BiRD Bioreactor Report

BioReactorDesign Simulation Report

Process-bigraph wrapper for BiRD: 0D bioreactor models with Higbie kLa, Monod kinetics, and temperature-dependent Henry's law. Three E. coli fermentation scenarios — from 2 L bench to 10,000 L production — demonstrating scale-up mass transfer challenges.

1

E. coli Lab-Scale Batch

2 L bubble column — exponential growth, O₂ crash

A benchtop bubble column (2 L) growing E. coli K-12 at 37°C in minimal medium. With moderate aeration (0.5 vvm), the culture initially enjoys excess dissolved oxygen. As biomass doubles every ~60 min (μ_max = 0.7 h⁻¹), the oxygen uptake rate overtakes the mass transfer capacity, causing a characteristic DO crash. This is the classic aerobic E. coli batch profile seen in teaching labs.

ReactorBubble Column
Volume2 L
Final DO0.02 mg/L
Biomass55.5x0.05 → 2.77 g/L
Avg kLa45.4 h⁻¹
Gas Holdup0.81%
Runtime0.59s

3D Reactor Geometry

9.0
0.0
mg/L
t = 0 h
Reactor vessel colored by selected variable. Blue = highRed = low (inverted for CO₂: red = high accumulation). Drag to rotate. Scroll to zoom.

Time-Series Dynamics

Architecture & Document

Bigraph Architecture

Bigraph architecture diagram

PBG Composite Document

2

E. coli High-Cell-Density (Stirred Tank)

50 L stirred tank — high OD, impeller-enhanced kLa

A 50 L stirred-tank bioreactor growing E. coli BL21 for recombinant protein production at 37°C. The Rushton impeller (200 W) dramatically improves kLa, enabling much higher biomass than a bubble column alone. Starting from a higher inoculum (OD≈ 1), the culture reaches high cell density while the combined agitation + sparging maintains dissolved oxygen above the critical threshold for aerobic metabolism.

ReactorStirred Tank
Volume50 L
Final DO0.01 mg/L
Biomass90.0x0.50 → 44.98 g/L
Avg kLa473.1 h⁻¹
Gas Holdup6.18%
Runtime13.35s

3D Reactor Geometry

9.2
0.0
mg/L
t = 0 h
Reactor vessel colored by selected variable. Blue = highRed = low (inverted for CO₂: red = high accumulation). Drag to rotate. Scroll to zoom.

Time-Series Dynamics

Architecture & Document

Bigraph Architecture

Bigraph architecture diagram

PBG Composite Document

3

E. coli Industrial Scale-Up

10,000 L airlift — mass transfer bottleneck at scale

An industrial airlift reactor (10,000 L) scaling up E. coli fermentation at 37°C. Despite 50 L/min of air, the large vessel diameter yields low superficial gas velocity and poor kLa. The culture quickly becomes oxygen-limited, demonstrating the classic scale-up problem: mass transfer that was adequate at bench scale becomes the bottleneck at production scale. Growth rate collapses as DO drops below the critical concentration.

ReactorAirlift
Volume10000 L
Final DO0.01 mg/L
Biomass3.3x0.50 → 1.63 g/L
Avg kLa10.7 h⁻¹
Gas Holdup0.41%
Runtime1.16s

3D Reactor Geometry

7.0
0.0
mg/L
t = 0 h
Reactor vessel colored by selected variable. Blue = highRed = low (inverted for CO₂: red = high accumulation). Drag to rotate. Scroll to zoom.

Time-Series Dynamics

Architecture & Document

Bigraph Architecture

Bigraph architecture diagram

PBG Composite Document