| 摘要 |
A process generates a middle distillate from hydrocarbonaceous energy sources. In the process, at least one hydrocarbonaceous energy source, if appropriate at least one catalyst and if appropriate at least one filler are fed as input materials to a reactor which contains a process oil mixture. The process oil mixed stream is removed from the reactor and heated to a process temperature between 150 degrees C. and 400 degrees C., preferably between 350 degrees C. and 380 degrees C. The heated process oil mixed stream is fed to a degasser. The vaporous middle distillate is separated in the degasser from the heated process oil mixed stream and a process oil mixed stream which is expanded from the vaporous middle distillate is recirculated from the degasser, to the process oil mixture which is present in the reactor. |
