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Low temperature carbonization process for coal hydrogenation residues
| Details |
Inventors: Winckler, Lothar; Fuhrmann, Klaus; Graeser, Ulrich; Wenning, Peter;
Assignee: Veba Oel Entwicklungs-Gesellschaft mbH (Gelsenkirchen, DE)
Primary Examiner:
Assistant Examiner:
Attorney, Agent or Firm:
A method for low temperature carbonization of coal hydrogenation residues, wherein a coal hydrogenation residue is subjected to a reduced pressure distillation in a one-shaft or multishaft screw extruder, liberated gases and vapors are drawn off, and non-volatilized remaining material is subjected to low temperature carbonization in a screw extruder. |
|
DETAILED DESCRIPTION What is claimed as new and intended to be secured by Letters Patent is: 1.
A method for low temperature carbonization of coal hydrogenation residues, which comprises: subjecting a coal hydrogenation residue to reduced pressure distillation in a screw extruder comprising an evaporation zone and a low temperature carbonization zone, which zones are separated from each other by means of a mechanical compression stage, and having a liquid space at its entry, thereby producing gases and vapors and a non-volatilized remaining material; drawing off said gases and vapors; and subjecting said non-volatilized material to low temperature carbonization in said screw extruder.
2.
The method according to claim 1, wherein said distillation is carried out at pressures of from about 0.
01 to 0.
6 bar.
3.
The method according to claim 2, wherein said pressures are from about 0.
02 to 0.
1 bar.
4.
The method according to claim 2, wherein said pressure decreases over the length of an evaporation zone of said screw extruder beginning at a point of entry of said hydrogenation residue, with said pressure decrease being from about 0.
6 bar to about 0.
01 bar.
5.
The method according to claim 4, wherein said pressure decrease is from about 0.
1 to about 0.
02 bar.
6.
The method according to claim 1, wherein said distillation is carried out at temperatures of from about 20.
degree.
to 400.
degree.
C.
7.
The method according to claim 6 wherein said temeratures are from about 250.
degree.
to 350.
degree.
C.
8.
The method according to claim 6, wherein said temperature increases over the length of an evaporation zone of said screw extruder, beginning at a point of entry of said hydrogenation residue and extending to a point of exit of said residue, with said temperature increase being from about 200.
degree.
to about 400.
degree.
C.
9.
The method according to claim 8, wherein said temperature increase is from about 250.
degree.
to about 350.
degree.
C.
10.
The method according to claim 1, wherein said low temperature carbonization is carried out from about 350
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