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I always felt sorry for the real refinery mogas blenders. Lots of components, crappy price forecasts, pressure to hit octane with nil giveaway etc, etc. And by the way, never run out or have tanks too full.
Prior to my current job (Process Engineering Team Leader over North Sea projects), I was doing blending and scheduling in a refinery in Montana. I have done a few hundred gasoline blends over the past few years.
You are correct that octane giveaway is a constant concern, and units are tweaked to balance everything. But the vast majority of the difference in summer and winter blends boils down to butane.
You should post here more often. We need more people who understand the energy industry and are willing to share that knowledge. Of course you may get the occasional "Big Oils sucks, and so do you", but most people here will engage and are seriously interested in learning new things.
thanks
I worked in a Process Design shop for 6-8 years on FCCs, visbreakers, H2 plants, hydrocrackers/treaters, some upstream processing (nat gas treating) etc. Had lunch every day with the Shale oil folks, the reformer experts, the crude unit designers and had a little rub off as can be expected. When the fun stopped in the mid 80's I found a way to get into the S&D end of things and ended up trading for a large bank's oil group. That didn't take long to get old.
I wander here from time to time. Comment when I think I have something useful to add. I don't worry much about negative feedback of the "big oil sucks" variety. What I do sometimes find offputting is the "we'e all going to die" pessimism. The problem is large but I can't accept the Kunstler collapse model.