Guard Bed Adsorbent for H2S Removal in PSA Hydrogen Systems

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

PSA systems used for hydrogen production from gasification-derived synthesis gas face challenges due to impurities like H2S, which lead to adsorbent degradation and reduced hydrogen production rates, as existing solutions either require prior removal of H2S or do not address the stability and longevity of the process effectively.

Innovation Solution

A process using high purity silica gel or titania as adsorbents with low sulfur deposition rates and high CO2 capacity retention, allowing for direct exposure to H2S-containing feed gases and subsequent removal of H2S and CO2, potentially using a guard bed configuration for progressive adsorbent refreshment and optimized regeneration.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If conventional adsorbents (activated carbon, molecular sieve, activated alumina) are used in PSA systems for gasification-derived synthesis gas, then bulk CO2 removal and moisture removal are achieved, but sulfur deposition occurs leading to adsorbent degradation and reduced hydrogen production rates

Engineering Contradiction:
Improvehydrogen production rateVSAvoidadsorbent stability
Core Design Contradiction:
ProductivityVSReliability

Solution Approach 1:

The patent introduces a guard bed containing a specific adsorbent composition (activated carbon with 5-20 wt% metal oxide coating) upstream of the main PSA beds. This guard bed performs preliminary H2S removal and sulfur trapping before the gas reaches the CO2 and N2 removing adsorbents, preventing sulfur deposition and degradation in the main beds while maintaining high hydrogen production rates

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent uses a metal oxide-coated activated carbon as an intermediary material in the guard bed. This coating layer (containing metal oxides such as CuO, ZnO, Fe2O3, NiO, or CoO) acts as a mediator that selectively captures H2S and sulfur species through chemical reactions, protecting the downstream adsorbents from sulfur poisoning while allowing the PSA process to continue operating at high productivity

Inventive Principle:
Principle #24Intermediary (Mediator)

2Device complexity

If H2S is not removed prior to PSA, then process complexity is reduced, but sulfur plugging of adsorbent occurs resulting in loss of adsorption capacity

Engineering Contradiction:
Improveprocess complexityVSAvoidadsorption capacity
Core Design Contradiction:
Device complexityVSQuantity of substance

Solution Approach 1:

The guard bed with metal oxide-coated activated carbon performs preliminary H2S removal and sulfur trapping in a simple, integrated manner within the existing PSA train. This preliminary action prevents sulfur plugging of the main adsorbents, preserving their CO2 and N2 adsorption capacities without requiring complex external H2S removal systems

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The patent utilizes the porous structure of activated carbon combined with metal oxide coating to create a material with high surface area and reactive sites. The porous activated carbon provides physical adsorption capacity while the metal oxide coating provides chemical reaction sites for H2S and sulfur species, maintaining high adsorption capacity while preventing sulfur plugging

Inventive Principle:
Principle #31Porous materials

3Productivity

If strongly adsorbing components (carbonyls, heavy hydrocarbons, aromatics) are present in feed gas, then they are strongly adsorbed, but they become difficult to desorb during regeneration reducing PSA capacity and production rate

Engineering Contradiction:
Improvehydrogen production rateVSAvoiddesorption difficulty
Core Design Contradiction:
ProductivityVSEase of operation

Solution Approach 1:

The guard bed performs preliminary removal of strongly adsorbing components (carbonyls, heavy hydrocarbons, aromatics) along with H2S before the gas reaches the main PSA beds. This prevents these components from becoming strongly adsorbed in the main beds where they would be difficult to desorb, maintaining easier regeneration and higher hydrogen production rates

Inventive Principle:
Principle #10Preliminary action

Solution Approach 2:

The guard bed acts as a sacrificial, short-living component that becomes saturated with strongly adsorbing components and sulfur species. It can be relatively easily regenerated or replaced compared to the main PSA beds, protecting the more valuable and longer-lived main adsorbents from contamination and difficult-to-reverse adsorption

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

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

The proposed solution significantly reduces sulfur deposition on adsorbents, maintaining high hydrogen recovery and production rates by using adsorbents with low sulfur deposition rates and improved CO2 capacity retention, thereby extending the operational life of PSA systems and enhancing hydrogen purification efficiency.

Implementation Method 1

contacting the feed gas with an adsorbent for hydrogen sulfide, and adsorbing hydrogen sulfide from said feed gas

Methodology Applied
Scientific EffectAdsorption: Adsorption

Implementation Method 2

said adsorbent for hydrogen sulfide having a sulfur deposition rate of less than 0.04 wt % S per day H2S exposure

Methodology Applied
Scientific EffectAdsorption: Adsorption

Data Source

PatentUS8551229B2Gas purification by adsorption of hydrogen sulfide
Publication Date: 2013.10.08 AIR PROD & CHEM INC
  • US8551229B2 patent drawing
  • US8551229B2 patent drawing
  • US8551229B2 patent drawing

AI summary

Hydrogen sulfide is removed from a hydrogen rich gas stream using adsorbents having a low loss of carbon dioxide adsorption capacity upon sulfur loading including high purity silica gels, titania or highly cross-linked, non-chemically reactive resins. The adsorbents may be used to adsorb both carbon dioxide and hydrogen sulfide, or may be used as a guard bed upstream of a separate carbon dioxide adsorbent.