Method for extracting magnesium oxide and preparing active porous silicon dioxide material by using serpentine
A technology of porous silicon dioxide and silicon dioxide, applied in the direction of silicon dioxide, silicon oxide, magnesium sulfate, etc., can solve the problems of low operation and calcination temperature, small reaction temperature range, high particle size requirements of raw materials, etc., and achieve leaching time The effect of shortening, short roasting time and uniform distribution
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example 1
[0033] This example chooses serpentine as raw material.
[0034] 1) Crushing, grinding, and magnetically separating the serpentine raw materials to process them into serpentine powder. The particle size is 60 mesh, and the mass percentage of MgO is 45%. The pretreatment includes conventional crushing, grinding and magnetic separation processes.
[0035] 2) Calculate the mass ratio of the serpentine mineral powder obtained in step 1) based on the molar ratio of MgO and ammonium bisulfite being 1:5, weigh the material and mix and stir evenly; after roasting at 800°C for 0.2h, the obtained Roasting products and tail gas; Among them, sulfur trioxide, sulfur dioxide or ammonia in the tail gas are collected by conventional sulfuric acid solution absorption method.
[0036] 3) post-treatment the roasted product obtained in step 2); wherein the post-treatment includes leaching, filtering and washing steps; Mix in a device with a stirrer to extract the sulfate in the roasted product; a...
example 2
[0040] This implementation example selects serpentine tailings as raw material; its preparation method is basically the same as Example 1, and will not be repeated here; its difference is:
[0041] 1) crushing, grinding, and magnetically separating the serpentine tailings to obtain serpentine powder, the particle size of which is 600 mesh, and the mass percentage of MgO in the serpentine powder is 30%;
[0042] 2) Calculate the mass ratio of the serpentine ore powder obtained in step 1) according to the molar ratio of MgO and ammonium bisulfate as 1:0.5, weigh the material and mix and stir evenly; put it into a temperature-controlled reaction with an exhaust gas collection device In the device, the reaction was roasted at 110° C. for 4 hours; the gas generated during the reaction was collected by conventional sulfuric acid solution absorption method.
[0043] 3) post-processing the roasted product obtained in step 2); wherein the post-treatment includes leaching, filtering and...
example 3
[0047] This example chooses chrysotile tailings as raw material. Its preparation method is basically the same as Example 1, and will not repeat them here; its difference is:
[0048] 1) Crushing, grinding, and magnetically separating the chrysotile tailings to obtain chrysotile tailings ore powder, the particle size of which is 200 mesh, and the mass percentage of MgO is 35%;
[0049] 2) Calculate the mass ratio of the chrysotile tailings powder obtained in step 1) according to the molar ratio of MgO and sodium bisulfate as 1:3.0, weigh the material and mix and stir evenly; put it into a temperature control system with a tail gas collection device In the reaction device, the reaction was roasted at 380° C. for 2 hours; the tail gas generated during the reaction was collected by conventional sulfuric acid solution absorption method.
[0050] 3) post-treatment the roasted product obtained in step 2); wherein the post-treatment includes leaching, filtering and washing steps; Mi...
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