TECHNOLOGY
TECHNOLOGY FOR SULPHUR REDUCTION IN MARINE FUEL TO 0.5%
TR EATMENT FACILITIES
- Maximum return of up to 100% of purified water to production
- Modern solutions for demineralization and selective removal of heavy metals
- Achievement of MPC standards for fish farm without additional treatment unit
TREATMENT FACILITIES
- Closed waste water treatment cycle with zero discharge
- The placement area is 4-6 times lower than that of analogues.
- YDRO-EJECTOR VACUUM SYSTEM
- Implemented by: LLC “Mari Oil Refinery” (Republic of Mari El)
HYDROGEN SULFIDE REMOVAL FROM OIL
- Highly efficient cleaning in one step
- Hydrogen sulfide removal from oil – 99%
- Oil extraction from oil potential – 99%
HEAVY SUPER-VISCOUS OIL REFINING TECHNOLOGY
- Possibility of implementation in block execution
- Raw materials for a typical refinery
- Highly efficient low cost technology
- HYDRO-EJECTOR VACUUM SYSTEM
HEAVY SUPER-VISCOUS OIL REFINING TECHNOLOgy
- Highly efficient low cost technology
- Possibility of implementation in block execution
- Raw materials for a typical refinery
ELOU AT-3
- Flexible scheme for processing different types of oil
- Production of liquefied gases of various brands
- Gasoline stabilization
- Environmental impact is 20% lower
DIESEL FUEL HYDROTREATER
SYNTHETIC OIL AND COKE PRODUCTION FOR ALUMINUM PRODUCTION
Raw materials VVN
density – 941 kg / m3
sulfur content – 0.7%
viscosity at 20 ° С – 1550 cSt
Synthetic oil
density – 907 kg / m3
viscosity at 20 ° С – 42 cSt
sulfur – 0.3%
vanadium – 2 ppm
nickel – 1 ppm
Petroleum coke
volatiles yield – 9%
sulfur – 0.8%
vanadium – 120 ppm
nickel – 70 ppm
OBTAINING RAW MATERIALS FOR HYDROCRACKING AND ROAD BITUMEN
Raw materials VVN
density – 969 kg / m3
sulfur – 4.1%
viscosity at 20 ° С – 2140 cSt
Synthetic oil
density – 907 kg / m3
viscosity at 20 ° С – 42 cSt
sulfur – 0.3%
vanadium – 2 ppm
nickel – 1 ppm
Petroleum coke
volatiles yield – 9%
sulfur – 0.8%
vanadium – 120 ppm
nickel – 70 ppm
TECHNOLOGICAL SCHEME OF OIL SLUDGE PROCESSING TO OBTAIN BITUMEN RAW MATERIALS
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SYNTHETIC OIL PRODUCTION
Raw materials BBN
density – 969 kg / m3
sulfur content – 4.1%
viscosity at 20 ° С – 2140 cSt
Synthetic oil
density – 943 kg / m3
sulfur content – 3.7%
viscosity at 20 ° С – 88 cSt
TECHNOLOGY FOR SULPHUR REDUCTION IN MARINE FUEL TO 0.5%
TR EATMENT FACILITIES
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TREATMENT FACILITIES
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YDRO-EJECTOR VACUUM SYSTEM
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HYDROGEN SULFIDE REMOVAL FROM OIL
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HEAVY SUPER-VISCOUS OIL REFINING TECHNOLOGY
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HYDRO-EJECTOR VACUUM SYSTEM
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HEAVY SUPER-VISCOUS OIL REFINING TECHNOLOgy
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ELOU AT-3
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DIESEL FUEL HYDROTREATE
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SYNTHETIC OIL AND COKE PRODUCTION FOR ALUMINUM PRODUCTION
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OBTAINING RAW MATERIALS FOR HYDROCRACKING AND ROAD BITUMEN
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TECHNOLOGICAL SCHEME OF OIL SLUDGE PROCESSING TO OBTAIN BITUMEN RAW MATERIALS
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SYNTHETIC OIL PRODUCTION
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