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TECHNICAL TOOL

Explore the effect of over-dilution.

Configure a production and blending scenario. Results are indicative and require validation with operating data.

Illustrative scenarios:

Field operating parameters

28,000 bbl/d
3,000 20,000 40,000 60,000 bbl/d
8.5 °API
7.0° 16.0° 28.0° 35.0° API
16.0 °API
8.0° 16.0° 30.0° 40.0° API
1.4 °API
0.2° (Low) 1.0° (Typical) 2.0° 3.0° API (Severe)
$74 / bbl
$50 $65 $80 $100 / bbl

Estimated technical and financial savings

Estimated monthly savings: — Direct OPEX reduction in naphtha purchases
Estimated annual savings: — Cumulative impact over 12 months of operation
— Diluent saved per day: Estimated volume of diluent avoided
— Estimated diluent reduction: Share of the total blend flow rate

Indicative estimate: assumes ideal volumetric blending and 47° API diluent. It excludes service costs and does not replace laboratory testing.

How to interpret the estimate

The result compares diluent consumption in the current blend with consumption at the configured target.

ASSUMPTIONS

Simplified balance

The calculation uses specific gravity, ideal volumetric blending and a 47° API diluent. The entered flow rate represents the total diluted crude oil volume.

PROJECTION

Constant scenario

Monthly savings assume 30 days and annual savings 365 days at the same flow rate and cost. Service costs and operational changes are excluded.

NEXT STEP

Technical validation

Blend selection requires laboratory testing, transport conditions and the project's commercial specifications.

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