Process for preparing p-xylene
A technology of p-xylene and xylene, which is applied in the field of preparing p-xylene and can solve the problems of hydrogen consumption and the like
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[0034] Zeolite ZSM-5 and conventional methods of preparation are described in US Patent 3,702,886. Zeolite ZSM-11 and its general method of preparation are described in US Patent 3,709,979. Zeolite ZSM-12 and its general method of preparation are described in US Patent 3,832,449. Zeolite ZSM-23 and its general method of preparation are described in US Patent 4,076,842. Zeolite ZSM-35 and its general method of preparation are described in US Patent 4,016,245. ZSM-48 and its general method of preparation are taught by US Patent 4,375,573. The entire disclosures of these US patents are incorporated by reference into this application.
[0035] The medium pore zeolites described above are preferred for the process of the invention because their pore size and shape favor the production of para-xylene over the other xylene isomers. However, the values of the diffusion parameters of these zeolites in conventional form exceed the preferred values for the present invention of 0....
Embodiment 1
[0087] Embodiment 1 (comparative example)
[0088] figure 1 A process flow 100 of a comparative example different from the present invention is shown by way of example. In this process, a feed stream 101 comprising gas, water and fresh methanol, toluene and benzene is fed to mixing device M1 where it is mixed with a recycle stream 106 comprising benzene and toluene to form a combined stream 103 , the combined stream 103 is sent to the alkylation reactor R1. In Rl, benzene and toluene are reacted with methanol in the presence of an alkylation catalyst such as a zeolite molecular sieve to obtain a first reaction product mixture stream 105 comprising benzene, toluene and mixed xylenes. Stream 105 is passed to a first separation apparatus S1 (rectification column), where a light stream 106 comprising benzene and toluene and a xylene stream 107 comprising xylenes are produced. Additional streams, collectively referred to as stream 108 , may also be generated from S1 that may inc...
Embodiment 2
[0090] Embodiment 2 (the present invention)
[0091] figure 2A method flow 200 of the present invention is schematically shown. In this process, a feed stream 201 comprising water, gas and fresh methanol and toluene and / or benzene is fed to mixing device M1 where it is combined with a recycle stream 206 comprising toluene and a recycle stream comprising toluene Streams 225 combine to form combined stream 203, which is delivered to alkylation reactor R1. In R1, toluene and / or benzene is reacted with methanol in the presence of an alkylation catalyst, such as a zeolite molecular sieve, to obtain a first reaction product mixture stream 205 comprising toluene, mixed xylenes, and optionally benzene. Stream 205 is passed to a first separation apparatus S1 (rectification column), where a light stream 206 comprising toluene and optionally benzene and a xylene stream 207 comprising mixed xylenes are produced. Other streams may also be generated from S1, collectively referred to as ...
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Abstract
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