Phototrophic H2S Purification via Iron Chelate Mediator

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Solution Overview

Problem

Current methods for removing hydrogen sulfide from hydrocarbon streams are energy-inefficient and costly, particularly in smaller scale operations, and do not effectively address carbon dioxide emissions in refinery and gas production processes.

Innovation Solution

The use of genetically modified green sulfur bacteria in conjunction with an anaerobic metal redox reaction to oxidize hydrogen sulfide to elemental sulfur, while also fixing carbon or nitrogen, reducing the need for costly metal chelators and energy-intensive processes.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If phototrophic bacteria are used to oxidize H2S at high light intensities, then productivity increases, but energy efficiency decreases due to light saturation and waste as heat or fluorescence

Engineering Contradiction:
ImproveH2S oxidation rateVSAvoidlight energy waste
Core Design Contradiction:
ProductivityVSLoss of energy

Solution Approach 1:

An iron chelate is introduced as an intermediary substance that mediates between light energy and H2S oxidation. The iron chelate absorbs light energy and transfers it to drive H2S oxidation, acting as a mediator that decouples direct bacterial light absorption from the oxidation process, thereby improving overall energy efficiency

Inventive Principle:
Principle #24Intermediary (Mediator)

Solution Approach 2:

The natural photosynthetic mechanism of phototrophic bacteria is replaced with a photochemical system using iron chelate. Instead of relying on bacterial photosynthesis which suffers from light saturation, the system uses iron chelate photochemistry that can operate more efficiently across a broader light intensity range, substituting a biological mechanism with a chemical one

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

2Ease of manufacture

If traditional Claus process is implemented for H2S removal, then sulfur recovery is achieved, but capital cost increases making it impractical for smaller scale operations

Engineering Contradiction:
Improvesulfur recovery capabilityVSAvoidcapital cost
Core Design Contradiction:
Ease of manufactureVSDevice complexity

Solution Approach 1:

The system uses inexpensive, readily available iron chelates that can be easily replenished, replacing the need for expensive, complex Claus plant infrastructure. The iron chelate acts as a consumable reagent that is cheap and can be continuously supplied, making the process economically viable for small-scale operations

Inventive Principle:
Principle #27Cheap short-living objects (Disposable)

Solution Approach 2:

The core sulfur recovery function is extracted from the complex Claus process infrastructure and implemented through a simplified system using iron chelate and phototrophic bacteria. This extracts the essential chemical transformation while eliminating the need for large-scale equipment, making the process suitable for smaller operations

Inventive Principle:
Principle #2Taking out (Extraction)

3Productivity

If redox processes with transition metals are used for H2S oxidation, then sulfur is produced, but metal chelators decompose over time requiring constant replenishment

Engineering Contradiction:
ImproveH2S oxidation rateVSAvoidmetal chelator depletion
Core Design Contradiction:
ProductivityVSLoss of substance

Solution Approach 1:

The system is designed to continuously replenish iron chelate at a controlled rate, discarding decomposed chelate and recovering/adding fresh chelate to maintain the reaction. This continuous replacement strategy ensures steady-state operation despite chelator decomposition, maintaining productivity while using inexpensive replacement material

Inventive Principle:
Principle #34Discarding and recovering

4Productivity

If aerobic bacteria like Thiobacillus are used to treat H2S, then large quantities of H2S can be treated, but sulfate formation increases requiring energy-intensive removal

Engineering Contradiction:
ImproveH2S treatment capacityVSAvoidsulfate production
Core Design Contradiction:
ProductivityVSObject-generated harmful factors

Solution Approach 1:

The oxidation process is changed from aerobic biological oxidation (producing sulfate) to photochemical oxidation using iron chelate (producing elemental sulfur). By changing the chemical parameters of the oxidation process - using photochemical instead of biochemical pathways - the product distribution is altered to favor elemental sulfur over sulfate, eliminating the need for energy-intensive sulfate removal

Inventive Principle:
Principle #35Parameter changes

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 provides a cost-effective and energy-efficient method for hydrogen sulfide removal and carbon fixation, suitable for use in locations where traditional Claus plants are impractical, producing elemental sulfur and organic compounds while reducing greenhouse gas emissions.

Implementation Method 1

introducing the reduced metal chelate to a photobioreactor comprising a phototrophic bacterium

Methodology Applied
Scientific EffectPhotosynthesis: Photosynthesis

Implementation Method 2

The use of genetically modified green sulfur bacteria in conjunction with an anaerobic metal redox reaction to oxidize hydrogen sulfide to elemental sulfur

Methodology Applied
Scientific EffectRedox reactions: Redox Reactions

Data Source

PatentUS12115492B2Phototrophic purification of hydrogen sulfide containing streams
Publication Date: 2024.10.15 EXXONMOBIL TECHNOLOGY & ENGINEERING CO
  • US12115492B2 patent drawing

AI summary

The present disclosure relates to processes for desulfurizing hydrocarbon feedstocks. The processes may include introducing a feedstock comprising hydrogen sulfide to an absorber comprising a metal chelate to form a reduced metal chelate. The processes may further include introducing the reduced metal chelate to a photobioreactor comprising a phototrophic bacterium. The present disclosure also relates to apparatuses for desulfurizing hydrocarbon feedstock. An apparatus may include and absorber and a photobioreactor fluidly connected to the absorber. The photobioreactor may be an anaerobic vessel with a light source.