KR100541777B1 - Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash - Google Patents

Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash Download PDF

Info

Publication number
KR100541777B1
KR100541777B1 KR1020020033856A KR20020033856A KR100541777B1 KR 100541777 B1 KR100541777 B1 KR 100541777B1 KR 1020020033856 A KR1020020033856 A KR 1020020033856A KR 20020033856 A KR20020033856 A KR 20020033856A KR 100541777 B1 KR100541777 B1 KR 100541777B1
Authority
KR
South Korea
Prior art keywords
ash
aluminum silicate
clay mineral
water
clay
Prior art date
Application number
KR1020020033856A
Other languages
Korean (ko)
Other versions
KR20030096812A (en
Inventor
서희동
서영진
서영준
Original Assignee
서희동
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by 서희동 filed Critical 서희동
Priority to KR1020020033856A priority Critical patent/KR100541777B1/en
Publication of KR20030096812A publication Critical patent/KR20030096812A/en
Application granted granted Critical
Publication of KR100541777B1 publication Critical patent/KR100541777B1/en

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/20Silicates
    • C01B33/36Silicates having base-exchange properties but not having molecular sieve properties
    • C01B33/38Layered base-exchange silicates, e.g. clays, micas or alkali metal silicates of kenyaite or magadiite type
    • C01B33/40Clays

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Water Treatment By Sorption (AREA)

Abstract

본 발명은 석탄을 연료로 사용하는 화력발전소나 제철소등에서 발생되는 석탄회(Fly ash)나 산업폐기물을 소각로에서 소각후 발생되는 소각회를 이용하여 하 · 폐수의 질소, 인 제거제나 녹 · 적조처리제로 사용하는 양질의 앨로페인(Allophane)질점토광물을 위생적으로 안전한 인공제조 방법을 제시하는 것을 목적으로 한다.The present invention utilizes fly ash or industrial waste generated from coal-fired power plants or steel mills as incinerators after incineration to remove nitrogen, phosphorus, rust and red tide treatment agents. The purpose of the present invention is to propose an artificially safe method for manufacturing high quality Allophane vaginal clay mineral.

이를 위하여 석탄을 연료로 사용하는 화력발전소, 제철소나 소각로에서 연소후 발생되는 무수(無水)의 비정질(非晶質)규산알루미늄염(Aluminosilicate)을 수용액 상태에서 90∼180℃로 가열하면서 염산(HCl)을 주입하여 pH가 4정도에서 처리를 하여 비정질화수(非晶質和水)의 규산알루미늄염인 앨로페인질점토광물을 제조함에 있어 유해 중금속물질을 산성상태에서 수세처리를 하여 위생적으로 안전한 제품을 만드는 것이다.To this end, hydrochloric acid (HCl) is heated by heating anhydrous amorphous aluminum silicate salt produced after combustion in a coal-fired power plant, steel mill or incinerator to 90-180 ° C in an aqueous solution. Product is treated at a pH of about 4 to produce allophosphorus clay mineral, an aluminum silicate salt of amorphous water, which is hygienic and safe by washing with harmful heavy metals in an acidic state. To make.

특이한 사항은, 앨로페인질점토광물은 양이온교환능력(CEC ; Cation exchage capacity)과 음이온교환능력(AEC ; Anion exchange capacity)을 가지고 있어 질소, 인 제거능력이 우수하기 때문에 하 · 폐수처리에서 질소, 인 제거제, 녹 · 적조처리와 미생물 배양공정 등에 널리 이용될 것으로 기대된다.Of particular note, because allophosphorus clay minerals have a cation exchange capacity (CEC) and anion exchange capacity (AEC), they are excellent in removing nitrogen and phosphorus. It is expected to be widely used for phosphorus remover, green / red tide treatment and microbial culture process.

석탄회(Fly ash), 소각회, 앨로페인(Allophane), 점토광물(Clay mineral), 규산알루미늄염(Aluminosilicate), 양이온교환능력(Cation exchange capacity), 음이온교환능력(Anion exchange capacity)Fly ash, incineration ash, allophane, clay mineral, aluminum silicate, cation exchange capacity, anion exchange capacity

Description

석탄회나 소각회로부터의 인공앨로페인질점토광물의 제조방법{Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash}Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash}

도 1은 석탄회나 소각회로부터의 인공앨로페인질점토광물 제조공정도1 is a process chart for manufacturing artificial allotropin clay mineral from coal ash or incineration ash

본 발명은 석탄을 연료로 사용하는 화력발전소나 제철소 등에서 발생되는 석탄회나 산업폐기물을 소각하는 소각로에서 배출되는 소각회로부터 하·페수중 질소, 인 제거제, 녹·적조 처리제, 유기물질을 부식물질로 전환하는 부식화반응에서 토양미생물에 미네랄 공급제 등으로 사용하는 앨로페인(Allophane)질점토광물(Clay minerals)의 인공제조방법에 관한 것이다.In the present invention, nitrogen, phosphorus remover, rust / red tide treatment agent and organic substances in sewage and wastewater are discharged from incineration ash discharged from an incinerator for burning coal ash or industrial waste generated from a coal-fired power plant or steel mill. The present invention relates to an artificial manufacturing method of allophane clay minerals used as a mineral supply to soil microorganisms in converting corrosive reactions.

천연적으로 앨로페인질점토광물은 화산지대의 산성화산회토양에 다량 존재하며, 규반비( SiO2/Al2O3)는 0.3∼2.0로 폭이 넓으며, 주로 규소(Si), 알루미늄(Al), 산소(O), 수소(H)가 화학적으로는 다수의 Si-O-Al 결합에 실라놀(Silanol)기(Si-OH)와 활성알루미늄으로된 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 결합되어있어 X선회절적(X線回折的)으로는 비정질(非晶質)로 나타나기 때문에 비결정질점토(Non-crystalline clay)라고도 한다.Naturally allophosphorus clay minerals are present in the volcanic acid volcanic soil, and the silica ratio (SiO 2 / Al 2 O 3 ) is 0.3 ~ 2.0 wide, mainly silicon (Si) and aluminum (Al). ), Oxygen (O), hydrogen (H) is chemically the site of the Al (OH) H 2 O group consisting of a silanol group (Si-OH) and activated aluminum to a number of Si-O-Al bonds Clay minerals of aluminum silicate salts with condensation (dehydration-bonding) of silicic acid, each hollow spherical particle has a certain form. It is also called non-crystalline clay because silicon, aluminum, oxygen, and hydrogen are randomly combined and appear to be amorphous by X-ray diffraction.

앨로페인질점토광물의 특성은 활성알루미늄 및 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 있으며, 특히 앨로페인질광물에는 활성화된 미네랄(수용성미네랄) 성분이 많으며, 입자간의 결합력이 약하기 때문에 자연 중에서 풍식(風蝕)이나 수식(水蝕)에 의한 물리 · 화학적 풍화작용(Physical & Chemical weathering)과 토양미생물의 대사산물에 의해서 침식되는 생물학적 풍화작용(Biological weathering)을 받아 토양미생물 및 식물에 미네랄을 공급하는 기능이 우수다.Because of the large amount of active aluminum and active minerals, allophyllin clay minerals have high anion exchange capacity (AEC), which is very effective in fixing phosphate, and in soils, it contains large amounts of corrosive substances (organic soils). It exists as aggregated 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 + . Allophyllin minerals contain many active minerals (water-soluble minerals), and because of their low binding strength, they are characterized by physical and chemical weathering and soil microorganisms caused by wind and water in nature. It is excellent in the function of supplying minerals to soil microorganisms and plants by receiving biological weathering which is eroded by metabolites.

그래서 앨로페인질 함량이 많은 다공질의 부석(Pumice)을 하 · 폐수처리의 생물학적 부식화반응에 의해서 유기오염물질을 처리하는 공정, 악취처리공정 및 가축의 음용수처리공정 등에 널리 이용되고 있다.Therefore, it is widely used in the process of treating organic pollutants by biological corrosive reaction of sewage and wastewater treatment, odor treatment process, and drinking water treatment of livestock.

앨로페인질점토광물이 천연적으로 생성되는 메커니즘(Mechanism)은 규산질광물이 지열에 의해 에너지(Energy)를 받아 용융상태로된 용암(Lava)이 화산활동에 의해서 대기로 분출된 초기의 화산회는 무수(無水)의 비정질규산알루미늄염의 상태로 퇴적되었다가 우수 등에 의해서 물과 반응하여 산성화되었으며, 이때 반응 메커니즘은 다음과 같다.Mechanism in which allotropin clay mineral is produced naturally is the early volcanic ash from which siliceous minerals are energized by geothermal heat and molten lava is released into the atmosphere by volcanic activity. It was deposited in the state of amorphous aluminum silicate (non-water) and acidified by reaction with water by rainwater, etc. The reaction mechanism is as follows.

Figure 112002514788144-pat00002
Figure 112002514788144-pat00002

기타 활성화된 미네랄(Mn +)도 상기 ① ∼ ④의 반응과 동일한 반응에 의해서 수소이온( H+)을 방출하면서 산성화되었다.Other activated minerals (M n + ) were also acidified while releasing hydrogen ions (H + ) by the same reactions as those of the above ① to ④.

Mn + nH2O ---→ nM(OH)n(aq) + n H+ (aq)············⑤ M n + nH 2 O --- → nM (OH) n (aq) + n H + (aq) ・ ・ ・ ・ ・ ・ ⑤

pH가 4∼6정도의 약산성의 상태에서 무수의 비정질규산알루미늄염은 화수의 비정질규산알루미늄염인 앨로페인질점토광물로 되었으며, pH가 2이하의 강산성으로 된 경우에는 화수의 결정질규산알루미늄염인 이모고라이트(Imogolite)질점토광물로 전환되었다.Anhydrous amorphous aluminum silicate salt in the state of weakly acidic pH of 4 ~ 6 became an allophospholipid clay mineral, an amorphous aluminum silicate salt of Hwasu, and when the pH becomes strong acid less than 2, it is a crystalline aluminum silicate salt of Hwasu. It was converted to an imogolite vaginal clay mineral.

반면에, 화산분출물중 유리상태의 알칼리산화물(Na2O, K2O 등)이나 알칼리토금속산화물(CaO, MgO, BaO 등)이 상대적으로 많은 경우에는 알칼리 상태에서 지열에 의한 가열반응이 일어난 경우에는 비석(沸石, Zeolite)이 생성되었다.On the other hand, when there are relatively large amounts of free alkali oxides (Na 2 O, K 2 O, etc.) or alkaline earth metal oxides (CaO, MgO, BaO, etc.) of volcanic eruptions, geothermal heating reactions occur in alkali state. Zeolite was formed in.

석탄회(Fly ash)는 석탄 중 비가연성분인 점토광물은 연소시(1,400∼1,700℃) 연소되지 않고 에너지를 받아 용융상태로 되었다가 배기가스와 함께 비산하여 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 MnO, TiO2, P2O5 등으로 구성되어있으며, 화산분출물의 초기상태와 같이 무수의 비정질규산알루미늄염이 주성분으로 되어있다.Fly ash is a non-combustible clay mineral in coal. When it is burned (1,400 ~ 1,700 ℃), it is not burned and is energized to be melted. It is then scattered with the exhaust gas and cooled by recovering heat from the boiler. Collected and discharged in the electrostatic precipitator in the form of particulate spherical particles, about 70wt% of silicic acid (SiO 2 ) and alumina (Alumina; Al 2 O 3 ), about 5wt% of iron oxide (Fe 2 O 3 ), etc. It is composed of MnO, TiO 2 , P 2 O 5, etc., and has anhydrous amorphous aluminum silicate salt as the main component like the initial state of volcanic eruption.

따라서, 석탄회나 소각회를 약산성(pH=4∼6)에서 가온처리를 하면 화수의 비정질규산알루미늄염인 앨로페인이 생성되며, pH가 2이하의 강산성에서 가온처리를 하면 음이온교환능력이 높은 화수의 결정질규산알루미늄염인 이모고라이트(Imogolite)가 생성되고, 알칼리상태에서 가온처리를 하면 양이온 교환능력이 높은 비석(Zeolite)이 생성된다.Therefore, when coal ash or incineration is heated at weak acidity (pH = 4 ~ 6), allophane, an amorphous aluminum silicate salt, is heated, and when warmed at strong acidity of 2 or less pH, Imogolite, which is a crystalline aluminum silicate of, is produced, and zeolite, which has a high cation exchange capacity, is formed by heating in an alkali state.

전술한 앨로페인질점토광물의 생성원리를 이용하여 대한민국특허 공개번호 2001-0089935호에서 석탄회 및 소각회를 산성상태에서 가온 처리를 하여 인공앨로페인질 광물의 제조방법이 제시되어 있으나 석탄회 중에는 대부분 미네랄이 연소시 에너지를 받아 활성화된 수용성 미네랄 성분이 다량 존재하는데 이중 인체에 해로운 구리(Cu), 카드뮴(Cd), 크롬(Cr)과 같은 중금속성분이 미량 존재하는데, 이 중금속성분을 제거하지 않은 상태의 제품으로 녹·적조처리를 위해서 하천이나 해역에 살포시 유해중금속 성분이 먹이사슬에 의해서 인체에 유해한 작용을 줄 수 있다고 하여 널리 이용되지 못하고 있는 문제점이 있으며, 대한민국특허 공개번호 2002-0039292호에서는 석탄회나 소각회를 알칼리성 상태에서 안정화처리 후 산성상태에서 가온 처리를 하여 인공앨로페인질 광물의 제조방법이 제시되어 있으나 이 역시 석탄회나 소각회에 함유되어 있는 중금속이 제거되지 않아 사용상 문제점이 있다.Using the above-mentioned principle of the production of allophosphorus clay minerals in Korea Patent Publication No. 2001-0089935, coal ashes and incineration ashes are heated in an acidic state to produce artificial allopein minerals. When minerals are burned and energized, there are a large amount of water-soluble minerals activated. Among them, trace metals such as copper (Cu), cadmium (Cd), and chromium (Cr) are harmful to the human body. It is a problem that it is not widely used because the harmful heavy metal component can cause harmful action to human body by the food chain when spraying it in rivers or sea areas for rust and red tide treatment as a product in the state. In Korea Patent Publication No. 2002-0039292 Coal ash or incineration ash is stabilized in alkaline state and warmed in acidic state. It presented a method for producing mineral quality to the campaign, but also do not have the heavy metals contained in fly ash or incinerated once removed there is a usability problem.

본 발명의 목적은 대부분 폐기물로 처리되고 있는 석탄회나 산업폐기물 소각장에서 배출되는 소각회를 종래기술의 문제점을 해결하면서 위생적으로 안전한 유가의 인공앨로페인질점토광물 제조방법을 제시하는 것이다.It is an object of the present invention to propose a method for producing artificial allotropin clay minerals of hygienic and safe oil value while solving the problems of the prior art incineration ash discharged from coal ash or industrial waste incinerator, which is mostly treated as waste.

상기의 목적을 달성하기 위하여 석탄회나 소각회를 알칼리수용액 상태에서 90∼180℃ 범위로 가열하여 안정화한 다음에, 염산(HCl)을 가해서 pH를 4로 조정한 후 가열(90∼180℃)하는 상태에서 교반반응을 하여 비정질화수의 규산알루미늄염인 앨로페인질점토광물로 전환한 후 탈수기로 보내어 탈수시 수세수로 수세를 하여 유해 중금속성분을 제거한 다음에, 위생적으로 안전한 앨로페인질점토광물 제품을 만든다.In order to achieve the above object, coal ash or incineration ash is stabilized by heating to 90-180 ° C in alkaline aqueous solution, and then heated (90-180 ° C) after adjusting the pH to 4 by adding hydrochloric acid (HCl). After agitating in the state, it is converted to allotropin clay mineral, which is an aluminum silicate salt of amorphous water, sent to a dehydrator and washed with water to remove harmful heavy metals. Make

이하 첨부된 도면을 중심으로 상세히 설명하면 다음과 같다.Hereinafter, with reference to the accompanying drawings in detail as follows.

무수비정질규산알루미늄염의 성분을 함유한 미립상의 구상입자 분발인 석탄회나 소각회 중에는 알칼리금속산화물(Na2O, K2O 등)과 알칼리토금속산화물(CaO, MgO 등)이 존재하기 때문에 수용액상태에서는 pH가 12∼13 범위의 알칼리성을 나타낸다.Alkaline metal oxides (Na 2 O, K 2 O, etc.) and alkaline earth metal oxides (CaO, MgO, etc.) are present in coal ashes and incineration ashes, which are particulate spherical particle powders containing anhydrous amorphous aluminum silicate salts. pH shows alkalinity in the range of 12-13.

석탄회나 소각회를 화수의 규산알루미늄염인 앨로페인질점토광물로 반응효율을 향상하기 위해서는 수용액상태에서 바로 산을 가해서 산성상태에서 가열처리를 하는 것보다 알칼리상태에서 가열처리를 하여 제올라트(Zeolite; 沸石)로 안정화처리를 한 다음에, 가열상태에서 염산(HCl)을 가해서 pH를 4로 조정한 다음 교반반응을 하는 것이 반응효율이 높기 때문에 석탄회나 소각회에는 알칼리성분을 함유하고 있으나 소량 함유하고 있기 때문에 가성소다(NaOH)와 소금(NaCl)을 4∼5wt%를 가한 다음 90∼180°C로 가열하면서 교반반응을 4시간 이상하여 제올라이트로 안정화한 다음 염산을 가해서 pH를 4로 조정한 후 가열( 90∼180℃)상태에서 4시간 이상 교반반응을 하여 비정질화수규산알루미늄염인 앨로페인질점토광물로 전환한다.To improve the reaction efficiency of coal ash or incineration ash with allophosphorus clay mineral, which is an aluminum silicate salt of Hwahwa, zeolite (heat treatment is performed in alkali state rather than acid in aqueous solution and heat treatment in acidic state). After stabilizing with zeolite, adjusting the pH to 4 by adding hydrochloric acid (HCl) in a heated state and then stirring the reaction, coal ash or incineration ash contains an alkali component, but a small amount Since it contains 4 ~ 5wt% of caustic soda (NaOH) and salt (NaCl), the mixture is heated to 90 ~ 180 ° C and stirred for more than 4 hours to stabilize with zeolite, and then hydrochloric acid is added to adjust pH to 4. Then, the mixture is stirred for 4 hours or more in a heated (90 to 180 ° C.) state, and is converted into an allophosphorus clay mineral, which is an amorphous aluminum silicate salt.

그러나 석탄회나 소각회는 유가(有價)의 물질이 아니기 때문에 하·폐수처리의 질소, 인제거제나 녹·적조 처리제로 사용하는 경우에는 경제적인 문제를 고려시 알칼리안정화반응에서 가성소다나 소금과 같은 유가의 물질을 사용할 필요가 없으므로 반응효율이 다소 떨어지더라도 석탄회나 소각회 중에 있는 알칼리성분만으로 알칼리안정화반응을 한다.However, coal ash or incineration ash is not an oil-based substance, so when it is used as nitrogen, phosphorus remover or rust / red tide treatment agent for sewage and wastewater treatment, it is considered to be economical, such as caustic soda and salt. Since there is no need to use oil-based materials, even if the reaction efficiency decreases, the alkali stabilization reaction is carried out using only alkali components in coal ash or incineration ash.

앨로페인질점토광물로 반응이 완료되면 탈수기로 보내어 탈수처리를 하면서 수세수를 분무노즐(Spray nozzle)로 탈수되는 앨로페인질점토광물을 수세하여 수용성 유해중금속 성분을 제거한다.When the reaction is completed with allophyllin clay mineral, it is sent to the dehydrator for dehydration, and the water is washed with an allophosphorus clay mineral dehydrated with a spray nozzle to remove water-soluble harmful heavy metal components.

유해중금속성분의 수세제거처리 및 수분을 탈수처리한 약산성의 습윤상태의 앨로페인질점토광물은 하·폐수처리의 질소, 인제거제나 녹·적조 처리제로 제품화한다.The weakly acidic allotropin clay mineral, which is washed with water, and dehydrated with harmful heavy metals, is commercialized as nitrogen, phosphorus remover, or rust and red tide treatment in sewage and wastewater treatment.

필요에 필요에 따라서는 탈수처리된 앨로페인질점토광물을 수용액상태에서 가성소다를 가해서 pH를 7로 중화처리 후 탈수하여 이용한다.If necessary, dehydrated allophosphorus clay mineral is added to caustic soda in an aqueous solution, neutralized to pH 7, and dehydrated.

그리고 가축음용수처리나 폐수처리의 생물반응기(Bio-reactor) 등에서 미생물이나 동·식물에 미네랄 공급용으로 사용하는 경우에는 펠렛트(Pellet)상으로 성형가공하여 사용한다.In addition, when used for supplying minerals to microorganisms, animals and plants, etc. in a bio-reactor of animal drinking water treatment or wastewater treatment, they are molded and processed into pellets.

펠렛트상으로 성형가공은 유해중금속성분의 제거와 탈수처리가 된 앨로페인질점토광물에 앨로페인질점토광물의 건량기준으로 무기바인더(Binder)로 벤토나이트(Bentonite)를 5wt%, 유기바인더로는 알긴산소다(Sodium alginate)나 셀룰로오스(Cellulose) 수지를 10wt%를 혼합하고, 이들에 염화암모늄(NH4Cl)을 10wt%을 혼합한 후 펠렛트상으로 성형가공이 용이하도록 이들에 물을 가해서 전체혼합물의 함수율이 38∼43wt%범위로 조정한 다음에 교반혼합하여 막대형 환상(環狀)의 펠렛트(Pellet)로 성형 가공하여 상온에서 자연건조한 후 전기로나 가열로에서 1,000℃ 이상으로 가열하여 다공질(多孔質)의 건조된 펠렛트를 가공한다.Molding process of pellets is 5wt% of bentonite with inorganic binder and alginic acid with inorganic binder on the basis of dry weight of allophosphorous clay minerals to allotropin clay minerals that have been removed and dehydrated from harmful heavy metals. Sodium (Sodium alginate) or cellulose (Cellulose) resin is mixed with 10wt%, ammonium chloride (NH 4 Cl) is mixed with 10wt% and water is added to them to facilitate the molding process to pellet form of the whole mixture After adjusting the water content in the range of 38-43wt%, stirring and mixing, forming and processing into rod-shaped pellets and drying them naturally at room temperature, and then heating them to 1,000 ℃ or higher in an electric furnace or a heating furnace, Process a variety of dried pellets.

유해중금속성분이 함유된 탈수여액 및 수세수는 중화조로 보내어 중화제(NaOH, Ca(OH)2 등)로 pH를 7∼8로 조정하여 수용성 중금속성분을 고형의 금속수산화물로 전환한 다음에, 응집조로 보내어 침전조에서 침전분리가 용이하도록 응집제를 주입하여 플록(Floc)을 형성한 다음 침전조로 보내어 고형물은 침전시키고, 상등수는 처리수조로 보내어 수세수로 재이용하거나 방류하며, 침전된 슬러라(Slurry)는 탈수기로 보내어 탈수처리한다.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 neutralizing agents (NaOH, Ca (OH) 2, etc.) to convert the water-soluble heavy metal components into solid metal hydroxides, Flock is formed by injecting flocculant to facilitate sedimentation in the sedimentation tank, and then sent to the sedimentation tank to settle the solids, and the supernatant is sent to the treatment tank to be reused or discharged as flushing water, and slurries are deposited. Sent to the dehydrator for dehydration.

전술한 기술내용으로부터 자명하듯이, 본 발명은, 폐기물로 발생하는 석탄회나 소각회로부터 앨로페인질점토광물의 펠렛트로 만드는 자체가 폐자원을 자원화하는 효과가 있으며, 이를 미생물배양공정이나 가축의 음용수처리공정 등에서 미네랄 공급용으로 사용시 현재까지 주로 사용하여 오던 천연의 부석(浮石)에 비해서 성능이 월등히 우수하기 때문에 미네랄 공급용으로도 널리 이용될 것으로 기대된다.As will be apparent from the above description, the present invention has the effect of self-cycling waste resources from pellets of allophospholipid clay minerals from coal ashes and incineration ashes generated as wastes, and this is a microbial culture process or drinking water for livestock. It is expected to be widely used for mineral supply because of its superior performance compared to natural pumice which has been used mainly until now when used for mineral supply in processing processes.

Claims (3)

석탄회(Fly ash)나 소각회(燒却灰)로부터 비정질화수(非晶質和水)의 규산알루미늄염(Aluminosilicate)인 앨로페인(Allophane)질점토광물 제조에서 반응효율을 향상하기 위해서 가성소다(NaOH)와 소금(NaCl)을 4∼5wt% 가한 알칼리수용액상태에서 90∼180℃로 가열하면서 4시간이상 교반반응을 하여 제올라이트(Zeolite)로 안정화처리를 한 다음에, 동일한 온도로 가열하는 상태에서 염산(HCl)을 가하여 pH를 4로 조정하면서 4시간이상 교반반응을 하여 비정질화수규산알루미늄염인 앨로페인질점토광물로 전환후 탈수처리시 유해중금속성분을 수세수로 수세처리를 하여 제거한 다음에, 위생적으로 안전한 인공 앨로페인질점토광물을 제조하는 방법In order to improve the reaction efficiency in the production of allophane vaginal clay minerals, which are aluminum silicate salts of amorphous water from fly ash or incineration ash, NaOH) and salt (NaCl) were added to 4-5 wt% alkaline aqueous solution and heated at 90-180 ° C for stirring for at least 4 hours to stabilize with zeolite, and then heated to the same temperature. After hydrochloric acid (HCl) was added, the pH was adjusted to 4, followed by stirring for at least 4 hours to convert allophospholipid clay mineral, which is an amorphous aluminum silicate salt, to remove harmful heavy metals by washing with water. To manufacture artificially safe hyaluronic clay minerals 제1항에 있어서, 석탄회나 소각회는 유가(有價)의 물질이 아니기 때문에 하·폐수처리의 질소, 인 제거제나 녹·적조 처리제로 사용하는 경우에는 경제적인 문제를 고려시 반응효율이 다소 떨어지더라도 알칼리상태의 안정화반응에서 가성소다나 소금과 같은 유가의 물질을 사용하지 않고 석탄회나 소각회 중에 있는 알칼리성분만으로 알칼리안정화반응을 한 다음, 동일온도로 가열하는 상태에서 염산(HCl)을 가하여 pH를 4로 조정하면서 4시간이상 교반반응을 하여 비정질화수규산알루미늄염인 앨로페인질점토광물로 전환후 탈수처리시 유해중금속성분을 수세수로 수세처리를 하여 제거한 다음에 위생적으로 안전한 인공 앨로페인질점토광물을 제조하는 방법According to claim 1, since coal ash and incineration ash are not oily substances, the reaction efficiency is somewhat reduced when considering the economic problems when using nitrogen, phosphorus remover or rust / red tide treatment agent in sewage and wastewater treatment. Even if the alkaline stabilization reaction does not use valuable materials such as caustic soda or salt, alkali stabilization reaction is carried out using only alkali components in coal ash or incineration ash, and then hydrochloric acid (HCl) is added at the same temperature. Is adjusted to 4 and stirred for at least 4 hours to convert allotropin clay mineral, which is an amorphous aluminum silicate salt, to remove detrimental heavy metals by washing with water. How to make clay minerals 제1항에 있어서, 유해중금속성분의 제거와 탈수처리가된 분말상태의 앨로페인질점토광물에 앨로페인질점토광물의 건량기준으로 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 함수율을 38∼43wt%로 조정한 다음에 교반혼합하여 구상(球狀)이나 막대형 환상(環狀)의 펠렛트상으로 성형가공하여 상온에서 자연건조한 후 전기로나 가열로에서 1,000℃이상으로 가열하여 다공질(多孔質)의 건조된 펠렛트상의 인공 앨로페인질점토광물을 제조하는 방법.According to claim 1, 5% by weight of bentonite (Bentonite) in an inorganic binder (organic binder) on the basis of the dry weight of the allopein clay mineral in the powdered allophosphorus clay mineral, which has been removed from the harmful heavy metal components and dehydrated Furnace is mixed with 10 wt% of Alginic acid Soda or Cellulose, 10 wt% of ammonium chloride (NH 4 Cl), and is easily molded into pellets. Water was added to them to adjust the water content of the entire mixture to 38 to 43 wt%, followed by stirring and mixing to form spherical or rod-shaped pellets, followed by natural drying at room temperature. A method for producing artificial allopine-like clay minerals on porous dried pellets by heating to 1,000 ° C. or higher in a heating furnace.
KR1020020033856A 2002-06-17 2002-06-17 Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash KR100541777B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020020033856A KR100541777B1 (en) 2002-06-17 2002-06-17 Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020020033856A KR100541777B1 (en) 2002-06-17 2002-06-17 Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash

Publications (2)

Publication Number Publication Date
KR20030096812A KR20030096812A (en) 2003-12-31
KR100541777B1 true KR100541777B1 (en) 2006-01-20

Family

ID=32387410

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020020033856A KR100541777B1 (en) 2002-06-17 2002-06-17 Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash

Country Status (1)

Country Link
KR (1) KR100541777B1 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100541776B1 (en) * 2002-07-11 2006-01-20 서희동 Manufacturing method of artificial zeolite from fly ash
CN114317061B (en) * 2021-11-16 2023-01-24 华阳新材料科技集团有限公司 Chemical purification method for preparing ultra-low ash coal from clean coal

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5986687A (en) * 1982-11-08 1984-05-18 Akio Henmi Preparation of zeolite-based soil conditioner from coal ash
KR19980033471A (en) * 1998-04-16 1998-07-25 구용회 Low-temperature granulation method of coal ash zeolite and its use
KR19990065036A (en) * 1998-01-06 1999-08-05 김강권 Manufacturing method of granular zeolite using waste
KR20010089935A (en) * 2000-03-14 2001-10-17 서희동 method for producing artificial allophane mineral from fly ash of coal and waste
KR20020039292A (en) * 2002-04-20 2002-05-25 서영진 Purifying agent manufacturing and using method for treatment of sewage, wastewater, nightsoil, red tide, green algal ... etc by using peat and fly ash or cinder

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5986687A (en) * 1982-11-08 1984-05-18 Akio Henmi Preparation of zeolite-based soil conditioner from coal ash
KR19990065036A (en) * 1998-01-06 1999-08-05 김강권 Manufacturing method of granular zeolite using waste
KR19980033471A (en) * 1998-04-16 1998-07-25 구용회 Low-temperature granulation method of coal ash zeolite and its use
KR20010089935A (en) * 2000-03-14 2001-10-17 서희동 method for producing artificial allophane mineral from fly ash of coal and waste
KR20020039292A (en) * 2002-04-20 2002-05-25 서영진 Purifying agent manufacturing and using method for treatment of sewage, wastewater, nightsoil, red tide, green algal ... etc by using peat and fly ash or cinder

Also Published As

Publication number Publication date
KR20030096812A (en) 2003-12-31

Similar Documents

Publication Publication Date Title
Zhang et al. Use of electroplating sludge in production of fired clay bricks: Characterization and environmental risk evaluation
Zhang et al. Simultaneous removal of ammonium and phosphate by zeolite synthesized from coal fly ash as influenced by acid treatment
JP5658270B2 (en) Manufacturing method of lightweight construction materials using sludge waste
CN101786777B (en) Formula for treating domestic sludge or animal wastes and its uses
CN101941755B (en) Modified coal ash, preparation method thereof and method thereof for treating humic acid
Padmapriya et al. Synthesis of seawater based geopolymer: Characterization and adsorption capacity of methylene blue from wastewater
CN106413857A (en) Stabilization of at least one heavy metal contained in a sodic fly ash using a water-soluble source of silicate and a material containing calcium and/or magnesium
CN107867790A (en) A kind of sludge confession heat dehydration drying means and system
CN111848130A (en) Modified ceramsite capable of efficiently removing phosphorus and preparation method thereof
JP2007014923A (en) Phosphorus removal material
KR100654609B1 (en) Method for manufacturing purifying agent for teatment of wastewater and soil using natural materials
CN101585522B (en) Method for recovering phosphorus from urban mud anaerobic digestion solution
HU226926B1 (en) Sorbent, method for producing the same and use of the same for immobilisation of heavy metals and phosphates
KR100464865B1 (en) Using method of purifying agent for sewage, wastewater, night-soil, red tide, green algal ... etc from fly ash or cinder
KR100854036B1 (en) The soil aggregate manufacturing method which uses the sewage sludge and the soil aggregate which it uses
KR100541777B1 (en) Manufacturing method of artificial allophanic clay minerals from the fly ash and incinerator's ash
JP4005447B2 (en) Heavy metal immobilization material and treatment method for contaminated soil
CN101560008B (en) Method for treating low-concentration phosphorus-containing wastewater
KR100541776B1 (en) Manufacturing method of artificial zeolite from fly ash
KR100464866B1 (en) Purifying agent manufacturing method for treatment of sewage, wastewater, night soil, red tide, green algal ... etc by using peat and fly ash or cinder
CN206872653U (en) A kind of sludge confesses heat dehydration drying system
CN1119209C (en) Comprehensive innocuous utilization technique of lake and city sludge
JPH08197095A (en) Treatment of sewage sludge and treated sewage sludge
KR101766861B1 (en) A Complex Adsorbent To Treat Ethyanolamine And Preparation Method Of The Same
JP4387040B2 (en) Soil improver and / or organic fertilizer and method for producing the same

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
AMND Amendment
E601 Decision to refuse application
AMND Amendment
J201 Request for trial against refusal decision
E801 Decision on dismissal of amendment
E902 Notification of reason for refusal
B701 Decision to grant
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20090102

Year of fee payment: 4

LAPS Lapse due to unpaid annual fee