WO1994021349A1 - Flocculant composition for removing trihalomethane and its precursors - Google Patents
Flocculant composition for removing trihalomethane and its precursors Download PDFInfo
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- WO1994021349A1 WO1994021349A1 PCT/KR1994/000018 KR9400018W WO9421349A1 WO 1994021349 A1 WO1994021349 A1 WO 1994021349A1 KR 9400018 W KR9400018 W KR 9400018W WO 9421349 A1 WO9421349 A1 WO 9421349A1
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/52—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities
- C02F1/5236—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents
- C02F1/5245—Treatment of water, waste water, or sewage by flocculation or precipitation of suspended impurities using inorganic agents using basic salts, e.g. of aluminium and iron
Definitions
- Coagulant composition excluding trihalomethane and its forerunner substances
- the present invention relates to the field of purifying various industrial wastewaters such as metals, fibers, and papermaking, foods, domestic wastewaters such as municipal sewage, etc., and tap water.
- the former includes aluminum oxide (M 2 (S0-) 3 ), polyaluminum chloride (hereinafter referred to as PAS), and the latter includes compounds of various polymers.
- the coagulant composition of the present invention (hereinafter, referred to as composition) belongs to the inorganic type.
- An inorganic flocculant is required to have a high flocculating effect on suspended matter and a low residual amount of harmful metals and aluminum, iron, etc. in the treated water. Low residual amount is required even in water source water.
- inorganic aluminum-based coagulants are used in the treatment of tap water, so that these substances such as THMs and Humic Acid must be removed. Have difficulty,
- ozone or ozone is not used without chlorine sterilization, which causes THHs formation.
- Some oxide sterilization method that by the CI0 2 or the like is ⁇ are used.
- these disinfectants have problems that their safety has not been approved and their processing costs are expensive.
- the present invention is added to industrial and industrial wastewater, domestic wastewater, etc., and acts as an effective flocculant for flocculation of suspended solids and removal of harmful metals, and at the same time, effectively removes THMs and their precursors. It is an object of the present invention to provide a flocculant composition to be used as a water purification agent for water supply and the like.
- the present inventors have conducted long-term test research to achieve the technical background and problems as described above and the object thereof, and as a result, the water-soluble aluminum salt, the water-soluble iron salt, and the water-soluble magnesium salt were determined in atomic ratio.
- Fe 0 ⁇ 01-2 to al 1, to 2 contains Hg 0.01 to 2
- novel scavenger is the sum of HgO 1 to 15 wt%
- a water-soluble salt of aluminum, iron, or magnesium is used as a raw material of the composition of the present invention.
- These can also be used in the form of solids or solutions such as anhydrides, hydrates and double salts.
- Mineral acid decomposed products of minerals containing Al, Fe and Hg can also be used.
- vermiculite typically A 1 2 0 3] 0 ⁇ 182, Fe 2 0 3 10 ⁇ : .? 18;, containing MgO 5-202, other oxides and moisture, etc. 44-75 .
- Mineral acid decomposition products of these minerals can be used.
- composition of the present invention coagulant, Fe 0.01 to 2 with respect to Al 1 in the atomic weight ratio, contains Hg 0 ⁇ 0 ⁇ 2, its oxide A1 2 0 3, Fe 2 0 3, the sum of HgO is 1-15 %
- composition of% by weight is appropriate, and the effect is small outside this range.
- Formulations of these compositions are prepared by mixing various water-soluble Al, Fe, Mg or by adding decomposed products of Al, Fe, Mg-containing minerals and water-soluble Al, Fe, Mg salts.
- composition of the present invention is used in the same manner as a general inorganic flocculant. Although it can be used as a solid mixture, it is better to use it as an aqueous solution.
- composition solution to the wastewater and source water while stirring, adjust the pH to about 7, stir the mixture, and allow to separate and separate suspended matters and other substances.
- Amount of composition used The use amount of the composition of the present invention varies depending on the degree of pollution of wastewater and source water, the degree of S, and the like, but the overall high purification effect is as follows.
- the total amount of oxides is 5-10 weight%, and about 50-300 ⁇ is added to the wastewater and source water. It is effective to use.
- the composition of the present invention has the ability to remove THMs and its precursors, and is not inferior to the ordinary S product in cohesion as described above, but rather, the mutual effect of coexistence of Al, Fe, and Mg is expected. .
- Floe increases due to the presence of Fe salts, which indicates the need for aggregation, and the specific gravity is large, so that the precipitation rate of Floe is increased and the water purification effect is improved.
- composition of the present invention is not inferior to ordinary products in the ability to remove harmful metals. Rather, it is expected that the effects of these metals will be improved due to the improvement of the contact force due to the interaction of Al, Fe and Hg. In addition, the residual amounts of Al and Fe in the service water after coagulant treatment are very small and negligible.
- THMs are subject to regulation around the world, and their regulation values are less than 50 to 100 ppb.
- Test conditions 1 1) .Sample sample-artificial Kaolin concentration 50 eg / 1
- the present invention provides the composition of the present invention based on the surprising findings, and it is recognized that the removal of THMs is very effective. Economic effects
- composition of the present invention has a good flocculating effect and at the same time has the ability to remove THMs and its precursors, and Fe, Mg-salts are relatively inexpensive in comparison with A] salts in terms of raw material price.
- minerals containing Al, Fe, and Mg can be used and their economic effects are great.
- Figure 1 is a graph showing the effect of removing THMs with the addition ratio of ME.
- Test sample a) Artificial Kaolin portability 50 mg / 1 b) Hg, Cd, Cr, Pd concentration 1 rag / 1 c each) Huli ic Acid 5 mg / 1 2) Adjust PH 7.0
- Chlorination solution Chlorine concentration 10 t / g
- composition of the present invention is the same as a flocculant compared to ordinary products.
- the added amount of various flocculants is 200 PP.
- the composition of the present invention exhibits the same or better effect as a flocculant than conventional products even when the composition from mineral acid decomposed matter is mixed, and the effect of removing THMs is The same tendency was observed when using vermiculite hydrochloric acid or nitric acid extract.
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Abstract
Description
ト リハロ メ タ ン及びその前鹿物質を除外する凝集剤組成物 利用分野 Coagulant composition excluding trihalomethane and its forerunner substances
本発明は化学. 金属、 繊維、 製紙等の各種の産業廃水、 食品、 都市 下水等の生活廃水及び水道の源水等を浄化する分野に関するものであ る。 The present invention relates to the field of purifying various industrial wastewaters such as metals, fibers, and papermaking, foods, domestic wastewaters such as municipal sewage, etc., and tap water.
背景技術 Background art
一般的 g集剤と して無機系と有機系がある。 前者は «酸アルミ ニゥ ム (M2(S0-)3), ポリ塩化アルミ ニウム (以下 PAS と ¾称) 等があ り後者には各高分子の化合物がある。 本発明の凝集剤組成物 (以下 組成物と喀称) は無機系に属する。 In general, there are inorganic and organic g-collectors. The former includes aluminum oxide (M 2 (S0-) 3 ), polyaluminum chloride (hereinafter referred to as PAS), and the latter includes compounds of various polymers. The coagulant composition of the present invention (hereinafter, referred to as composition) belongs to the inorganic type.
無機系の凝集剤と しては浮遊物の凝集効果が高く処理後用水中の有 害金属及びアルミ 二ゥム、 鉄等の残留量の低いのが要望されている。 水道用源水 *理においても低い残留量が一層要望される。 An inorganic flocculant is required to have a high flocculating effect on suspended matter and a low residual amount of harmful metals and aluminum, iron, etc. in the treated water. Low residual amount is required even in water source water.
水道用源水処理においてはアルミ ニウム系の無機凝集剤が多く使用 されており、 処理後の用水中に微量のアルミ ニ ウムが残留する問題が あってこれがアルッハイマ病の原因であるとも言われる, In water source water treatment, aluminum-based inorganic coagulants are often used, and there is a problem that trace amounts of aluminum remain in the treated water, which is said to be the cause of Alheimer's disease.
X . 現在は水道の水中に CHC13, CHCl2Br, CHClBr2, CHBr., 等 の ト リハロ メ タ ン (以下 THMs と略称) が存在する問題があって、 こ れらは健康保健の観点から世界的に問題視されているので規制の対照 となっている《 X. CHC1 3, CHCl 2 Br in the water of the water supply is now, CHClBr 2, CHBr., Door Riharo meta emissions (less than THMs and abbreviation) of equal if there is a problem that there are, in terms of these are health Has been viewed as a global issue by
水道源水の処理は一般的に無機系アルミ ニウム系の凝集剤が使用さ れているので、 これらで THMs 及び ヒ ュ一 ミ ッ ク酸 (Hu ic Acid)等 のその前躲物質の除去は困難である, In general, inorganic aluminum-based coagulants are used in the treatment of tap water, so that these substances such as THMs and Humic Acid must be removed. Have difficulty,
これを解決する為、 THHs 生成の原因となる塩素殺菌をせずオゾン又 は CI02 等によ る酸化殺菌法が試図され一部は使用されている。 然し これらの殺菌剤は、 その安全性が碹認されておらず又、 その処理費が 高価である問題点がある。 To solve this, ozone or ozone is not used without chlorine sterilization, which causes THHs formation. Some oxide sterilization method that by the CI0 2 or the like is試図are used. However, these disinfectants have problems that their safety has not been approved and their processing costs are expensive.
発明の 目的 Purpose of the invention
本発明は、 産-業廃水、 生活廃水等に添加して浮遊物の凝集、 有害金 属の去等の効果的凝集剤と して作用する と 同時に THMs 及びその前暁 物質を効果的に除去する水道等の浄水剤となる凝集剤組成物を提供す る こ と を 目的とする。 INDUSTRIAL APPLICABILITY The present invention is added to industrial and industrial wastewater, domestic wastewater, etc., and acts as an effective flocculant for flocculation of suspended solids and removal of harmful metals, and at the same time, effectively removes THMs and their precursors. It is an object of the present invention to provide a flocculant composition to be used as a water purification agent for water supply and the like.
発明の概要 Summary of the Invention
本発明者等は上記の如き技術的背景及び問題点とその 目的を達成す る為長期間試験研究を行した結果、 水溶性アルミ ニウム塩と水溶性鉄 塩及び水溶性マグネシウム塩を原子量比で Al 1に対し Fe 0·01〜2, 〜2, Hg 0.01〜2を含有し、 その酸化物 A1203 , Fe203, HgO の合計が 1〜15 重量%である新規ほ集剤組成物を使用すること によ リ効果的に 問題を解決する こ との出来る驚く べき事実を発見した。 組成物の原料 The present inventors have conducted long-term test research to achieve the technical background and problems as described above and the object thereof, and as a result, the water-soluble aluminum salt, the water-soluble iron salt, and the water-soluble magnesium salt were determined in atomic ratio. Fe 0 · 01-2 to al 1, to 2, contains Hg 0.01 to 2, the oxide A1 2 0 3, Fe 2 0 3, novel scavenger is the sum of HgO 1 to 15 wt% We have found a surprising fact that the use of the composition can effectively solve the problem. Composition raw materials
本発明組成物の原料と してアルミ ニウム、 鉄、 マグネシウムの水溶 性塩親を使用する。 これらは無水物、 水化物、 複塩等の固形状物や溶 液状も使用出来る。 又, アルミ ニウム、 鉄、 マグネシウムの金属を単 独又はこれらの混合物を塩酸、 窒酸、 硗酸等の鉱酸 (Mineral Acid) で »理して得た反応物の溶液又はこれを乾燥して得た無水物、 水化物 具体的に例示すれば、 A1 塩と して A1 - 61^0, A1(N03)3, Al2 (SO, )a. Al2 (S0 -18H20, A1(N1 )(S0,)2-18H20 等、 Fe 塩と しては 3 価の Fe 塩が好ま し く , FeC]3, FeCl3 - 6H20, Fe(N03)3, Fe2 (S04)3 Fe2 (S0 'xHz0, FeiNH^) (S04)2 *6~ 12H20 又は 2 価の鉄塩 FeSO, - 7HZ0 等を酸化状態の環境では使用する こ と が出来る。 HK 塩と して は MgCl2 , MgC]2*6H2o, MgSO MgS04*7H20 等の無水物、 水化物 . 複塩等がある。 A water-soluble salt of aluminum, iron, or magnesium is used as a raw material of the composition of the present invention. These can also be used in the form of solids or solutions such as anhydrides, hydrates and double salts. In addition, a solution of a reaction product obtained by treating a metal of aluminum, iron, or magnesium alone or a mixture thereof with a mineral acid such as hydrochloric acid, nitric acid, and sulfuric acid, or by drying the solution. the resulting anhydride, if hydrates specific examples, as the A1 salt A1 -. 61 ^ 0, A1 (N0 3) 3, Al 2 (sO,) a Al 2 (S0 -18H 2 0, A1 (N1) (S0,) 2 -18H 2 0 , etc., as the Fe salt rather then preferred trivalent Fe salt, FeC] 3, FeCl 3 - 6H 2 0, Fe (N0 3) 3, Fe 2 (S0 4) 3 Fe 2 (S0 'xH z 0 , FeiNH ^) (S0 4) 2 * 6 ~ 12H 2 0 or a divalent iron salt FeSO, - 7H Z can that you use the is a 0, etc. in the oxidation state environment. Is an H K salt MgCl 2, MgC] 2 * 6H 2 o, MgSO MgS0 4 * 7H 2 anhydride such as 0, there is hydrates. Double salt.
又、 Al, Fe, Hg を含有 している鉱物の鉱酸分解物も使用が可能で ある。 例えば . 蛭石 ( Verniculite ) は一般的に A 1203 】0〜182, Fe203 10〜: 18?;, MgO 5- 202, その他の酸化物及び水分等 44〜75 を含有する。 Mineral acid decomposed products of minerals containing Al, Fe and Hg can also be used. For example vermiculite (Verniculite) typically A 1 2 0 3] 0~182, Fe 2 0 3 10~: .? 18;, containing MgO 5-202, other oxides and moisture, etc. 44-75 .
これら鉱物の鉱酸分解物は使用が可能である„ Mineral acid decomposition products of these minerals can be used.
凝集剤の組成 Coagulant composition
本発明凝集剤の組成は、 原子量比で Al 1 に対し Fe 0.01〜2, Hg 0·0Ι〜2 を含有し、 その酸化物 A1203, Fe203 , HgO の 合計が 1〜 15 % 重量%の組成が適当であ り、 この範囲外では効果が少ない。 これら組成の調剤は各種の水溶性 Al, Fe, Mgの混合又は Al, Fe, Mg含有鉱物の分解物やこれに水溶性 Al, Fe, Mg 塩を補給して調整さ れる。 The composition of the present invention coagulant, Fe 0.01 to 2 with respect to Al 1 in the atomic weight ratio, contains Hg 0 · 0Ι~2, its oxide A1 2 0 3, Fe 2 0 3, the sum of HgO is 1-15 % The composition of% by weight is appropriate, and the effect is small outside this range. Formulations of these compositions are prepared by mixing various water-soluble Al, Fe, Mg or by adding decomposed products of Al, Fe, Mg-containing minerals and water-soluble Al, Fe, Mg salts.
凝集剤の使用法 How to use flocculant
本発明組成物の使用法は、 一般的無機凝集剤と同 じ方法で使用され る。 固形混合物と しても使用が可能であるが、 その水溶液に して使用 するのが良い。 The composition of the present invention is used in the same manner as a general inorganic flocculant. Although it can be used as a solid mixture, it is better to use it as an aqueous solution.
廃水及び源水に組成物溶液を挽拌しながら添加 し、 PH を約 7 に調 整攬拌した後放置して浮遊物、 その他を凝集させて分離し通常の方法 に依って実施する。 組成物の使用量 本発明組成物の使用量は廃水、 源水の汚染度、 S度等によって異な るが総合的に浄化効果が高いのは次ぎのよ うである。 Add the composition solution to the wastewater and source water while stirring, adjust the pH to about 7, stir the mixture, and allow to separate and separate suspended matters and other substances. Amount of composition used The use amount of the composition of the present invention varies depending on the degree of pollution of wastewater and source water, the degree of S, and the like, but the overall high purification effect is as follows.
その組成と して原子量比 Al 1 に対し Fe 0.1〜0.3, Ηκ 0.1〜0.3 のものが酸化物の合計が 5〜10 重量 度の水瑢液を廃水、 源水に 対し 50〜 300ΡΡΒ 程度添加 して使用するのが効果的である。 With a composition of Fe 0.1-0.3 and Ηκ 0.1-0.3 with respect to the atomic weight ratio Al 1, the total amount of oxides is 5-10 weight%, and about 50-300ΡΡΒ is added to the wastewater and source water. It is effective to use.
発明の効果 The invention's effect
凝集効果 Aggregation effect
一般的無機凝集剤である硫酸アルミ ニウム、 PAC 等は良好な凝集 剤であるが、 なお一層の凝集効果が要望されている。 Common inorganic coagulants such as aluminum sulfate and PAC are good coagulants, but further coagulation effects are required.
本発明組成物は THMs 及びその前翻物質の除去能力を具備して凝集 力においては前記の如き通常の S品に比して劣らず、 むしろ Al, Fe, Mg 共存の相互効果が期待される。 即ち、 Fe 塩類の存在によって Floe は増大 して集合化の煩向を表し比重が大きいので Floe の沈殿速度を 高め浄水効果を向上させる。 The composition of the present invention has the ability to remove THMs and its precursors, and is not inferior to the ordinary S product in cohesion as described above, but rather, the mutual effect of coexistence of Al, Fe, and Mg is expected. . In other words, Floe increases due to the presence of Fe salts, which indicates the need for aggregation, and the specific gravity is large, so that the precipitation rate of Floe is increased and the water purification effect is improved.
Mg の存在はよ り一層この傾向を助長する。 The presence of Mg further facilitates this trend.
金属類の除去効果 Metal removal effect
在来の無機凝集剤では有害金属の除去能力があるが廃水、 源水の種 類によっては此れらの金属が微量に残存する煩向がある。 Conventional inorganic coagulants have the ability to remove harmful metals, but depending on the type of wastewater and source water, these metals may remain in trace amounts.
本発明組成物は有害金属の除去能力は通常の製品に比して劣らず、 むしろ Al, Fe, Hg の相互作用による接集力向上に依ってこれら金属 の効果の向上が期待される。 又, 凝集剤 ¾理後の用水中の Al, Fe の 残存量は微量で無視出来る程度である。 The composition of the present invention is not inferior to ordinary products in the ability to remove harmful metals. Rather, it is expected that the effects of these metals will be improved due to the improvement of the contact force due to the interaction of Al, Fe and Hg. In addition, the residual amounts of Al and Fe in the service water after coagulant treatment are very small and negligible.
THMs 及びその前鹿物質の除去効果 Removal effect of THMs and forerunner substances
前記した通 り、 通常の凝集剤は THHs 及びその前鹿物質の除去は困 難な傾向がある。 As mentioned above, ordinary flocculants are difficult to remove THHs and their deer substances. Tends to be difficult.
この THMs は世界的に規制の煩向にあ り、 その規制値は 50〜 lOOppb 以下である。 These THMs are subject to regulation around the world, and their regulation values are less than 50 to 100 ppb.
本発明者は THHs 及びその前翻物質の生成や又は効果的に除去出来 る凝集剤を開発する為試験を実施した。 その試験の一例を提示すれば 次の通 りである。 試験条件 1) . 検体試料一人工 Kaolin ¾度 50 eg/1 The present inventor has conducted tests to develop a flocculant capable of producing or effectively removing THHs and its precursors. An example of the test is as follows. Test conditions 1) .Sample sample-artificial Kaolin concentration 50 eg / 1
Hu屬: ic Acid 5 羅 g/1 Hu gen: ic Acid 5 Ra g / 1
2) . 調整 pH 7.0 2) Adjust pH 7.0
3) . 水温 13.2 て 3). Water temperature 13.2
4) . 添加塩素液濃度 (塩素 «度) 10 ng/J4). Concentration of added chlorine solution (chlorine «degree) 10 ng / J
5) . 塩素接触時間 1 Hr 5). Chlorine contact time 1 Hr
6) . 凝集剤添加量 215 ppm 試験値 表 6). Flocculant addition amount 215 ppm Test value table
試験結果第 1 表に表した如 く通常の凝集剤に比して Al,Fe系及び A1 Fe,Hg 系が THMs の残量が顕著に低いこ と を知る こ と が出来る。 本発明者等は A],Fe系よ り A1,ト' e,Mg 系の THMs残量が顕著に低いので Mgの効果を確認するため下記の条件で Al,Feを固定 し Mgを活性させて 実験を実施し各組成物の濃度は酸化物合計量 8Ϊに したと ころ第 1 図の 如き結果を得た。 As shown in the test results in Table 1, it can be seen that the residual amount of THMs in the Al, Fe system and A1 Fe, Hg system is significantly lower than that of ordinary flocculants. The present inventors have found that the amount of THMs remaining in A1, Toe, and Mg systems is significantly lower than that of A] and Fe systems. Experiments were carried out to obtain the results shown in Fig. 1 when the concentration of each composition was adjusted to 8% of the total amount of oxides.
第 1 図で見られる よ う に Hg 量が ¾加するに伴い残存 THMs 量は低 Fして Hg が非常に効果的であるこ と を発見した。 As can be seen in Fig. 1, the amount of residual THMs was reduced as the amount of Hg increased, and Hg was found to be very effective.
このよ う に驚く べき発見を根挞に本発明組成物を提供するものであ り THMs の除去が非常に効果的である と認める。 経済効果 Thus, the present invention provides the composition of the present invention based on the surprising findings, and it is recognized that the removal of THMs is very effective. Economic effects
本発明組成物は良好な凝集効果を表すと同時に THMs 及びその前駆 物質を除去する能力を持っており又原料の価格面で A】 塩に比べ Fe, Mg-塩 は比較的低廉である。 又、 Al , Fe, Mg を含有 し鉱物も利用出 来てその経済効果は大きい。 The composition of the present invention has a good flocculating effect and at the same time has the ability to remove THMs and its precursors, and Fe, Mg-salts are relatively inexpensive in comparison with A] salts in terms of raw material price. In addition, minerals containing Al, Fe, and Mg can be used and their economic effects are great.
図面の簡単な説明 BRIEF DESCRIPTION OF THE FIGURES
第 1 図は ME の添加比に伴う THMs の除去効果を表したク グラ フで ある。 Figure 1 is a graph showing the effect of removing THMs with the addition ratio of ME.
[実施例] [Example]
次ぎに本発明の実施例を提示する。 Next, examples of the present invention will be presented.
実施例 1 Example 1
廃水及び水道源水に該当する検査試料に対し下記の条件で実験を実 施した。 Experiments were performed on test samples corresponding to wastewater and tap water under the following conditions.
実施条件 1) 検査試料 a) 人工 Kaolin 港度 50 mg/1 b) Hg, Cd, Cr, Pd 濃度 各 1 rag/1 c ) Hu麗 ic Acid 5 mg/1 2) 調整 P H 7.0 Implementation conditions 1) Test sample a) Artificial Kaolin portability 50 mg / 1 b) Hg, Cd, Cr, Pd concentration 1 rag / 1 c each) Huli ic Acid 5 mg / 1 2) Adjust PH 7.0
3) 水温 15 3) Water temperature 15
4) 塩素処理液 塩素濃度 10腿 g/1 4) Chlorination solution Chlorine concentration 10 t / g
5) 塩素接触時間 1 hr 5) Chlorine contact time 1 hr
6) 凝集剤添加量 z86 ppB 6) Flocculant addition amount z86 ppB
7) 測定法 一原子吸光分光光度計 7) Measurement method: Atomic absorption spectrophotometer
THMs 一ガスクロマトグラフィー THMs-one gas chromatography
ECD検出器 ECD detector
2. 測定値 2. Measured value
表. 2 Table. 2
(ND) : 不検出 (ND): Not detected
表 2の通り本発明の組成物は凝集剤として通常の製品に比して同 As shown in Table 2, the composition of the present invention is the same as a flocculant compared to ordinary products.
等又はそれ以上の効果を表し THMs の除去効果も顕著である。 実施例 2 It shows equal or better effect, and the effect of removing THMs is also remarkable. Example 2
韓国産蚝石 (Verniculite) : A1203 10〜12, Fe203 11〜13, MgO 6-7, その他 73-68 wtS! ) を鉱酸で *理した抽出物 ( 比重 1 · 18, Α1203 2.1 , Fe203 1.8, HgO 0.63, その他の酸化物 0.43 » ) に各種の塩類を添加して実施例 1と同じ条件 で実験した。 Korean蚝石(Verniculite):! A1 2 0 3 10~12, Fe 2 0 3 11~13, MgO 6-7, the other 73-68 wtS) with mineral acid * management extracts (specific gravity 1 - 18 , Α1 2 0 3 2.1, Fe 2 0 3 1.8, Experiments were performed under the same conditions as in Example 1 except that various salts were added to HgO 0.63 and other oxides 0.43 »).
但し、 各種凝集剤の添加量は 200 PP. である。 However, the added amount of various flocculants is 200 PP.
表 3 Table 3
( ND ) : 不検出 (ND): Not detected
表 3で見るように、 本発明の組成物は鉱物の酸分解物から褽造藹整しても凝集 剤として在来品に比して同等又はそれ以上の効果を表し、 THMs の除去効果は髙い, 又、 蛭石 (Ver icuii te) 塩酸又は窒酸抽出液を使用したのも同じ程度の傾向を見 せた。 実施例 3 As can be seen from Table 3, the composition of the present invention exhibits the same or better effect as a flocculant than conventional products even when the composition from mineral acid decomposed matter is mixed, and the effect of removing THMs is The same tendency was observed when using vermiculite hydrochloric acid or nitric acid extract. Example 3
重金属を含有する産業廃水 (PH 4, Cr 5 PPB, Ni 8 PP»含有) に蛭石に鉱酸を 反応させて得た本発明組成の抽出物 (原子量比 Al :Fe:Mg= l : l, 14 : 0· 34,酸化物 合計 5 vt%) を 300 PP. 添加して石灰油で PH 7 で調整して慣行法に従って *理 したところ浄化液 (PH 7, Cr 0.45, Ni 0.67 ΡΡ») を得ることが出来た。 Industrial wastewater containing heavy metals (PH 4, Cr 5 PPB, Ni 8 PP » containing) the extract of the present invention the composition obtained by reacting a mineral acid in vermiculite (atomic weight ratio of Al: Fe: Mg = l: l , 14: 0 · 34, oxides totaling 5 vt%) was added to 300 PP., Adjusted with PH7 with lime oil and treated according to the customary method. * Purified solution ( PH7, Cr0.45, Ni0.67 ) ) Was obtained.
これは無機凝集剤として十分な浄化効果を認めることが出来る。 実施例 4 都市下水 <PH 6.5, SS 120ΡΡΠ, BOD 210PPB, 大腸菌群 (410X10S/ 100B1) >に蛭石の硗酸反応物 (原子量比 Al, Fe, Kg = 1 :0.27:0.07 酸化物合計 8.7 wt¾) を 100ΡΡ· 添加して ΡΗ を 7.0 に纜整して通 常の方法で処理した結果、 浄化液 < ΡΗ 7.0, SS 10.2, BOD 17PP«, 大腸菌群 (4X102/100B1) > を得た。 これは無機凝集剤と して十分な浄 化効果を表すと いう こ と を認める こ と が出来る。 This can be recognized as a sufficient purifying effect as an inorganic flocculant. Example 4 Urban sewage <PH 6.5, SS 120ΡΡΠ, BOD 210 PP B, coliforms (410X10 S / 100B1)> and vermiculite reactant (atomic ratio Al, Fe, Kg = 1: 0.27: 0.07 Total oxides 8.7 wt¾ ) Was added to 100 ΡΡ ·, ΡΗ was conditioned to 7.0, and treated as usual. As a result, purified solution <ΡΗ 7.0, SS 10.2, BOD 17 PP «, coliform group (4X10 2 / 100B1)> was obtained. . It can be seen that this shows sufficient purification effect as an inorganic flocculant.
Claims
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR93-3995 | 1993-03-16 | ||
| KR1019930003995A KR960008085B1 (en) | 1993-03-16 | 1993-03-16 | Coagulant preparation to remove trihalomethane and its precursors |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1994021349A1 true WO1994021349A1 (en) | 1994-09-29 |
Family
ID=19352245
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/KR1994/000018 Ceased WO1994021349A1 (en) | 1993-03-16 | 1994-03-09 | Flocculant composition for removing trihalomethane and its precursors |
Country Status (5)
| Country | Link |
|---|---|
| JP (1) | JP2788552B2 (en) |
| KR (1) | KR960008085B1 (en) |
| CN (1) | CN1070721C (en) |
| RU (1) | RU94046154A (en) |
| WO (1) | WO1994021349A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000050345A3 (en) * | 1999-12-02 | 2001-02-01 | Minox Corp Usa | Mineral oxide liquid concentrates for water and wastewater treatment |
| WO2008027446A3 (en) * | 2006-08-30 | 2008-04-24 | Veolia Es Technical Solutions | Process for recycling waster acid |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57184489A (en) * | 1981-05-08 | 1982-11-13 | Asahi Glass Co Ltd | Purification of waste water containing turbid substance and phosphorus component |
| JPS62234511A (en) * | 1986-04-02 | 1987-10-14 | Jitsuo Inagaki | Flocculating agent for precipitation |
| JPS6344993A (en) * | 1986-08-12 | 1988-02-25 | Asao Shimanishi | Method for removing organic substance of the like dissolved in sewage |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1009990B (en) * | 1988-04-09 | 1990-10-17 | 冶金工业部建筑研究总院 | Mg-fe compound type waste-water processing agent and its production method |
-
1993
- 1993-03-16 KR KR1019930003995A patent/KR960008085B1/en not_active Expired - Lifetime
-
1994
- 1994-03-09 WO PCT/KR1994/000018 patent/WO1994021349A1/en not_active Ceased
- 1994-03-09 RU RU94046154/25A patent/RU94046154A/en unknown
- 1994-03-09 CN CN94190129A patent/CN1070721C/en not_active Expired - Fee Related
- 1994-03-09 JP JP6520886A patent/JP2788552B2/en not_active Expired - Lifetime
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS57184489A (en) * | 1981-05-08 | 1982-11-13 | Asahi Glass Co Ltd | Purification of waste water containing turbid substance and phosphorus component |
| JPS62234511A (en) * | 1986-04-02 | 1987-10-14 | Jitsuo Inagaki | Flocculating agent for precipitation |
| JPS6344993A (en) * | 1986-08-12 | 1988-02-25 | Asao Shimanishi | Method for removing organic substance of the like dissolved in sewage |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000050345A3 (en) * | 1999-12-02 | 2001-02-01 | Minox Corp Usa | Mineral oxide liquid concentrates for water and wastewater treatment |
| US6527975B1 (en) | 1999-12-02 | 2003-03-04 | Minox Corporation Usa | Mineral oxide liquid concentrates for water and wastewater treatment |
| WO2008027446A3 (en) * | 2006-08-30 | 2008-04-24 | Veolia Es Technical Solutions | Process for recycling waster acid |
| US7473409B2 (en) | 2006-08-30 | 2009-01-06 | Veolia Es Technical Solutions L.L.C. | Process for recycling waste acid |
Also Published As
| Publication number | Publication date |
|---|---|
| KR940021432A (en) | 1994-10-17 |
| JP2788552B2 (en) | 1998-08-20 |
| CN1105797A (en) | 1995-07-26 |
| RU94046154A (en) | 1996-12-20 |
| CN1070721C (en) | 2001-09-12 |
| KR960008085B1 (en) | 1996-06-19 |
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