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PSA Biogas Upgrading Sizing

CMS / 13X / 4A · Yang & Ruthven PSA · 40 CFR 80.1426 · LCFS slip CO₂e

PSA cycle-based sizing
Sizes a pressure-swing-adsorption unit to upgrade raw biogas (35–50% CO₂) to pipeline-quality RNG (≥96% CH₄), compute the methane-slip CO₂e (a major CARB LCFS pathway-CI driver), and estimate compression power + OPEX. Recovery defaults by bed count: 2-bed 80% / 4-bed 93% / 6-bed 96.5% / 8-bed 98.5%. Off-gas combustion efficiency: flare 95% / RTO 99.5%.

Feed Biogas

scfm
%
Landfill 45–55, dairy 55–65, WWTP 60–65, food waste 55–70.
%
Balance = CO₂; LFG has higher N₂ than dairy.
°C
psig

PSA Cycle & Pressures

psig
Industry typical 80–150 psig (~6–10 bar).
psia
Atmospheric typical (VSA uses sub-atm).
beds
2 legacy / 4 mid / 6–8 modern RNG / 10–12 premium.
min
%
Auto-set by # beds; override for vendor spec.
%
%

Adsorbent

kg CO₂/kg
At ~6–7 bar adsorption / ~1 bar regen.
kg/m³
$/kg
years

Compression & Off-gas

%
%
$/kWh

Engineering Basis

  • Cycle-based sizing: M_bed = (CO₂_load_per_min × t_ads_step) / WC; one bed adsorbing at all times in N-bed synchronous PSA.
  • Recovery vs slip: 2-bed 80% / 4-bed 93% / 6-bed 96.5% / 8-bed 98.5% — bed count drives recovery via pressure-equalization opportunities.
  • Working capacities: CMS 0.10 / 13X 0.15 / 4A 0.08 / AC 0.12 kg CO₂/kg at 6–7 bar adsorption.
  • Methane slip CO₂e: (1−η_recovery) × CH₄_feed × (1−CE_offgas) × GWP_CH4 — major CARB LCFS pathway CI driver.
  • Compression: isentropic W = c_p·T·[(P₂/P₁)^((γ−1)/γ) − 1] for γ=1.30 biogas; η_comp × η_motor losses.
  • Off-gas combustion: flare 95% / RTO 99.5% / RNG engine 98.5% / vent 0%.
  • Standards: Yang/Ruthven PSA, GPSA 14e §17, 40 CFR 80.1426 (RFS2 D3), CARB LCFS §95488, IPCC AR6.

Learn the Theory

Understand CO₂ upgrading technologies, PSA vs membrane vs amine processes, efficiency metrics, and RNG specifications

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