KR910002385B1 - Production of magnesium hydroxide from sea water - Google Patents
Production of magnesium hydroxide from sea water Download PDFInfo
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- KR910002385B1 KR910002385B1 KR1019880017919A KR880017919A KR910002385B1 KR 910002385 B1 KR910002385 B1 KR 910002385B1 KR 1019880017919 A KR1019880017919 A KR 1019880017919A KR 880017919 A KR880017919 A KR 880017919A KR 910002385 B1 KR910002385 B1 KR 910002385B1
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Abstract
Description
본 발명은 해수로부터 수산화마그네숨(이하 Mg(OH)2로 표시함)을 제조하는 방법, 보다 상세하게는, 마그네시아 클링커를 비롯한 해수로부터의 각종 Mg(OH)2를 제조하는 과정중에서 특히, 담수 세척 공정을 개선하여 불순물을 저감시킴으로써 보다 순수한 Mg(OH)2를 제조하는 방법에 관한 것이다.The present invention relates to a method for producing magnesium hydroxide (hereinafter referred to as Mg (OH) 2 ) from seawater, and more particularly, to preparing various Mg (OH) 2 from seawater including magnesia clinker. It relates to a process for producing purer Mg (OH) 2 by improving the washing process to reduce impurities.
일반적으로, 해수로부터의 Mg(OH)2를 제조하는 방법은 해수와 석회석을 하소(CaCo3 CaO+Co2) 및 소화(CaO+H2O→Ca(OH)2)시켜 만든 소석회와의 반응으로 이루어 진다.In general, the process for producing Mg (OH) 2 from seawater calcined seawater and limestone (CaCo 3 CaO + Co 2 ) and digestion (CaO + H 2 O → Ca (OH) 2 ) to react with slaked lime.
즉, 해수중에 3-4g/L정도 함유되어 있는 Mg2+이온이 소석회중에 포함된 Ca2+과 이온화 경향의 차이로 인해 이온교환을 일으켜 Mg2++Ca(OH)2-Ca2++Mg(OH)2와 같은 반응으로 Mg(OH)2를 얻게 된다.That is, Mg 2+ ions contained in about 3-4 g / L in seawater cause ion exchange due to the difference in ionization tendency with Ca 2+ contained in slaked lime, resulting in Mg 2+ + Ca (OH) 2 -Ca 2+ + the reaction, such as Mg (OH) 2 are obtained a Mg (OH) 2.
이 제조과정중에서 Mg(OH)2의 순도를 높이기 위해 필수적인 것으로는 1) 해수 및 담수 중에 포함된 탄산이온을 H2SO4등을 이용하여 제거하므로 Ca2+이온이 CaCO3형태로 되어 불순물로 되는 것을 방지하는 공정, 2) 반응물을 해수로 세척하여 Ca(OH)2상태의 미반응 불순물을 해수중 Mg2+이온과 반응시켜 제거하는 공정, 3) 이온 상태로 Mg(OH)2슬러리에 흡착 또는 용해되어 있는 Ca2+, Na+, K+등 불순물 이온을 용해, 제거하기 위해 담수로 세척하는 공정등이 있다.In order to improve the purity of Mg (OH) 2 during the manufacturing process, 1) Ca 2+ ions form CaCO 3 as impurities by removing carbonate ions contained in seawater and fresh water using H 2 SO 4 . 2) washing the reactants with sea water to remove unreacted impurities in the Ca (OH) 2 state with Mg 2+ ions in sea water, and 3) washing the reactants with Mg (OH) 2 slurry in ionic state. There is a process of washing with fresh water to dissolve and remove impurity ions such as Ca 2+ , Na + , and K + that are adsorbed or dissolved.
상기의 방법에서는 해수와 소석회를 반응시킨후 해수 세척 및 침전공정을 거쳐 생성된 Mg(OH)2슬러리(Mg(OH)2고형분 약 20%)를 5-10배의 담수로 세척한 후 이를 침전시키면 다시 고형분 약 20%의Mg(OH)2슬러리가 침전되어 불순성분을 일부 용해한 담수와 분리된다.In the above method, after washing seawater and slaked lime, Mg (OH) 2 slurry (about 20% of Mg (OH) 2 solid) generated through seawater washing and precipitation process is washed with 5-10 times fresh water and then precipitated. Then, a slurry of about 20% Mg (OH) 2 in solid content is precipitated again and is separated from fresh water in which some impurities are dissolved.
이중 침전물을 추출하여 윗조작을 1-2회 반복하여 Mg(OH)2를 제조한다.Extracting the double precipitate to repeat the above operation 1-2 times to prepare Mg (OH) 2 .
그러나 상기 방법에 의해 제조된 슬러리에는 Mg(OH)2가 매우 미세하게 불규칙적으로 분포되어 분산매체내에서 불규칙한 브라운 운동을 하며 입자와 입자의 충돌이 일어나게 되고 이 과정에서 van der Waals 인력에 의해 입자들의 응집이 일어나게 된다.However, in the slurry prepared by the above method, Mg (OH) 2 is distributed very finely and irregularly, thus causing irregular brown motion in the dispersion medium and collision of particles and particles. In this process, particles are agglomerated by van der Waals attraction. This will happen.
또한, 입자들이 물과 같은 극성매체와 접촉하게 될때 입자들은 표면에 전하를 띄게되며 하전된 입자표면은 주위의 매체로부터 전기적으로 중화되기 위해 반대 이온을 흡착하게 된다. 이런 과정에서 Mg(OH)2-물계의 클로이드Ca2+, Na+, K+등 알카리나 알칼리 토류이온, 심지어는 물분자까지도 포위하여 세척수의 용해에 의한 불순물의 저감을 어렵게 하며 이러한 불순물 이온들을 용해시킬 새로운 물의 출입이 용이하지 않아 세척에는 다량의 담수가 필요하다.In addition, when the particles come into contact with a polar medium such as water, they charge on the surface and the charged particle surface adsorbs counter ions to electrically neutralize from the surrounding medium. In this process, alkaline or alkaline earth ions such as Mg (OH) 2 -water clad Ca 2+ , Na + , K + and even water molecules are surrounded, making it difficult to reduce impurities by dissolving the wash water. New water to dissolve them is not easy to access, so a large amount of fresh water is required for cleaning.
또, MgO 클링커의 경우 클링커나 불순물 중 CaO/SiO2비가 높은것이 슬래그에 대한 침식에 강한데 이경우 CaO의 양을 늘이는 것 보다는 SiO2양을 줄이는 것이 전체 MgO 순도를 높여주므로 바람직한데, 공업용수중에는 보통 25-40ppm정도의 SiO2가 용해되어 있고 고형물로서는 1~5ppm이 존재하고 있으므로 SiO2가 공업용수 세척공정에서 Mg(OH)2에 흡착되어 최종 MgO중 불순물로서의 SiO2양을 증가시키게 된다.In the case of MgO clinker, the higher CaO / SiO 2 ratio among clinker or impurities is more resistant to erosion of slag. In this case, it is preferable to reduce the amount of SiO 2 rather than to increase the amount of CaO to increase the overall MgO purity. Since about 2 to 40 ppm of SiO 2 is dissolved and 1 to 5 ppm is present as a solid, SiO 2 is adsorbed to Mg (OH) 2 in the industrial water washing process to increase the amount of SiO 2 as impurities in the final MgO.
본 발명은, 상기 문제점을 개선하기 위하여, 해수 세척을 끝낸 Mg(OH)2슬러리를 건조시킴으로써 보다 적은 공업용수 또는 SiO2를 제거한 정제수를 사용하여 보다 고순도의 Mg(OH)2를 제조하고자 하는 것으로써, 이를 상세히 설명하면 다음과 같다.The present invention, to improve the above problems, to prepare a higher purity Mg (OH) 2 using less industrial water or purified water from which SiO 2 is removed by drying the seawater washed Mg (OH) 2 slurry. If this is described in detail as follows.
즉, 본 발명은 통상의 방법에 의해서 해수 세척을 끝낸 Mg(OH)2슬러리를 일단 건조시킨 다음 이 건조품을 볼밀(ball mill) 등의 습식 분쇄기에Mg(OH)2고형분에 대해 5배 정도의 공업 용수 또는 SiO2를 제거한 정제수와 함께 넣어 분쇄 및 혼합시키고, 이것을 침전시켜 침전물을 다시 고형분에 대해 5배 정도의 공업용수 또는 SiO2를 제거한 정제수로 1-2회 세척하는 Mg(OH)2의 제조방법에 관한 것이다. 해수 세척이 끝난 후에 건조과정을 거치면서 건조중에 부착수가 증발하면서 입자들은 성장하여 물속에서 개개의 입자로 분리되어 있을 수 있는 상태로 존재한다.That is, according to the present invention, the dried Mg (OH) 2 slurry, which has been washed by the conventional method, is dried once, and then the dried product is subjected to about 5 times the amount of Mg (OH) 2 solid in a wet mill such as a ball mill. Mg (OH) 2 is washed 1-2 times with industrial water or purified water from which SiO 2 is removed by precipitation by mixing with it and grinding it with industrial water or purified water from which SiO 2 is removed. It relates to a manufacturing method. After seawater washing, the drying process is followed by evaporation of adhering water during drying. The particles grow and exist in a state where they can be separated into individual particles in water.
그러나 이 입자들은 건조 후에 매우 약한 힘으로 결합된 덩어리의 상태로 되어 있어 세척수와 접촉할 비표면적이 작다.However, after drying, these particles are in the form of agglomerated masses with very weak forces, so that the specific surface area in contact with the wash water is small.
따라서, 처음 담수 세척시에 가볍게 분쇄를 겸하여 줌으로써 세척수가 Mg(OH)2에 덩어리 상태로 흡착되어 있는 불순물 이온을 용해, 제거하는 것을 촉진하여 주는 것이 좋다.Therefore, it is good to facilitate the dissolution and removal of the impurity ions adsorbed in the form of agglomerate to Mg (OH) 2 by lightly pulverizing during the first fresh water washing.
이렇게 분리되 입자들은 해수 세척을 끝낸 Mg(OH)2슬러리내의 입자들보다 크고, 개개의 입자로 분리된 상태로 존재하기 때문에 불순물 이온이나 물분자에 대한 포위능력이 거의 없어져 Mg(OH)2에 흡착된 불순물들이 단위 세척수에 용해되는 속도가 종래 방법에 비해 매우 높을뿐만 아니라 침전물중의 고형분의 비율도 높아 침전능이 좋아지므로 세척수의 양을 대폭 줄일 수 있다.This separation are particles larger than Mg (OH) particles in the second slurry finishing the water washing, due to the presence of a discrete state to the individual particles are surrounded capacity for impurity ions and water molecules almost disappeared on Mg (OH) 2 The rate of dissolving the adsorbed impurities in the unit washing water is not only very high compared to the conventional method, but also the ratio of solids in the precipitate is high, so that the settling ability is improved, thereby greatly reducing the amount of washing water.
또한 세척수 양이 줄어듦으로 인해 Mg(OH)2의 수거율도 향상될 뿐만 아니라 Mg(OH)2에 부착되어 불순물로 남게되는 SiO2의 양도 줄일 수 있다.In addition, as the amount of washing water is reduced, not only the collection rate of Mg (OH) 2 is improved but also the amount of SiO 2 attached to Mg (OH) 2 and remaining as impurities can be reduced.
해수 세척이 끝난 슬러리의 건조방법으로는 오븐식 건조기(dry oven)내에서의 단속적인 건조, 회전 킬른(kiln)을 이용한 연속건조뿐만 아니라 분무식 건조기(spray dryer), 동결건조기(freeze dryer)등의 건조방법이 유효하며 적은 부착수분을 제거하여도 효과는 있지만 상기 건조품중의 Mg(OH)2의 양이 70% 이상이 되도록 부착수분이 제거되는 것이 보다 바람직하다.As a method of drying the washed slurry, intermittent drying in a dry oven, continuous drying using a rotary kiln, spray dryer, freeze dryer, etc. Although the drying method is effective and effective to remove less adherent moisture, it is more preferable that the adhered moisture is removed so that the amount of Mg (OH) 2 in the dried product is 70% or more.
본 발명에 의한 담수세척 방법에서도 담수로 1차 세척후 침전물이 50% 이상의 수분을 함유하고 있으므로 1회에 다량의 물론 세척하는 것보다는 2-3회로 나누어서 하는 것이 효과적이며, 담수량은 얻고자하는 수산화마그네슘 Mg(OH)2의 순도에 따라 변화시키면 되나Mg(OH)2고형분에 대해 5배 정도가 바람직하다.In the fresh water washing method according to the present invention, since the precipitate after the first washing with fresh water contains more than 50% of water, it is effective to divide 2-3 times at a time rather than washing a large amount of water at a time, and the fresh water amount is to be hydrated. when magnesium varies with the purity of Mg (OH) 2, but it is preferably about 5 times for Mg (OH) 2 solids.
이하, 실시예를 통하여 본 발명을 상세히 설명한다.Hereinafter, the present invention will be described in detail through examples.
[실시예 1]Example 1
본 발명 및 종래방법의 공업용수 양에 따른 Mg(OH)2의 순도를 조사하기 위하여, 소석회와 해수를 pH11.2에서 반응시키고, 2회의 세수세척을 실시한 후Mg(OH)2슬러리를 건조하여 불순물조성을 측정하였더니, 하기 표 1과 같았다.In order to investigate the purity of Mg (OH) 2 according to the amount of industrial water of the present invention and the conventional method, the slaked lime and seawater were reacted at pH11.2, washed twice and washed, and then the Mg (OH) 2 slurry was dried. Impurity composition was measured, as shown in Table 1 below.
[표 1]TABLE 1
상기 표 1과 같은 불순물을 포함하는 Mg(OH)2슬러리 100%[발명예(1)] 및 80%[발명예(2)]의 건조비Drying ratio of 100% [Inventive Example (1)] and 80% [Inventive Example (2)] of Mg (OH) 2 slurry containing impurities as shown in Table 1 above
로 건조한 다음 공업용수 5리터에 각각 건조된 Mg(OH)2슬러리 1Kg씩을 넣고 볼밀에서 약 5분간 분쇄 및 혼합한 후 메스 실린더에 넣고 침전시켜 이 침전물을 건조하여 화학분석을 행하였다.1 g of dried Mg (OH) 2 slurry was added to 5 liters of industrial water, and then ground and mixed in a ball mill for about 5 minutes. The precipitate was placed in a measuring cylinder and dried to conduct chemical analysis.
상기의 침전물에 다시 공업용수 5리터를 첨가하고 위의 조작으로 침전물을 건조하여 화학분석을 다시 행하였다.5 liters of industrial water was further added to the precipitate, and the precipitate was dried by the above operation, and chemical analysis was performed again.
위와같은 조작을 1회 더 반복한 후 이들의 화학분석 결과치를 각각 하기표 2에 표시하였다(산화물로 환산하여 표시함)After repeating the above operation once more, their chemical analysis results are shown in Table 2 below (in terms of oxides).
또한, 상기 표 1과 같은 불순물 조성을 갖는 Mg(OH)2침전물 5리터(Mg(OH)2고형분 약 1Kg)에 5리터의 공업용수를 넣고 충분히 섞은 후 침전물을 건조하여 화학분석을 행하였다(종래예). 상기의 침전물에 다시 공업용수 5리터를 넣고 침전물을 건조하여 화학분석을 행하였다.In addition, 5 liters of industrial water was added to 5 liters of Mg (OH) 2 precipitate (about 1 Kg of Mg (OH) 2 solid) having an impurity composition as shown in Table 1 above, followed by sufficient mixing, and the precipitate was dried for chemical analysis. Yes). 5 liters of industrial water was added to the precipitate again, and the precipitate was dried for chemical analysis.
위와 같은 조작을 1회 더 반복하여 그 결과를 하기 표2에 다시 표시하였다.The above operation was repeated once more and the results are shown again in Table 2 below.
[표 2]TABLE 2
상기 표 2에 나타난 바와 같이 Ca2+, Na+, K+등 물에 가용성인 불순물들이 같은 양의 세척수로 세척했을 경우 본 발명의 세척방법을 사용했을 때 종래의 방법에 비해 현저히 빠른 비율로 제거됨을 알 수 있다.As shown in Table 2, when impurities soluble in water, such as Ca 2+ , Na + , K + , are washed with the same amount of washing water, they are removed at a significantly faster rate than the conventional method when the washing method of the present invention is used. It can be seen.
[실시예2]Example 2
SiO2를 0.2ppm 이하 함유되고 있는 정제수를 사용하여 실시예 1의 발명에 1과 동일한 조작을 행하였으며, 이에 대한 결과를 하기 표3에 나타내었다.Purified water containing 0.2 ppm or less of SiO 2 was performed in the same manner as in Example 1, and the results thereof are shown in Table 3 below.
또한, 상기 표1과 같은 불순물 조성을 갖는 Mg(OH)2침전물1 리터 (Mg(OH)2고형분 약 1Kg 포함)에 30리터의 공업용수를 넣고 충분히 섞은 후 침전물을 건조하여 화학분석을 행하였다(종래예).In addition, 30 liters of industrial water was added to 1 liter of Mg (OH) 2 precipitate (containing about 1 Kg of Mg (OH) 2 solid) having an impurity composition as shown in Table 1 above, and the precipitate was dried for chemical analysis ( Conventional example).
위의 세척이 끝난 침전물로 위와 같은 조작을 1-2회 반복하여 이 결과들을 하기 표 3에 나타내었다.The above operation was repeated 1-2 times with the above washed precipitates, and the results are shown in Table 3 below.
[표 3]TABLE 3
상기 표 3에 나타난 바와 같이 본 발명이 종래방법에 비하여 작은 세척수 양으로 고순도의 Mg(OH)2를 얻을 수 있으며, 특히 세척이 반복되어도 SiO2성분이 거의 증가되지 않음을 알 수 있다.As shown in Table 3, the present invention can obtain high purity Mg (OH) 2 with a small amount of washing water compared to the conventional method, and it can be seen that the SiO 2 component is hardly increased even when the washing is repeated.
상술한 바와 같이, 본 발명에서는 통상의 방법에 비해 단위 세척수량에 대한 불순물 제거효과가 커서 같은 양의 세척수를 사용했을때 불순물의 양을 대폭 낮출 수 있으며, 거의 동등한 양의 불순물 조성을 갖는 Mg(OH)2제조에 있어서 본 발명에 의한 세척방법은 통상의 방법에 비해 약 1/6정도의 세척수로도 불순물 제거가 가능한 효과가 있는 것이다.As described above, in the present invention, since the impurity removal effect on the unit washing water amount is larger than that of the conventional method, when the same amount of washing water is used, the amount of impurities can be greatly reduced, and Mg (OH) having an almost equivalent amount of impurity composition is used. 2 ) In the preparation, the washing method according to the present invention has the effect of removing impurities even with about 1/6 degree of washing water, compared to the conventional method.
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KR1019880017919A KR910002385B1 (en) | 1988-12-30 | 1988-12-30 | Production of magnesium hydroxide from sea water |
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KR100727239B1 (en) * | 2006-09-13 | 2007-06-11 | 재단법인 포항산업과학연구원 | Method for manufacturing super pure fine powder of mgo using rf plasma device |
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KR100467802B1 (en) * | 2001-12-24 | 2005-01-24 | 주식회사 포스렉 | Slurry comprising magnesium hydroxide produced from seawater with high concentration |
KR101975469B1 (en) * | 2016-12-15 | 2019-05-07 | 주식회사 포스코 | Apparatus and method for solid-liquid seperating |
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KR100727239B1 (en) * | 2006-09-13 | 2007-06-11 | 재단법인 포항산업과학연구원 | Method for manufacturing super pure fine powder of mgo using rf plasma device |
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