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Catalyst composition and process for converting aliphatic oxygenates to aromatics

A composition and catalyst technology, applied in the direction of carbon compound catalysts, hydrocarbon production from oxygen-containing organic compounds, chemical instruments and methods, etc., to achieve the effects of low cost, good selectivity, and high yield

Inactive Publication Date: 2014-01-08
SAUDI BASIC IND CORP SA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This catalyst was used to prepare mixtures containing C2-C4 olefins from methanol but only showed 2% conversion of methanol

Method used

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  • Catalyst composition and process for converting aliphatic oxygenates to aromatics
  • Catalyst composition and process for converting aliphatic oxygenates to aromatics

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0062] Similar to Comparative Experiment C, 0.6 g of lanthanum nitrate dissolved in 100 g of distilled water, and 0.5 g of molybdenum oxide, 0.06 g of zinc oxide and 2.6 g of copper nitrate trihydrate dissolved in 100 g of water at 85 ° C were used to prepare the improved Proactive ZSM-5 catalyst. The two solutions were mixed and 10 g of ZSM-5 was added to the solution and heated at 85° C. in a closed vessel for 8 h; resulting in approximately 2 mass % La, 3 mass % Mo, 0.5 mass % Zn and 7% by mass of Cu was added to ZSM-5.

[0063] Similar to Comparative Experiments C and D, the dried and calcined catalyst was used to convert methanol. Table 1 shows that the yield and BTX selectivity are significantly improved.

Embodiment 2

[0065] Catalysts were prepared by ion exchange and heat treatment of ZSM-5, commercially available from Zeolists, with the desired amount of metal. Dissolve 0.6 g of lanthanum nitrate (fluka) in 100 g of distilled water and heat at 60-65° C. with constant stirring. 0.5 g of molybdenum oxide and 0.06 g of zinc oxide were dissolved in 100 g of water at 85° C. and pH 5. The two solutions were mixed and 10 g of ZSM-5 was added to the solution and heated at 85° C. for 8 h in a closed vessel. This reflects the addition of about La (2%), Mo (3%) and Zn (0.5%) to ZSM-5. The prepared catalyst was filtered and washed with 3 liters of hot water. The prepared catalyst slurry was dried at 120° C. for 16 h in a closed oven. The dried catalyst was calcined to 450 °C in a rotary furnace with a temperature rise of 1 °C per minute and kept at 450 °C for 6 h.

[0066] A catalyst with a mesh size of 40-60 is loaded into a tubular fixed-bed reactor to convert methanol. The reaction was carrie...

Embodiment 3

[0068] Similar to Comparative Experiment C, ZSM-5 (from Zeolists) was ion-exchanged and heat-treated using 0.6 g of lanthanum nitrate dissolved in 100 g of distilled water and 0.5 g of molybdenum oxide dissolved in 100 g of water to prepare the catalyst; resulting in ZSM- 5 has about 2% by mass of La and 3% by mass of Mo.

[0069]Similar to Comparative Experiment C, a dry and calcined 40-60 mesh catalyst was used to convert methanol. Table 1 summarizes the results.

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Abstract

The invention relates to a novel catalyst composition La-M / zeolite, which consists essentially of from 0.0001 to 20 mass % of La (lanthanum); from 0.0001 to 20 mass % of at least one element M selected from the group consisting of molybdenum (Mo), cerium (Ce) and caesium (Cs); a zeolite of the 10-ring structure type; and optionally a binder (mass % based on total catalyst composition). The invention also relates to the use of the catalyst composition according to the invention in various reactions, for examples in making aromatics from aliphatic hydrocarbons or oxygenated hydrocarbons with good selectivity and activity. The invention further relates more specifically to a process for converting a feed stream comprising oxygenated lower aliphatic hydrocarbon compounds, especially methanol, to a product stream comprising aromatic hydrocarbons and olefins, especially BTX, which process comprises a step of contacting said feed with the catalyst composition according to the invention.

Description

technical field [0001] The present invention relates to catalyst compositions comprising lanthanum-containing zeolites. The present invention also relates to the use of the catalyst compositions according to the invention for various reactions such as the preparation of aromatic compounds from oxygen-containing aliphatic hydrocarbons. The invention also relates to a process for converting a feed stream comprising oxygenated lower aliphatic hydrocarbon compounds into a product stream comprising aromatics, said process comprising the step of contacting said feed with a catalyst composition according to the invention. [0002] More particularly, the present invention relates to catalyst compositions and processes for converting a feed stream comprising C1 to C4 oxygenates to a product stream comprising C6 to C8 aromatics. Background technique [0003] Such a catalyst composition is known in patent publication US 4156698, wherein a feed containing C1-C4 monohydric alcohols is c...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/20B01J29/06B01J29/40
CPCB01J29/46B01J29/7057C07C2529/40C07C2529/48B01J29/405B01J2229/42B01J29/48C07C1/20Y02P20/52C07C15/02
Inventor K·卡利姆N·埃尔-奥泰比S·扎希尔A·埃尔-沙波南
Owner SAUDI BASIC IND CORP SA