Modular Biogas CO2 Absorption Risers for Lower-Cost Separation

Resolve Bottlenecks,
Find Innovative Solutions
Generate Solutions

Solution Overview

Problem

Existing biogas separation systems, such as water wash processes, are cumbersome and costly due to the need for large, corrosion-resistant stainless steel vessels and substantial weight, requiring significant capital expenditures.

Innovation Solution

A biogas separation system utilizing a series of absorption risers with inlets and outlets at the top for installation below grade, allowing for flexible configurations in series, parallel, or combined connections, using chemical or biological liquid absorbents to separate carbon dioxide from methane, with optional recirculation and regeneration of the absorbent.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Quantity of substance

If water wash process is used with elevated pressure and reduced temperature, then carbon dioxide solubility in water is enhanced, but substantial vessel height and weight are required

Engineering Contradiction:
Improvecarbon dioxide solubilityVSAvoidvessel weight
Core Design Contradiction:
Quantity of substanceVSWeight of stationary object

Solution Approach 1:

The patent divides the single large water wash vessel into multiple smaller vessels arranged in series. Each vessel provides a portion of the total contact time and absorption capacity, eliminating the need for one extremely tall and heavy vessel while achieving the same carbon dioxide removal efficiency.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

Instead of increasing vessel height vertically, the patent distributes the absorption function across multiple vessels arranged horizontally or in stacked configurations. This transforms the problem from a vertical dimension constraint to a horizontal or modular arrangement, reducing individual vessel weight while maintaining total treatment capacity.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

2Reliability

If stainless steel vessels are used for corrosion resistance, then hydrogen sulfide and carbonic acid corrosion is prevented, but capital expenditure increases

Engineering Contradiction:
Improvecorrosion resistanceVSAvoidcapital expenditure
Core Design Contradiction:
ReliabilityVSEase of manufacture

Solution Approach 1:

By segmenting the system into multiple smaller vessels, the patent reduces the amount of expensive stainless steel required per vessel and overall. Each smaller vessel requires less corrosion-resistant material while the series arrangement maintains the same total corrosion protection capability.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent allows for the use of less expensive materials in the divided vessel system, as the reduced size and distributed configuration enables easier replacement and maintenance of individual vessels, effectively treating them as more replaceable components rather than a single permanent installation.

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

3Quantity of substance

If large volume of absorbent liquid is used, then carbon dioxide absorption capacity is increased, but vessel size and foundation requirements increase

Engineering Contradiction:
Improveabsorbent liquid volumeVSAvoidphysical foundation area
Core Design Contradiction:
Quantity of substanceVSArea of stationary object

Solution Approach 1:

The patent distributes the absorbent liquid volume across multiple smaller vessels rather than concentrating it in one large vessel. This segmentation maintains the total absorbent volume and associated absorption capacity while reducing the footprint and foundation requirements of each individual vessel.

Inventive Principle:
Principle #1Segmentation

Solution Approach 2:

The patent transitions from a single large-volume vessel requiring substantial foundation area to multiple smaller vessels that can be arranged in space-efficient configurations, effectively trading vertical or concentrated horizontal space for distributed space, reducing overall foundation requirements.

Inventive Principle:
Principle #17Another dimension (Dimensionality change)

4Loss of time

If tall vessels are constructed for sufficient contact time, then carbon dioxide absorption is adequate, but system complexity and capital expenditure increase

Engineering Contradiction:
Improvecontact timeVSAvoidvessel configuration complexity
Core Design Contradiction:
Loss of timeVSDevice complexity

Solution Approach 1:

The patent achieves the required contact time by segmenting the absorption process into multiple vessels in series, where each vessel contributes a portion of the total contact time. This modular approach simplifies individual vessel design and construction while maintaining the cumulative contact time needed for adequate carbon dioxide removal.

Inventive Principle:
Principle #1Segmentation

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 system reduces the physical footprint and material costs while enhancing flexibility and efficiency in producing purified methane and carbon dioxide streams, allowing for cost-effective and adaptable biogas separation.

Implementation Method 1

carbon dioxide and hydrogen sulfide are many times more soluble in water than methane... As the biogas rises through the water, the carbon dioxide, hydrogen sulfide, and other water-soluble trace constituents are absorbed into the water

Methodology Applied
Scientific EffectAbsorption (physical): Absorption (physical)

Data Source

PatentUS12528726B2Method and apparatus for treating biogas
Publication Date: 2026.01.20 ENERGY TECH INNOVATIONS LLC
  • US12528726B2 patent drawing
  • US12528726B2 patent drawing
  • US12528726B2 patent drawing

AI summary

A system for separating carbon dioxide from a biogas stream includes a first pipe and a second pipe extending within the first pipe. A first inlet at a first end of the second pipe receives the biogas stream, and a second inlet at a first end of the first pipe receives a liquid absorbent. The biogas stream is dispensed from the second pipe into the first pipe to mix with the liquid absorbent, separating the carbon dioxide from the biogas stream. A first outlet is in fluid communication with the first pipe to deliver a purified biogas stream. A first end of a third pipe extends from the first pipe and a second end of the third pipe extends into a mixed liquid absorbent stream within the first pipe. A second outlet, in fluid communication with the first end of the third pipe, delivers the mixed liquid absorbent stream.