KR100894872B1 - The method for manufacturing magnesium hydroxide having excellent dispersibility for flame retardant - Google Patents

The method for manufacturing magnesium hydroxide having excellent dispersibility for flame retardant Download PDF

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KR100894872B1
KR100894872B1 KR1020070057785A KR20070057785A KR100894872B1 KR 100894872 B1 KR100894872 B1 KR 100894872B1 KR 1020070057785 A KR1020070057785 A KR 1020070057785A KR 20070057785 A KR20070057785 A KR 20070057785A KR 100894872 B1 KR100894872 B1 KR 100894872B1
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magnesium hydroxide
magnesia
flame retardant
pulverized
dispersibility
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KR20080109445A (en
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손동환
김동한
신길재
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주식회사 포스렉
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    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F5/00Compounds of magnesium
    • C01F5/14Magnesium hydroxide
    • C01F5/16Magnesium hydroxide by treating magnesia, e.g. calcined dolomite, with water or solutions of salts not containing magnesium
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/20Particle morphology extending in two dimensions, e.g. plate-like
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/61Micrometer sized, i.e. from 1-100 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2004/00Particle morphology
    • C01P2004/60Particles characterised by their size
    • C01P2004/62Submicrometer sized, i.e. from 0.1-1 micrometer
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/20Powder free flowing behaviour
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/18Oxygen-containing compounds, e.g. metal carbonyls
    • C08K3/20Oxides; Hydroxides
    • C08K3/22Oxides; Hydroxides of metals
    • C08K2003/2217Oxides; Hydroxides of metals of magnesium
    • C08K2003/2224Magnesium hydroxide
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/02Flame or fire retardant/resistant
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2666/00Composition of polymers characterized by a further compound in the blend, being organic macromolecular compounds, natural resins, waxes or and bituminous materials, non-macromolecular organic substances, inorganic substances or characterized by their function in the composition
    • C08L2666/66Substances characterised by their function in the composition
    • C08L2666/84Flame-proofing or flame-retarding additives

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
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  • Inorganic Chemistry (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

난연제용으로 사용되는 경제성이 우수한 고분산성 수산화마그네슘의 제조방법이 제공된다.Provided is a method for producing highly dispersible magnesium hydroxide, which is economically effective for use as a flame retardant.

이 수산화마그네슘의 제조방법은 해수로부터 제조된 마그네시아를 45㎛ 이하의 평균 입경을 가지도록 분쇄하는 단계; 상기 분쇄된 마그네시아를 물에 수화하여 수산화마그네슘을 제조하는 단계로서, 이때 초산 및 염산을 단독 또는 복합첨가하여 수화하는 것을 특징으로 하는 단계; 상기 수산화마그네슘을 세척한 다음 건조 및 분쇄하는 단계;를 포함하여 이루어지며 상기 분쇄된 수산화마그네슘의 순도는 98% 이상이고, 상기 분쇄된 수산화마그네슘의 금속화합물로 이루어진 불순물 함량은 0.05중량% 이하이다.This magnesium hydroxide production method comprises the steps of grinding the magnesia prepared from seawater to have an average particle diameter of 45㎛ or less; Hydrating the pulverized magnesia in water to produce magnesium hydroxide, wherein the step of hydrating acetic acid and hydrochloric acid alone or in combination; Washing and then drying and pulverizing the magnesium hydroxide; the purity of the pulverized magnesium hydroxide is 98% or more, and the impurity content of the pulverized magnesium hydroxide metal compound is 0.05% by weight or less.

본 발명에 따르면, 낮은 제조비용으로 분산성이 우수한 수산화마그네슘을 제공할 수 있으며, 이와 같이 제조된 수산화마그네슘은 고무 및 플라스틱 등에 난연제로 적용될 수 있다.According to the present invention, it is possible to provide a magnesium hydroxide having excellent dispersibility at a low manufacturing cost, the magnesium hydroxide prepared in this way can be applied as a flame retardant to rubber and plastics.

수산화마그네슘, 마그네시아, 분산성, 난연제, 초산, 불순물 Magnesium Hydroxide, Magnesia, Dispersibility, Flame Retardant, Acetic Acid, Impurities

Description

난연제용 분산성이 우수한 수산화마그네슘의 제조방법{The method for manufacturing magnesium hydroxide having excellent dispersibility for flame retardant}The method for manufacturing magnesium hydroxide having excellent dispersibility for flame retardant}

일본 공개특허공보 제2000-233924호Japanese Laid-Open Patent Publication No. 2000-233924

국내 공개특허공보 제2001-0086246호Korean Unexamined Patent Publication No. 2001-0086246

국내 공개특허공보 제2006-0112624호Korean Unexamined Patent Publication No. 2006-0112624

본 발명은 난연제용으로 사용되는 수산화마그네슘의 제조방법에 관한 것이다. 보다 상세하게는, 제조비용이 저렴할 뿐만 아니라 우수한 분산성을 갖는 수산화마그네슘의 제조방법에 관한 것이다.The present invention relates to a method for producing magnesium hydroxide used for a flame retardant. More specifically, the present invention relates to a method for producing magnesium hydroxide, which is not only low in manufacturing cost but also excellent in dispersibility.

수산화마그네슘(Mg(OH)2)은 염기성 내화재료인 마그네시아(MgO)의 원료로 널리 알려져 있으며, 의약용, 공업용으로서 넓은 분야에서 사용되고 있다. 예컨대, 의약용으로서는 제산제, 사하제 및 동물용 약제 등이 있으며, 공업용으로서는 열가 소성 수지에 배합하여 이 수지에 난연성을 부여하는 난연제, 함유폐수용 흡착제, 배연탈황제, 배수중화제 및 토질개량제 등이 있다.Magnesium hydroxide (Mg (OH) 2 ) is widely known as a raw material of magnesia (MgO), which is a basic refractory material, and is used in a wide range of fields for medicine and industrial purposes. For example, medicaments include antacids, hypothalamic agents, and veterinary agents. Industrial applications include flame retardants which are incorporated into thermoplastic resins to impart flame retardancy to these resins, adsorbents for containing wastewater, flue gas desulfurization agents, drainage neutralizers, and soil improvers. .

일반적으로 수산화마그네슘 입자의 제조방법도 다양하여, 예컨대 마그네슘 이온을 함유하는 마그네슘염 용액으로서 간수 또는 염화마그네슘염 용액 등을 사용하고 알칼리 용액으로서 가성소다, 암모니아수, 석회 등과 침전반응시켜 사용하는 방법; 브루사이트광(Brucite)의 정제나 천연산 마그네사이트를 소성, 수화하여 생성시키는 방법; 탈탄산 해수와 소석회의 치환반응에 의해 생성시키는 방법; 및 산화마그네슘을 수성매체와 수화반응시켜 사용하는 방법 등이 있다.In general, there are various methods for producing magnesium hydroxide particles, for example, a method of using magnesium salt as a magnesium salt solution using precipitated water, magnesium chloride salt solution, and the like as a alkaline solution by precipitation reaction with caustic soda, ammonia water, lime and the like; Purification of brucite or a method of calcining and hydrating the natural magnesite produced; A method produced by substitution reaction of decarbonated seawater and slaked lime; And a method of hydrating magnesium oxide with an aqueous medium for use.

그러나, 브루사이트광의 정제나 분쇄를 통하여 난연제로 사용되는 경우에는 수지내 수산화마그네슘의 분산성이 저하되어 난연제로 사용되기에 한계가 있고, 천연산 마그네사이트를 소성, 수화하여 생성시키는 방법은 순도가 낮아 난연제로서 사용되기에 한계가 있다. 또한, 해수와 알칼리를 반응시켜 수산화마그네슘을 제조함에 따라 고순도의 수산화마그네슘을 얻는 것은 가능하나, 생성된 입자의 형상이 원형상으로 응집되어 분산이 어려운 문제점이 있다. 또한, 상기 제조방법 중 간수나 염화마그네슘을 이용하는 방법은 염화마그네슘을 알칼리와 반응시켜 수산화마그네슘을 제조함에 따라 고순도 및 육각판상의 결정형태를 지닌 수산화마그네슘을 제조하는 것은 가능하나, 제조비용이 너무 상승하여 경제성이 떨어지는 문제점이 있다.However, when used as a flame retardant through the purification or pulverization of brucite ore, the dispersibility of magnesium hydroxide in the resin is lowered, and thus it is limited to be used as a flame retardant. The method of calcining and hydrating the natural magnesite produced by low purity is low There is a limit to being used as a flame retardant. In addition, it is possible to obtain magnesium hydroxide with high purity as seawater and alkali react with magnesium to produce magnesium hydroxide, but the shape of the particles produced is agglomerated into a circular shape, which makes it difficult to disperse the magnesium hydroxide. In addition, the method of using the brine or magnesium chloride of the above manufacturing method, it is possible to produce magnesium hydroxide having a high purity and hexagonal crystal form as the magnesium hydroxide is prepared by reacting magnesium chloride with alkali, the manufacturing cost is too high There is a problem that the economy is poor.

수산화마그네슘을 제조하는 대표적인 종래기술로는 일본 공개특허공보 제2000-233924호 및 국내 공개특허공보 제2001-0086246호가 있다. 상기 종래기술들은 염화마그네슘과 알칼리물질을 수성매체 중에서 반응시켜 수산화마그네슘 입자를 제조하는 것으로서, 상기 반응은 첨가제로서 유기산, 붕산, 규산 및 이들의 수가용성 염으로 이루어지는 군에서 선택된 적어도 1종의 화합물을 염화마그네슘에 대하여 0.01~150몰% 첨가하여 실시하고 있다. Representative prior arts for producing magnesium hydroxide include Japanese Patent Laid-Open No. 2000-233924 and Korean Patent Laid-Open No. 2001-0086246. The prior art is to prepare magnesium hydroxide particles by reacting magnesium chloride with an alkali in an aqueous medium, the reaction comprising at least one compound selected from the group consisting of organic acids, boric acid, silicic acid and their water-soluble salts as an additive It is performed by adding 0.01-150 mol% with respect to magnesium chloride.

또한, 이러한 수산화마그네슘 입자가 난연제용으로 사용 가능한 입자의 특성을 갖기 위해서 120~200℃ 온도와 2~10kgf/㎠의 고압에서 30분~8시간 동안 수열처리함으로써 입자 형태, 크기 및 분포를 제어하고 있는데, 이러한 공정을 거친 수산화마그네슘 입자는 그 특성이 우수하나 제조공정이 복잡하고 반응도가 낮아 생산성이 저하되며 반응으로 생성된 수산화마그네슘 입자 이외의 불순물처리를 위한 비용 및 수열처리를 위한 다량의 에너지가 소요되어 그 제조비용이 높은 단점을 가지고 있다. In addition, to control the particle shape, size and distribution of the magnesium hydroxide particles by hydrothermal treatment for 30 minutes to 8 hours at a temperature of 120 ~ 200 ℃ and high pressure of 2 ~ 10kgf / ㎠ to have the characteristics of particles that can be used for flame retardant Magnesium hydroxide particles, which have undergone such a process, have excellent properties, but the manufacturing process is complicated and the reactivity is low, resulting in low productivity, and a large amount of energy for the treatment of impurities other than the magnesium hydroxide particles produced by the reaction and a large amount of energy for hydrothermal treatment. It has a disadvantage that the manufacturing cost is high.

최근, 해수로부터 제조된 마그네시아를 이용하여 수산화마그네슘을 제조하는 대표적인 종래기술로는 국내 공개특허공보 제2006-0112624호가 있다. 상기 종래기술은 해수 MgO를 수화 및 산처리하여 분산성이 우수한 고순도 수산화마그네슘의 제조방법을 제시하고 있다. 그러나, 99 중량% 이상의 MgO 순도를 지닌 수산화마그네슘을 얻기 위하여, 제조비용이 높은 단점을 가지고 있다.In recent years, Korean Patent Application Publication No. 2006-0112624 is a representative conventional technique for producing magnesium hydroxide using magnesia prepared from seawater. The prior art proposes a method for producing high purity magnesium hydroxide having excellent dispersibility by hydration and acid treatment of seawater MgO. However, in order to obtain magnesium hydroxide having a MgO purity of 99% by weight or more, the manufacturing cost has a disadvantage.

본 발명은 상기한 종래의 문제점을 개선하기 위한 것으로, 해수로부터 제조된 마그네시아를 원료로 이용하고, 첨가제 및 수화반응을 제어하여 수산화마그네슘의 순도 및 불순물 함량을 적절히 관리함에 따라 제조비용을 낮추는 동시에 분산성을 향상시킨 수산화마그네슘의 제조방법을 제공하는데, 그 목적이 있다.The present invention is to improve the above-mentioned problems, by using magnesia prepared from seawater as a raw material, by controlling the additives and hydration reaction to properly control the purity and impurities content of magnesium hydroxide while reducing the production cost To provide a method for producing magnesium hydroxide with improved acidity, an object thereof is provided.

상기 목적을 달성하기 위한 본 발명은 해수로부터 제조된 마그네시아를 45㎛ 이하의 평균 입경을 가지도록 분쇄하는 단계;The present invention for achieving the above object is a step of grinding the magnesia prepared from seawater to have an average particle diameter of 45㎛ or less;

상기 분쇄된 마그네시아를 물에 수화하여 수산화마그네슘을 제조하는 단계로서, 이때 초산 및 염산을 단독 또는 복합첨가하여 수화하는 것을 특징으로 하는 단계;Hydrating the pulverized magnesia in water to produce magnesium hydroxide, wherein the step of hydrating acetic acid and hydrochloric acid alone or in combination;

상기 수산화마그네슘을 세척한 다음 건조 및 분쇄하는 단계;를 포함하여 이루어지며 상기 분쇄된 수산화마그네슘의 순도는 98% 이상이고, 상기 분쇄된 수산화마그네슘의 금속화합물로 이루어진 불순물 함량은 0.05중량% 이하인 것을 특징으로 하는 난연제용 분산성이 우수한 수산화마그네슘의 제조방법에 관한 것이다.Washing and then drying and pulverizing the magnesium hydroxide; the purity of the pulverized magnesium hydroxide is 98% or more, and the impurity content of the pulverized magnesium hydroxide metal compound is 0.05% by weight or less. It is related with the manufacturing method of magnesium hydroxide which is excellent in the dispersibility for flame retardants.

이하, 본 발명을 상세하게 설명한다.EMBODIMENT OF THE INVENTION Hereinafter, this invention is demonstrated in detail.

본 발명자들은 해수로부터 제조된 마그네시아를 이용하여 수산화마그네슘을 제조하는 방법에 있어서, 고순도를 위한 불순물 제거 비용이 높고 해수에서 추출된 수산화마그네슘 입자의 형상이 원형상으로 응집되어 분산이 어려운 문제점을 해결 하기 위한 방안을 연구하던 중 해수로부터 제조된 마그네시아를 원료로 이용하고, 첨가제로서 초산 및/또는 염산을 첨가하여 물과 수화반응시켜 수산화마그네슘의 순도와 금속화합물의 불순물 함량을 적절히 관리하면 제조비용을 낮추는 동시에 고분산성을 갖는 수산화마그네슘을 확보할 수 있다는 것을 실험을 통해 확인하고, 그 실험결과에 기초하여 본 발명을 완성하게 된 것이다.The present inventors in the method for producing magnesium hydroxide using magnesia prepared from sea water, high impurity removal cost for high purity and the shape of magnesium hydroxide particles extracted from sea water aggregated in a circular shape to solve the difficult problem of dispersion While researching the solution, magnesia manufactured from seawater is used as a raw material, and by adding acetic acid and / or hydrochloric acid as an additive, it is hydrated with water to properly control the purity of magnesium hydroxide and the impurity content of the metal compound to lower the manufacturing cost. At the same time, it was confirmed through experiments that magnesium hydroxide having high dispersibility was obtained, and the present invention was completed based on the experimental results.

본 발명에서는 해수로부터 제조된 마그네시아를 원료로 이용하게 되며, 해수로부터 마그네시아를 제조하는 통상적인 방법으로는 탈탄산 처리된 해수를 석회유와 반응시켜 수산화마그네슘을 제조하고, 이어 상기 수산화마그네슘을 세척, 건조, 소성함으로써 제조된다.In the present invention, magnesia prepared from seawater is used as a raw material, and a conventional method of preparing magnesia from seawater is made of magnesium hydroxide by reacting decarbonated seawater with lime oil, and then washing and drying the magnesium hydroxide. It is manufactured by baking.

이하, 본 발명의 수산화마그네슘 입자의 제조방법에 대하여 설명한다.Hereinafter, the manufacturing method of the magnesium hydroxide particle of this invention is demonstrated.

먼저, 본 발명에서는 상기와 같이 해수로부터 제조된 마그네시아를 45㎛ 이하의 평균 입경을 가지도록 분쇄한다. 분쇄는 산화마그네슘을 미세하게 분쇄할 수 있는 방법이면 어느 것이든 적용할 수 있다. 상기 입자크기보다 큰 입자를 사용하는 경우에는 이후의 수화처리 시간이 장시간 필요하며, 균일한 입자 생성이 어려울 수 있다. 분쇄시, 분쇄기계 등에서 혼입되는 Fe2O3 등의 중금속 제거를 위해 바람직하게는 탈철이 행해질 수 있다.First, in the present invention, the magnesia prepared from the sea water as described above is pulverized to have an average particle diameter of 45㎛ or less. Crushing can be applied to any method that can finely grind magnesium oxide. In the case of using particles larger than the particle size, subsequent hydration time is required for a long time, and uniform particle generation may be difficult. At the time of pulverization, degassing may be preferably performed in order to remove heavy metals such as Fe 2 O 3 mixed in a crushing machine or the like.

또한, 상기 해수로부터 제조된 마그네시아는 95중량% 이상의 MgO를 함유하는 것을 이용하는 것이 바람직한데, 상기 MgO 함량이 95중량% 미만인 경우에는 본 발명에서 목표로 하는 고순도의 수산화마그네슘을 확보하기 어려울 수 있다.In addition, the magnesia prepared from the seawater is preferably used containing 95% by weight or more of MgO, when the MgO content is less than 95% by weight it may be difficult to secure a high-purity magnesium hydroxide targeted in the present invention.

이어 상기 분쇄된 마그네시아를 물에 수화하여 수산화마그네슘을 제조하게 되며, 이때 초산 및 염산을 단독 또는 복합첨가하여 산처리한다. 이러한 첨가제 사용은 육각판상의 입자형성을 가능하게 하여 분산성 향상에 기여할 수 있다. 첨가되는 초산 및/또는 염산의 함량은 물 1리터에 0.1~5M 사용하는 것이 바람직하다. 0.1M 미만으로 첨가될 경우에는 생성되는 수산화마그네슘 입자의 형상이 균일하지 않거나 수산화마그네슘이 완전히 생성되기 어려울 수 있다. 또한, 5M를 초과하여 첨가될 경우 육각판상의 입자가 형성되나 그 크기가 미분화되고 비표면적이 증가하여 분산성을 저해할 수 있으며 다량의 첨가제 사용은 경제성을 악화시키는 요인을 제공할 수 있다.Subsequently, the pulverized magnesia is hydrated in water to prepare magnesium hydroxide, wherein acetic acid and hydrochloric acid are added alone or in combination to perform acid treatment. The use of such additives can contribute to the improvement of dispersibility by enabling the formation of hexagonal particles. The content of acetic acid and / or hydrochloric acid to be added is preferably 0.1 to 5 M per liter of water. When added below 0.1 M, the shape of the resulting magnesium hydroxide particles may be uneven or it may be difficult for magnesium hydroxide to be completely produced. In addition, when added in excess of 5M to form a hexagonal plate-shaped particles, but the size is undifferentiated and the specific surface area is increased may inhibit the dispersibility and the use of a large amount of additives may provide a factor to deteriorate the economics.

상기 수화반응은 해수로부터 제조된 마그네시아가 완전히 수산화마그네슘으로 되기 위한 시간과 온도를 적절히 조절할 수 있으며, 특히 수화반응 온도는 시간과 에너지 비용을 고려하여 70℃ 이상으로 행하는 것이 바람직하다. 또한, 본 발명에서는 목표로 하는 수산화마그네슘 입자를 형성시키기 위하여 수화반응시 산을 첨가하는데, 목표로 하는 반응성, 순도 및 입자크기를 위하여 초산 및 염산을 단독 또는 복합첨가할 수 있다. The hydration reaction can appropriately control the time and temperature for the magnesia prepared from seawater to completely magnesium hydroxide, in particular, the hydration reaction temperature is preferably carried out at 70 ℃ or more in consideration of time and energy costs. In addition, in the present invention, an acid is added during the hydration reaction to form the target magnesium hydroxide particles, and acetic acid and hydrochloric acid may be added alone or in combination for the target reactivity, purity, and particle size.

이후, 상기 산처리된 수산화마그네슘을 통상의 방법을 이용하여 세척한 다음 건조하고 분쇄하게 된다. Thereafter, the acid treated magnesium hydroxide is washed using a conventional method, and then dried and pulverized.

또한, 상기 수산화마그네슘의 순도가 98% 이상인 것이 바람직하며, 순도가 98% 미만일 경우 나머지 성분들이 불순물로 작용하게 되어 최종 제품의 열안정성을 현저하게 저하시킬 수 있다. 또한, 본원발명에서는 고순도를 위한 높은 제조비용을 절감하기 위하여 상기 수산화마그네슘의 순도를 98~99 중량% 미만으로 제어하는 것이 바람직하다.In addition, it is preferable that the purity of the magnesium hydroxide is 98% or more, and if the purity is less than 98%, the remaining components act as impurities, which can significantly lower the thermal stability of the final product. In addition, in the present invention, in order to reduce the high manufacturing cost for high purity, it is preferable to control the purity of the magnesium hydroxide to less than 98 ~ 99% by weight.

또한, 본원발명에서는 분쇄된 수산화마그네슘의 금속화합물로 이루어진 불순물 함량이 0.05중량% 이하인 것이 바람직하며, 상기 불순물 함량이 0.05중량%를 초과하는 경우에는 난연성을 저하시킬 뿐만 아니라, 목표로 하는 기타 물성을 확보하는데 어려울 수 있다. 상기 불순물인 금속화합물로는 철화합물, 망간화합물, 코발트화합물, 크롬화합물, 구리화합물, 바나듐화합물 및 니켈화합물 등이 포함될 수 있다.In addition, in the present invention, it is preferable that the impurity content composed of the metal compound of crushed magnesium hydroxide is 0.05% by weight or less, and when the impurity content exceeds 0.05% by weight, not only the flame retardancy is lowered, but also other physical properties of interest. It can be difficult to secure. The impurity metal compound may include iron, manganese, cobalt, chromium, copper, vanadium and nickel.

또한, 상기 분쇄후 수산화마그네슘은 평균 입도가 0.8~3.0㎛ 이고, 비표면적이 4~10㎡/g 이하인 것이 바람직한데, 평균 입도가 0.8㎛ 미만이거나 비표면적이 10㎡/g을 초과하는 경우에는 작은 입자들로 인한 수지와의 분산성이 저하될 수 있고, 평균 입도가 3.0㎛을 초과하거나 비표면적이 4㎡/g 미만인 경우에도 큰 입자들 로 인하여 수지와의 분산성이 저하될 수 있다. 또한, 상기와 같이 제조된 수산화마그네슘의 결정상은 육각판상인 것이 바람직하며, 이는 결정상이 육각판상일 때 분산성 및 기타특성이 가장 우수하기 때문이다.In addition, the magnesium hydroxide after grinding is preferably an average particle size of 0.8 ~ 3.0㎛, the specific surface area is 4 ~ 10㎡ / g or less, when the average particle size is less than 0.8㎛ or more than 10㎡ / g The dispersibility with the resin due to the small particles may be reduced, and even when the average particle size exceeds 3.0 μm or the specific surface area is less than 4 m 2 / g, the dispersibility with the resin may be reduced due to the large particles. In addition, the crystal phase of magnesium hydroxide prepared as described above is preferably in the hexagonal plate shape, because the dispersibility and other properties are the best when the crystal phase is a hexagonal plate shape.

한편, 상기 분쇄된 수산화마그네슘은 용도에 따라 해쇄 및 표면처리공정을 행하여 수산화마그네슘의 최종입자, 기계적 강도 및 기타 물성을 향상시킬 수 있으며, 흡습하기 쉬운 물질에 따른 보관기간 등의 문제점을 해결할 수 있다.On the other hand, the pulverized magnesium hydroxide can improve the final particle, mechanical strength and other physical properties of magnesium hydroxide by performing the pulverization and surface treatment process according to the use, it can solve the problems such as storage period due to the material easily absorbed .

이하, 본 발명을 실시예를 통하여 보다 상세하게 설명한다.Hereinafter, the present invention will be described in more detail with reference to Examples.

[실시예]EXAMPLE

(발명예)(Invention example)

탈탄산 해수와 정제된 석회와의 반응에 의해 생성한 수산화마그네슘을 탈수, 건조, 소성하여 MgO함량 98.4중량%의 마그네시아를 제조하였으며, 이를 미분쇄하여 평균 입경이 23㎛인 MgO입자를 85℃에서 7시간 동안 수화반응시켰다. 이때 입자조절제로 0.25M의 초산을 첨가하였으며, 이후 통상의 방법으로 세척 및 건조한 후 다시 스테아르산(Stearic Acid)으로 표면처리한 수산화마그네슘(Mg(OH)2)에 대하여 MgO순도, 비중, 입자의 결정상, 평균입자경, 비표면적 및 제조비용지수를 평가하였다.Magnesium hydroxide produced by the reaction of decarbonated seawater with purified lime was dehydrated, dried and calcined to produce magnesia having a MgO content of 98.4 wt%, and finely ground MgO particles having an average particle diameter of 23 μm at 85 ° C. The reaction was hydrated for 7 hours. At this time, 0.25 M acetic acid was added as a particle control agent, and then MgO purity, specific gravity, and particles of magnesium hydroxide (Mg (OH) 2 ) surface-treated with stearic acid after washing and drying in a conventional manner. Crystal phase, average particle diameter, specific surface area and manufacturing cost index were evaluated.

(비교예)(Comparative Example)

비교예1은 천연산 원료인 브루사이트(Brucite)광을 정제하여 표면 처리한 수산화마그네슘, 비교예2는 천연 마그네사이트를 소성한 마그네시아를 상기 발명예의 제조조건을 이용하여 처리한 수산화마그네슘, 비교예3은 염화마그네슘과 알칼리인 암모니아수를 수열반응시켜 생성된 수산화마그네슘을 이용하였다. 상기 비교예1, 비교예2 및 비교예3의 MgO순도, 비중, 입자의 결정상, 평균입자경, 비표면적 및 제조비용지수를 평가하였으며, 그 결과는 하기 표 1과 같다.Comparative Example 1 is a magnesium hydroxide which is surface-treated by refining Brucite light as a natural raw material, Comparative Example 2 is a magnesium hydroxide treated with a magnesia calcined natural magnesite using the production conditions of the invention, Comparative Example 3 Magnesium hydroxide produced by hydrothermal reaction between silver chloride and alkali ammonia water was used. The MgO purity, specific gravity, crystal phase, average particle diameter, specific surface area and manufacturing cost index of Comparative Example 1, Comparative Example 2 and Comparative Example 3 were evaluated, and the results are shown in Table 1 below.

이후, 전선용 수지인 에틸렌 에틸 아세테이트(Ethylene Ethyl Acetate) 수지에 상기 제조한 발명예 및 비교예들의 수산화마그네슘을 50중량% 첨가하여 분산성, 난연성(산소지수), 인장강도 및 신장율을 측정하여 평가하였으며, 그 결과는 하기 표 1과 같다. Thereafter, 50% by weight of magnesium hydroxide of the invention examples and comparative examples prepared above was added to ethylene ethyl acetate (Ethylene Ethyl Acetate) resin, which is a wire resin, to measure dispersibility, flame retardancy (oxygen index), tensile strength, and elongation rate. The results are shown in Table 1 below.

[표 1]TABLE 1

구 분division 실시예Example 비교예 1Comparative Example 1 비교예 2Comparative Example 2 비교예 3Comparative Example 3 수산화 마그네슘Magnesium hydroxide MgO 순도MgO Purity 98.798.7 96.896.8 97.697.6 99.499.4 비 중importance 1.341.34 1.371.37 1.351.35 1.321.32 입자의 결정상Crystal phase of particles 육각판상Hexagonal plate shape 육각판상Hexagonal plate shape 육각판상Hexagonal plate shape 육각판상Hexagonal plate shape 평균입자경(㎛)Average particle size (㎛) 1.21.2 2.52.5 1.81.8 0.90.9 비표면적(㎡/g)Specific surface area (㎡ / g) 66 44 66 55 제조비용지수Manufacturing Cost Index 100100 9090 105105 187187 평가evaluation 분산성Dispersibility ×× 난연성(산소지수)Flame Retardant (Oxygen Index) 3232 2929 3030 3333 인장강도(kgf/㎠)Tensile strength (kgf / ㎠) 1.11.1 0.70.7 0.80.8 1.11.1 신장율(%)Elongation (%) 550550 370370 450450 560560 상기 제조비용지수는 발명예의 제조 원단가를 100으로 하여 비교예의 원단가를 비율로 나타낸 것임The manufacturing cost index is represented by the ratio of the production cost of the comparative example to 100 as the production cost of the invention example

상기 표 1에 나타난 바와 같이, 본 발명의 범위를 만족하는 발명예의 경우 분산성, 난연성 및 기계적 물성이 양호할 뿐만 아니라 제조비용도 상대적으로 저렴한 수산화마그네슘을 제조할 수 있었다. As shown in Table 1, in the case of the invention examples satisfying the scope of the present invention, not only good dispersibility, flame retardancy and mechanical properties, but also manufacturing magnesium hydroxide can be produced at a relatively low cost.

그러나, 천연산 원료인 브루사이트광을 정제하여 표면 처리한 수산화마그네슘을 이용한 비교예1의 경우, 제조비용은 저렴하였으나, 순도가 낮아 불순물이 많을 뿐만 아니라, 분산성 및 기타 물성에서도 불량한 문제점이 있었다. However, in the case of Comparative Example 1 using magnesium hydroxide, which is a surface-treated magnesium hydroxide purified from a natural raw material, the manufacturing cost is low, but the purity is low, there are many impurities, as well as poor dispersibility and other physical properties. .

또한, 천연 마그네사이트를 소성하여 제조된 마그네시아를 본 발명의 방법을 이용하여 처리한 비교예2의 경우, 순도와 분산성이 매우 열악하였다. In addition, in Comparative Example 2 in which magnesia produced by calcining natural magnesite was treated using the method of the present invention, purity and dispersibility were very poor.

또한, 염화마그네슘과 암모니아수를 수열반응시켜 생성된 수산화마그네슘을 이용한 비교예3의 경우, 순도, 분산성이 우수하기는 하였으나 제조비용이 현저하게 높아 실생간에 적용되기 어려웠다.In addition, in the case of Comparative Example 3 using magnesium hydroxide produced by hydrothermal reaction of magnesium chloride and ammonia water, the purity and dispersibility were excellent, but the manufacturing cost was remarkably high, and thus it was difficult to be applied in real life.

상술한 바와 같이, 본 발명에 따르면 낮은 제조비용으로 분산성이 우수한 수산화마그네슘을 제공할 수 있으며, 이와 같이 제조된 수산화마그네슘은 고무 및 플라스틱 등에 난연제로 이용하는 것이 가능하다.As described above, according to the present invention, it is possible to provide magnesium hydroxide having excellent dispersibility at a low manufacturing cost, and the magnesium hydroxide thus prepared can be used as a flame retardant in rubber and plastics.

Claims (3)

해수로부터 제조된 마그네시아를 45㎛ 이하의 평균 입경을 가지도록 분쇄하는 단계;Grinding magnesia prepared from seawater to have an average particle diameter of 45 μm or less; 상기 분쇄된 마그네시아를 물에 수화하여 수산화마그네슘을 제조하는 단계로서, 이때 초산 및 염산을 단독 또는 복합첨가하여 수화하는 것을 특징으로 하는 단계;Hydrating the pulverized magnesia in water to produce magnesium hydroxide, wherein the step of hydrating acetic acid and hydrochloric acid alone or in combination; 상기 수산화마그네슘을 세척한 다음 건조 및 분쇄하는 단계;를 포함하여 이루어지며 상기 분쇄된 수산화마그네슘의 순도는 98% 이상이고, 상기 분쇄된 수산화마그네슘의 금속화합물로 이루어진 불순물 함량은 0.05중량% 이하인 것을 특징으로 하는 난연제용 분산성이 우수한 수산화마그네슘의 제조방법.Washing and then drying and pulverizing the magnesium hydroxide; the purity of the pulverized magnesium hydroxide is 98% or more, and the impurity content of the pulverized magnesium hydroxide metal compound is 0.05% by weight or less. Method for producing magnesium hydroxide excellent in dispersibility for flame retardants. 제 1항에 있어서, 상기 해수로부터 제조된 마그네시아는 MgO 함량이 95중량% 이상인 것을 특징으로 하는 난연제용 분산성이 우수한 수산화마그네슘의 제조방법.The method of claim 1, wherein the magnesia prepared from seawater has a MgO content of 95% by weight or more. 제 1항에 있어서, 상기 분쇄된 수산화마그네슘은 평균 입도가 0.8~3.0㎛ 이고, 비표면적이 4~10㎡/g 이하이며, 결정상이 육각판상인 것을 특징으로 하는 난연제용 분산성이 우수한 수산화마그네슘의 제조방법.According to claim 1, wherein the magnesium hydroxide has a mean particle size of 0.8 ~ 3.0㎛, specific surface area of 4 ~ 10㎡ / g or less, the crystal phase is hexagonal plate-like magnesium hydroxide excellent dispersibility for flame retardant Manufacturing method.
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KR20180053963A (en) 2016-11-14 2018-05-24 (주)로송 Preparation process of incombustible magnesium hydroxide from bitterns

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US5461101A (en) 1992-04-23 1995-10-24 Defped Limited Particulate magnesium hydroxide
KR100415827B1 (en) 2001-05-21 2004-01-24 주식회사 액티마그 Manufacturing method for high concentration slurry of magnesium hydroxide
KR100467802B1 (en) 2001-12-24 2005-01-24 주식회사 포스렉 Slurry comprising magnesium hydroxide produced from seawater with high concentration
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US5461101A (en) 1992-04-23 1995-10-24 Defped Limited Particulate magnesium hydroxide
KR100415827B1 (en) 2001-05-21 2004-01-24 주식회사 액티마그 Manufacturing method for high concentration slurry of magnesium hydroxide
KR100467802B1 (en) 2001-12-24 2005-01-24 주식회사 포스렉 Slurry comprising magnesium hydroxide produced from seawater with high concentration
KR20060112624A (en) * 2005-04-25 2006-11-01 주식회사 포스렉 A method for manufacturing high purity magnesium hydroxide having excellent dispersibility

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20180053963A (en) 2016-11-14 2018-05-24 (주)로송 Preparation process of incombustible magnesium hydroxide from bitterns

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