Method for producing monocyclic aromatic hydrocarbon
The method for producing a monocyclic aromatic hydrocarbon includes a cracking and reforming reaction step in which a catalyst for producing a monocyclic aromatic hydrocarbon containing crystalline aluminosilicate which has been subjected to a heat treatment in an atmosphere containing water vapor in advance is loaded into a fixed-bed reactor, and a feedstock oil having a 10 volume % distillate temperature of 140° C. or higher and a 90 volume % distillate temperature of 390° C. or lower is brought into contact with the catalyst to cause a reaction, so as to obtain a product containing a monocyclic aromatic hydrocarbon having 6 to 8 carbon atoms.
1. A method for producing a monocyclic aromatic hydrocarbon, comprising:
a cracking and reforming reaction step comprising loading a catalyst containing crystalline aluminosilicate which has been subjected to a heat treatment in advance into a fixed-bed reactor, wherein the heat treatment is conducted at a temperature from 700° C. to 850° C., under an atmosphere comprising water vapor content of from 10 vol % to 100 vol %, and for a time from 15 minutes to 5 hours, and
bringing a feedstock oil having a 10 volume % distillate temperature of 140° C. or higher and a 90 volume % distillate temperature of 390° C. or lower into contact with the catalyst to conduct a reaction, thereby obtaining a product containing a monocyclic aromatic hydrocarbon having 6 to 8 carbon atoms, wherein a yield of the monocyclic aromatic hydrocarbon having 6 to 8 carbon atoms contained in the product 24 hours after the start of the reaction is 29% by mass or more.
2. The method according to claim 1 , wherein the crystalline aluminosilicate includes a medium-pore zeolite and/or a large-pore zeolite as a main component.
3. The method according to claim 1 , wherein the catalyst contains at least one member selected from the group consisting of phosphorus, an alkaline-earth metal and a rare-earth element.
4. The method according to claim 1 , wherein the catalyst contains at least one member selected from the group consisting of silica and alumina as a binder.
5. The method according to claim 1 , wherein, in the cracking and reforming reaction step, two or more fixed-bed reactors are used and a cracking and reforming reaction and a regeneration of spent catalyst are repeated while the fixed-bed reactors are periodically switched.
6. The method according to claim 1 , wherein the feedstock oil is a thermally-cracked heavy oil obtained from an ethylene production apparatus or a partially-hydrogenated product of the thermally-cracked heavy oil.
7. The method according to claim 1 , wherein the feedstock oil is a cracked light oil or a partially-hydrogenated product of the cracked light oil.