MESSAI collab · UFZ Electrobiotechnology · John-Oliver Gath · draft 8 Oct 2026

Which reactor and process parameters decide microbial electrosynthesis, and by how much

John-Oliver’s PhD (Electrobiotechnology group, UFZ Leipzig, since December 2024) is about characterising, optimising and standardising the bioreactors and process parameters for electrosynthesis by obligately anaerobic acetogens. That is also what the literature lacks: studies report reactors and rates in ways that cannot be compared. MESSAI’s corpus and his standardisation work fit together. We propose to build three things with him.

ProposalNothing is fitted yet, and nothing on this page is a result of John-Oliver’s. The numbers come from MESSAI’s literature corpus (staging database, 8 Oct 2026); the reporting set is MESSAI’s current taxonomy.
  1. A minimum reporting standardThe reactor and process facts a microbial electrosynthesis study must state so another lab can rebuild and compare it. It starts from the set MESSAI already checks.
  2. A harmonised MES datasetRates, potentials and areas on one basis, a precondition for cross-study comparison, not a guarantee of it. Today most pairs cannot be compared; the fixes are listed.
  3. Prediction of MES performanceAcetate rate, titre, faradaic efficiency and energy from reactor and process parameters, with intervals and ranked drivers.

The question the predictor answers

“For this reactor and these process conditions, what acetate rate, titre, faradaic efficiency and energy per kilogram should I expect, how sure are we, and which parameters matter most for this prediction?”

Answers follow MESSAI’s prediction format. Each answer lists the parameters driving it and the evidence behind it. If an input is missing, the predictor would say which one instead of filling in a default. Until the model is fitted, every field is pending.

query    strain = C. ljungdahlii · cathode = carbon felt   (example inputs)
         E_cathode = −0.60 V vs Ag/AgCl (sat. KCl)  →  ≈ −0.40 V vs SHE (25 °C offset; ≈ −0.41 V with the reference at 35 °C) · pH 6.8 · 35 °C
         CO₂ supply = ?  (flow, partial pressure, kLa)
answer   acetate_rate  { value: pending, unit: "g/L/d",  ci_low: pending, ci_high: pending }
         titre         { value: pending, unit: "g/L",    ci_low: pending, ci_high: pending }
         FE_acetate    { value: pending, unit: "%",      ci_low: pending, ci_high: pending }
         energy        { value: pending, unit: "kWh/kg", ci_low: pending, ci_high: pending }
drivers  cathode potential vs SHE · CO₂ supply · current density · cathode area   (ranked: pending)
evidence harmonised MES literature + John-Oliver’s reactor runs (pending)
missing  CO₂ supply  →  named as missing, no default filled in, answer flagged

How this works

The path from a published paper to a number on this page. Each step feeds the next. The first three show what this site holds right now for the papers cited here.

  1. Find the paper

    Partly done

    A paper enters the corpus as a record: DOI, title, authors, journal, date and abstract, taken from Crossref or the publisher.

    • 10 of 16 cited papers with a DOI are in this corpus.
    • Counted in this deployment on Oct 28, 2026.
    • On Oct 8, 2026 some of the papers cited by the protocol chart were added to the staging corpus, as records with no stored PDF and no extracted values. The counts in the first three steps are read from the deployment you are on.
    Open the corpus
  2. Get the full text

    Partly done

    Where the publisher allows it, the PDF is stored and converted to text, tables and equations. Values can also be read from open-access full text without storing the PDF. A paper with neither stays at its abstract: only what the abstract states is available, without its tables or methods.

    • 5 of 10 have a stored PDF.
  3. Extract values with their evidence

    Partly done

    A language model reads the text and tables and writes every value as one row: parameter, number, unit, the conditions it was measured under, the quote it came from, a confidence and the extractor version.

    • 5 of 10 have extracted values (239 distinct facts in all; a value extracted twice counts once).
    • These counts cover the papers the protocol chart cites. The readiness map below counts every paper in its scope (staging database, Oct 13, 2026).
  4. Harmonise

    Partly done

    Each row is mapped to a canonical parameter where a rule matches, so “power density” means one thing across papers, and its unit is converted to SI. Conversion is not comparability: the species, the reference electrode and the area or volume basis must match too. Those checks are incomplete, so some rows that cannot be compared still reach the models.

    • Part of the distinct facts in the MES scope are already harmonised and flagged as modelable; the share is given in the section “What blocks comparison today” (staging database, Oct 13, 2026). The fixes for the problems listed there are still to do.
    Open the parameters
  5. Model and predict

    Partly done

    Models are fitted on harmonised rows only: first the effect of one parameter inside each study, then pooled across studies. A prediction returns a value, a unit, an interval, a confidence and its source. The aim is that a missing input is named, never filled with a default; some MESSAI predictors still fill one today, such as an applied voltage of 0.6 V for an MEC.

    • Most of the methods already exist in MESSAI. The predictor for MES is still to be built, and nothing is fitted yet.
    Read how the predictions are made
  6. Check it

    Links listed

    The papers behind the protocol chart are listed below with a link to each publisher. The chart’s steps are steps of the shared protocol graph. Signed-in readers can comment on this page. A listed paper is a pointer for checking, not a check MESSAI has made.

    Go to the papers

Correlation-readiness map

Rows are 12 groups of reactor and process parameters, columns are 7 groups of outcomes. Each cell counts the papers in the microbial-electrosynthesis scope that report both, and how many of those have an SI-converted value for both (“usable”). This is paper-level co-reporting, not an effect estimate: it shows where a correlation could be quantified today and where it cannot. Select a cell for what blocks it and how within-study variation would quantify the effect.

No paper reports both15Reported, none usable321–2 usable253–5 usable76 or more usable5of 84 pairs

Each cell: papers with both values usable / papers reporting both. “Usable” here only means an SI-converted value exists for both, from any rows of the paper; reference electrode, species, rate basis and same-condition pairing are not checked. Material and membrane cells read zero by construction: they are categories, which have no SI value.

Parameter groupAcetate rateAcetate titreFaradaic / Coulombic efficiencyOther productsH₂Energy efficiencyCell voltage
Electrode potential (cathode or applied)
Current density
CO₂ supply
Electrode area
Cathode material
Membrane
Reactor volume
Hydraulic retention time
pH
Temperature
Electrolyte conductivity
Inoculum / strain

Paper-level co-reporting, not an effect estimate: a paper that used a single potential reports it but adds nothing to the effect of potential. “Usable” means both values have an SI-converted value; it does not mean the value is right. Snapshot: staging database, Oct 13, 2026, query scripts/collab/measure-mes-readiness.sql.

What blocks comparison today

The map shows how few pairs are usable. This section says why, from the same staging snapshot: the scope, the key parameters, and six harmonisation problems, each with a proposed fix.

Papers in scope
409
With extracted values
118
Distinct facts
4,044

from 6,066 live rows

Modelable facts
886

22% of the facts

Scope: papers whose title or abstract mentions electrosynthesis, plus papers with an acetate production rate or a CO₂ faradaic efficiency row. Live papers only (not archived, merged, hidden or retracted). Staging database, Oct 13, 2026.

Canonical slugFactsPapersUsable factsWhat the snapshot shows
acetate_production_rate2593316Only the exact strings g/l/d and mg/l/d convert (16). Of the rest, 42 are volumetric rates in other spellings, 62 areal (g/m²/d, deferred), 117 molar (mmol/m²/d, mM/d, µmol/cm²/h, dropped) and 22 something else (a concentration, a percentage, a per-biomass rate).
faradaic_efficiency615031
applied_potential23798219184 facts carry a bare V or mV with no reference electrode in the unit, the name or the conditions. Ag/AgCl, SCE and SHE values are pooled with factor 1.0.
cathode_potential943966Same reference-electrode pooling.
formic_acid_production_rate126274
butyrate_production_rate49140
acetate_yield611011

Distinct facts on live rows of live papers, corpus-wide: a value extracted twice counts once. 36% of live rows corpus-wide repeat a fact already counted. The map above counts papers.

Six problems, one per cause

  1. (a) Unit spellings that don’t match the conversion table

    One volumetric rate is written g l-1 d-1, mg·l−1·d−1 or kg m^-3 day^-1. All three are volumetric mass rates, but only the exact strings g/l/d and mg/l/d are in the table, so the rest never reach an SI value. 16 of 259 acetate-rate facts convert, and 42 more are volumetric rates in other spellings.

    Proposed fix. Add the spellings to the conversion table as aliases of g/L/d, once, instead of fixing rows one by one.

  2. (b) Areal rates are left unconverted on purpose

    62 acetate-rate facts are per electrode area (g/m²/d). They are not converted to the volumetric g/L/d, because that needs the electrode area and the liquid volume of each reactor. They need a parameter of their own and must never be pooled with volumetric rates.

    Proposed fix. A separate areal-rate parameter; convert between the two only where the area and the volume are both reported.

  3. (c) Molar rates are dropped although the molar mass is known

    117 acetate-rate facts are molar (mmol/m²/d, mM/d, µmol/cm²/h) and are dropped. Acetic acid is 60.05 g/mol and the acetate ion 59.04 g/mol, 1.7 % apart, so a molar rate converts to a mass rate once the paper’s species basis is known. The area or volume basis still has to be kept (see b).

    Proposed fix. Convert molar to mass rates with the species’ molar mass, and keep the original unit and basis next to the result.

  4. (d) Reference electrodes are not converted

    Potentials against Ag/AgCl, SCE and SHE are pooled with factor 1.0, a hidden 0.2–0.24 V error. 184 applied-potential facts state no reference at all, and a cell voltage is sometimes mixed in with an electrode potential. Only a potential with a stated reference can be put on one scale.

    Proposed fix. Convert to SHE where the reference is stated (ConditionSet already has the reference-electrode columns), flag the rest, and keep cell voltage a parameter of its own.

  5. (e) One quantity, several spellings

    The same quantity is stored under several names, so it never pools. In the electrosynthesis scope, current density sits in five slugs and applied potential in two:

    Current densityFacts
    current_density_areal70
    current_density29
    currentDensity29
    current_density_max7
    current_density_volumetric5
    Applied potentialFacts
    applied_potential23
    appliedPotential5

    Proposed fix. One canonical parameter per quantity and basis, with the other spellings kept as aliases.

  6. (f) The “MES” label means two things

    MES stands for both “microbial electrochemical system” and “microbial electrosynthesis”. 3,382 papers are labelled MES, but only 397 mention electrosynthesis, so the label cannot select the electrosynthesis papers.

    Proposed fix. Separate the system type (microbial electrosynthesis) from the name of the field in the taxonomy, then re-classify.

Why the reference electrode matters for comparing potentials

A potential means something only against a stated reference. Saturated Ag/AgCl (sat. KCl) sits at +0.197 V and SCE at +0.241 V against the standard hydrogen electrode (SHE). At pH 7, 25 °C and standard activities, CO₂ → acetate has a formal potential of about −0.28 V vs SHE and H₂ evolution about −0.41 V, a window of about 0.13 V. A reference error of 0.2–0.24 V is larger than that window, so the same reported number can sit on either side of the H⁺/H₂ potential. Which side it sits on does not by itself show the electron-uptake route: telling direct from H₂-mediated uptake needs H₂ measurements, abiotic and open-circuit controls and organism-specific evidence.

Reference or reactionKindE vs SHEV
Saturated calomel electrode (SCE)Reference electrode+0.241
Ag/AgCl, saturated KClReference electrode+0.197
Standard hydrogen electrode (SHE)Reference electrode0
CO₂ → acetateReaction at pH 7−0.28
H₂ evolutionReaction at pH 7−0.41

A reporting standard for MES reactors

A minimum reporting standard is what lets a reader rebuild a run and compare it with another lab’s. John-Oliver’s work on characterising and standardising reactors is the missing input. Below: what MESSAI requires of an electrosynthesis study today, then what reactor standardisation would add.

MESSAI scores every paper against a required set for its study type. For microbial electrosynthesis (taxonomy v2.0.0) that set has 13 conditions and 6 outcomes, plus 5 methodology and 7 equipment items. In MESSAI’s corpus coverage analysis every study type is also checked against a baseline of 10 items.

Conditions

ItemImportanceWhy it is required
Applied voltage / poised potentialCriticalThe driving input of a driven cell (MEC, MES, poised-potential biofilm study). Yield and efficiency are meaningless without the applied condition — and a whole-cell voltage is not interchangeable with a poised half-cell potential.
Potential reference basis (vs SHE)HighElectrode potentials are only comparable against a stated reference. Ag/AgCl (3 M KCl) sits ~+210 mV vs SHE and SCE ~+241 mV — omitting the basis silently shifts every half-cell potential by hundreds of millivolts.
Electrode surface areaCriticalNeeded to turn current or power into a density, and to convert a density to another area basis. Without it, a reported density can't be checked or re-normalized.
Cathode material + catalystHighDominates the oxygen-reduction overpotential in an MFC and the hydrogen-evolution overpotential in an MEC. Pt loading, MnO2, and a biocathode are entirely different cells.
Gas supply / sparging regimeCriticalFor electrosynthesis the CO2 feed is the substrate; for an air cathode the aeration regime sets the oxygen availability. Composition, rate and whether sparging is continuous all change the result.
Membrane / separatorHighSets ion-transport resistance and crossover. Nafion 117, a cloth separator, and no separator at all produce different internal resistances and different coulombic efficiencies.
Anolyte / catholyte pHHighSets the Nernst-potential offset and the biofilm health envelope. Anode and cathode pH diverge during operation, so a single 'pH 7' for a two-chamber cell is under-reporting.
Buffer type + concentrationHighBuffer capacity, not bulk pH, governs local proton accumulation at the biofilm. 50 mM vs 200 mM phosphate changes power substantially at identical starting pH.
Operating temperatureHighDrives the Arrhenius factor on biofilm kinetics and on ohmic resistance. A 10 °C shift moves power meaningfully; 'room temperature' is not a temperature.
Reactor / working volumeHighRequired for any volumetric normalization, for loading rates, and for HRT. 'Working volume' and 'total volume' differ by the headspace and are routinely conflated.
Inoculum sourceHighAnaerobic digester sludge from two plants gives two different communities and two different startup curves. Pure culture vs mixed culture is a categorical difference in what the result means.
Run duration / number of cyclesHighHow long the system ran before the reported number was taken. A day-3 peak and a day-90 steady state describe different systems.
Replication (n) + variance reportingCriticalHow many independent reactors the number came from, and whether the spread quoted is SD, SE or a range. A single-reactor result presented with error bars from triplicate measurements on one reactor is pseudo-replication.

Outcomes

ItemImportanceWhy it is required
Faradaic efficiencyCriticalHow much charge went to the target product versus side reactions. Without it you can't tell how much of the titre came from electrode current rather than from other electron or carbon sources.
Product titre + production rateCriticalAmount and rate of the value-added product — the point of an electrosynthesis run. Titre alone hides whether it took three days or three months.
Product selectivity / distributionMediumWhich product dominates. A single titre without the side-product distribution hides where the rest of the carbon went.
Current densityHighAnchors the polarization behaviour and cross-checks the power claim — power without current hides whether the gain came from current or from voltage.
Energy efficiency / electrical inputHighFor a driven cell the electricity consumed is half the story. Efficiency relative to electrical input (and to substrate) decides whether the process is net-positive.
Uncertainty on the headline numberCriticalThe reported value with its spread and n. Without them, a reader can't tell whether two papers differ by more than their measurement noise. This is uncertainty ON THE ESTIMATE (±, SD, SE, CI, n): a one-at-a-time sensitivity sweep over plausible inputs is a different claim and belongs to sensitivity-analysis, not here.

Also scored: Methodology. Liquid product quantification, Gas quantification method, How the density was computed, How electrode area was determined, and Statistical treatment.

Also scored: Equipment & tools. Potentiostat / electrochemical workstation, Reference electrode, Liquid analysis instrumentation, Gas analysis + measurement hardware, Pumps + flow control, Temperature + pH control hardware, and Reactor hardware specification.

Proposed additions from reactor standardisation

Proposed

Seven items that reactor characterisation and standardisation would add. They are proposals for John-Oliver to correct: none is in the scorer yet. “Sharpens” means a current item asked more precisely; “New” means nothing like it is in the set.

Proposed itemWhy it mattersWhat to reportWhere it lands in MESSAI
Gas–liquid mass transfer (kLa) and CO₂ partial pressureSharpens “Gas supply / sparging regime”CO₂ is the substrate and it dissolves slowly, so its supply can limit acetate formation before the electrode does. The current gas-supply item asks for composition and rate, not for the transfer the liquid actually sees.kLa and how it was determined; CO₂ partial pressure in the headspace; gas flow; mixing (stirring or recirculation).The CO₂ sparging rate is a column (co2SpargingRateMLMin). kLa and partial pressure would be new columns.
Electrode spacingIn the baseline as “Electrode spacing”, not named for MESThe ionic path between cathode and counter electrode sets the ohmic loss, so cell voltage and energy per kilogram of acetate depend on it. It is already checked for every study type, but not named for MES.Distance between the cathode and anode surfaces, and the position of the membrane between them.Already a column (electrodeSpacingMM).
Specific and projected cathode area, with the basis statedSharpens “Electrode surface area”Areal and volumetric rates convert into each other only if both the projected area and the specific area (per volume of catholyte) are known, and it is clear which of the two the rate is divided by. This is problem (b).Projected cathode area (cm²), specific area (m² per m³ of catholyte), and which of the two a rate or current density is normalised to.Projected area is a column (cathodeAreaCM2). cathodeAreaBasis records whether that area was stated or computed from dimensions, not whether it is projected or specific. The specific area, and which area a rate uses, would be new.
Catholyte volume against reactor volumeSharpens “Reactor / working volume”A volumetric rate depends on which volume it is divided by: the catholyte, the whole liquid, or the reactor with its headspace. Working volume and total volume are routinely conflated.Catholyte volume, total liquid volume, reactor volume including headspace, and which one the rate uses.Already columns: cathodeChamberVolumeML, workingVolumeML, totalVolumeML and volumeBasis, which records how the total volume was derived. No column yet records which volume a rate is divided by.
Current distribution at the cathodeNewA poised potential is controlled at one point. On a large or three-dimensional cathode the potential, and so the local current, varies over the surface, so the same setpoint in two reactors is not the same condition.Cathode geometry and orientation, counter-electrode position, where the reference electrode sits relative to the cathode (for example a Luggin capillary), and any evidence of uniformity.Reference-electrode type and location are columns (referenceElectrodeLocation). Geometry-level detail would be new.
Run duration and stabilitySharpens “Run duration / number of cycles”A rate averaged over the start-up and one averaged over a stable period are different quantities. How long the reactor ran before the number was taken, and whether it held, decide what the number means.Days to steady state, the window the reported value is averaged over, and whether rate and efficiency held or decayed over the run.The scorer asks for run duration today. operationalPhase on the condition set separates start-up from steady state.
Inoculum and strain; biofilm or planktonicSharpens “Inoculum source”A pure culture and a mixed community mean different things, and so does whether acetate is made by a biofilm on the cathode or by cells in suspension.Strain or community with its source and collection number, pure or mixed culture, growth mode (biofilm, planktonic or both), and a biomass measure where available.Inoculum source is in the current set. Organisms already have fields: a per-paper organism table with rank and abundance, and isPureCulture and dominantOrganism on the condition set. Growth mode would be new.

Reactor descriptions land in ReactorGeometry, a typed table with more than fifty columns (chambers, electrodes with area and area basis, membrane, reference electrode, volumes, gas handling), not in free text. A checklist item that is not a column there yet is the gap to close with the reactor and run template.

How MESSAI turns this into predictions

MESSAI already runs this pipeline on the bioelectrochemistry corpus. For MES it needs the harmonisation fixes above, a parameter set and his reactor and run data. The steps run in this order because each one feeds the next.

  1. Within-study effects

    Exists in MESSAI

    For each study, estimate how one parameter moves an outcome while the others are held fixed: cathode potential on acetate rate, CO₂ supply on faradaic efficiency. This is the cleanest evidence for a trend: differences between labs drop out, though confounders inside a study, such as run order or biofilm age, remain. MESSAI fits these as population-level Bayesian effects and shows them in the lab’s sensitivity chart (for example, hydraulic retention time → COD removal in wastewater treatment, which has not converged yet). Runs that vary one parameter at a time are the ideal input; which ones he has is an open question for him.

  2. Cross-study pooling

    Exists in MESSAI

    Pool the same effect across MES papers with a hierarchical meta-analysis (MESSAI’s meta-analysis forest plots). This answers whether an effect of potential or CO₂ supply holds for other strains, reactors and labs, and how much it varies between studies. It works only on values on one basis, which is what the harmonisation fixes are for.

  3. Correlation structure between parameters

    Exists in MESSAI

    Some parameters move together: a more negative cathode potential raises current density, and the area and volume used fix which basis a rate is on. MESSAI’s learned dependency graph and knowledge graph record such links, so the predictor doesn’t count one effect twice. Correlation across studies isn’t causation, so causal claims rest on step 1.

  4. Compact laws by symbolic regression

    Exists in MESSAI

    MESSAI already uses symbolic regression (PySR) to search for short equations between parameters. For MES the target is a readable law such as acetate rate = f(cathode potential vs SHE, CO₂ supply, current density, cathode area) that a researcher can test, rather than a black box.

  5. Predictor with intervals and drivers

    To build for MES

    A hierarchical model with study as a random effect, using the effects from steps 1–4 as priors and his reactor and run data as the core data. His own studies would be left out of those priors, so his runs are not counted twice. It would return each prediction with an interval and a ranked list of the parameters driving it. The intervals would still need calibrating on held-out studies: MESSAI’s served predictors do not return calibrated intervals yet.

    outcome ~ f(E vs SHE, j, CO₂ supply, kLa, pH, T, cathode, area, volume, strain, …) + (1 | study) + residual GP
    To be validated by
    leaving one study out at a time. The real test is predicting another lab’s results, not interpolating within one reactor.
    Planned guardrail
    outside the conditions covered by data, the answer is flagged as an extrapolation; a wider interval alone would not make it reliable

Protocol

The microbial-electrosynthesis methodology as a graph of steps, from the medium and the cathode to the electron balance and the acetate rate. Click a step for its setpoints, readouts, precautions and sources. Left to right is execution order, and every step links to the full /protocols graph. A selected step also shows which items of the reporting standard it records.

Loading the protocol graph…

Click a step for its measurements, equipment, precautions and references. Drag to pan.Open the full protocol graph →

Models

The cell the predictor is about, the hydrogen route acetogens can use, and the downstream step that turns the acids into fuel. All are shared MESSAI 3D models; drag to orbit.

The subject

Microbial electrosynthesis cell

Illustrative MES cell: an abiotic Ti/MMO anode that oxidises water, a cation-exchange membrane, and a graphite-brush biocathode carrying an acetogen biofilm. CO₂ goes in at the cathode, acetate comes out. The geometry is illustrative, not John-Oliver’s reactor.

Microbial electrosynthesis cell

For the Kolbe step see the page for Max Pohl. More models are in the lab.

Cathode microstructure: inputs to the reactor model

A reactor model of a 3D biocathode needs five numbers per electrode. Porosity and permeability set how catholyte and dissolved CO₂ flow through the electrode; specific surface sets how much area the biofilm can colonise per volume; tortuosity sets effective diffusion; thickness sets the depth the current has to reach. A pore-scale simulation of the real electrode could supply all five, with a range, in place of the textbook values below.

Illustrative literature ranges: not measured, not simulated

Graphite granule bed

pore-scale simulation (proposed)
PropertyValue · Range
Porosity0.450.38–0.52
Tortuosity1.51.3–2
Specific surface1,800m²/m³800–3,600
Permeability7.00e-9m²1.00e-9–4.00e-8
Thickness50mm20–200

Packed bed of 1 to 4 mm granules; specific surface is the geometric 6(1-ε)/d_p (BET micropore area is ~10⁶× larger and not resolved here); permeability from Kozeny-Carman; thickness is bed depth; illustrative

Carbon felt

pore-scale simulation (proposed)
PropertyValue · Range
Porosity0.930.9–0.96
Tortuosity1.81.4–2.6
Specific surface30,000m²/m³10,000–100,000
Permeability3.00e-10m²1.00e-10–1.00e-9
Thickness5mm4–6

Manufacturer datasheet range (SGL / Sigracell felt series); specific surface is a geometric estimate from fibre diameter; illustrative

Graphite fibre brush

pore-scale simulation (proposed)
PropertyValue · Range
Porosity0.960.95–0.98
Tortuosity1.51.2–2
Specific surface16,000m²/m³5,000–50,000
Permeability1.00e-8m²1.00e-9–1.00e-7
Thickness30mm20–100

Typical graphite fibre brush range; specific surface quoted per brush volume; thickness is the brush envelope diameter and varies widely by design; illustrative

How a pore-scale simulation would deliver these numbers: the lab demo.

Papers behind this page

Every paper the protocol chart cites, with what it is cited for and where you can check it. Each row links the publisher and, if this site holds the paper, its corpus record.

16 works cited · 16 with a DOI · 10 in this corpus

PaperCited forStepsCheck itIn the MESSAI corpus
Marshall et al. 2012, Appl. Environ. Microbiol.
  • brewery-waste community on a graphite cathode with CO₂ as the only carbon source
  • a brewery-waste community on a granular graphite cathode
  • granular graphite cathode
  • 2-BES stops methanogenesis in a brewery-waste community
  • Acetobacterium dominated when acetogenesis dominated
  • cathode poised at −590 mV vs SHE
  • acetogenesis above 4 mM/d per cathode liquid volume
Prepare the mineral medium and CO₂ supply · Select the biocatalyst · Choose and prepare the cathode · +4 morePublisherNot in this corpus
Nevin et al. 2010, mBio
  • Sporomusa ovata biofilms on graphite cathodes reduce CO₂ to acetate
  • graphite cathodes for Sporomusa ovata
  • Sporomusa ovata biofilms on graphite cathodes
  • products accounted for more than 85 % of the consumed electrons
Select the biocatalyst · Choose and prepare the cathode · Inoculate the cathode chamber · +1 morePublisherNot in this corpus
Jourdin et al. 2016, ChemElectroChemBiologically Induced Hydrogen Production Drives High Rate/High Efficiency Microbial Electrosynthesis of Acetate from Carbon Dioxide
  • biologically induced H₂ and (99 ± 1) % electron recovery into acetate
  • (99 ± 1) % electron recovery into acetate
Poise the cathode potential · Close the electron balancePublisherCorpus record
Abstract
yes
Full text
stored; publisher only (licence)
Values
53 facts extracted
Harnisch et al. 2024, Trends Biotechnol.
  • pure cultures in MES
Title only
Select the biocatalystPublisherNot in this corpus
Boto et al. 2023, Green Chem.Microbial electrosynthesis with Clostridium ljungdahlii benefits from hydrogen electron mediation and permits a greater variety of products
  • Clostridium ljungdahlii and H₂ electron mediation
Select the biocatalystPublisherCorpus record
Abstract
yes
Full text
stored; publisher only (licence)
Values
48 facts extracted
Aryal et al. 2017, Green Chem.An overview of cathode materials for microbial electrosynthesis of chemicals from carbon dioxide
  • cathode material and its interaction with the biocatalyst in MES
Choose and prepare the cathodePublisherCorpus record
Abstract
yes
Full text
not stored
Values
none extracted
Giddings et al. 2015, Front. Microbiol.Simplifying microbial electrosynthesis reactor design
  • simplified reactor design
Title only
Assemble a divided reactor with a membranePublisherCorpus record
Abstract
yes
Full text
stored; publisher only (licence)
Values
55 facts extracted
Deutzmann et al. 2025, Bioresour. Technol.
  • improved reactor design and productivity
Title only
Assemble a divided reactor with a membranePublisherNot in this corpus
Madjarov et al. 2017, J. Power SourcesRevisiting methods to characterize bioelectrochemical systems: The influence of uncompensated resistance (iR-drop), double layer capacitance, and junction potential
  • uncompensated resistance, double-layer capacitance and junction potentials in bioelectrochemical measurements
Title only
Convert potentials to SHEPublisherCorpus record
Abstract
no
Full text
not stored
Values
none extracted
Patil et al. 2015, Environ. Sci. Technol.Selective Enrichment Establishes a Stable Performing Community for Microbial Electrosynthesis of Acetate from CO₂
  • selective enrichment establishes a stable performing acetate community
Title only
Enrich the biocathodePublisherCorpus record
Abstract
yes
Full text
stored; publisher only (licence)
Values
19 facts extracted
Marshall et al. 2013, Environ. Sci. Technol.
  • long-term operation improves acetate production
Title only
Enrich the biocathodePublisherNot in this corpus
Blanchet et al. 2015, Energy Environ. Sci.
  • hydrogen route at −0.36 V and −0.66 V vs SHE with a sludge inoculum
Poise the cathode potentialPublisherNot in this corpus
Karthikeyan et al. 2019, J. Ind. Microbiol. Biotechnol.Microbial electron uptake in microbial electrosynthesis: a mini-review
  • mini-review: direct and mediated electron uptake in MES
Poise the cathode potentialPublisherCorpus record
Abstract
yes
Full text
not stored
Values
none extracted
Jourdin et al. 2019, Bioresour. Technol. Rep.Enhanced selectivity to butyrate and caproate above acetate in continuous bioelectrochemical chain elongation from CO2: Steering with CO2 loading rate and hydraulic retention time
  • steering butyrate and caproate with CO₂ loading rate and HRT
Title only
Operate with a continuous CO₂ supplyPublisherCorpus record
Abstract
yes
Full text
not stored
Values
none extracted
Ganigué et al. 2015, Chem. Commun.Microbial electrosynthesis of butyrate from carbon dioxide
  • butyrate from CO₂
Operate with a continuous CO₂ supplyPublisherCorpus record
Abstract
yes
Full text
not stored
Values
none extracted
Fruehauf et al. 2020, Biotechnol. J.Microbial Electrosynthesis—An Inventory on Technology Readiness Level and Performance of Different Process Variants
  • key process indicators to report for MES
Close the electron balancePublisherCorpus record
Abstract
yes
Full text
stored; publisher only (licence)
Values
64 facts extracted

Corpus read from this deployment on Oct 28, 2026.

“Title only”: the claim is what the paper’s title says. We have not read its text for this claim.

“Values” counts the distinct facts the extractor read from the paper, not only the ones cited here: a value written twice (same name, value, unit, quote and conditions) counts once. A paper whose full text was never read has none; values read from open-access text count even when no PDF is stored.

Our to-dos (MESSAI)

In priority order. Estimates are rough and assume one person part-time.

  1. Fix MES harmonisation (a)–(e)~1–2 weeksNot started

    Unit-spelling aliases, a separate areal-rate parameter, molar-to-mass conversion, reference-electrode conversion to SHE, and one canonical parameter per quantity. Staging first, a dry run, then prod. Every cross-study comparison on this page depends on it.

  2. MES taxonomy fix~2–3 daysNot started

    Separate the system type “microbial electrosynthesis” from the field name “MES”, then re-classify, so the 397 papers that mention electrosynthesis can be selected by label.

  3. Use-case spec for microbial electrosynthesis~2–3 daysNot started

    A microbial-electrosynthesis spec in @messai/use-case-specs, after the nitrogen one: scope, the parameters and outcomes of the map with canonical names and units, plausible ranges, and potentials stored against SHE. To be sent to John-Oliver to correct.

  4. MES section of the minimum-reporting checklist~1 week, with himNeeds John-Oliver

    Turn the proposed additions into a checklist section, co-written with him, and add it to the reproducibility taxonomy so the scorer checks it.

  5. Re-measure this map after the fixes~1 dayAfter the fixes

    Re-run scripts/collab/measure-mes-readiness.sh (read-only, staging) and compare: which pairs gained usable papers, which stay empty.

  6. Within-study effects and predictor v1~3–4 weeksWaiting on data

    Encode his runs and the harmonised literature as within-study effects, pool them, and fit the hierarchical model with conformal intervals, ranked drivers and a leave-one-study-out validation report, including where it fails.

  7. Reactor and run template aligned with ReactorGeometry~3–4 daysNeeds his parameter list

    A CSV template whose columns match ReactorGeometry and the run conditions (area and volume with their basis, reference electrode and offset against SHE, gas supply, run duration), so his runs land with full provenance.

  8. Measurement upload~1 week (roadmap)Planned 21 Nov 2026

    The upload route (roadmap C3-M1) so lab runs land in the database with “measured” provenance.

  9. In-app what-if~3–4 daysLater

    /collab/gath in English and German with parameter inputs, a prediction with interval, drivers and the live readiness map.

Deliverables to UFZ

L0 is the day John-Oliver’s parameter list arrives, T0 the day his reactor and run data arrive. Nothing is promised before the data exists; the harmonisation fixes and the reporting-standard draft do not need it.

  1. This weekThis page and the proposed reporting items

    The readiness map, what blocks comparison and the proposed additions to the reporting set, for him to correct, with the open questions below.

  2. L0 + 2 weeksMES parameter set v1

    Canonical names and units for the parameter and outcome groups of the map, aligned with his list, with potentials stored against SHE and the rate basis stated.

  3. In ~2 weeks, no data neededHarmonisation fixes and a re-measured map

    Fixes (a)–(e) on staging, then the readiness map measured again: which pairs gained usable papers.

  4. T0 + 1 weekHis runs encoded

    Within-study effects from his runs in the harmonised format, with the reactor and run template filled, or a note on what doesn’t fit.

  5. T0 + 4 weeksReadiness map with numbers

    Effect size, interval and number of studies for each filled pair; empty pairs ranked by importance.

  6. T0 + 6 weeksPredictor v1 and validation

    Predictions of acetate rate, titre, faradaic efficiency and energy with intervals and drivers, tested by leaving one study out at a time.

  7. T0 + 8 weeksReporting-standard section, interactive page, methods note

    The MES section of the checklist co-written with him, the prediction tool in MESSAI, a co-authored methods note draft, and the dataset on Zenodo with a DOI if UFZ agrees.

What we ask of John-Oliver and UFZ

  • His parameter list (L0): which reactor and process parameters he records or standardises, with the units and the basis he uses.
  • Reactor and run data (T0), including runs that failed or stopped early, in our CSV template, and any runs that vary one parameter at a time.
  • A check of the proposed reporting items and of the blocked cells in the map.
  • 30 minutes every two weeks to review results, an agreement on data terms and authorship, and a pointer to whoever coordinates data standards in SPP 2240, if anyone does.

Open decision

Which model should answer lab-design chat?

Lab-design answers take about 50 seconds today. A smaller model answers the same questions in about 19 seconds, for about 3% of the cost, but looks up the corpus less often. We would like your view on which matters more for your work.

Median time per answer
Claude Haiku 5.519 s
Claude Sonnet 4.6Current50 s

looking up papers and datawriting the answer

MeasureClaude Haiku 5.5Claude Sonnet 4.6
Time per answer (median)19 s50 s
First visible activity2.2 s2.4 s
Writing the final answer10.6 s33.7 s
Corpus look-ups per answer47
Answer length (tokens)3,0262,346
Estimated cost per answer$0.007$0.21

What the answers looked like

  • Both

    Both models cited papers from the corpus and said plainly when the evidence was thin.

  • Sonnet 4.6

    Split power density by the area it is normalised to (anode, cathode, membrane) and warned against comparing across bases.

  • Haiku 5.5

    Gave a direct estimate (100–150 mW/m², anode area) from a few acetate papers and flagged it as preliminary.

  • Sonnet 4.6

    Added a section on mechanisms that was general knowledge rather than drawn from the corpus.

Read for 2 of the 10 question pairs only.

The options

  1. 1Keep Sonnet 4.6Most careful with units and bases. Answers stay at about 50 seconds.
  2. 2Haiku 5.5 for lab-design onlyLab answers in about 19 seconds; general questions keep Sonnet.
  3. 3Haiku 5.5 everywhereFastest and cheapest. Every answer relies on a model that looks up the corpus less often.

Which would you pick, and is there a question you would want us to test both models on? Reply in the comments on this page or at founders@messai.io.

Method: 10 lab-design questions per model, sent in alternating order on Oct 26, 2026; no answer fell back to another provider. Times are measured on the server and exclude your network. Prices are the AI Gateway list prices; cost per answer is an estimate from median token counts with 81% of input read from cache.

Open questions for John-Oliver

  1. Which rate basis is primary: volumetric (g/L/d) or areal (g/m²/d)? Which of the two lets two reactors be compared?
  2. Potentials against which reference? SHE, or a named reference electrode, and with which KCl concentration? Is it stated for every run?
  3. Which acetogens and which cathode mode? For example C. ljungdahlii or S. ovata; fixed potential, galvanostatic, or H₂-mediated.
  4. How is CO₂ supplied and measured? Flow, partial pressure, kLa: which does he control and which does he report?
  5. What makes reactors comparable across labs? Which geometry and process parameters would he fix in a standard, and which may vary?
  6. Does SPP 2240 have a shared data standard or reporting template that this work should follow?
  7. Would he co-own the MES section of the checklist, as co-author of the standard?

Related: Max Pohl · Kolbe electrolysis · Benjamin Korth · collaboration · Lab · Meta-analysis

John-Oliver Gath: UFZ staff page (ufz.de/index.php?de=51894), B.Sc./M.Sc. biochemistry at FSU Jena, PhD topic and link to the DFG priority programme SPP 2240 eBiotech from his UFZ profile; co-author of the ISMET 2026 S15 talk “MES research as a freestyle stage of the Tour de France” (with Miriam Rosenbaum et al.). MESSAI figures: staging database, Oct 13, 2026, from scripts/collab/measure-mes-readiness.sql (snapshot in this page’s folder, readiness-snapshot.json). Reporting set: MESSAI reproducibility taxonomy v2.0.0 (apps/web/src/lib/reproducibility/taxonomy.json). Reference-electrode offsets and the potentials of the two reactions are standard tabulated values at 25 °C. Models, equations and estimates on this page are proposals. Prepared by MESSAI, draft of 8 Oct 2026.

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