Method for producing G-level high oil-resistant well cement clinker and cement clinker produced by method
An oil well cement and high-resistance technology, applied in the field of cement clinker, can solve problems such as environmental safety hazards, secondary pollution, and affecting the actual effect of comprehensive environmental management, so as to reduce urban pollution, increase mill production, and reduce manual labor. The effect of intensity
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Embodiment 1
[0014] Example 1: Take 5 parts by weight of iron powder, 80 parts by weight of marble, 7 parts by weight of quartz stone, and 7 parts by weight of pottery clay, add water and grind to produce a slurry, the particle size of the slurry is controlled at ≦3 microns, accounting for 6.5%-10%, 3-30 micron accounts for 66%-62.5%, 30-100 micron accounts for 25%-20%, and >100 micron accounts for 8.5%-7.5%. Add 1 part by weight of urban sludge to the slurry, and control the particle size below 100 microns. The above-mentioned slurry added with municipal sludge is input into a rotary kiln for calcination. Rotary kiln control parameters: calcination temperature 1400°C, kiln system negative pressure at 200pa, kiln tail temperature at 175°C, kiln speed at 1.2 rpm, clinker vertical weight at 1450g / l. The clinker produced after calcination is cooled by a single cylinder cooler and then transported to the closed-circuit cement mill for grinding. The ground cement is sorted by a high-efficienc...
Embodiment 2
[0015] Example 2: Take 4 parts by weight of iron powder, 78 parts by weight of marble, 8 parts by weight of quartz stone, and 7 parts by weight of pottery clay, add water to grind the slurry, the particle size of the slurry is controlled below 100 microns, add 1-3 parts by weight of urban sludge, the particle size is controlled below 100 microns. The above-mentioned slurry added with municipal sludge is input into a rotary kiln for calcination. Rotary kiln control parameters: calcination temperature 1350°C, kiln system negative pressure at 250pa, kiln tail temperature at 185°C, kiln speed at 1.2 rpm, clinker vertical weight at 1450g / l. The clinker produced after calcination is cooled by a single cylinder cooler and then transported to a closed-circuit cement mill for grinding. After the ground cement is selected by a high-efficiency classifier, the fine powder is packed as a qualified product.
Embodiment 3
[0016] Example 3: Take 6 parts by weight of iron powder, 82 parts by weight of marble, 9 parts by weight of quartz stone, and 7 parts by weight of pottery clay, add water and grind to produce a slurry, the particle size of the slurry is controlled at ≦3 microns, accounting for 6.5%-10%, 3-30 micron accounts for 66%-62.5%, 30-100 micron accounts for 25%-20%, and >100 micron accounts for 8.5%-7.5%. Add 2 parts by weight of urban sludge to the slurry, and control the particle size to 30-60 microns. The above-mentioned slurry added with municipal sludge is input into a rotary kiln for calcination. Rotary kiln control parameters: calcination temperature 1450°C, kiln system negative pressure at 220pa, kiln tail temperature at 180°C, kiln speed at 1.5 rpm, clinker vertical weight at 1450g / l. The clinker produced after calcination is cooled by a single cylinder cooler and then transported to a closed-circuit cement mill for grinding, and then packed by a high-efficiency separator. ...
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