Zeolite Catalyst Isomerization Selectivity for 2,5-Dichlorophenol
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Solution Overview
Problem
Current processes for producing 2,5-dichlorophenol face challenges such as high raw material costs, low process conversions, and high waste generation, with existing zeolite catalysts failing to achieve high selectivity for 2,5-dichlorophenol, leading to inefficient production of dicamba, an important herbicide.
Innovation Solution
The use of a zeolite catalyst with a SiO2/Al2O3 mole ratio of no greater than 35:1, specifically a desilicated zeolite with enhanced meso-macro pore volume, in conjunction with steam rejuvenation, to isomerize 2,4-dichlorophenol and hydroxylate 1,4-dichlorobenzene, improving selectivity and yield of 2,5-dichlorophenol.
Engineering Contradictions & Design Principles
Engineering Contradiction Analysis
1Manufacturing precision
If conventional zeolite catalysts are used for isomerization of 2,4-dichlorophenol, then the process can proceed, but the selectivity for 2,5-dichlorophenol is insufficient
Solution Approach 1:
The patent modifies the zeolite catalyst by changing the SiO2/Al2O3 mole ratio parameter to no greater than 35:1, and introduces desilication treatment to enhance meso-macro pore volume. These parameter changes in catalyst composition and structure significantly improve the selectivity for 2,5-dichlorophenol while maintaining productivity.
Solution Approach 2:
The patent utilizes the porous structure of zeolite catalysts, specifically enhancing the meso-macro pore volume through desilication. This porous material modification allows improved access to active sites and better selectivity for the desired isomerization product, resolving the contradiction between selectivity and productivity.
2Loss of substance
If existing production processes are used, then 2,5-dichlorophenol can be produced, but raw material costs are high and waste generation is large
Solution Approach 1:
By changing the catalyst parameters (SiO2/Al2O3 ratio ≤ 35:1 and desilication treatment), the process achieves higher conversion efficiency and reduces waste generation. The improved catalyst facilitates more efficient isomerization, reducing the need for additional raw materials and minimizing byproducts.
Solution Approach 2:
The patent converts the harmful effect of low selectivity (which causes waste) into a benefit by using desilicated zeolite catalysts that achieve high selectivity. This transforms the previous waste-generating process into a high-efficiency process with minimal waste, addressing both loss of substance and productivity concerns.
3Productivity
If 2,4-dichlorophenol is isomerized using conventional catalysts, then some conversion occurs, but the process conversion is low
Solution Approach 1:
The patent applies parameter changes to the catalyst (SiO2/Al2O3 ≤ 35:1 and desilication) that simultaneously improve both process conversion and selectivity. The modified catalyst structure provides more active sites and better pore accessibility, enabling higher conversion while maintaining high selectivity for 2,5-dichlorophenol.
Applied Scientific Principles
This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.
Function Achieved in This Case
This approach significantly enhances the selectivity and yield of 2,5-dichlorophenol, reducing waste and raw material costs, thereby improving the economic viability of dicamba production.
Implementation Method 1
contacting a feed gas or a liquid comprising 2,4-dichlorophenol with a zeolite catalyst in acid form in an isomerization zone to isomerize at least a portion of the 2,4-dichlorophenol to 2,5-dichlorophenol
Implementation Method 2
isomerize at least a portion of the 2,4-dichlorophenol to 2,5-dichlorophenol
Implementation Method 3
hydroxylating 1,4-dichlorobenzene with an oxidizing agent in the presence of a first zeolite catalyst in a hydroxylation zone to form a hydroxylation reaction product comprising 2,5-dichlorophenol and 2,4-dichlorophenol
Data Source
AI summary
Processes for producing 2,5-dichlorophenol and 3,6-dichloro-2-methoxybenzoic acid are described. Various processes for isomerizing 2,4-dichlorophenol over a zeolite catalyst to form 2,5-dichlorophenol are provided. Processes for preparing 2,5-dichlorophenol including hydroxylating 1,4-dichlorobenzene are also described. The present invention also relates to processes for producing 3,6-dichloro-2-methoxybenzoic acid.


