Process for the separation of cresols in a simulated moving bed

By using FAU-type zeolite adsorbent and 2-pentanol or 3-pentanol desorbent in cresol separation, the problems of insufficient selectivity and regenerability of desorbents in existing technologies are solved, achieving efficient cresol separation and increased productivity.

CN122295306APending Publication Date: 2026-06-26IFP ENERGIES NOUVELLES
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
IFP ENERGIES NOUVELLES
Filing Date
2024-11-20
Publication Date
2026-06-26

AI Technical Summary

Technical Problem

Existing technologies lack selectivity and regenerability of desorbents in cresol separation, resulting in low molecular sieve productivity, high distillation column energy consumption, and the desorbent is easily retained in the molecular sieve after regeneration, limiting the future productivity of the molecular sieve.

Method used

An adsorbent based on FAU-type zeolite and a desorbent selected from straight-chain 5-carbon alcohols, especially 2-pentanol and 3-pentanol, were used to simulate the separation of cresol in a moving bed. Through selective adsorption and desorption, the separation efficiency of p-cresol and m-cresol was improved, and the productivity was optimized.

Benefits of technology

This technology enables the production of high-purity p-cresol and m-cresol, reduces energy consumption in the distillation stage, and improves the productivity of molecular sieves and the efficiency of desorbent use.

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Abstract

This invention relates to a method for separating cresol using agglomerated zeolite adsorbent solids in a simulated moving bed, and to an optimized desorbent selected from 2-pentanol or 3-pentanol.
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Citation Information

Patent Citations

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  • Aromatic hydrocarbon separation by adsorption

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  • Zeolitic adsorbent for xylene separation

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    US5382747A