Regeneration method of toluene disproportionation catalyst
A toluene disproportionation and catalyst technology, which is applied in the direction of catalyst regeneration/reactivation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems of inability to realize automatic operation of the device, long analysis time, complicated operation, etc., and achieves easy operation. , good technical effect, the effect of improving work efficiency
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Publication Date
- 2014-03-26
Smart Images
Figure 1 Figure 2 Figure 3
Abstract
Description
technical field
[0001] The invention relates to a regeneration method of a toluene disproportionation catalyst. Background technique
[0002] Para-xylene in xylene is one of the main basic organic raw materials in the petrochemical industry. It is widely used in chemical fiber, synthetic resin, pesticide, medicine, plastic and many other chemical production fields. In 1989, the toluene disproportionation catalyst developed by Shanghai Petrochemical Research Institute of China Petroleum and Chemical Corporation was industrialized, that is, toluene and C9 aromatics were used as raw materials, catalyzed by the toluene disproportionation catalyst in a fixed bed reactor, and disproportionation and transalkylation reactions occurred , producing benzene and xylene.
[0003] U.S. Patent USP5030787 has reported a kind of improved toluene disproportionation / C 9 Aromatic hydrocarbon transalkylation process, the patent uses a zeolite catalyst that has been protonated and ion-exchanged...
Examples
Embodiment 1
[0026] Refer to attached figure 1 , the gas chromatograph used is Agilent 6890, equipped with double valves, double TCD and two capillary column injection ports to provide two paths of carrier gas, the carrier gas is high-purity helium. Column 1 is HP-Molesieve 30mx0.53mmx40μm, column 2 is HP-PLOT Q 30mx0.53mmx20μm. The chromatographic conditions are as follows:
[0027] Column 13: 5? molecular sieve column, carrier gas, helium, 4ml / min;
[0028] Column 14: PLOT-Q column, carrier gas, helium, 4ml / min;
[0029] TCD temperature is 180°C;
[0030] Injector temperature is 140 DEG C; split ratio, 50:1;
[0031] Injection volume: 250 microliters;
[0032] When preparing for sample injection, the six-way valves 10 and 11 are in the OFF state. Open the ball valve 4, and the sample gas, that is, the regenerated product of the toluene disproportionation catalyst, flows through the tee 5, and then passes through the quantitative tubes 6, 7 of the six-way valves 10, 11 to the vent o...