All Issue

2009 Vol.46, Issue 6 Preview Page
31 December 2009. pp. 736-743
Abstract
A process to produce ultra white aluminium trihydroxide from a commercial grade aluminium trihydroxide produced by KC Corporation Ltd was developed. First of all, supersaturated sodium aluminate solution of A/C (Alumina/Caustic ratio, g/L) concentration 0.55~0.75 was produced by redissolving a commercial grade aluminium trihydroxide in sodium hydroxide solution (dissolution temperature 100~160℃, NaOH 180~220 g/L). Dissolved organics which influence the whiteness of aluminium trihydroxide was removed (more than 70% by precipitation) by adding calcium hydroxide (at 5 g/L), to the supersaturated slurry and stirring at 80°C for 30 minutes. The filtered sodium aluminate solution was then maintained at A/C 0.60~0.69, reaction temperature 52℃~88℃, reaction time 24~72 hours, for precipitation of the product to occur. Seeding using particles with an average size of 45 ㎛ was maintained at 5~40 g/L to facilitate the precipitation process. Ultra white aluminium trihydroxide was produced containing Al2O3 > 99.7%, Na2O < 0.20%, Fe2O3 < 0.010%, SiO2 < 0.01%, CaO < 0.01%, Whiteness > 97. The product produced from this process has a mean particle size within the range 65~85 ㎛ and is of radial or mosaic structure.
Bayer 공정에서 생산되는 일반 수산화알루미늄을 이용하여 고백색의 수산화알루미늄을 제조하고자 하였다. 수산화알루미늄을 용해 온도 100~160℃, 가성소다 용액 180~220 g/l의 조건에서 재용해하여 A/C비(Alumina/Caustic ratio) 0.55~0.75로 과포화된 소듐알루미네이트용액을 제조하였다. 이때 수산화알루미늄에 함유되어 있던 유기물이 소듐알루미네이트 용액중에 함유됨으로 이를 제거하기 위하여 소석회의 농도 5 g/l, 반응온도 80℃, 반응시간 30 min의 조건에서 반응시킨후 GF/C 필터로 여과하여 유기물의 70%이상을 제거할 수 있었다. 정제된 소듐알루미네이트 용액을 이용하여 A/C비 0.60~0.69, 반응온도 52℃~88℃, 반응시간 24~72시간, 종자 5~40 g/ℓ, 종자입도 45 ㎛의 조건에서 석출시킨 결과 Al2O3 99.7% 이상, Na2O 0.20% 이하, Fe2O3 0.010% 이하, SiO2 0.01% 이하, CaO 0.01% 이하의 화학적 특성을 가지며, 백색도 97이상, 평균입도 65 내지 85 ㎛의 레디얼(Radial) 및 모자이크 구조(Mosaic)를 가진 고백색도의 수산화알루미늄을 제조할 수 있었다.
References
  1. Brown, N., 1975, A Quantitative Study of New Crystal Formation in Seeded Caustic Aluminate Solution, J. of Crystal Growth, Vol. 29, pp. 309-315.
  2. Habashi, F., 1998, A Hundred Years of Bayer Process for Alumina Production, Light Metals, pp. 3-11.
  3. Keil, R.H., 1976, A New Method of Separating Sodium Carbonate from Bayer Liquors, 105th Annual Meeting of AIME, Las Vegas.
  4. Kim, M.J and Lee, S.O., 2003, Overview of the Behavior of Sodium Oxalate in Bayer Liquor and its Effect of the Process, Light Metals, pp. 19-24.
  5. Lee, S.O., Kim, M.J. Shin, B.S. and Tran, T., 2000, Kinetics of Crystal Growth of Radial Aluminium Tri-hydroxide, J. of MMI of Japan, Vol. 116, pp. 187-192.
  6. Misra, C. and White, R.T., 1971, Kinetics of Crystallization of Aluminum Tri-hydroxide from Seeded Caustic Aluminate Solutions, Chemical Engineering Program Symposium, Vol. 67, No. 109, pp. 53-65.
  7. Misra, C., 1970, Solubility of Alumina Trihydrate in Sodium Hydroxide Solution, Chemistry and Industry, Vol. 9, pp. 619-623.
  8. Ohkawa, J., Tsuneizumi, T. and Hirao, T., 1985, Technology of Controlling Soda Pick-up in Alumina Tri-hydroxide Precipitation, Light Metal, pp. 345-366.
  9. Rijkeboer, A. and Arnhem, AT., 1994, Bauxite Processing, US Patent No. 5279645.
  10. Shibue, Y., Sakamoto, A., Arakawa, N., Kawai, Y. and Ishida, H., 1990, Liquor Burning Process-It’s Modification and Increase in Capacity, Light Metal, pp. 35-40.
  11. White, E.T. and Bateman, S.H., 1988, Effect of Caustic Concentration on the Growth Rate of Al(OH)3 Particles, Light metal, pp. 157-162.
  12. Yamada, Y. and Shibue, Y., 1981, Method for Treatment of Bayer Liquor, US Patent No. 4,280,987.
Information
  • Publisher :The Korean Society of Mineral and Energy Resources Engineers
  • Publisher(Ko) :한국자원공학회
  • Journal Title :Journal of the Korean Society for Geosystem Engineering
  • Journal Title(Ko) :한국지구시스템공학회지
  • Volume : 46
  • No :6
  • Pages :736-743