Manufacture of intermediate strength proppant or lost circulation material from drill cuttings
US-9714377-B2 · Jul 25, 2017 · US
US10927622B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10927622-B2 |
| Application number | US-201515563604-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 24, 2015 |
| Priority date | Apr 24, 2015 |
| Publication date | Feb 23, 2021 |
| Grant date | Feb 23, 2021 |
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In some embodiments, a pre-treatment source generates pre-treated oilfield fluid from oilfield fluid, prior to injection into an inverting filter centrifuge system. The pre-treatment source increases an efficiency of separating solids from the injected oilfield fluid. An inverting filter centrifuge coupled to the pre-treatment source generates filtered oilfield fluid from the pre-treated oilfield fluid. Post-treatment may be applied to the filtered oilfield fluid. Additional apparatus, systems, and methods are disclosed.
Opening claim text (preview).
What is claimed is: 1. A system for removal of fine solids from oilfield fluids including drilling fluid and completion fluid returned from downhole, the system comprising: a solids pre-treatment to generate solids pre-treated fluid from the drilling fluid or both the drilling fluid and the completion fluid; a chemical pre-treatment to generate chemically pre-treated or reduced viscosity fluid from the solids pre-treated fluid or the drilling fluid; and an inverting filter centrifuge comprising a rotating drum and filter and coupled to the solids pre-treatment and the chemical pre-treatment, the inverting filter centrifuge to generate filtered oilfield fluid by removing fine solids from the chemically pre-treated or reduced viscosity fluid or the completion fluid, wherein the fine solids to be removed are less than approximately 10 microns. 2. The system of claim 1 , wherein the solids pre-treatment comprises a hydrocyclone, a centrifuge, a decanter centrifuge, elevated temperatures, or an inclined plate separator. 3. The system of claim 1 , wherein the chemical pre-treatment comprises a filter aid addition. 4. The system of claim 1 , wherein the solids pre-treatment is to increase an efficiency of separating the solids from the drilling fluid. 5. The system of claim 3 , wherein the filter aid addition comprises rice haul ash, diatomaceous earth, expanded amorphous aluminum silicates, calcium and magnesium silicates, cellulose fibers, modified organosilica, nanoporous organosilica, swellable nanoporous organosolica, non-crystalline solids, glass beads, perlite, zeolite, fly ash, and/or zeolites. 6. The system of claim 1 , wherein the chemical pre-treatment includes solvents, liquefied gases, oils, water, chemicals, such heavy brines, polyols, surfactants, coagulants, flocculants, and/or settling aids. 7. The system of claim 1 , further comprising sensors coupled to the inverting filter centrifuge to determine whether to perform pre-treatment of the drilling fluid or post-treatment of the filtered drilling fluid. 8. The system of claim 7 , wherein the sensors determine a type of pre-treatment of the drilling fluid or a type of post-treatment for the filtered drilling fluid. 9. The system of claim 7 , wherein the sensors include flowmeters, thermal conductivity sensors, near infrared (NIR) sensors, X-ray based sensors, optical-based sensors, electrochemical sensors, or electromagnetic sensors. 10. The system of claim 1 , further comprising a post-treatment to remove pre-treatment aids. 11. A method for removing fine solids from oilfield fluids including drilling fluid and completion fluid returned from downhole, the method comprising: pre-treating the drilling fluid or both the drilling fluid and; the completion fluid to generate solids pre-treated fluid; chemically pre-treating the solids pre-treated fluid or the drilling fluid to generate chemically pre-treated fluid; and filtering, through an inverting filter centrifuge, the chemically pre-treated fluid or the completion fluid to generate filtered oilfield fluid by removing fine solids, wherein the fine solids to be removed are less than approximately 10 microns. 12. The method of claim 11 , further comprising performing post-treatment of the filtered oilfield fluid to condition the filtered oilfield fluid. 13. The method of claim 11 , further comprising performing sensor measurements of the filtered oilfield fluid to determine whether to perform post-treatment of the filtered oilfield fluid. 14. The method of claim 11 , further comprising performing sensor measurements of the drilling fluid or the completion fluid to determine a type of pre-treating. 15. The method of claim 11 , further comprising performing post-treatment of the filtered oilfield fluid to remove pre-treatment aids. 16. The method of claim 11 , further comprising performing sensor measurements of the filtered oilfield fluid to determine a type of post-treatment.
Precoating the filter medium; Addition of filter aids to the liquid being filtered {(devices for feeding reagents C02F1/685 and sub-groups; filter aids)} · CPC title
by using a centrifuge · CPC title
Control equipment · CPC title
with further treatment of the solids, e.g. for disposal · CPC title
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