I’m thinking it can be done with a shell and tube, FFE style, ideally by applying pressure to the head space of the feed vessel to push the crude through the heat exchanger.
What about a reboiler option for large batches? scavange the residual etoh and terps at the same time? mabey a longer thinner heat exchanger like a pasturizer?
Other than changing the outlet on the output to the bottom of the tank, I don’t see why this wouldn’t work.
If you stack it into a vertical arrangement you might even be able to get a siphon effect from the first crude tank and not have to push it. Might be too viscous to flow nicely though. Depends on the input temperature/composition.
Because a gear pump and heat exchanger with liquid-vapor separator would be much faster . . .
But your suggestion definitely works, and it’s what I’ve done as well as seen others do consistently.
Probably 3-5L an hour decarbed. I have 2 50 L triple jacketed reactors/ rotary evap. How would you best reccomend I decarb 20L at a time in these anyone? Thanks!
When you say inner jacket… Why would you use that jacket? Internal coil I understand. Vacuum on the outer jacket, hot middle jacket and cold inner jacket immediately next to it?
Are you considering the inner vessel and “insulated fluid line” and inner jacket? That’s not a jacket lol. That is the vessel itself. I’m not sure why they call it triple jacketed. Triple walled? That makes sense but that’s not what they called it haha.