|
Topics covered are as follows:
Goals of the
Gasoline Blender:
On Time, On Spec
False Blending
Values:
They don't work when composition changes
Maximizing Your
Octane:
Use your positive
interactions
Interaction
Blending:
Interactions can be predicted from component types and octane
level
Two Other
Approaches:
Critique of "RT-70" and
"Transformation Method"
BLENOC For
Octane:
Interactions from component type & octane level
Octane
Demonstration Program:
Download it - see how it works
Applying Interaction
Equations:
Use blending values or interaction coefficients
Doing Your Own
Blending Study:
Consider the long term cost
BLENDIS for ASTM
Distillation:
Includes pure hydrocarbons and oxygenates
BLENRVP for Reid
Vapor Pressure:
Takes hydrocarbon composition into account
Data Input and
Component Types:
We cover the Waterfront
Prices of BLENOC,
BLENDIS and BLENRVP:
No "Sticker Shock " here
Evaluating BLENOC,
BLENDIS & BLENRVP:
A free service
Typical Component Data:
Useful for evaluating components you don't have
Handling
Mixtures:
Optimize with combined tankage - evaluate alternative combinations
Comparing Two
"Optimums":
If you really want to
Predicting End
Point:
Interaction can't do everything
ASTM
Distillation Loss:
Pentane prevents it
Blends of Pure
Hydrocarbons:
Huge octane interactions
Octanes Above 100:
How to measure without TEL
Interaction for
Diesel Fuel:
Predict blend distillation
Testing Diesel
in Octane Engines:
Low octane means high cetane
Potpourri:
There must be a pony in here somewhere
References:
Publications by
William E. Morris:
Appendix:
| 
