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A process for the preparation of alkylation catalyst from natural kaolinitic clay

机译:由天然高岭土制备烷基化催化剂的方法

摘要

A process for the preparation of alkylation catalyst fromnatural kaolinitic clay which comprises purifying the run-off mine clay for separating the coarse minerals by sedimentation followed by wet sieving, drying the bulk clay fraction of size 45µ at a temperature in trie range of 90- 110°C for a period of 10 to 20 hours, calcining the resultant clay at a temperature in the range of 300-600°C for 5-10 h. grinding the calcined clay by known methods, activating the calcined clay by treating with 0:1-6 M mineral acid for 0.25-8 h, filtering the slurry and washing the resultant product repeatedly with water till free from chloride ions, drying the residue obtained at a temperature of 90-110°C for 10-20 h, grinding the resullnat acid treated clay, calcining the treated clay obtained at a temperature in the range of 300- 600°C for 3-6 h and then cooling to room temperature, incorporating at least one active element selected from the metals of group V-VIII in the form of their compound as herein described to the acid treated clay and drying the product at 100-150"C for 10-20 h to obtain alkylation catalyst.
机译:一种由天然高岭土制备烷基化催化剂的方法,该方法包括纯化径流式矿山粘土,以便通过沉降分离粗矿物,然后进行湿筛,在90-300℃的温度下干燥尺寸小于45µ的块状粘土级分在110℃下持续10至20小时,在300-600℃的温度下煅烧所得粘土5-10小时。通过已知方法研磨煅烧的粘土,通过用0:1-6 M的无机酸处理0.25-8 h活化煅烧的粘土,过滤浆液,并反复用水洗涤所得产物直至无氯离子,干燥所得残余物在90-110℃的温度下10-20小时,研磨经去甲萘二酸处理的粘土,在300-600℃的温度范围内煅烧所得的处理的粘土3-6小时,然后冷却至室温将至少一种选自本文所述的化合物形式的选自V-VIII族金属的活性元素引入到酸处理过的粘土中,并在100-150℃下干燥产物10-20h以获得烷基化催化剂。

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