Parallel Catalyst Testing Reactor System

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Solution Overview

Problem

Current catalyst testing processes in hydrocarbon processing are inefficient and costly, as they typically require evaluating catalysts one at a time in small-scale systems, which do not accurately represent commercial-scale performance due to limited control over reaction conditions and flow dynamics, leading to run-to-run variations and increased time and resource expenditure.

Innovation Solution

A reactor system capable of conducting multiple continuous reactions in parallel, featuring a preheating unit with parallel heating tubes, a reactor unit with multiple reactor tubes, and a multi-chamber separator, allowing for simultaneous evaluation of multiple catalysts with independent control of operating conditions and efficient energy management.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Loss of time

If multiple catalysts are tested sequentially in small-scale systems, then testing time and resource costs are reduced, but performance data accuracy and reliability deteriorate due to scale-up deviations

Engineering Contradiction:
Improvecatalyst testing timeVSAvoidperformance data accuracy
Core Design Contradiction:
Loss of timeVSMeasurement precision

Solution Approach 1:

The system divides the testing process into multiple parallel reactor channels (e.g., 2-10 reactors), each capable of independently testing different catalysts simultaneously. This segmentation allows parallel processing of multiple catalyst evaluations, reducing total testing time while maintaining pilot-scale conditions for accurate performance data.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The invention transitions from sequential single-reactor testing to parallel multi-reactor testing, adding the dimension of temporal parallelism. Multiple catalysts that would traditionally be tested one after another in sequence are now evaluated simultaneously across multiple reactor channels, fundamentally changing the testing paradigm from 1D sequential to 2D parallel processing.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Productivity

If catalysts are tested in small-scale combinatorial systems, then testing speed increases, but flow dynamics and reaction conditions cannot be properly controlled

Engineering Contradiction:
Improvecatalyst evaluation speedVSAvoidflow dynamics control
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

Each reactor channel is equipped with independent feed systems, preheaters, and control mechanisms, allowing individual optimization of flow dynamics and reaction conditions for each catalyst test while maintaining overall system productivity through parallel operation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The system enables independent adjustment of critical parameters (flow rates, temperatures, pressures) for each reactor channel, allowing operators to optimize reaction conditions for different catalysts and feed compositions while maintaining pilot-scale flow dynamics that accurately represent commercial operations.

Inventive Principle:
Principle #35Parameter changes

3Device complexity

If sequential catalyst testing is performed, then system complexity is reduced, but energy consumption increases due to repeated heating and cooling cycles

Engineering Contradiction:
Improvesystem structure simplicityVSAvoidheating and cooling energy consumption
Core Design Contradiction:
Device complexityVSUse of energy by moving object

Solution Approach 1:

The parallel reactor system maintains continuous operation with all reactors running simultaneously at optimal temperatures. By eliminating the stop-start nature of sequential testing, the system avoids repeated heating and cooling cycles, maintaining continuous catalytic activity and significantly reducing energy consumption associated with thermal cycling.

Inventive Principle:
Principle #20Continuity of useful action

Solution Approach 2:

Multiple reactor channels share common infrastructure including feed preparation systems, heating/cooling utilities, and product analysis equipment. This merging of supporting systems reduces overall system complexity while enabling parallel operation that minimizes energy consumption through continuous thermal operation.

Inventive Principle:
Principle #5Merging (Combining)

4Measurement precision

If pilot-scale testing is conducted to achieve accurate commercial performance prediction, then performance data reliability improves, but testing time and costs increase significantly

Engineering Contradiction:
Improvecommercial performance prediction accuracyVSAvoidtesting duration
Core Design Contradiction:
Measurement precisionVSLoss of time

Solution Approach 1:

The parallel reactor system divides pilot-scale testing capacity into multiple independent channels, allowing simultaneous evaluation of multiple catalysts at scales (10-100 times larger than combinatorial systems) that accurately predict commercial performance. This segmentation enables comprehensive catalyst screening at pilot scale without the time and cost penalties of traditional sequential testing.

Inventive Principle:
Principle #1Segmentation

Data Source

PatentUS11344860B2Multiple reactor system for parallel catalyst testing
Publication Date: 2022.05.31 SAUDI ARABIAN OIL CO
  • US11344860B2 patent drawing
  • US11344860B2 patent drawing
  • US11344860B2 patent drawing

AI summary

A reactor system for conducting multiple continuous reactions in parallel may include a preheating unit that includes an outer preheater shell and a plurality of heating tubes disposed within the preheating shell and arranged in parallel. The reactor system may include a reactor unit downstream of the preheating unit, the reactor unit comprising a plurality of reactor tubes disposed within a reactor shell and an outer heating element disposed about the reactor shell. An inlet end of at least one of the reactor tubes may be fluidly coupled to at least one of the heating tubes of the preheating unit. The reactor unit may include a multi-chamber separator downstream of the reactor unit, the multi-chamber separator having a plurality of separation chambers. At least one of the separation chambers may be fluidly coupled to at least one of the reactor tubes.