Isothermal HDO Reactor Heat Management

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Solution Overview

Problem

Conventional hydrodeoxygenation reactors face challenges in managing the exothermic nature of the reaction, leading to localized heat releases that can compromise reactor integrity and require larger equipment, increasing capital and operating costs due to the need for extensive recycling and quenching methods.

Innovation Solution

The implementation of isothermal HDO reactors with a shell-and-tube configuration, where a water stream is used to remove heat of reaction, generating steam that is then utilized to produce renewable power, thereby controlling the reaction temperature and reducing equipment size.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If conventional HDO reactors are used to remove oxygen from bio-derived feedstocks, then deoxygenation is achieved, but large localized heat release occurs compromising reactor integrity and requiring larger equipment

Engineering Contradiction:
Improveoxygen removal efficiencyVSAvoidlocalized heat release
Core Design Contradiction:
Quantity of substanceVSTemperature

Solution Approach 1:

The reactor is divided into multiple catalyst beds separated by quench zones. This segmentation allows the exothermic deoxygenation reaction to occur in distributed stages rather than a single large heat release event, with each bed managing a portion of the oxygen removal and heat generation.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A quench gas (inert or reactive) is introduced as an intermediary between catalyst beds to absorb and remove heat from the reaction zones. This mediator prevents excessive temperature buildup by carrying heat away from the catalyst beds and transferring it to downstream sections of the reactor.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Temperature

If substantial recycle streams are used to control heat release, then temperature control is improved, but reactor size and equipment complexity increase

Engineering Contradiction:
Improvetemperature controlVSAvoidreactor size
Core Design Contradiction:
TemperatureVSVolume of stationary object

Solution Approach 1:

The heat management function is extracted from the main reaction zone and placed in dedicated quench zones between catalyst beds. This separation allows temperature control to occur in specific locations without requiring the entire reactor to be oversized, concentrating the heat removal function where it is most needed.

Inventive Principle:
Principle #2Taking out (Extraction)

Solution Approach 2:

Quench gas is introduced in advance between catalyst beds to prepare for heat removal before excessive temperatures can develop. This preliminary cooling action prevents temperature runaways and reduces the need for large reactor volumes to accommodate heat management.

Inventive Principle:
Principle #10Preliminary action

3Reliability

If conventional heat management methods are used, then reaction safety is maintained, but capital and operating costs increase due to larger equipment

Engineering Contradiction:
Improvereaction safetyVSAvoidequipment complexity
Core Design Contradiction:
ReliabilityVSDevice complexity

Solution Approach 1:

The deoxygenation reaction and heat management functions are merged into a single integrated reactor design with multiple catalyst beds and quench zones. This combination eliminates the need for separate heat exchangers and recycle compression systems, reducing overall equipment complexity while maintaining safety.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The reactor system uses its own reaction heat to drive the deoxygenation process forward, with the exothermic reaction providing the energy needed for the endothermic quenching sections. This self-sufficient heat management reduces external utility requirements and simplifies equipment needs.

Inventive Principle:
Principle #25Self-service

Data Source

PatentUS11788016B2Methods and systems for hydrodeoxygenating bio-derived feedstocks and generating renewable power
Publication Date: 2023.10.17 EXXONMOBIL TECHNOLOGY & ENGINEERING CO
  • US11788016B2 patent drawing
  • US11788016B2 patent drawing
  • US11788016B2 patent drawing

AI summary

Methods and systems for hydrodeoxygenating a bio-derived feedstock during the production of renewable diesel and generating renewable power as part of the hydrodeoxygenation (HDO) process are provided herein. One method includes providing an HDO catalyst within either a shell or tube side of an isothermal HDO reactor including a shell-and-tube configuration and exposing a bio-derived feedstock to the HDO catalyst within the isothermal HDO reactor to form an HDO reactor effluent. The method also includes flowing a water stream through the opposite side of the isothermal HDO reactor as compared to the side including the HDO catalyst to remove the heat of reaction between the bio-derived feedstock and the HDO catalyst, where the removal of the heat of reaction using the water stream forms steam. The method further includes flowing the steam through a steam turbine to provide for the generation of renewable power.