム0.05重量%以上、およびチタン0.05重量%以上を含有する鉄粉微粒子からなる水処理剤。
(5)アルミニウム0.1重量%以上、カルシウム0.05重量%以上、およびチタン0.05重量%以上を含有し、50%累積粒子径が30〜80μm、および最頻粒子径が30〜150μmである鉄粉微粒子からなる上記(4)の水処理剤。
The present invention relates to a method for treating selenium-containing contaminated water having the following configuration.
(1) In a treatment method in which contaminated water is brought into contact with iron fine particles to reduce and precipitate heavy metals contained in the contaminated water, 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and titanium A method for treating selenium-containing contaminated water, comprising using iron powder fine particles containing 0.05% by weight or more, bringing the iron powder fine particles into contact with contaminated water containing selenium, and reducing and precipitating selenium. .
(2) Iron powder fine particles containing 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05% by weight or more of titanium, in a non-oxidizing atmosphere and weakly acidic in a closed reaction tank, The method for treating selenium-containing contaminated water as described in (1) above, wherein contaminated water containing selenium is brought into contact.
(3) For selenium-containing contaminated water having a selenium concentration of 0.05 to 0.5 mg / L before treatment, the selenium concentration after treatment is reduced to the environmental standard value (0.01 mg / L) or less (1) or above The method for treating selenium-containing contaminated water as described in (2).
(4) A water treatment agent comprising iron powder fine particles containing 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05% by weight or more of titanium.
(5) 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05% by weight or more of titanium, 50% cumulative particle size of 30 to 80 μm, and mode particle size of 30 to 150 μm The water treatment agent according to (4), comprising iron powder fine particles.
本発明の処理方法によれば、工場排水や下水、河川水など各種の汚染水に含まれるセレンの除去効果を高めることができる。具体的には、例えば、処理前のセレン濃度0.05〜0.5mg/Lのセレン含有汚染水について、処理後のセレン濃度を環境基準値(0.01mg/L)以下に低減することができる。 According to the treatment method of the present invention, the effect of removing selenium contained in various polluted waters such as factory waste water, sewage, and river water can be enhanced. Specifically, for example, for selenium-containing contaminated water having a selenium concentration of 0.05 to 0.5 mg / L before treatment, the selenium concentration after treatment may be reduced to an environmental standard value (0.01 mg / L) or less. it can.
本発明の処理方法は、特定量のアルミニウム、カルシウム、およびチタンを含有する鉄粉微粒子にセレンを含有する汚染水を接触させてセレンを還元処理する方法であるので、特別な装置を必要とせず、また、常温で処理することができるので、容易に実施することができる。 Since the treatment method of the present invention is a method of reducing selenium by bringing contaminated water containing selenium into contact with iron powder fine particles containing specific amounts of aluminum, calcium, and titanium, no special equipment is required. Moreover, since it can process at normal temperature, it can implement easily.
本発明の処理方法は、汚染水を鉄粉微粒子に接触させて汚染水に含まれる重金属類を還元し析出させて除去する処理方法において、アルミニウム0.1重量%以上、カルシウム0.05重量%以上、およびチタン0.05重量%以上を含有する鉄粉微粒子を用い、この鉄粉微粒子にセレンを含有する汚染水を接触させてセレンを還元析出させて除去することを特徴とするセレン含有汚染水の処理方法である。 The treatment method of the present invention is a treatment method in which contaminated water is brought into contact with iron powder fine particles to reduce and precipitate heavy metals contained in the contaminated water, and is 0.1% by weight or more of aluminum and 0.05% by weight of calcium. The selenium-containing contamination is characterized by using iron powder fine particles containing 0.05% by weight or more of titanium and bringing the iron powder fine particles into contact with contaminated water containing selenium and reducing and precipitating selenium. Water treatment method.
本発明の処理方法において、汚染水とは重金属類を含む水を広く意味し、自然発生的および人為的に生じた各種の廃水や排水等を含み、例えば、工場排水や下水、海水、河川水、沼や湖池の水、地表の溜り水、河川等の堰止域の水、地下の流水や溜り水、暗渠の水などであって重金属類を含有するものを云う。なお、汚染水を排水等と云う場合がある。 In the treatment method of the present invention, contaminated water broadly means water containing heavy metals, and includes various types of wastewater and wastewater generated naturally and artificially. For example, industrial wastewater, sewage, seawater, river water This refers to water that contains heavy metals, such as water from swamps and lakes, surface water from the surface, water from dams such as rivers, underground running water and water, and culvert water. In some cases, the contaminated water is called drainage.
また、本発明において重金属類とは、例えば、セレン、カドミウム、六価クロム、鉛、亜鉛、銅、ニッケル、ヒ素、アンチモンなどの重金属元素や金属元素などを云う。セレン含有汚染水とは重金属類としてセレンを含む汚染水を云う。 In the present invention, heavy metals refer to heavy metal elements such as selenium, cadmium, hexavalent chromium, lead, zinc, copper, nickel, arsenic, and antimony, and metal elements. Selenium-containing contaminated water refers to contaminated water containing selenium as a heavy metal.
通常、排水等に含まれているセレンは亜セレン酸イオン[SeO3 2-](4価セレン)や、セレン酸イオン[SeO4 2-](6価セレン)の形態で存在している。本発明の処理対象である汚染水はセレンの他に、セレンの還元を大きく妨げない限り他の重金属金属イオン等を含有するものでも良い。 Usually, selenium contained in waste water or the like is present in the form of selenite ion [SeO 3 2- ] (tetravalent selenium) or selenate ion [SeO 4 2- ] (hexavalent selenium). In addition to selenium, the contaminated water to be treated according to the present invention may contain other heavy metal ions as long as the reduction of selenium is not greatly hindered.
本発明の処理方法において用いる鉄粉微粒子は、アルミニウムを0.1重量%以上、カルシウムを0.05重量%以上、およびチタンを0.05重量%以上含有する鉄粉、鉄微粒子、鉄片、鉄切削屑などである。なお、鉄粉、鉄微粒子、鉄片、鉄切削屑などを含めて鉄粉微粒子と云う。汚染水に接触した鉄粉微粒子から還元性の第一鉄イオンが溶出し、これがセレンイオンや他の重金属イオンを還元して析出させる。鉄粉に含まれているアルミニウム、カルシウム、チタンはセレンの還元を促進する作用を有すると考えられる。 The iron powder fine particles used in the treatment method of the present invention are iron powder, iron fine particles, iron pieces, iron containing 0.1 wt% or more of aluminum, 0.05 wt% or more of calcium, and 0.05 wt% or more of titanium. Such as cutting waste. In addition, iron powder, iron fine particles, iron pieces, iron cutting waste, etc. are referred to as iron powder fine particles. Reducible ferrous ions are eluted from the iron powder fine particles in contact with the contaminated water, and this reduces and precipitates selenium ions and other heavy metal ions. Aluminum, calcium and titanium contained in the iron powder are considered to have an action of promoting reduction of selenium.
後述の実施例および比較例に示すように、上記金属成分を含む鉄粉微粒子を用いた場合には97%以上のセレン還元率を得ることができる。一方、アルミニウム、カルシウム、チタンの何れかが上記含有量より少ない鉄粉微粒子を用いた場合のセレン還元率は高くてもせいぜい57%程度であり、処理効果が顕著に異なる。なお、上記アルミニウム、カルシウム、およびチタンの含有量は何れも1.0重量%より多くても、セレンの還元率は大差ないので、アルミニウム含有量は0.1〜1.0重量%、カルシウム含有量およびチタ含有量はおのおの0.05〜1.0重量%であれば良い。 As shown in the examples and comparative examples described later, when iron powder fine particles containing the metal component are used, a selenium reduction rate of 97% or more can be obtained. On the other hand, the selenium reduction rate in the case of using iron powder fine particles in which any one of aluminum, calcium, and titanium is less than the above content is at most about 57%, and the treatment effect is remarkably different. Note that even if the contents of aluminum, calcium and titanium are all greater than 1.0% by weight, the reduction rate of selenium is not so different, so the aluminum content is 0.1 to 1.0% by weight and calcium is contained. The amount and the titanium content may be 0.05 to 1.0% by weight, respectively.
また、上記鉄粉微粒子は、上記含有量のアルミニウム、カルシウム、およびチタンを含むものであれば良く、炭素鋼に限らずクロムやマンガンなどの金属成分を含む各種の鉄鋼の鉄粉や鉄片、あるいは切削屑などを用いることができる。これらの鉄粉等は排水等との接触面積が大きいほど好ましいので、出来るだけ微細なものが良い。具体的には、50%累積粒子径が30〜80μm、および最頻粒子径が30〜150μmである鉄粉微粒子が好ましい。 Moreover, the iron powder fine particles may be any material as long as it contains aluminum, calcium, and titanium with the above contents, and are not limited to carbon steel, and various iron and iron pieces and pieces of iron containing metal components such as chromium and manganese, or Cutting waste or the like can be used. These iron powders and the like are preferably as fine as possible because they have a larger contact area with drainage and the like. Specifically, iron powder fine particles having a 50% cumulative particle size of 30 to 80 μm and a mode particle size of 30 to 150 μm are preferable.
鉄粉微粒子の使用量は、セレン濃度0.05〜0.5mg/Lの排水等1Lに対して、1〜3g/L程度であれば良い。また、密閉反応槽を用い、非酸化性雰囲気下および弱酸性下(例えば、pH=3〜5)で、攪拌しながら排水等のセレンと鉄粉微粒子とを接触させるのが好ましい。排水等の温度は常温(15℃〜25℃)で良い。 The amount of iron powder fine particles used may be about 1 to 3 g / L with respect to 1 L of drainage or the like having a selenium concentration of 0.05 to 0.5 mg / L. In addition, it is preferable to use selenium such as waste water and iron powder fine particles in contact with each other under stirring in a non-oxidizing atmosphere and under weak acidity (for example, pH = 3 to 5) using a sealed reaction tank. The temperature of the drainage or the like may be room temperature (15 ° C. to 25 ° C.).
汚染水に含まれるセレンイオンは鉄粉微粒子に接触して還元され、鉄粉表面に析出する。一方、弱酸性下で鉄粉微粒子の表面は僅かづつ溶けるので、鉄粉表面の析出したセレンは攪拌下で液中に離れて鉄粉表面は新鮮な状態となり、セレンイオンの還元が繰り返し進行する。 Selenium ions contained in the contaminated water are reduced upon contact with the iron powder fine particles, and are deposited on the iron powder surface. On the other hand, the surface of the iron powder particles dissolves little by little under weak acidity, so the selenium deposited on the iron powder surface is separated into the liquid under stirring and the iron powder surface becomes fresh, and the reduction of selenium ions proceeds repeatedly. .
還元されて析出したセレンは液中で澱物化し、あるいは液中に懸濁しているので、これを固液分離してセレンを排水等から除去する。固液分離手段としては遠心分離またはシックナーなどを用いることができる。さらに、析出したセレンと鉄粉とを含む排水等を湿式サイクロンに導いて分離しても良い。 The selenium deposited by reduction is starched or suspended in the liquid, and this is solid-liquid separated to remove the selenium from the waste water or the like. Centrifugation or thickener can be used as the solid-liquid separation means. Further, the drainage containing precipitated selenium and iron powder may be guided to a wet cyclone and separated.
上記処理方法によれば、例えば、処理前のセレン濃度0.05〜0.5mg/Lの排水等について、セレンイオンを還元除去することによって、処理後の排水等のセレン濃度を環境基準値(0.01mg/L)以下に低減することができる。また、本発明の鉄粉微粒子を用いればセレンの他に還元される重金属類を析出して除去することができる。従って、本発明の鉄粉微粒子はセレンの処理に限らず、他の重金属類の処理に用いることができる。 According to the above treatment method, for example, the selenium concentration in the wastewater after treatment is reduced to the environmental standard value by reducing and removing selenium ions in the wastewater etc. in the selenium concentration of 0.05 to 0.5 mg / L before treatment. 0.01 mg / L) or less. Moreover, if the iron powder fine particle of this invention is used, the heavy metals reduced besides selenium can be deposited and removed. Therefore, the iron powder fine particles of the present invention can be used not only for the treatment of selenium but also for the treatment of other heavy metals.
処理槽(容量5L)にセレンおよびクロムを含有する汚染水(セレン濃度およびクロム濃度0.40mg/L)を入れ、このセレンおよびクロムを含有する汚染水に表1に示す微量金属成分を含有する鉄粉1.0〜2.5g/Lを添加し、液温15℃〜25℃、pH=3.5〜4.5、300〜500rpmの回転数で槽内を回転しながら90分反応させ、セレンを還元析出させ後に析出したセレンを固液分離した。クロムは鉄粉に吸着したものを鉄粉ごと固液分離した。使用した鉄粉ごとの処理結果を表1に示した。なお、使用した鉄粉の粒度は50%累積粒子径が30〜80μm および最頻度粒子径が30〜150μmである。 Contaminated water (selenium concentration and chromium concentration 0.40 mg / L) containing selenium and chromium is placed in a treatment tank (capacity 5 L), and the trace metal components shown in Table 1 are contained in the contaminated water containing selenium and chromium. Iron powder 1.0-2.5g / L is added, and it is made to react for 90 minutes, rotating the inside of a tank at the rotation temperature of liquid temperature 15-25 degreeC, pH = 3.5-4.5, 300-500 rpm. Then, selenium was reduced and precipitated, and the precipitated selenium was separated into solid and liquid. The chromium adsorbed on the iron powder was separated into solid and liquid together with the iron powder. The processing results for each iron powder used are shown in Table 1. The iron powder used has a 50% cumulative particle size of 30 to 80 μm and a most frequent particle size of 30 to 150 μm.
表1に示すように、本発明の鉄粉を用いて処理した汚染水(試料No.5、No.6)は何れもセレンの還元率が97.5%以上であり、処理後のセレン濃度は環境基準値以下に低減されており、優れたセレン還元率(セレン除去率)が得られる。また、クロムについても本発明の鉄粉を用いて処理したものは除去率が97.5%以上であり、除去率が高い。 As shown in Table 1, all of the contaminated water (samples No. 5 and No. 6) treated with the iron powder of the present invention had a selenium reduction rate of 97.5% or more, and the selenium concentration after the treatment Is reduced below the environmental standard value, and an excellent selenium reduction rate (selenium removal rate) can be obtained. Moreover, also about the chromium processed using the iron powder of this invention, the removal rate is 97.5% or more, and the removal rate is high.
一方、アルミニウム含有量、カルシウム含有量およびチタン含有量が本発明の範囲より少ない鉄粉を用いて処理した汚染水(試料No.1〜No.4)は、処理後の残留セレン濃度が0.17mg/L以上(セレン除去率57.5%以下)、処理後の残留クロム濃度は0.02mg/L以上であり、セレンおよびクロムの残留濃度が何れも環境基準(0.01mg/L)を上回る結果となっている。 On the other hand, the contaminated water (samples No. 1 to No. 4) treated with iron powder whose aluminum content, calcium content and titanium content are less than the range of the present invention has a residual selenium concentration of 0. 17mg / L or more (selenium removal rate of 57.5% or less), residual chromium concentration after treatment is 0.02mg / L or more, and both selenium and chromium residual concentrations are environmental standards (0.01mg / L) The result is higher.
Claims (5)
In a treatment method in which contaminated water is brought into contact with iron powder fine particles to reduce and precipitate heavy metals contained in the contaminated water, 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05 of titanium A method for treating selenium-containing contaminated water, comprising using iron powder fine particles containing at least wt%, bringing the iron powder fine particles into contact with contaminated water containing selenium, and reducing and precipitating selenium.
Iron powder fine particles containing 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05% by weight or more of titanium contain selenium in a non-oxidizing atmosphere of a closed reaction tank and under weak acidity. The method for treating selenium-containing contaminated water according to claim 1, wherein the contaminated water is contacted.
The selenium according to claim 1 or 2, wherein the selenium-containing contaminated water having a selenium concentration of 0.05 to 0.5 mg / L before treatment is reduced to an environmental standard value (0.01 mg / L) or less after treatment. Treatment method of contained contaminated water.
A water treatment agent comprising fine iron powder containing 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium, and 0.05% by weight or more of titanium.
Iron containing 0.1% by weight or more of aluminum, 0.05% by weight or more of calcium and 0.05% by weight or more of titanium, 50% cumulative particle size of 30 to 80 μm, and mode particle size of 30 to 150 μm The water treatment agent according to claim 4, comprising fine powder particles.
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008004488A1 (en) * | 2006-07-04 | 2008-01-10 | Kurita Water Industries Ltd. | Method and apparatus for treating selenium-containing wastewater |
JP2009011915A (en) * | 2007-07-03 | 2009-01-22 | Kurita Water Ind Ltd | Selenium-containing wastewater treatment method and apparatus |
JP2009011914A (en) * | 2007-07-03 | 2009-01-22 | Kurita Water Ind Ltd | Selenium-containing wastewater treatment method and apparatus |
CZ304650B6 (en) * | 2011-08-16 | 2014-08-20 | Vysoká škola chemicko-technologická v Praze | Adsorbents for removing arsenic and selenium from water |
-
2006
- 2006-02-22 JP JP2006044701A patent/JP2007054818A/en not_active Withdrawn
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2008004488A1 (en) * | 2006-07-04 | 2008-01-10 | Kurita Water Industries Ltd. | Method and apparatus for treating selenium-containing wastewater |
JP2008030020A (en) * | 2006-07-04 | 2008-02-14 | Kurita Water Ind Ltd | Method and apparatus for treating selenium-containing waste water |
US8182697B2 (en) | 2006-07-04 | 2012-05-22 | Kurita Water Industries Ltd. | Method and apparatus for treating selenium-containing wastewater |
JP2009011915A (en) * | 2007-07-03 | 2009-01-22 | Kurita Water Ind Ltd | Selenium-containing wastewater treatment method and apparatus |
JP2009011914A (en) * | 2007-07-03 | 2009-01-22 | Kurita Water Ind Ltd | Selenium-containing wastewater treatment method and apparatus |
CZ304650B6 (en) * | 2011-08-16 | 2014-08-20 | Vysoká škola chemicko-technologická v Praze | Adsorbents for removing arsenic and selenium from water |
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