Production of high yields of light olefins from heavy hydrocarbons
US-11891356-B2 · Feb 6, 2024 · US
US9968922B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9968922-B2 |
| Application number | US-201214366209-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 26, 2012 |
| Priority date | Dec 19, 2011 |
| Publication date | May 15, 2018 |
| Grant date | May 15, 2018 |
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This application provides a catalyst for producing paraxylene by co-conversion of methanol and/or dimethyl ether and C 4 liquefied gas, and preparation and application thereof. The catalyst is an aromatization molecular sieve catalyst with a shape-selective function co-modified by bimetal and siloxane compound. Methanol and/or dimethyl ether and C 4 liquefied gas are fed in reactor together, wherein aromatization reaction occurring on a modified shape-selective molecular sieve catalyst. The yield of aromatics is effectively improved, in which paraxylene is the main product. In products obtained by co-conversion of methanol and/or dimethyl ether and C 4 liquefied gas, the yield of aromatics is greater than 70 wt %, and the content of paraxylene in aromatics is greater than 80 wt %, and the selectivity of paraxylene in xylene is greater than 99 wt %.
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The invention claimed is: 1. A process for producing paraxylene by co-conversion of methanol and/or dimethyl ether and C 4 liquefied gas, comprising the steps as follows: passing a gas mixture containing methanol and/or dimethyl ether and C 4 liquefied gas through a reactor comprising an aromatization molecular sieve catalyst with a shape-selective function to produce paraxylene by aromatization reaction; wherein said aromatization reaction is carried out at a temperature from 400° C. to 550° C., a pressure from atmospheric pressure to 2 MPa and a weight hourly space velocity of said gas mixture from 1 h −1 to 10 h −1 ; wherein said aromatization molecular sieve catalyst comprises HZSM-5 and/or HZSM-11 zeolite molecular sieve co-modified by bimetal and a siloxane compound; wherein said bimetal are zinc and gallium; wherein said siloxane compound has the structural formula wherein, R 1 , R 2 , R 3 and R 4 are independently selected from C 1 -C 10 alkyl group, and wherein a loading amount of said zinc is 0.5-8 wt % of a total weight of said catalyst, a loading amount of said gallium is 0.5-8 wt % of the total weight of said catalyst, and a loading amount of said siloxane compound, which is based on silicon oxide, is 0.5-10 wt % of the total weight of said catalyst; wherein the process comprises the following step to prepare said aromatization molecular sieve catalyst: (a) impregnating a molecular sieve comprising HZSM-5 and/or HZSM-11 in a solution containing at least one soluble salt of one of zinc or gallium, which is then filtered, dried and calcined to obtain a metal-modified molecular sieve; (b) impregnating said metal-modified molecular sieve obtained from step (a) in a solution containing at least one soluble salt of the other of zinc or gallium, which is then filtered, dried and calcined to obtain a bimetal-modified molecular sieve; and (c) impregnating said bimetal-modified molecular sieve obtained from step (b) in a siloxane compound, which is then filtered, dried and calcined to obtain said aromatization molecular sieve catalyst. 2. The process according to claim 1 , wherein said siloxane compound is tetraethoxysilane. 3. The process according to claim 1 , wherein said process is conducted in a fixed bed or a fluidized bed reactor.
Xylenes · CPC title
not in framework positions · CPC title
General concepts, e.g. reviews, relating to methods of using catalyst systems, the concept being defined by a common method or theory, e.g. microwave heating or multiple stereoselectivity · CPC title
also containing elements or functional groups covered by B01J31/0201 - B01J31/0269 · CPC title
of the pentasil type, e.g. types ZSM-5, ZSM-8 or ZSM-11, as exemplified by patent documents US3702886, GB1334243 and US3709979, respectively · CPC title
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