Fluidized Bed Steam Cracking Heat Integration

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Solution Overview

Problem

Conventional steam cracking furnaces are energy-intensive, produce excessive emissions, have a large footprint, and suffer from inefficiencies due to non-uniform temperatures and coking, leading to lower yields and increased operational costs.

Innovation Solution

A process and system that utilize the heat from Syngas production to provide heat to an endothermic reaction zone, potentially using a fluidized bed for uniform heat transfer, reducing the need for traditional furnaces and minimizing emissions and coking issues.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional steam-cracking furnaces are used to heat hydrocarbon feedstocks to cracking temperatures, then the cracking reactions can proceed to produce olefins, but the process becomes highly energy intensive with excessive fuel usage and high emissions of NOx and carbon dioxide

Engineering Contradiction:
Improveolefin productionVSAvoidenergy consumption
Core Design Contradiction:
ProductivityVSUse of energy by moving object

Solution Approach 1:

The patent combines the steam cracking reactor with a reforming reactor in an integrated system where the reforming process generates Syngas that provides heat to the cracking zone. This merging eliminates the need for separate external furnaces and their associated fuel consumption, while the Syngas produced becomes a useful byproduct for downstream synthesis processes.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The steam cracking system serves itself by using the hydrocarbon feedstock to generate Syngas through reforming, and the Syngas combustion provides the heat required for cracking. The system's own byproducts (Syngas and heat) are utilized to sustain the cracking process, reducing external energy inputs and emissions.

Inventive Principle:
Principle #25Self-service

2Productivity

If conventional steam-cracking furnaces are used, then cracking reactions can occur, but the furnaces require a large footprint and must be placed at specified distances from other processing equipment for safety reasons

Engineering Contradiction:
Improveolefin productionVSAvoidfootprint
Core Design Contradiction:
ProductivityVSArea of stationary object

Solution Approach 1:

The patent merges the cracking reactor and reforming reactor into a single integrated unit, eliminating the need for separate external furnaces. This consolidation reduces the overall plant footprint and allows closer placement of processing equipment while maintaining safety requirements.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The Syngas acts as an intermediary that transfers energy from the reforming process to the cracking process within a compact integrated design, replacing the need for large external furnace systems and enabling more flexible plant layout.

Inventive Principle:
Principle #24Intermediary (Mediator)

3Productivity

If high temperatures are used in steam-cracking furnaces to achieve cracking reactions, then olefins can be produced, but coking occurs on the reactor walls which degrades efficiency and requires frequent shutdowns for de-coking

Engineering Contradiction:
Improveolefin productionVSAvoidcontinuous operation
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent creates different local conditions within the reactor: the reforming zone operates at conditions optimized for Syngas production, while the cracking zone operates at conditions optimized for olefin production. The fluidized bed provides uniform heat distribution that prevents localized hot spots that cause coking, while maintaining the high temperatures needed for cracking.

Inventive Principle:
Principle #3Local quality

Solution Approach 2:

The fluidized bed acts as an intermediary heat transfer medium that distributes heat uniformly throughout the cracking zone, preventing localized overheating and coking while maintaining the high temperatures required for cracking reactions. This allows continuous operation without frequent shutdowns for de-coking.

Inventive Principle:
Principle #24Intermediary (Mediator)

4Productivity

If conventional steam-cracking furnaces are used, then cracking can occur, but the low heat transfer coefficients require excessive reactor tube surface area and lead to longer residence times which reduce yields

Engineering Contradiction:
Improveolefin productionVSAvoidreactor tube surface area
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The patent replaces the conventional furnace-based heat transfer system with a fluidized bed heat transfer system. The fluidized bed provides intense and uniform heat transfer throughout the cracking zone, eliminating the need for extensive reactor tube surface area and reducing residence time while maintaining high cracking efficiency and yields.

Inventive Principle:
Principle #28Mechanics substitution (Replace mechanical system)

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 enhances energy efficiency, reduces emissions, and maintains isothermal conditions, thereby increasing yield and reducing the need for frequent shutdowns, while minimizing the environmental impact and operational costs.

Implementation Method 1

endothermic chemical reactions... endothermic reaction zone... allowing reactants in the endothermic reaction stream to react

Methodology Applied
Scientific EffectEndothermic reaction: Endothermic Reaction

Implementation Method 2

recovering heat from the producing of the Syngas to heat an endothermic reaction stream in a heat transfer zone

Methodology Applied
Scientific EffectHeat transfer: Conduction (thermal)

Data Source

PatentUS11103844B2Advanced steam cracking
Publication Date: 2021.08.31 STRATEC SE
  • US11103844B2 patent drawing
  • US11103844B2 patent drawing
  • US11103844B2 patent drawing

AI summary

A process and system that use the heat produced in the generation of Syngas to provide heat to an endothermic reaction zone are disclosed. A method for providing heat to an endothermic reaction may comprise producing Syngas in a reforming reactor. The method may further comprise recovering heat from the producing the Syngas to heat an endothermic reaction stream in a heat transfer zone. The method may further comprise allowing reactants in the endothermic reaction stream to react to form an endothermic reaction product stream. The method may further comprise withdrawing the endothermic reaction product stream from the heat transfer zone.