Transalkylation Catalyst Stability via Benzene Recycling

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Solution Overview

Problem

Current alkylbenzene production processes face challenges in achieving desirable product quality and economic viability due to the formation of 'heavies' and high energy consumption, particularly in transalkylation operations for detergent range alkylbenzenes, which require excessive benzene and result in increased capital and operating costs.

Innovation Solution

The integration of a transalkylation unit operation with a cyclic loop of benzene and multiple transalkylation zones using solid catalysts, where the molar ratio of benzene to dialkylbenzene is maintained high to enhance catalyst stability, allowing for reduced fresh benzene consumption and lower energy usage, while minimizing the load on benzene distillation.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Manufacturing precision

If a large excess of benzene is used to reduce heavies formation, then product quality is improved, but capital and operating costs increase due to additional recovery and recycling requirements

Engineering Contradiction:
Improveproduct qualityVSAvoidprocess complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent changes the operating parameters by using a moderate benzene excess (6:1 to 8:1 molar ratio) rather than large excess, and compensates by optimizing other parameters such as temperature (80-150°C), pressure (1-10 atm), and catalyst selection to maintain product quality while reducing process complexity

Inventive Principle:
Principle #35Parameter changes

Solution Approach 2:

The patent applies different conditions to different parts of the process: homogeneous HF catalysis is used in the alkylation reactor where high activity is needed, while heterogeneous solid acid catalysts are used in the transalkylation reactor where selectivity is prioritized, allowing each stage to operate under optimized local conditions

Inventive Principle:
Principle #3Local quality

2Productivity

If homogeneous hydrogen fluoride catalysis is used, then alkylation activity is improved, but safety risks and corrosion issues worsen

Engineering Contradiction:
Improvealkylation activityVSAvoidsafety and corrosion
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent extracts the harmful homogeneous HF catalyst from the transalkylation step and replaces it with a heterogeneous solid acid catalyst, eliminating the safety and corrosion issues associated with HF while maintaining catalytic activity through the solid catalyst's acidic sites

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

The patent introduces a heterogeneous solid acid catalyst as an intermediary substance that mediates the transalkylation reaction, providing the necessary catalytic function without the harmful properties of homogeneous HF, thus bridging the gap between activity and safety requirements

Inventive Principle:
Principle #24Intermediary (Mediator)

3Object-affected harmful factors

If solid catalysts are used for alkylation, then safety is improved, but heavies formation increases

Engineering Contradiction:
ImprovesafetyVSAvoidheavies formation
Core Design Contradiction:
Object-affected harmful factorsVSObject-generated harmful factors

Solution Approach 1:

The patent uses the alkylation product (alkylbenzene) as an intermediary reactant in a subsequent transalkylation step with a heterogeneous catalyst, converting the harmful heavies back into useful alkylbenzene product, thus eliminating the waste problem while maintaining the safety benefits of solid catalysts

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The patent creates a continuous process where alkylation produces alkylbenzene which then undergoes transalkylation to convert heavies back to alkylbenzene, maintaining continuous useful action and preventing heavies accumulation while keeping the system safe through heterogeneous catalysis

Inventive Principle:
Principle #20Continuity of useful action

4Manufacturing precision

If transalkylation is practiced to convert heavies, then heavies are reduced, but incremental benzene production requirements increase capital and operating costs

Engineering Contradiction:
Improveproduct purityVSAvoiddistillation requirements
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent designs the transalkylation reactor to serve multiple functions: it acts as both a transalkylation reactor for converting heavies and a source of incremental benzene production, eliminating the need for separate distillation infrastructure and reducing capital and operating costs

Inventive Principle:
Principle #6Universality (Multi-functionality)

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 enables the production of alkylbenzenes with improved quality and reduced energy consumption, achieving high catalyst stability and minimizing the incremental benzene demand, thus optimizing the alkylbenzene production process economically.

Implementation Method 1

maintaining said at least one transalkylation zone at transalkylation conditions comprising a catalytically effective amount of solid transalkylation catalyst

Methodology Applied
Scientific EffectCatalysis: Catalysis

Implementation Method 2

subjecting at least a portion of the transalkylation product to fractionation conditions to provide a lower boiling, benzene-rich fraction and a higher-boiling, alkyl substituted benzene-containing fraction

Methodology Applied
Scientific EffectDistillation: Distillation

Data Source

PatentUS7692055B2Transalkylation of dialkylbenzene
Publication Date: 2010.04.06 UOP LLC
  • US7692055B2 patent drawing
  • US7692055B2 patent drawing
  • US7692055B2 patent drawing

AI summary

Dialkylbenzenes are transalkylated in the presence of benzene and solid catalyst. The transalkylation product is subjected to distillation to provide a lower-boiling, benzene-containing fraction which is fed to a transalkylation reactor as at least a portion of the benzene. Thus, high benzene to dialkylbenzene molar ratios can be economically maintained in order to enhance catalyst stability.