摘要:
Porous substrates containing seeds of hydrous crystalline alumina are contacted with an aqueous solution of alkaline aluminate, thereby causing additional crystalline hydrous alumina to grow on the seeds within the pores of the substrate.
摘要:
Aluminum hydroxide aggregated particles which have an average particle diameter of not less than 40 μm, an average particle diameter as determined after pressing at 1,000 kg/cm2 of not more than 35 μm, and an L value of slurry obtained by mixing 20 ml of glycerol and 10 g of the aluminum hydroxide aggregated particles of not more than 69, are obtained by a process comprising the steps of: (a) feeding a supersaturated aqueous sodium aluminate solution to a vessel, (b) adding aluminum hydroxide seeds to the supersaturated aqueous sodium aluminate solution, (c) stirring the seed-added solution in the vessel while continuously feeding an additional supersaturated aqueous sodium aluminate solution into the vessel to hydrolyze the supersaturated aqueous sodium aluminate solution, (d) separating the aluminum hydroxide aggregated particles from the aqueous sodium aluminate solution, and (e) continuously discharging the aqueous sodium aluminate solution out of the vessel.
摘要翻译:平均粒径为40μm以上的氢氧化铝凝集粒子,1000kg / cm 2以上压制后的平均粒径为35μm以下,通过混合20ml甘油获得的浆液的L值 和10g不超过69的氢氧化铝凝集颗粒,通过包括以下步骤的方法获得:(a)将过饱和的铝酸钠水溶液进料到容器中,(b)将氢氧化铝种子加入到过饱和水溶液 铝酸钠溶液,(c)在容器中搅拌添加种子的溶液,同时连续向容器中加入过饱和的铝酸钠水溶液以水解过饱和的铝酸钠水溶液,(d)将氢氧化铝凝集颗粒与水溶液 铝酸钠溶液,和(e)将铝酸钠水溶液连续排出容器。
摘要:
Aluminum hydroxide aggregated particles which have an average particle diameter of not less than 40 μm, an average particle diameter as determined after pressing at 1,000 kg/cm2 of not more than 35 μm, and an L value of slurry obtained by mixing 20 ml of glycerol and 10 g of the aluminum hydroxide aggregated particles of not more than 69, are obtained by a process comprising the steps of: (a) feeding a supersaturated aqueous sodium aluminate solution to a vessel, (b) adding aluminum hydroxide seed to the supersaturated aqueous sodium aluminate solution, (c) stirring the seed-added solution n the vessel while continuously feeding an additional supersaturated aqueous sodium aluminate solution into the vessel to hydrolyze the supersaturated aqueous sodium aluminate solution, (d) separating the aluminum hydroxide aggregated particles from the aqueous sodium aluminate solution, and (e) continuously discharging the aqueous sodium aluminate solution out of the vessel.
摘要翻译:平均粒径为40μm以上的氢氧化铝凝集粒子,1000kg / cm 2以上压制后的平均粒径为35μm以下,L值为 通过包括以下步骤的方法获得通过混合20ml甘油和10g不大于69的氢氧化铝凝集颗粒获得的浆料:(a)将过饱和的铝酸钠水溶液进料到容器中,(b) 将氢氧化铝种子加入到过饱和的铝酸钠水溶液中,(c)在容器中搅拌加入种子的溶液,同时连续地向容器中加入过饱和的铝酸钠水溶液以水解过饱和的铝酸钠水溶液,(d)分离 来自铝酸钠水溶液的氢氧化铝凝集颗粒,和(e)将铝酸钠水溶液连续排出容器。
摘要:
A method for the recovery and recycling of sodium hydroxide from the waste solution of aluminum etching operations. The method utilizes a dialysis membrane column or stack to initially remove sodium hydroxide from the waste solution and return it to the etch tank base solution sufficiently concentrated to carry on the basic etching operation. The method permits the recovery of salable quantities of aluminum hydroxide.
摘要:
Method for processing bauxite, including grinding the bauxite and extracting iron; separating the resulting pulp into a solid phase and a liquid phase; extracting aluminium from the liquid phase at a pH of about 7 to 8 to form a precipitate of sodium hydrogen carboaluminate; separating the precipitate of sodium hydrogen carboaluminate from the neutralized pulp; extracting iron from the neutralized liquid phase at a pH of at least about 12 using to form a precipitate of iron hydroxide; separating the precipitate of iron hydroxide from the basic pulp to form an iron ore concentrate and a mother liquor chelate; concentrating the mother liquor chelate using evaporation; cooling the concentrated solution; carbonizing the cooled solution with gaseous carbon dioxide under pressure to crystallize sodium hydrogen carbonate; and separating the crystallized sodium hydrogen carbonate from the carbonized solution to form a chelate liquid phase and a sodium hydrogen carbonate solid phase.
摘要:
An improved process for producing alumina from bauxite is disclosed comprising the steps of: a) wet grinding of the bauxite in the presence of an agent capable of reducing the viscosity of the semiliquid paste obtained; b) caustic etching of the bauxite ground in step a) with a concentrated solution of sodium hydroxide until a liquid phase is obtained comprising aluminium hydroxide and a solid phase; c) removal of the solid phase formed in step b) from the liquid phase; d) precipitation of the aluminium hydroxide from the liquid phase of step c); e) filtration of the aluminium hydroxide precipitated in step d); and f) calcination of the aluminium hydroxide of step e).
摘要:
Aluminum hydroxide aggregated particles which have an average particle diameter of not less than 40 μm, an average particle diameter as determined after pressing at 1,000 kg/cm2 of not more than 35 μm, and an L value of slurry obtained by mixing 20 ml of glycerol and 10 g of the aluminum hydroxide aggregated particles of not more than 69, are obtained by a process comprising the steps of: (a) feeding a supersaturated aqueous sodium aluminate solution to a vessel, (b) adding aluminum hydroxide seeds to the supersaturated aqueous sodium aluminate solution, (c) stirring the seed-added solution in the vessel while continuously feeding an additional supersaturated aqueous sodium aluminate solution into the vessel to hydrolyze the supersaturated aqueous sodium aluminate solution, (d) separating the aluminum hydroxide aggregated particles from the aqueous sodium aluminate solution, and (e) continuously discharging the aqueous sodium aluminate solution out of the vessel.
摘要翻译:平均粒径为40μm以上的氢氧化铝凝集粒子,1000kg / cm 2以上压制后测定的平均粒径为35μm以下,通过将20ml甘油 和10g不超过69的氢氧化铝凝集颗粒,通过包括以下步骤的方法获得:(a)将过饱和的铝酸钠水溶液进料到容器中,(b)将氢氧化铝种子加入到过饱和水溶液 铝酸钠溶液,(c)在容器中搅拌添加种子的溶液,同时连续向容器中加入过饱和的铝酸钠水溶液以水解过饱和的铝酸钠水溶液,(d)将氢氧化铝凝集颗粒与水溶液 铝酸钠溶液,和(e)将铝酸钠水溶液连续排出容器。
摘要:
Silane and/or organic titanate and/or organic zirconate coated, mill-dried ATH particles, methods of making them, their use in flame retarded polymer formulations, and molded or extruded articles made from the flame retarded polymer formulations.