| 1 |
Use techno-economic benchmark to review supply-chain models - Value profile of crude and high vacuum unit fractions is the key for crude selection and, thus, refinery profitability
Hartmann JCM
Hydrocarbon Processing, 84(10), 63, 2005 |
| 2 |
Case history: Revisit fundamentals for blending rules - Refiners use models to optimize operations, but are these models totally accurate?
Hartmann JCM
Hydrocarbon Processing, 83(3), 71, 2004 |
| 3 |
Judging model validity
Hartmann JCM
Hydrocarbon Processing, 81(2), 13, 2002 |
| 4 |
Planning models for joint venture refineries function as a contract
Hartmann JCM
Hydrocarbon Processing, 81(8), 13, 2002 |
| 5 |
Why is it so difficult to combine experience and theory in business decisions?
Hartmann JCM
Hydrocarbon Processing, 81(11), 81, 2002 |
| 6 |
Determine the optimum crude intake level - a case history
Hartmann JCM
Hydrocarbon Processing, 80(6), 77, 2001 |
| 7 |
Balance hydrogen consumption
Hartmann JCM
Hydrocarbon Processing, 80(12), 45, 2001 |
| 8 |
Interpreting LP outputs
Hartmann JCM
Hydrocarbon Processing, 78(2), 64, 1999 |
| 9 |
Is your refinery model balanced?
Hartmann JCM
Hydrocarbon Processing, 78(11), 73, 1999 |
| 10 |
Distinguish between scheduling and planning models
Hartmann JCM
Hydrocarbon Processing, 77(7), 93, 1998 |
