KR100541776B1 - Manufacturing method of artificial zeolite from fly ash - Google Patents

Manufacturing method of artificial zeolite from fly ash Download PDF

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KR100541776B1
KR100541776B1 KR1020020040521A KR20020040521A KR100541776B1 KR 100541776 B1 KR100541776 B1 KR 100541776B1 KR 1020020040521 A KR1020020040521 A KR 1020020040521A KR 20020040521 A KR20020040521 A KR 20020040521A KR 100541776 B1 KR100541776 B1 KR 100541776B1
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zeolite
water
aluminum silicate
heavy metal
fly ash
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서희동
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    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof

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Abstract

본 발명은 석탄을 연료로 사용하는 화력발전소에서 발생하는 석탄회(Fly ash)를 이용하여 토양개량제나 하·폐수처리의 암모니아, 중금속이온의 제거제와 담체로 사용할 수 있는 양질의 제올라이트(Zeolite)를 위생적으로 안전한 인공제조방법을 제시하는 것을 목적으로 한다.The present invention sanitizes a high quality zeolite that can be used as a soil improver, ammonia for sewage and wastewater treatment, a heavy metal ion remover, and a carrier using fly ash generated from a coal-fired power plant. It aims to suggest a safe artificial manufacturing method.

이를 위하여 석탄을 연료로 사용하는 화력발전소에서 연소 후 발생하는 무수(無水)의 비정질(非晶質)규산알루미늄염(Aluminosilicate)을 수용액 상태에서 90∼180℃로 가열하면서 염산(HCl)을 주입하여 pH가 4로 처리를 하여 비정질화수(非晶質和水)의 규산알루미늄염인 앨러페인(Allophane)질 점토광물로 1차 전환하면서 산 가용성(수용성)의 유해중금속물질을 탈수 및 수세처리를 하여 제거한 다음 가성소다(NaOH)나 수산화칼륨(KOH), 수산화칼슘(Ca(OH)2 ), 탄산소다(Na2CO3 ), 탄산칼륨(K2CO3 )과 같은 알칼리(Alkali)수용액을 가해서 90∼180℃로 가열교반반응을 하여 위생적으로 안전하면서 고수율의 인공제올라이트를 만드는 것이다.To this end, hydrochloric acid (HCl) is injected while heating anhydrous amorphous aluminum silicate salt, which is produced after combustion, in a coal-fired thermal power plant at 90-180 ° C in aqueous solution. When the pH is 4, the primary conversion to an allophane clay mineral, which is an aluminum silicate salt of amorphous water, is carried out by dehydration and washing with an acid soluble (water-soluble) harmful heavy metal substance. After removal, add an aqueous alkali solution such as sodium hydroxide (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca (OH) 2 ), sodium carbonate (Na 2 CO 3 ), and potassium carbonate (K 2 CO 3 ). Heat stirring at ˜180 ° C. makes the sanitary safe and high yield of artificial zeolite.

특이한 사항은, 제올라이트는 양이온교환능력(CEC; Cation exchange capacity)이 높은 특성이 있기 때문에 질소 및 중금속과 같은 양이온의 흡착능력이 우수하며, 미생물의 생육에서 담지체(擔持體)의 역할을 하기 때문에 하·폐수처리에서 질소 및 중금속의 제거 목적이나 담체로 사용하며, 또한 보비력(保肥力)이 우수하면서 토양개량효과가 우수하여 토양개량제 등으로 널리 이용될 것으로 기대된다.Specifically, zeolite has a high cation exchange capacity (CEC), so it has excellent adsorption capacity of cations such as nitrogen and heavy metals, and plays a role in supporting the growth of microorganisms. Therefore, it is expected to be used as a purpose of removing nitrogen and heavy metals in wastewater and wastewater treatment, and as a carrier, and also having excellent retention effect and excellent soil improvement effect.

석탄회(Fly ash), 제올라이트(Zeolite), 규산알루미늄염(Alumino-silicate), 양이온교환능력(Cation exchange capacity), 토양개량제, 질소 및 중금속제거제Fly ash, zeolite, aluminum silicate, cation exchange capacity, soil improver, nitrogen and heavy metal remover

Description

석탄회로부터의 인공제올라이트의 제조방법{Manufacturing method of artificial zeolite from fly ash }Manufacturing method of artificial zeolite from fly ash

본 발명은 석탄을 연료로 사용하는 화력발전소나 제철소 등에서 발생하는 석탄회(Fly ash)로부터 유해중금속성분을 제거한 다음 하·폐수 중에서 질소 및 중금속제거제, 미생물담체, 토양개량제 등에 사용할 수 있는 인공제올라이트(Zeolite)의 제조방법에 관한 것이다.The present invention removes harmful heavy metals from fly ash generated from coal-fired power plants or steel mills, and then artificial zeolites that can be used in nitrogen and heavy metal removers, microbial carriers, and soil improvers in sewage and wastewater. It relates to a method of manufacturing).

석탄회(Fly ash)는 화력발전소나 제철소 등에서 석탄이 연소시(1,400∼1,700℃) 비가연성분인 점토광물은 연소하지 않고 에너지(Energy)를 받아 용융상태로 되었다가 배기가스와 함께 비산되어 보일러(Boiler)에서 열이 회수되면서 냉각되어 미립상태의 구상입자 상태로 전기집진기에 포집되어 배출된 것으로 규산(SiO2) 및 알루미나(Alumina; Al2O3)성분이 약 70wt%, 산화철(Fe2O3)성분이 약 5wt%, 기타 MnO2 , TiO2, P2O5 등으로 구성되어있으며, 화산분출물의 초기상태와 같이 무수의 비정질규산알루미늄염(Non-crystalline aluminosilicate)이 주성분으로 되어있다.Fly ash is a non-combustible clay mineral that is not combustible when coal is burned (1,400 ~ 1,700 ℃) in a coal-fired power plant or steel mill. ) Is recovered as heat is collected and collected by the electrostatic precipitator in the form of fine spherical particles, and discharged. About 70wt% of silicic acid (SiO 2 ) and alumina (Alumina; Al 2 O 3 ) and iron oxide (Fe 2 O 3) ) Is composed of about 5wt%, other MnO 2 , TiO 2 , P 2 O 5, etc., and anhydrous non-crystalline aluminosilicate as the initial state of the volcanic eruption is the main component.

석탄회를 약산성(pH=4∼6)에서 가온처리를 하면 화수(和水)의 비정질규산알루미늄염인 앨러페인(Allophane)이 생성되며, pH가 2 이하의 강산성에서 가온 처리를 하면 음이온교환능력(AEC; Anion exchange capacity)이 높은 화수(和水)의 결정질규산알루미늄염인 이모고라이트(Imogolite)가 생성되고, 알칼리상태에서 가온 처리를 하면 양이온교환능력(CEC; Cation exchange capacity)이 높은 제올라이트(沸石; Zeolite)가 생성된다.When the coal ash is heated at weak acidity (pH = 4 to 6), allophane, an amorphous aluminum silicate salt of Hwasu, is produced. Imogolite, a crystalline aluminum silicate salt of Hwasu water with high anion exchange capacity (AEC), is produced, and zeolite (CEC) with high cation exchange capacity (CEC) is obtained when heated in an alkaline state. Zeolite is produced.

앨러페인질 점토광물은 주로 규소(Si), 알루미늄(Al), 산소(O), 수소(H)가 화학적으로는 다수의 Si-O-Al 결합에 실라놀(Silanol)기(Si-OH)와 활성알루미늄으로 된 Al(OH)H2O기의 부위에 규산이 축합(탈수적으로 결합)된 구조로 되어있는 화수(和水)규산알루미늄염(Aluminosilicate)의 점토광물(Clay mineral)로 개개의 중공구상입자(中空球狀粒子)는 일정한 형태를 가지지 않고 규소, 알루미늄, 산소, 수소가 무질서하게 결합되어 있어 X선회절적(X線回折的)으로는 비정질(非晶質)로 나타나기 때문에 비결정질점토라고도 한다.Allerpine clay clays are mainly composed of silicon (Si), aluminum (Al), oxygen (O), and hydrogen (H) chemically with a number of Si-O-Al bonds. And clay minerals of aluminum silicate salts, in which the silicic acid is condensed (dehydratedly bonded) to the Al (OH) H 2 O group of activated aluminum. The hollow spherical particles of amorphous do not have a certain form and are amorphous because silicon, aluminum, oxygen, and hydrogen are randomly combined and appear to be amorphous by X-ray diffraction. Also called clay.

천연의 앨러페인질 점토광물은 활성알루미늄 및 기타 활성미네랄 성분을 다량함유하고 있기 때문에 음이온교환능력(AEC; Anion exchange capacity)이 높아 인산 고정능력이 아주 우수하며, 토양에서는 부식물질(유기토양)을 다량 집적(集積)한 부식토양(Humus soil)으로 존재하며, 그리고 양이온교환능력(CEC; Cation exchange capacity)도 가지고 있기 때문에 K+, Na+, NH4 +와 같은 양이온을 고정하는 능력도 있다.Natural allergenic clay minerals contain a large amount of active aluminum and other active minerals, so they have a high anion exchange capacity (AEC), which is excellent in fixing phosphates. It exists as a large amount of humus soil, and also has a Cation exchange capacity (CEC), so it also has the ability to fix cations such as K + , Na + , and NH 4 + .

천연의 제올라이트는 알칼리 및 알칼리토금속의 결정질 규산알루미늄 수화물(水化物)인 광물로서 종류는 많으나 함수량(含水量)이 많은 점, 결정의 성질, 산상(産狀) 등에 공통성이 있으며, 일반적으로 무색 투명하거나 백색 반투명하며, 취관(吹管)으로 가열하면 끓어서 팽대하기 때문에 비석(沸石)이라고 하였으며, 대부분의 종류는 염산(HCl)에 녹아 흔히 아교 모양이 되지만, 소수의 종류는 염산에 녹지 않는 것도 있으며, 주요한 종류로서 방비석(方沸石; Analcime), 어안석(魚眼石; Apophyllite), 캐버자이트(Chabazite), 소다비석(Natrolite), 휼란다이트(Heulandite), 스틸바이트(Stilbite), 로몬타이트(Laumontite), 이네사이트(Inesite) 등이 있으며, 현무암(玄武岩)이나 휘록응회암(輝綠凝灰岩) 등 염기성 화성암(火成岩)의 공동(空洞) 속이나 열극(裂隙)에서 산출되며, 때로는 화강암(花崗岩), 편마암(片麻岩) 중에 2차 광물(二次鑛物)로서 존재하며, 또한 금광맥과 같은 광맥 중에서 산출되는 경우도 있으며, 결정구조적으로 각 원자의 결합이 느슨하여, 그 사이를 채우고 있는 수분을 고열로 방출시켜도 골격은 그대로 있으므로 다른 미립물질(微粒物質)을 흡착할 수가 있어 이 성질을 이용해서 흡착제로 사용하며, 크기가 다른 미립물질을 분리시키는 분자체(分子篩; Molecular sieve)로도 사용한다.Natural zeolites are minerals that are crystalline aluminum silicate hydrates of alkali and alkaline earth metals, but they are common in many types but have a high water content, crystal properties, and acid phase. Or it is white translucent, and it is called zeolite because it boils and expands when it is heated by blowing pipe. Most kinds are melted in hydrochloric acid (HCl), so it is often glued, but few kinds are insoluble in hydrochloric acid. The main varieties include: Analcime, Apophyllite, Cabbazite, Natrolite, Helandite, Stilbite, Laumontite. ) And Inesite, which are produced in the cavity of a basic igneous rock such as basalt or whirlwind, or in a hot pole. It exists as a secondary mineral in granite and gneiss, and is also produced in mineral veins such as gold mine veins. The crystal structure of each atom is loose and therebetween. Molecular sieve that separates particulates of different sizes by using this property to adsorb other particulate matters. Also used as).

석탄회는 비정질 무수규산알루미늄인데, 앨러페인은 비정질 화수규산알루미늄으로 차이점은 석탄회는 무수물(無水物)인데 반해서 앨러페인은 화수물(和水物)인 차이점이 있다.Coal ash is amorphous aluminum silicate anhydrous. Allergy is amorphous aluminum silicate silicate. The difference is that coal ash is anhydrous, whereas allergy is an anhydrous substance.

앨러페인을 알칼리와 반응을 하면 결정화되면서 제올라이트로 전환되며, 무수물인 석탄회도 알칼리와 반응을 하면 결정화되면서 제올라이트로 전환된다.When allerphan is reacted with alkali, it is crystallized and converted to zeolite. Anhydrous coal ash is also converted to zeolite as it is crystallized when reacted with alkali.

전술한 제올라이트의 생성원리를 이용하여 대한민국 특허 공개번호 1998-033471호, 1999-0065036호와 일본특허 공개번호 소(昭) 59-86687호, 평(平) 6-100314호, 평(平) 6-144829호, 평(平) 6-340417호, 평(平) 7-196315호, 평(平) 7-232913호, 평(平) 9-255324호, 2000-72435호, 2001-106523호, 2001-146417호, 2001-220132호 등에서는 석탄회를 알칼리처리를 하여 인공제올라이트의 제조방법이 제시되었으나, 석탄회 중에는 대부분 미네랄이 연소시 에너지를 받아 활성화된 수용성 미네랄 성분이 다량 존재하는데 이중 인체에 해로운 구리(Cu), 카드뮴(Cd), 크롬(Cr)과 같은 유해중금속성분도 존재하는데, 이들 유해중금속성분을 제거하지 않은 상태의 제품을 토양개량제 등으로 사용하였을 때는 유해중금속성분이 먹이사슬에 의해서 인체에 유해한 작용을 줄 수 있다고 하는 문제점이 제시되어 널리 보급되지 못하고 있다.
대한민국 특허 공개번호 2000-0012888호의 석탄 회 및 소각회로부터 인공 앨러페인의 제조공정에서 pH의 2∼4로 조정을 탄산(H2CO3)이나 황산으로 조정한 경우는 탄산 또는 황산 미네랄염(유해 중금속성분의 탄산 또는 황산염 포함)이 생성되어 탈수 및 수세를 할 때 유해 중금속성분이 충분히 제거되지 않아, 이 앨러페인을 이용하여 제올라이트를 제조하였을 때 제품 중에 유해중금속 함량이 높은 문제점이 있었다.
By using the above-described production principle of zeolite, Korean Patent Publication Nos. 1998-033471, 1999-0065036 and Japanese Patent Publication Nos. 59-86687, 6-6314, and 6 -144829, Pyeong 6-340417, Pyeong 7-196315, Pyeong 7-232913, Pyeong 9-255324, 2000-72435, 2001-106523, In 2001-146417 and 2001-220132, a method of producing artificial zeolite by alkali treatment of coal ash has been proposed. However, most of the coal-soluble ash contains a large amount of water-soluble minerals activated by the combustion of minerals. There are also harmful heavy metals such as (Cu), cadmium (Cd), and chromium (Cr). When the products without these harmful heavy metals are used as soil improving agents, the harmful heavy metals are introduced to the human body by the food chain. It is widely reported that the problem of harmful action has been suggested. I'm not in a hurry.
In the process of manufacturing artificial allergy from coal ash and incineration ash of Korean Patent Publication No. 2000-0012888, when adjusting the pH to 2-4 with carbonic acid (H 2 CO 3 ) or sulfuric acid, When the heavy metal component (including carbonic acid or sulfate) is generated and the heavy metal component is not sufficiently removed when dehydrated and washed with water, there is a problem in that the product contains high harmful heavy metal in the product when the zeolite is prepared using this allergy.

본 발명은 상기와 같은 문제점을 해소하기 위해 석탄회에 포함되어 있는 유해중금속 성분을 제거한 다음 위생적으로 안전하면서 반응수율이 높은 인공제올라이트의 제조방법을 제공하는데 본 발명의 목적이 있는 것이다.It is an object of the present invention to remove the harmful heavy metal components contained in coal ash in order to solve the above problems, and then to provide a method for producing artificial zeolite which is hygienically safe and has a high reaction yield.

이와 같은 목적을 달성하기 위한 본 발명은, 석탄회를 가열상태에서 염산(HCl)을 가해서 pH를 4로 조정하면서 앨러페인질로 전환 후 수세탈수를 하여 유해중금속 성분을 제거한 다음 알칼리수용액을 주입한 후 가열교반반응을 하여 위생적으로 안전한 인공제올라이트 제조방법을 제시한다.In order to achieve the above object, the present invention is to change the pH to 4 by adding hydrochloric acid (HCl) in a heated state of coal ash, and then washed with water and dehydrated to remove harmful heavy metal components, and then injected with alkaline aqueous solution. The present invention provides a method for preparing artificial zeolite that is hygienically safe by stirring.

석탄회를 알칼리수용액 상태에서 90℃로 가열하면서 염산(HCl)을 가해서 pH를 4로 조정한 후 가열(90∼180℃)하는 상태에서 교반반응을 하여 비정질화수의 규산알루미늄염인 앨러페인질 점토광물로 전환후 탈수기로 보내어 탈수시 수세수로 수세를 하여 수용성 유해중금속성분을 제거한 다음 위생적으로 안전한 제품을 만든다.Alkaline clay minerals, which are aluminum silicate salts of amorphous water, are subjected to agitation in the state of heating (90-180 ° C) by adding hydrochloric acid (HCl) while heating the coal ash to 90 ° C in an alkaline aqueous solution. After dehydration, it is sent to a dehydrator, and when dehydrated, it is washed with water to remove water-soluble harmful heavy metals and make a hygienically safe product.

석탄회 중에는 알칼리금속산화물(Na2O, K2O 등)과 알칼리토금속산화물(CaO, MgO 등)이 존재하기 때문에 수용액상태에서 pH가 12∼13 범위의 알칼리성을 나타내기 때문에 1차 수세처리를 한 다음 염산(HCl)을 가해서 pH를 4로 조정한 후 90∼180℃로 가열하면서 4시간 이상 교반반응을 하여 비정질화수규산알루미늄염인 앨러페인질 점토광물로 전환한다.Alkaline metal oxides (Na 2 O, K 2 O, etc.) and alkaline earth metal oxides (CaO, MgO, etc.) are present in the coal ash, so the pH is 12-13 in aqueous solution. Then, hydrochloric acid (HCl) is added to adjust the pH to 4, followed by stirring for at least 4 hours while heating to 90-180 ° C. to convert to allerpineic clay mineral, an amorphous aluminum silicate salt.

앨러페인질 점토광물로 반응이 완료되면 탈수기로 보내어 탈수처리를 하면서 수세수를 분무노즐(Spray nozzle)로 탈수되는 앨러페인질 점토광물을 수세하여 수용성 유해중금속 성분을 제거한다.When the reaction is completed with an allerpine clay clay, it is sent to a dehydrator for dehydration, and the water is washed with an allerpine clay clay dehydrated with a spray nozzle to remove water-soluble harmful heavy metals.

유해중금속성분의 제거와 탈수 처리된 앨러페인질 점토광물에 알칼리금속의 염(NaCl, Na2SO4, KCl, K2SO4 등)이나 알칼리토금속의 염(MgCl2, MgSO4, CaCl2 등)과 0.1∼0.5N의 가성소다(NaOH)나 수산화칼륨(KOH), 수산화칼슘(Ca(OH)2 ), 탄산소다(Na2CO3 ), 탄산칼륨(K2CO3 )을 단독 또는 2종류 이상을 혼합한 알칼리(Alkali)수용액을 가해서 90∼180℃로 가열하면서 4시간 이상 교반반응을 하여 제올라이트로 전환한다.Alkaline metal salts (NaCl, Na 2 SO 4 , KCl, K 2 SO 4, etc.) or alkaline earth metal salts (MgCl 2 , MgSO 4 , CaCl 2, etc.) ) And 0.1 to 0.5 N caustic soda (NaOH), potassium hydroxide (KOH), calcium hydroxide (Ca (OH) 2 ), sodium carbonate (Na 2 CO 3 ), potassium carbonate (K 2 CO 3 ) alone or two types Alkali aqueous solution mixed with the above was added, and the mixture was stirred for 4 hours or more while heated to 90-180 占 폚 to convert to zeolite.

제올라이트로 반응이 완료되면 탈수 및 수세처리를 한 다음 건조하여 분발 상태로 제품화하거나, 바인더(Binder)를 혼합하여 구상이나 입상의 펠렛트(Pellet)로 성형가공하여 건조 후 제품화한다.When the reaction is completed with zeolite, it is dehydrated and washed with water and then dried to produce a powder, or a binder is mixed and molded into spherical or granular pellets and dried to produce a product.

필요에 따라서는 pH를 7로 중화처리 후 필요한 형태로 가공하여 제품화한다.If necessary, neutralize the pH to 7, and then process the product into the required form to produce a product.

펠렛트상으로 성형가공은 유해중금속성분의 제거와 탈수처리가 된 제올라이트에 제올라이트 무게를 기준으로 무기바인더(Binder)로 벤토나이트(Bentonite)를 5wt%, 유기바인더로는 알긴산(Alginic acid)소다(Soda)나 셀룰로오스(Cellulose) 계를 10wt%를 혼합하고, 이들에 염화암모늄(NH4Cl)을 10wt% 혼합한 후 펠렛트상으로 성형가공이 용이하도록 이들에 물을 가해서 전체혼합물의 함수율이 38∼43wt%로 조정한 다음 교반혼합하여 구상(球狀)이나 막대형 환상(環狀)의 펠렛트로 성형 가공하여 상온에서 자연 건조한 후 전기로나 가열로에서 1,000℃ 이상으로 가열하여 다공질(多孔質)의 건조된 펠렛트를 가공한다.Molding process in pellet form is 5% by weight of bentonite as inorganic binder and 5% by weight of zeolite based on the weight of zeolite to zeolite which has been removed harmful metals and dehydrated, and soda (Alginic acid) soda as organic binder. 10% by weight of cellulose (Cellulose), 10% by weight of ammonium chloride (NH 4 Cl) is added to the water to facilitate the molding process in pellet form, water content of the mixture is 38 ~ 43wt% After mixing, stirring and mixing, forming into spherical or rod-shaped pellets, drying them naturally at room temperature, and heating them to at least 1,000 ℃ in an electric furnace or a heating furnace, and drying the porous Process the pellets.

유해중금속성분이 함유된 탈수여액 및 수세수는 중화조로 보내어 중화제로 pH를 7∼8로 조정하여 수용성 중금속성분을 고형의 금속수산화물로 전환한 다음, 응집조로 보내어 침전조에서 침전분리가 용이하도록 고분자 응집보조제를 주입하여 풀록(Floc)을 형성한 다음 침전조로 보내어 고형물은 침전되고, 상등수는 처리수조로 보내어 수세수로 재이용하거나 방류하며, 침전된 슬러리(Slurry)는 탈수기로 보내어 탈수 처리한다.The dehydration liquid and the flushing water containing the harmful heavy metal components are sent to the neutralization tank to adjust the pH to 7-8 with a neutralizing agent to convert the water-soluble heavy metal components into solid metal hydroxides, and then to the flocculation tank to facilitate the sedimentation and separation in the precipitation tank. Inject the adjuvant to form a floc, and then send it to the settling tank to precipitate solids, and the supernatant is sent to a treatment tank for reuse or discharge as washing water, and the precipitated slurry is sent to a dehydrator for dehydration.

전술한 기술내용으로부터 자명하듯이, 본 발명은, 폐기물로 발생하는 석탄회를 유가의 제올라이트로 만드는 자체가 폐자원을 자원화하는 효과가 있으며, 이를 하·폐수처리의 질소, 중금속의 제거 및 미생물의 담지체로 이용될 수 있으며, 농업분야에서는 토양개량제로 사용하였을 때 효능이 우수하기 때문에 이들 분야에 널리 이용될 것으로 기대된다.As will be apparent from the above description, the present invention has the effect of recycling the waste resources by itself to make coal ash generated as a waste of oil price zeolite, and to remove nitrogen and heavy metals in sewage and wastewater treatment and to support microorganisms. It can be used as a sieve, and in the agricultural field is expected to be widely used in these fields because of its excellent efficacy when used as a soil improving agent.

Claims (2)

석탄회(Fly ash)로부터 제올라이트(Zeolite)의 제조에서 유해한 수용성 중금속 성분을 제거하기 위해서 가열하는 상태에서 염산(HCl)을 가하여 pH를 4로 조정하면서 4시간 이상 교반반응을 하여 비정질화수규산알루미늄염인 앨러페인질 점토광물로 전환한 후 유해중금속성분을 탈수 및 수세처리를 하여 제거한 다음, 알칼리금속의 염(NaCl, Na2SO4, KCl, K2SO4)이나 알칼리토금속의 염(MgCl2, MgSO4, CaCl2 )과 0.1∼0.5N의 가성소다(NaOH)나 수산화칼륨(KOH), 수산화칼슘(Ca(OH)2 ), 탄산소다(Na2CO3 ), 탄산칼륨(K2CO3 )을 단독 또는 2종류 이상을 혼합한 알칼리(Alkali)수용액을 가해서 90∼180℃로 가열하면서 4시간 이상 교반반응을 한 다음 탈수 및 수세처리를 한 후 건조하여 인공제올라이트를 제조하는 방법.In order to remove harmful water-soluble heavy metal components in the production of zeolite from fly ash, hydrochloric acid (HCl) was added and the pH was adjusted to 4 while stirring for at least 4 hours to obtain amorphous aluminum silicate salt. After conversion to an allergenic clay mineral, the detrimental heavy metals were removed by dehydration and washing, and then salts of alkali metals (NaCl, Na 2 SO 4 , KCl, K 2 SO 4 ) or salts of alkaline earth metals (MgCl 2 , MgSO 4 , CaCl 2 ) and 0.1 ~ 0.5N Caustic Sodium (NaOH) or Potassium Hydroxide (KOH), Calcium Hydroxide (Ca (OH) 2 ), Sodium Carbonate (Na 2 CO 3 ), Potassium Carbonate (K 2 CO 3 ) Method of preparing an artificial zeolite by adding an aqueous alkali solution mixed with one or two or more of them and stirring the mixture for at least 4 hours while heating to 90 to 180 ° C., followed by dehydration and washing with water. 제1항에 있어서, 탈수처리가 된 분말상태의 인공 제올라이트에 제올라이트 무게를 기준으로 무기바인더(Binder)로 벤토나이트(Bentonite)를 5wt%, 유기바인더로는 알긴산(Alginic acid)소다(Soda)나 셀룰로오스(Cellulose)계를 10wt%를 혼합하고, 이들에 염화암모늄(NH4Cl)을 10wt% 혼합한 후 펠렛트(Pellet)상으로 성형가공이 용이하도록 이들에 물을 가해서 전체혼합물의 함수율이 38∼43wt%로 조정한 다음 교반혼합한 후 구상(球狀)이나 막대형 환상(環狀)의 펠렛트상으로 성형 가공하여 상온에서 자연 건조한 후 전기로나 가열로에서 1,000℃ 이상으로 가열하여 다공질(多孔質)의 건조된 펠렛트상의 인공 제올라이트를 제조하는 방법According to claim 1, 5 wt% of bentonite in an inorganic binder (Binder) based on the weight of the zeolite in the dehydrated powder artificial zeolite, Alginic acid soda (Soda) or cellulose as an organic binder 10 wt% of the (Cellulose) system is mixed, and 10 wt% of ammonium chloride (NH 4 Cl) is mixed therein, and water is added to them to facilitate the molding process into pellets. After adjusting to 43wt%, the mixture is stirred and mixed, then formed into spherical or rod-shaped pellets and dried naturally at room temperature, and then heated to 1,000 ° C or above in an electric furnace or a heating furnace to be porous. To prepare artificial zeolite on dried pellets)
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