Proppant, proppant production method and use of proppant
The invention relates to the area of oil and gas production (especially, to the production in which the propping technique is used for the stimulation of a well) and can be used in the development of a composition and a method of production of propping agents (proppant), as well as a method of application of these propping agents. A new type of proppant, proppant production method and use of the proppant are based on allowing the production of proppant having an apparent density of 2.5 to 4.0 g/cm 3 , as well as a high mechanical strength and a high chemical durability. A proppant contains granules made of the sintered feedstock, wherein the charge mixture containing at least one of the following materials—silicon carbide, boron carbide, titanium carbide, silicon nitride, titanium nitride, boron nitride, silicon oxynitrides, SIALON-type compounds, was used as the feedstock.
1. A proppant comprising
granules made of sintered feedstock, wherein a charge mixture containing
40 - 95 wt % of bauxites; and
at least one of the following materials: silicon carbide, titanium carbide, silicon nitride, titanium nitride, silicon oxynitrides, and SIALON-type compounds, comprises the feedstock,
wherein the charge mixture contains less than 10 wt % of alumina.
2. The proppant of claim 1 wherein the charge mixture additionally contains at least one of the following materials: natural unfired aluminum hydrates, nepheline syenites, clays, kaolines, pyrophyllites, disthene-sillimanite concentrates, andalusite, sillimanite, kyanite, feldspars, pegmatites, pearlite, vermiculite and clay shales; commercial alumina consisting of a mixture of transitional metastable forms of aluminum oxide and corundum oxide; blast-furnace slags; tailings and wastes from the nonferrous metals industry; bauxite slurry; kaoline cleaning rejects; scrap and wastes resulting from stone and ceramics sawing and processing; dioxides of silicone, magnesium, calcium, zinc, titanium, zirconium, iron, zinc, manganese and stannum, as well as zirconium silicate.
3. The proppant of claim 1 further comprising an organic temporary process binder.
4. The proppant of claim 3 wherein the organic temporary process binders are burnt out in a preliminary firing stage.
5. The proppant of claim 1 wherein the granules are dried and sized, and fired at temperatures and within exposure periods required for the achievement of an apparent density of below about 4 g/cm 3 .
6. The proppant of claim 1 wherein the granules which fail to meet the size requirements are recycled.
7. The proppant of claim 1 which has a collapsing stress up to 20,000 psi.
8. A method for producing proppant comprising:
a) preliminary crushing and mixing of initial components; and,
b) subsequent granulation, drying and screening of the initial components into target fractions;
wherein a mixture containing
40-95 wt % of bauxites and
at least one of the following materials, silicon carbide, titanium carbide, silicon nitride, titanium nitride, silicon oxynitrides, SIALON-type compounds, comprises the initial components,
wherein the charge mixture contains less than 10 wt % of alumina.
9. A method of claim 8 wherein the initial components are admixed with at least one of natural unfired aluminum hydrates, nepheline syenites, clays, kaolines, pyrophyllites, disthene-sillimanite concentrates, andalusite, sillimanite, kyanite, feldspars, pegmatites, pearlite, vermiculite and clay shales; commercial alumina consisting of a mixture of transitional metastable forms of aluminum oxide and corundum oxide; blast-furnace slags; tailings and wastes from the nonferrous metals industry; bauxite slurry; kaoline cleaning rejects; scrap and wastes resulting from stone and ceramics sawing and processing; dioxides of silicone, magnesium, calcium, zinc, titanium, zirconium, iron, zinc, manganese and stannum, and zirconium silicate.
10. The method of claim 8 wherein the initial components comprise an organic temporary process binder.
11. The method of claim 10 wherein the organic temporary process binders are burnt out in a preliminary firing stage.
12. The method of claim 8 wherein the proppant comprises granules which are dried and sized, and fired at temperatures and within exposure periods required for the achievement of an apparent density of below about 4 g/cm 3 .
13. The method of claim 8 wherein the proppant comprises granules, and wherein granules which fail to meet the size requirements are recycled.
14. The method of claim 8 wherein the proppant has collapsing stresses up to 20,000 psi.
15. The method of claim 8 wherein granules are dried and screened to a size allowing compensation of shrinkage resulting from the firing process.