The research, led by Gebrehiwot Kunom Hagos of Mekelle University in Ethiopia together with Wondalem Misganaw Golie of the Ethiopian Defense University and Gebremeskel Kahsay Atsbha of Raya University, set out to demonstrate what the authors call a dual-function biorefinery. Rather than treating waste conversion and gas cleaning as separate engineering problems, the team coupled them into a single process chain. Organic waste is first co-digested to produce biogas, and that same gas is then scrubbed through tailored adsorption beds until it approaches the purity of commercial natural gas. The concept is deliberately frugal: every major input, from the feedstock to the sorbent, is a locally generated waste or low-value material.

The feedstock side of the experiment paired cow dung with banana peel, an agricultural residue rich in readily degradable carbohydrates. Anaerobic co-digestion of the two streams was carried out at ambient conditions, and the researchers systematically varied the mixing ratio to find the composition that maximized methane yield. The sweet spot turned out to be a blend of 60 percent cow dung and 40 percent banana peel by volume. Under those conditions the digester produced gas containing 71.23 percent methane, 27.89 percent carbon dioxide, and 1470 parts per million of hydrogen sulfide. That starting composition is typical of agricultural biogas, which is precisely why the team chose it: any upgrading technology that works on this gas should be broadly applicable.

With the raw biogas characterized, attention shifted to the scrubbing stage. The heart of the system is bentonite clay, a naturally abundant smectite mineral whose layered structure and cation-exchange capacity make it a versatile adsorbent. In its raw form, however, bentonite is not especially selective for acidic gases. The researchers modified the clay in two complementary ways. Carbide slag, which consists largely of calcium hydroxide, was used to functionalize the material for hydrogen sulfide capture, exploiting the strong affinity between sulfide species and alkaline calcium sites. A second modification integrated monoethanolamine, a well-known amine absorbent, into the clay matrix to target carbon dioxide. The result is a tailored adsorbent in which the mineral scaffold hosts two distinct chemistries, each tuned to one of the two principal contaminants.

The physical configuration of the adsorption bed matters as much as its chemistry, and this is where the study’s statistical rigor comes in. The team used response surface methodology, a design-of-experiments framework that maps how multiple variables jointly influence an outcome, to optimize the upgrading process. Using a Box–Behnken design implemented in Design-Expert version 13, they explored three numeric factors: clay particle size ranging from 0.1 to 2 millimeters, gas flow rate from 0.1 to 2 liters per minute, and bed height from 10 to 50 centimeters. The responses tracked were the outlet concentrations of methane, carbon dioxide, and hydrogen sulfide, with statistical significance accepted at a probability level below 0.05.

The regression models that emerged from the analysis were strikingly strong. The coefficients of determination reached 99.99 percent for methane, 99.99 percent for carbon dioxide, and 99.80 percent for hydrogen sulfide, meaning the fitted equations explained essentially all of the variation in the experimental data. Such high values indicate that the three chosen factors, and their interactions, capture the behavior of the adsorption column almost completely, which in turn means the model can be used to predict performance across the entire experimental space rather than only at the tested points. For process engineers, that predictability is what turns a laboratory demonstration into a designable technology.

The optimum operating point combined the smallest clay particle size tested, 0.10 millimeters, with a bed height of 30 centimeters and a gas flow rate of 0.10 liters per minute. At those settings the gas leaving the column contained 96.22 percent methane, up from 71.23 percent at the inlet, while carbon dioxide had fallen from 27.89 percent to 3.65 percent and hydrogen sulfide from 1470 parts per million to just 71. The upgraded gas achieved a calorific value of 34.6392 megajoules per cubic meter, a figure that places it firmly in the territory of high-quality biomethane suitable for cooking, electricity generation, and, in principle, injection into gas grids. The trends behind those numbers are physically intuitive: finer particles expose more adsorption surface, a taller bed provides longer contact time, and a slower flow rate gives the gas more opportunity to interact with the reactive sites before breaking through.

What makes the result notable is not merely the purity achieved but the economics implied by the materials involved. Bentonite deposits are widespread and inexpensive, and Ethiopia’s Afar region in particular hosts significant reserves that have already found local industrial applications. Carbide slag is a disposal liability for acetylene plants, and converting it into a gas-cleaning reagent turns one waste stream into the remedy for another. Monoethanolamine is the priciest component, but it is used in modest quantities as an integration agent rather than as the bulk sorbent. Compared with conventional upgrading routes such as water scrubbing, pressure swing adsorption with engineered zeolites, membrane separation, or amine scrubbing in dedicated columns, all of which demand capital equipment and operating expertise, a packed bed of modified local clay represents a dramatically lower barrier to entry for small-scale and rural installations.

The study also situates itself within a broader shift in how biogas is conceptualized. Instead of viewing the digester as a single-purpose machine that turns manure into a mediocre fuel, the dual-function framing treats the whole plant as a biorefinery in which waste treatment, fuel production, and gas purification are integrated stages of one circular process. The digestate left after anaerobic digestion retains fertilizer value, the banana peel that would otherwise rot is converted into energy, and the sorbent bed polishes the product to a standard that unlocks higher-value uses. Each step consumes something the surrounding economy discards, which is exactly the logic that circular-economy advocates have been pressing for in the biogas sector.

Caveats remain, as they do with any laboratory-scale optimization. The experiments were conducted at ambient conditions with controlled flow rates, and real digesters produce gas whose composition and humidity fluctuate with feedstock and season. The longevity of the modified clay, its regenerability, and its performance over extended breakthrough cycles will need to be demonstrated at pilot scale before the approach can be certified for continuous operation. The presence of 71 parts per million of residual hydrogen sulfide, while a reduction of more than 95 percent, may still exceed the tolerance of some sensitive fuel cells and pipeline specifications, suggesting that a polishing stage could be required for the most demanding applications. Even so, the core demonstration stands: a methane content above 96 percent, achieved with ground clay and industrial byproducts, optimized through a transparent statistical framework, and grounded in materials that a rural workshop could plausibly source. If follow-up work confirms durability at scale, the humble mineral underfoot may prove to be one of the cheapest keys yet to making renewable gas genuinely renewable in practice.

Subject of Research: Biogas upgrading by adsorption of hydrogen sulfide and carbon dioxide on modified bentonite clay following anaerobic co-digestion of organic waste

Article Title: Dual-function biorefinery: simultaneous organic waste treatment and biogas quality improvement via tailored clay adsorption

Article References: Hagos, G. K., Golie, W. M., & Atsbha, G. K. (2026). Dual-function biorefinery: simultaneous organic waste treatment and biogas quality improvement via tailored clay adsorption. Clean Technologies and Environmental Policy, 28(10), Article 268. https://doi.org/10.1007/s10098-026-03626-1

Image Credits: AI Generated

DOI: 10.1007/s10098-026-03626-1

Keywords: biogas upgrading, bentonite clay, adsorption, anaerobic co-digestion, hydrogen sulfide removal, carbon dioxide capture, carbide slag, monoethanolamine, response surface methodology, biomethane, circular economy, renewable energy