KR100621356B1 - Method of extracting boric-acid using microwave from borate-ore - Google Patents

Method of extracting boric-acid using microwave from borate-ore Download PDF

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KR100621356B1
KR100621356B1 KR1020040066344A KR20040066344A KR100621356B1 KR 100621356 B1 KR100621356 B1 KR 100621356B1 KR 1020040066344 A KR1020040066344 A KR 1020040066344A KR 20040066344 A KR20040066344 A KR 20040066344A KR 100621356 B1 KR100621356 B1 KR 100621356B1
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boric acid
microwave
acid
extraction
sulfuric acid
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KR20060018021A (en
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최병현
지미정
백종후
이미재
장재훈
임형미
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요업기술원
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    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
    • C01B35/08Compounds containing boron and nitrogen, phosphorus, oxygen, sulfur, selenium or tellurium
    • C01B35/10Compounds containing boron and oxygen
    • C01B35/12Borates
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    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/08Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor
    • B01J19/12Processes employing the direct application of electric or wave energy, or particle radiation; Apparatus therefor employing electromagnetic waves
    • B01J19/122Incoherent waves
    • B01J19/123Ultra-violet light
    • B01J19/124Ultra-violet light generated by microwave irradiation
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    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B35/00Boron; Compounds thereof
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Abstract

본 발명은 천연광물자원인 보레이트 광물(주성분 B2O3외에 CaO, MgO, Na2 O, SiO2등을 포함)로부터 마이크로웨이브를 이용하여 붕산을 제조하는 방법에 관한 것이다. The present invention relates to a method for producing boric acid using microwaves from borate minerals (including CaO, MgO, Na 2 O, SiO 2, etc. in addition to the main component B 2 O 3) , which is a natural mineral resource.

기존의 붕산 추출공정은 과량의 황산사용으로 환경오염과 추출시간이 길어 반응용기의 부식이 심각하며, 에너지가 많이 필요하고, 작업중 인체에 악영향을 줄 수 있다. 따라서 열분해방법의 단점을 보완하고자 추출공정에서 용매물질이 마이크로파를 흡수할 수 있는점에 착안하여 마이크로웨이브(Microwave)를 이용하여 추출시간과 황산의 양을 최소화함으로써 공해와 부식등의 문제를 감소시키고 에너지를 절약할 수 있는 방법을 발명하였다. 마이크로파로 가열하면, 분해 처리 시간을 1/6로 단축시켜도 붕산을 합성할 수 있으므로 에너지 절약과 함께 폐수의 양을 25%이상 줄임으로 환경보존에 큰 기여를 할 수 있는 방법이다.Existing boric acid extraction process has a long environmental pollution and extraction time due to the use of excess sulfuric acid, the corrosion of the reaction vessel is serious, requires a lot of energy, may adversely affect the human body during work. Therefore, in order to make up for the shortcomings of the pyrolysis method, pay attention to the fact that the solvent substance can absorb microwaves in the extraction process, and reduce the problems such as pollution and corrosion by minimizing the extraction time and the amount of sulfuric acid by using microwave. Invented a method that can save energy. When heated by microwave, boric acid can be synthesized even if the decomposition treatment time is shortened to 1/6. Therefore, it is a method that can greatly contribute to environmental conservation by saving energy and reducing the amount of waste water by more than 25%.

이와 같은 공정으로 제조된 붕산은 탄화 혹은 질화 공정을 거쳐 B4C, BN 등의 고부가가치화된 제품을 제조할 수 있고, 붕산 및 붕소화합물은 유리의 내수성 향상 및 유리섬유의 점도조절용 첨가물, 반도체용, 고급연마재, 기판, 원자력발전소 반응도 조절용, 세제나 페인트 첨가물 등에 광범위한 분야에 활용되고 있다. Boric acid produced in such a process can be a high value-added product such as B 4 C, BN through the carbonization or nitriding process, boric acid and boron compounds are additives for improving the water resistance of glass and viscosity control of glass fiber, semiconductor It is used in a wide range of fields such as high quality abrasives, substrates, nuclear power plant reactivity control, detergents and paint additives.

저가의 원광인 보레이트 광물로부터 붕산을 합성하고, 합성된 붕산을 이용하여 첨단원료소재를 추출함으로써 산업원료소재의 안정적인 확보, 자원의 고부가가치화, 수입대체 효과 등을 기대할 수 있다.By synthesizing boric acid from borate minerals, which are inexpensive ores, and extracting advanced raw materials using the synthesized boric acid, it is possible to secure stable industrial raw materials, high added value of resources, and import substitution effects.

Description

보레이트 광물로부터 마이크로웨이브를 이용한 붕산을 추출하는 제조방법{Method of extracting boric-acid using microwave from borate-ore}Method for extracting boric acid using microwave from borate minerals {Method of extracting boric-acid using microwave from borate-ore}

본 발명은 보레이트 광물로부터 마이크로웨이브를 이용하여 붕산을 추출하는 방법에 관한 것이다.The present invention relates to a method for extracting boric acid using microwaves from borate minerals.

본 발명에서 언급하는 붕산은 낮은 융점으로 인해 붕규산유리, 내열유리, 프리트, 유리섬유, 안료, 법랑 및 금속용접등의 융제(flux)로, 붕산을 glass형 또는 입자형의 무수붕산으로 하여 광학유리, 렌즈, display용 프리트, 액체봉폐제로, 또한 붕산을 탄화 또는 질화하여 고부가가치화한 붕소화합물인 B4C, BN은 반도체용 치구 원소재, 방탄소재, 중성자흡수제, 윤활제, 페인트 첨가제, polymer의 filler, 화장품 보습제, Al 증착 boat제, 연마제 원소재등 광범위한 분야에 활용되고 있다. Boric acid referred to in the present invention is a flux of borosilicate glass, heat-resistant glass, frit, glass fiber, pigment, enamel and metal welding due to low melting point, and boric acid as glass or granular boric anhydride. , a lens, display frit, liquid rod monetary system for, and the boric acid carbide or nitride, high value-added boron compound is B 4 C, BN is a jig for semiconductor source material, ballistic materials, neutron absorbers, lubricants, paint additives, polymer It is used in a wide range of fields such as fillers, cosmetic moisturizers, Al deposition boats, and abrasive raw materials.

위와 같은 넓은 산업분야에서 사용되고 있는 붕소화합물은 붕소상태로는 존재하지 않고 B-N계 산화물, Ca-B-Si계 산화물, Ca-B계 산화물, Mg-B계 산화물등의 천연상태로 존재하나 불순물이 많아 저순도 glass fiber 제조시 사용이외에는 천연 상태로 사용하지 않고 천연원광을 황산등의 산처리에 의해 붕산을 제조하고 다시 붕산을 무수붕산화한 다음 B4C나 BN등의 첨단소재로 합성하여 윤활성, 내열성, 기계특성이 우수한 고부가가치 소재로 제조한다. 고부가가치화된 붕소화합물을 합성하기 위해서는 일반적으로 저가의 천연원광인 Colemanite(Ca2B6O11·xH2O), Datolite(Ca2B2SiO2·xH2O), Kurnakovite(Mg2B 6O11·xH2O), Szaibelyite(Mg2B6O5·xH2O), Pricetete(Ca2B2SiO2·xH2O), Kernite(Na 2B4O7·4H2O), Tricalconite(Na2B4O 7·5H2O)를 산처리하여 붕화물을 제조하고, 이 붕화물에 암모니아 가스, 질소가스, 수소+질소가스, 알곤가스, 염화암모늄, 칼슘인산산화물, 탄산암모늄, 시안화나트륨(칼륨), 우레아, 염화붕소, 붕화칼슘등을 통과시키거나 첨가하여 붕소화합물을 합성하게 된다. 산 처리하여 붕소화합물을 제조할 때 일반적으로 황산으로 붕소가 혼합된 천연원광을 용해하게 되는데 이때 붕산제조공정에서 사용되는 황산의 양이 많고 전력 또한 35% 이상이 오염 제어장치에 사용되므로 친환경적인 공정을 개발하여 황산의 양을 감소시키고 생산비를 절감할 필요가 있다. Boron compounds used in such a wide industrial field do not exist in the boron state but exist in the natural state such as BN oxide, Ca-B-Si oxide, Ca-B oxide, Mg-B oxide, but impurities Many low-purity glass fibers are used in the manufacture of boric acid by acid treatment, such as sulfuric acid, without using it in its natural state, and boric acid is anhydrous borated again, and then synthesized with high-tech materials such as B 4 C or BN for lubricity. Manufactured with high value-added materials with excellent heat resistance and mechanical properties. In order to synthesize high value-added boron compounds, in general, inexpensive natural ores such as Colemanite (Ca 2 B 6 O11.xH 2 O), Datolite (Ca 2 B 2 SiO 2 .xH 2 O), Kurnakovite (Mg 2 B 6 O) 11 · xH 2 O), Szaibelyite (Mg 2 B 6 O 5 · xH 2 O), Pricetete (Ca 2 B 2 SiO 2 · xH 2 O), Kernite (Na 2 B 4 O 7 · 4H 2 O), Tricalconite (Na 2 B 4 O 7 · 5H 2 O) is acid treated to produce a boride, which is ammonia gas, nitrogen gas, hydrogen + nitrogen gas, argon gas, ammonium chloride, calcium phosphate oxide, ammonium carbonate, The boron compound is synthesized by passing or adding sodium cyanide (potassium), urea, boron chloride, calcium boride, and the like. When manufacturing boron compound by acid treatment, natural ore mixed with boron with sulfuric acid is generally dissolved. At this time, the amount of sulfuric acid used in the boric acid manufacturing process is high, and more than 35% of the power is used for pollution control devices. It is necessary to reduce the amount of sulfuric acid and reduce the production cost by developing.

따라서 본 발명에서는 기존의 열분해 방법으로 붕산을 추출하는 공정은 용해시간이 길고 추출과정에서 다량의 황산사용으로 인해 과량의 폐수가 발생되므로 이 폐수를 처리하기 위하여 비용이 과다하게 들어가며, 또한 반응용기가 부식이 심하고 공정중 인체에 해로울 수도 있다. 본 발명에서는 생산비 절감, 친환경적인 공정개발을 위해 2.45㎓ 마이크로파 대역의 가열특성, 즉 쌍극자 재배열, 공간전하현 상, ferrimagnetic resonance등으로 설명되는 마이크로파 특성을 이용하여 용해과정에서 용해시간을 단축하고 황산의 양을 최소화 하는 방법에 대한 공정을 설계하여 붕산을 추출하였다. Therefore, in the present invention, the process of extracting boric acid by the conventional pyrolysis method has a long dissolution time and excessive wastewater is generated due to the use of a large amount of sulfuric acid in the extraction process. Corrosion is severe and may be harmful to the human body during the process. In the present invention, in order to reduce production costs and develop an environment-friendly process, heating characteristics of the 2.45 대역 microwave band, ie, dipole rearrangement, space charge phenomenon, and ferrimagnetic resonance, can be used to shorten the dissolution time in the dissolution process. Boric acid was extracted by designing a process for minimizing the amount.

그렇게 함으로써 마이크로파를 이용하여 낮은 온도에서 빠른 시간에 최소로 황산(acid)을 사용하는 공정으로 붕산을 제조하면서 에너지 절약과 함께 폐수의 양을 줄일 수가 있었다.By doing so, it was possible to reduce the amount of waste water with energy savings while producing boric acid in a process that uses sulfuric acid at a low temperature and at a short time in a short time using microwave.

Ca-B, Mg-B, Si-B, Na-B계의 산화물을 포함하고 있는 천연원료로 붕산을 제조하는 종래의 방법으로는 열분해방법이 일반적으로 사용되는데 열분해방법은 붕소를 포함한 천연원광에 황산을 첨가하여 고온으로 상당시간 heating 장치를 써서 가열하여 붕소화합물을 용해하여 solution 상태로 만들면 그 외의 물질은 침전시켜 분리 추출하는 방법으로 항상 황산량을 화학양론적으로 반응할 수 있는 양보다 1.3∼1.8배 첨가해야 하고 heater를 써서 95℃이상으로 가열하고 분리시간도 1시간이상 유지해야 되는 점 때문에 황산의 다량 사용에 의한 다량의 폐수발생, heater 가열에 의한 에너지 소모(전 제조원가의 ⅓이 전력비임), 장시간 반응에 따른 용기의 부식, 냄새에 의한 인체건강을 해치는 등의 단점이 있다. As a conventional method for preparing boric acid from natural materials containing Ca-B, Mg-B, Si-B, Na-B-based oxides, pyrolysis is generally used. When sulfuric acid is added and heated at a high temperature for a long time using a heating device to dissolve the boron compound into a solution state, other substances are precipitated and separated and extracted.The amount of sulfuric acid is 1.3 ~ higher than the amount that can be stoichiometrically reacted. Since 1.8 times should be added, the heater should be heated above 95 ℃ and the separation time should be maintained for more than 1 hour. Therefore, a large amount of waste water is generated by the use of sulfuric acid, and the energy consumption by heater heating. ), Corrosion of the container due to a long time reaction, harm to human health due to smell, etc.

따라서 본 발명에서는 붕소원광을 출발원료로 하여 붕산을 제조하는 공정에서 마이크로파를 이용하여 황산 사용의 양을 줄이고, 반응시간도 짧게 하기 위함이다. 위와 같은 문제점이 해결되기 위해서는 친환경공정이 개발되어야만 하는데 본 발명에서는 가열방법을 일반적으로 사용하는 히터에 의한 가열방식이 아닌 물의 극성을 붕산추출에 적용한 가열방법을 마이크로파에 의한 가열방법 즉 분해반응에서 물을 용매로 사용했을 경우 용매가 마이크로파를 흡수할 수 있는 점을 확인하여 마이크로파를 가열원으로 선택하였다. Therefore, the present invention is to reduce the amount of sulfuric acid using the microwave in the process for producing boric acid using boron ore as a starting material, and to shorten the reaction time. In order to solve the above problems, an environmentally friendly process must be developed, but in the present invention, a heating method in which the polarity of water is applied to the boric acid extraction, not the heating method by a heater that generally uses the heating method, is used in the heating method using microwaves, that is, in the decomposition reaction When using as a solvent, it was confirmed that the solvent can absorb the microwave, the microwave was selected as the heating source.

마이크로파는 주로 가열 목적으로 사용할 때 주파수가 900MHz와 2.45GHz이다. 주파수에 따라 마이크로파가 통과하는 깊이가 달라지는 특성 때문에 많은 연구자들이 각 분야에 적용하기 위하여 많은 연구를 행하고 있다. 물질의 추출 및 합성 공정에서 마이크로파를 조사하면 모든 저분자량의 극성 용매는 마이크로파의 주파수에 해당하는 속도만큼의 분자회전 혹은 재배치에 의한 마찰력으로 가열된다 따라서 용매를 이용하여 이루어지는 많은 화학반응에 적용이 가능하고, 유기 합성의 경우 우수한 반응속도 및 수득율, 선택성이 있는 반응에 대한 많은 보고가 이루어지고 있다. 다양한 무기물의 합성에도 마이크로파가 적용된 사례가 많은데, 마이크로파를 적용하면 반응이 빠르고, 간단하고, 효율적이게 할 수 있다. 화학반응에서 마이크로파의 효과는 물질에 의한 마이크로파의 흡수로 설명될 수 있고, 흡수 메커니즘은 쌍극자 재배열(dipole reorientation), 공간 전하 현상(space charge phenomena), ferrimagnetic resonance, 등으로 설명되고 있다. 하지만, 반응 중에 일어나는 마이크로파와 반응물 간의 정확한 작용은 아직까지도 다소 불분명하다.Microwaves have frequencies of 900 MHz and 2.45 GHz when used primarily for heating purposes. Due to the nature of the microwave passing depth depending on the frequency, many researchers are doing a lot of research to apply to each field. Microwave irradiation in the extraction and synthesis of materials causes all low molecular weight polar solvents to be heated by frictional forces caused by molecular rotation or rearrangement at a rate corresponding to the frequency of the microwave. Therefore, they can be applied to many chemical reactions using solvents. In the case of organic synthesis, many reports have been made on reactions having excellent reaction rates, yields, and selectivities. In many cases, microwaves have been applied to the synthesis of various inorganic materials. Applying microwaves can make the reaction quick, simple and efficient. The effects of microwaves in chemical reactions can be explained by the absorption of microwaves by materials, and the absorption mechanisms are explained by dipole reorientation, space charge phenomena, ferrimagnetic resonance, and the like. However, the exact action between the microwave and the reactant during the reaction is still somewhat unclear.

상기와 같은 문제점을 해결하기 위하여 많은 연구들이 진행되고 있지만 만족할 만한 효과를 얻을 수 없었다.In order to solve the above problems, many studies have been conducted, but satisfactory effects could not be obtained.

이와같이 본 발명은 천연원광을 출발원료로 하여 기존의 열분해방법으로 붕산을 제조했을 때보다 황산사용을 대폭 감소시키고, 반응시간(추출시간)을 짧게하고자하며, 또한 반응온도(추출온도)를 낮추는 것을 그 목적으로 한다.As described above, the present invention is intended to significantly reduce the use of sulfuric acid, to shorten the reaction time (extraction time), and to lower the reaction temperature (extraction temperature), compared to when boric acid is prepared by conventional pyrolysis using natural ore as a starting material. For that purpose.

실시예를 통하여 본 발명을 상세히 설명한다.The present invention will be described in detail through examples.

[실시예 1]Example 1

본 발명에서는 붕산을 추출하기 위해 우선 보레이트 천연원광인 colemanite(CaB6O11·H2O), Datolite(Ca2B2Si 2O9·H2O), Kurnakovite(Mg2B6O11·xH 2O), Szaibelyite(Mg2B6O5·xH2O), Tincalconite(Na2 B4O7·5H2O), Kernite(Na2B4O7 ·4H2O)를 사용하여 표 1과 같은 조건으로 제조하였다. In the present invention, preferred borate natural ore is colemanite (CaB 6 O 11 · H 2 O), Datolite (Ca 2 B 2 Si 2 O 9 · H 2 O) in order to extract the acid, Kurnakovite (Mg 2 B 6 O 11 · use xH 2 O), Szaibelyite (Mg 2 B 6 O 5 · xH 2 O), Tincalconite (Na 2 B 4 O 7 · 5H 2 O), Kernite (Na 2 B 4 O 7 · 4H 2 O) Table It prepared under the same conditions as 1.

표. 1 반응시간에 따른 붕산추출 조건table. 1 Boric Acid Extraction Conditions According to Reaction Time

SampleSample 추출온도 (℃)Extraction temperature (℃) 추출시간 (min)Extraction time (min) 1차 황산첨가량 (real/standard)Primary Sulfate Addition (real / standard) 2차 황산첨가량 (real/standard)Secondary Sulfate Addition (real / standard) pHpH 1One 9595 1One 1.31.3 0.60.6 77 22 9595 33 1.31.3 0.60.6 77 33 9595 55 1.31.3 0.60.6 77 44 9595 3030 1.31.3 0.60.6 77

※ 1,2차 황산첨가량은 real(실제 첨가량 ㎖)과 standard(이론양 ㎖)의 비율이므로 단위가 없음.
보레이트 광물 25g을 건식으로 분쇄하고 95℃의 hotwater와 혼합한 후 25%로 희석한 황산을 첨가하여 마이크로웨이브를 열원으로 하여 가열하면서 표 1의 조건으로 시료마다 반응시간을 변화시켜 가며 용해하였다. 이때 95℃의 hot water와 25%로 희석한 황산의 부피비는 10 : 1로 하였고 용해한 반응물은 95℃의 hot water로 여과하였다. 여과할 때 필터를 통과한 여액은 대부분이 액상의 붕산이므로 다시 반응기에 넣고 끊는 점까지 가열시킨 후, 가열된 반응물에 칼슘화합물의 용액화와 붕산의 침전을 방지하고자 황산암모늄을 첨가하였으며, 1차 불용 성분 외의 불순물을 수화물로 침전시켜 제거하고자 pH 조정을 위해 암모니아수를 첨가하였다. 다음에는 반응에 참여하고 남은 암모니아 가스를 제거하고자 가열을 행하였다. 암모니아 가스가 제거된 현탁액은 침전물과 여액으로 분리, 여과를 실시하고, 여과된 여액의 대부분이 액상의 붕산암모늄의 형태로 존재하므로 붕산과 황산암모늄의 형태로 분리하기 위하여 여액에 2차로 황산 희석액을 변화시켜가며 첨가하였다. 붕산 여액이 농축될 수 있도록 vacuum evaporator를 이용하여 95℃에서 1시간 동안 농축시킨 후 재결정화를 위하여 실온까지 냉각을 실시하였다. 온도에 따른 용해도 차이에 의해 농축액으로부터 결정화된 붕산을 회수하고자 여과한 후 건조기에서 60℃로 일정시간 건조시켜 고상의 붕산을 추출하였다. 그 결과 기존 열원으로 30분 동안 가열하여 추출했을 때의 붕산보다 반응시간은 짧았지만 마이크로웨이브를 적용한 시료가 더욱 결정성이 높고 순도도 높았다.
※ There is no unit because the 1st and 2nd sulfuric acid addition amount is the ratio of real (actual addition amount ㎖) and standard (theoretical amount ㎖).
25 g of borate minerals were pulverized dry and mixed with hotwater at 95 ° C., and sulfuric acid diluted to 25% was added thereto, followed by melting with varying reaction time for each sample under the conditions shown in Table 1 while heating the microwave as a heat source. At this time, the volume ratio of sulfuric acid diluted to 95% hot water and 25% was 10: 1 and the dissolved reactant was filtered with hot water at 95 ℃. Since most of the filtrate passed through the filter during the filtration is a liquid boric acid, the filtrate is put back into the reactor and heated up to the point of breaking, and then ammonium sulfate is added to the heated reaction to prevent solution of calcium compound and precipitation of boric acid. Ammonia water was added for pH adjustment to remove impurities other than insoluble components by precipitation with hydrate. Next, heating was performed to participate in the reaction and remove the remaining ammonia gas. The ammonia gas-free suspension is separated into a precipitate and a filtrate, and filtered. Since most of the filtrate is present in the form of a liquid ammonium borate, a dilute sulfuric acid solution is added to the filtrate in order to separate it into a form of boric acid and ammonium sulfate. Variations were added. The boric acid filtrate was concentrated at 95 ° C. for 1 hour using a vacuum evaporator, and then cooled to room temperature for recrystallization. Filtered to recover the boric acid crystallized from the concentrate by the difference in solubility with temperature, and then dried at 60 ℃ for a certain period of time in the dryer to extract the solid boric acid. As a result, the reaction time was shorter than that of boric acid when extracted by heating for 30 minutes with the existing heat source, but the sample applied with microwave was more crystalline and the purity was higher.

[실시예 2]Example 2

반응 출발물질인 보레이트 광물과 실험방법은 실시예 1과 같다. Borate mineral as a reaction starting material and the experimental method are the same as in Example 1.

표 2. 반응온도와 시간에 따른 붕산추출 조건Table 2. Boric Acid Extraction Conditions According to Reaction Temperature and Time

SampleSample 추출온도 (℃)Extraction temperature (℃) 추출시간 (min)Extraction time (min) 1차 황산첨가량 (real/standard)Primary Sulfate Addition (real / standard) 2차 황산첨가량 (real/standard)Secondary Sulfate Addition (real / standard) pHpH 55 7575 55 1.31.3 0.60.6 77 66 7575 3030 1.31.3 0.60.6 77 77 5555 55 1.31.3 0.60.6 77 88 5555 3030 1.31.3 0.60.6 77

※ 1,2차 황산첨가량은 real(실제첨가량 ㎖)과 standard(이론량 ㎖)의 비율이므로 단위가 없음.
실시예 1과 마찬가지로 보레이트 광물 25g을 건식 분쇄하고 95℃의 hotwater와 혼합한 후 25%로 희석한 황산을 첨가하여 마이크로웨이브를 열원으로 하면서 추출온도를 75∼55℃로 변화시키고 추출시간은 각각 5분, 30분으로 하여 용해하였다. 이후 과정은 실시예 1과 같다. 그 결과 추출시간을 30분으로 고정한 경우, 추출온도 55℃에서 추출해도 95℃에서 추출했을 때와 마찬가지로 붕산을 얻을 수 있었고, 추출시간을 5분으로 한 경우는 시간을 길게 했을 때 보다는 결정성은 낮았지만 붕산이 추출되었다.
※ There is no unit because the 1st and 2nd sulfuric acid addition amount is the ratio of real (actual addition amount ㎖) and standard (theory amount ㎖).
As in Example 1, 25 g of borate mineral was dry pulverized, mixed with hot water at 95 ° C., and sulfuric acid diluted to 25% was added to change the extraction temperature to 75 to 55 ° C. while using microwave as a heat source. It melt | dissolved in 30 minutes. Since the process is the same as in Example 1. As a result, when the extraction time was fixed at 30 minutes, boric acid could be obtained in the same manner as when extracted at 55 ° C, but the extraction time was lower than when the extraction time was 5 minutes. Boric acid was extracted.

[실시예 3]Example 3

반응 출발물질인 보레이트 광물과 실험방법은 실시예 1과 같다. Borate mineral as a reaction starting material and the experimental method are the same as in Example 1.

표 3. 황산첨가양에 따른 붕산추출 조건Table 3. Boric Acid Extraction Conditions According to the Amount of Sulfuric Acid

SampleSample 추출온도 (℃)Extraction temperature (℃) 추출시간 (min)Extraction time (min) 1차 황산첨가량 (real/standard)Primary Sulfate Addition (real / standard) 2차 황산첨가량 (real/standard)Secondary Sulfate Addition (real / standard) pHpH 99 9595 55 1.01.0 0.60.6 77 1010 9595 55 0.80.8 0.60.6 77 1111 9595 55 0.20.2 0.60.6 77

※ 1,2차 황산첨가량은 real(실제첨가량 ㎖)과 standard(이론량 ㎖)의 비율이므로 단위가 없음.
실시예 1과 마찬가지로 보레이트 광물 25g을 건식 분쇄하고 95℃의 hotwater와 혼합한 후 25%로 희석한 황산을 첨가하여 마이크로웨이브를 열원으로 하면서 추출온도를 95℃, 추출시간은 5분으로 고정하였고 이후 첨가되는 황산량을 변화시켜 실험하였다.
※ There is no unit because the 1st and 2nd sulfuric acid addition amount is the ratio of real (actual addition amount ㎖) and standard (theory amount ㎖).
As in Example 1, 25 g of borate mineral was dry pulverized, mixed with hot water at 95 ° C., and sulfuric acid diluted to 25% was added to the microwave as a heat source, and the extraction temperature was fixed at 95 ° C. and the extraction time was set to 5 minutes. The experiment was carried out by varying the amount of sulfuric acid added.

그 결과 붕산추출 과정에서 마이크로웨이브를 열원으로 사용하였을 경우 황산의 첨가량을 줄여도 기존의 황산량을 사용했을 때와 마찬가지로 붕산이 추출되었고 수율이나 결정성은 오히려 더 우수하였다.As a result, when microwave was used as the heat source during boric acid extraction, boric acid was extracted and the yield and crystallinity were better, as in the case of using the amount of sulfuric acid, even though the amount of sulfuric acid was reduced.

본 발명은 천연광물자원의 활용 공정으로 붕소를 포함한 다양한 천연광물로부터 붕산을 추출하는 제조방법에 관한 것이다. 기존의 열분해 방법으로 추출하는 공정은 용해시간이 길고 추출과정에서 사용하는 산(acid)으로 인한 과량의 폐수와 반응용기의 부식이 일어난다. 이러한 단점을 보완하고자 용해과정에서 마이크로웨이브를 도입하여 추출시간을 30분에서 5분으로 줄이고 추출온도를 95℃에서 55℃로 낮추면서, 산(acid)의 양도 최대 40% 이상 줄이는 방법에 대한 공정을 확립하였다.The present invention relates to a manufacturing method for extracting boric acid from various natural minerals, including boron as a utilization process of natural mineral resources. Extraction by conventional pyrolysis method has a long dissolution time and corrosion of the reaction vessel and excess waste water due to acid used in the extraction process. In order to make up for these drawbacks, the process of reducing the amount of acid by up to 40% while reducing the extraction time from 30 minutes to 5 minutes and reducing the extraction temperature from 30 minutes to 5 minutes by introducing microwaves in the melting process. Was established.

Claims (2)

반응용기에 보레이트 천연원광을 95℃의 hotwater와 25%로 희석한 황산용액을 혼합한 후 마이크로웨이브 오븐안에 상기 반응용기를 넣고, 마이크로파를 조사하여 붕산을 추출하는 붕산 제조방법.A method of producing boric acid in which a borate natural ore is mixed with a hot water at 95 ° C. and a sulfuric acid solution diluted to 25% in a reaction vessel, and then the reaction vessel is placed in a microwave oven and irradiated with microwaves to extract boric acid. 제 1 항에 있어서,The method of claim 1, 보레이트 천연원광 25g에 95℃의 hotwater와 25%로 희석한 황산용액의 부피비가 10 : 1이 되게 하고 마이크로 웨이브의 추출온도는 55 내지 95℃로 하며 추출시간은 1 내지 30분으로 하는 보레이트 광물로부터 붕산을 추출하는 제조방법.From borate mineral 25g of borate natural ore, the volume ratio of hotwater at 95 ℃ and sulfuric acid solution diluted to 25% is 10: 1 and the extraction temperature of microwave is 55-95 ℃ and extraction time is 1-30 minutes. Method for extracting boric acid.
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US4756894A (en) 1986-01-29 1988-07-12 Materias Primas Magdalena S.A.DE C.V. Process for the obtainment of boric acid from colemanite and/or howlite minerals
US4804524A (en) 1986-01-29 1989-02-14 Materias Primas Magdalena, S.A. De C.V. Process for the preparation of boric acid from colemanite and/or howlite minerals
JPH03232717A (en) * 1990-02-06 1991-10-16 Asahi Glass Co Ltd Production of boric acid
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US4756894A (en) 1986-01-29 1988-07-12 Materias Primas Magdalena S.A.DE C.V. Process for the obtainment of boric acid from colemanite and/or howlite minerals
US4804524A (en) 1986-01-29 1989-02-14 Materias Primas Magdalena, S.A. De C.V. Process for the preparation of boric acid from colemanite and/or howlite minerals
JPH03232717A (en) * 1990-02-06 1991-10-16 Asahi Glass Co Ltd Production of boric acid
KR19990076364A (en) * 1998-03-31 1999-10-15 최태민 Preparation method of anhydrous boric acid

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