Biomass Gasification Hydrogen Purity via Membrane Separation

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Solution Overview

Problem

Current biomass gasification methods do not effectively separate nitrogen from combustion gases, leading to reduced caloric value and efficiency in hydrogen production from biomass.

Innovation Solution

A method involving biomass drying, pyrolysis, and combustion to produce synthesis gas, followed by heat exchange and gas scrubbing to remove nitrogen, with subsequent use of membrane separation to achieve high-purity hydrogen production, utilizing a multi-stage reduction process and heat recovery systems.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If nitrogen is not removed from combustion gases, then the process is simple, but the caloric value and efficiency of hydrogen production is reduced

Engineering Contradiction:
Improvehydrogen production efficiencyVSAvoidgas separation process complexity
Core Design Contradiction:
ProductivityVSDevice complexity

Solution Approach 1:

The gas separation process is divided into multiple stages: first removing nitrogen from combustion gases, then further purifying hydrogen through additional separation steps. This segmentation allows each stage to focus on specific impurities, achieving high-purity hydrogen while managing system complexity through modular design.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

A membrane separation unit is introduced as an intermediary component between combustion and hydrogen production stages. This membrane acts as a selective barrier that allows hydrogen to pass through while retaining nitrogen and other impurities, effectively mediating the separation process without requiring complex mechanical systems.

Inventive Principle:
Principle #24Intermediary (Mediator)

2Manufacturing precision

If membrane separation is used to achieve high-purity hydrogen, then hydrogen purity is improved, but the device complexity increases

Engineering Contradiction:
Improvehydrogen purityVSAvoidmembrane separation system complexity
Core Design Contradiction:
Manufacturing precisionVSDevice complexity

Solution Approach 1:

The patent replaces complex mechanical separation systems with a membrane-based separation process. Instead of using mechanical filters, centrifuges, or multiple compression stages, a selectively permeable membrane is used to separate hydrogen from impurities based on molecular size and diffusion properties, significantly simplifying the overall system while achieving high purity.

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

Solution Approach 2:

The membrane separation process exploits changes in physical parameters (permeability, diffusion rate) of different gases through the membrane material. By selecting appropriate membrane materials and operating conditions, hydrogen can be selectively separated at high purity levels without requiring complex mechanical intervention or multiple processing stages.

Inventive Principle:
Principle #35Parameter changes

3Loss of energy

If heat exchange steps are implemented, then energy efficiency is improved, but the process complexity increases

Engineering Contradiction:
Improveenergy recovery efficiencyVSAvoidheat exchange system complexity
Core Design Contradiction:
Loss of energyVSDevice complexity

Solution Approach 1:

The heat exchange system merges multiple functions into integrated heat exchangers that simultaneously perform heating, cooling, and pre-treatment of gases. The combustion gases that exit the combustion chamber are directly routed through heat exchangers that transfer their thermal energy to incoming biomass and process water, combining energy recovery with process integration in a single operational flow.

Inventive Principle:
Principle #5Merging (Combining)

Solution Approach 2:

The heat exchange system is designed to be self-sufficient, where the hot combustion gases automatically provide the necessary thermal energy for drying biomass and heating process water without requiring external energy inputs. The system uses its own waste heat to sustain the drying and heating requirements, creating a self-balancing thermal regime that reduces energy losses.

Inventive Principle:
Principle #25Self-service

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 the efficiency of hydrogen production from biomass by eliminating nitrogen, increasing the caloric value of the gas, and achieving high-purity hydrogen, making it suitable for industrial-scale use.

Implementation Method 1

drying of the biomass

Methodology Applied
Scientific EffectEvaporation: Evaporation

Implementation Method 2

pyrolysis of the biomass to achieve coke

Methodology Applied
Scientific EffectPyrolysis: Pyrolysis

Implementation Method 3

combustion of the pyrolysis gases to form synthesis gas

Methodology Applied
Scientific EffectCombustion: Combustion

Implementation Method 4

heat exchange and gas scrubbing to remove nitrogen, with subsequent use of membrane separation

Methodology Applied
Scientific EffectHeat exchange: Heat Exchanger

Data Source

PatentEP2291492B1Method and equipment for producing hydrogen gas utilizing biomass
Publication Date: 2015.07.29 CORTUS AB
  • EP2291492B1 patent drawingFigure 1
  • EP2291492B1 patent drawingFigure 2

AI summary

The present invention concerns a method for producing hydrogen from biomass, wherein said method comprises the stages of drying of the biomass, gasification of the biomass, and water gas shift reaction. The invention also concerns a equipment for conducting the method of the present invention. It is essential to the present invention that the method comprises the additional stages: of subjecting the outgoing gases (CO2, N2 and H2O) from the gasification stage to a first heat exchange, wherein the outgoing gases (CO2, N2 and H2O) are cooled, of evaporating water with heat from outgoing gases, of subjecting the steam to heat exchange wherein the steam is heated, of reducing the steam to synthesis gas (S), wherein the synthesis gas (S) is cooled and the air supply to the gasification is heated, of separating the synthesis gas (S) into a hydrogen stream and a carbon monoxide stream, of reacting the carbon monoxide with water steam to carbon monoxide and hydrogen, of separating also these secondary streams into a hydrogen stream and a carbon monoxide stream, and of bringing together the primary and secondary hydrogen stream into a product stream.