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The biomass yield $Y$ converts nutrient consumption into biomass production: consuming nutrient mass $m$ produces dry biomass mass $Ym$ under the assumed constant conversion. For $Y=0.5\mathrm{g}\text{ biomass}/(\mathrm{g}\text{ nutrient})$, consumption of $8\mathrm{g}$ of nutrient produces $4\mathrm{g}$ of dry biomass. Its numerical value depends on the measurement conventions; it is not a fraction of all feed mass converted into cells. With no separate maintenance consumption, biomass production $\mu (s)x$ requires nutrient consumption $\mu (s)x/Y$ in the chemostat balance.

A chemostat maintains a well-mixed culture at constant volume $V$ by feeding fresh nutrient solution and removing culture at the same volumetric flow $Q$. Its dilution rate is $D=Q/V$. Mixing makes the outflow's nutrient concentration and biomass concentration equal to those inside the vessel; continuous replacement supplies nutrient and also removes growing cells.

The simplest one-nutrient chemostat uses nutrient concentration $s(t)$, biomass concentration $x(t)$, constant feed nutrient concentration $s_{\mathrm{in}}>0$, and constant biomass yield $Y>0$. Assume a cell-free feed, one growth-limiting nutrient, constant volume, and no cell retention, death or additional nutrient consumption for maintenance. With specific growth rate $\mu (s)$, its ordinary differential equations areThe nutrient balance contains inflow $D{s}_{\mathrm{in}}$, outflow $Ds$, and consumption $\mu (s)x/Y$; the biomass balance contains production $\mu (s)x$ and removal $Dx$. If $s$ is in grams of nutrient per litre and $x$ in grams of dry biomass per litre, $Y$ is grams of dry biomass produced per gram of nutrient consumed. Thus both balances have units of their respective concentration per time. The Monod equation supplies an empirical choice of $\mu (s)$; the balances themselves express the stated production, consumption and transport assumptions.

The appeal of a chemostat is that, at a positive chemostat steady state, adjusting the pump sets the specific growth rate to $D$. The residual nutrient concentration then adjusts to that rate, and the available nutrient together with biomass yield sets the biomass concentration. This gives a controlled way to compare cultures at selected growth rates and a simple quantitative warning of chemostat washout.

Two 1950 publications on continuous culture are Novick and Szilard's Description of the Chemostat, Science 112(2920), 715-716, dated 15 December, and Monod's La technique de culture continue. Théorie et applications, Annales de l'Institut Pasteur 79, 390-410. The latter's original bibliographic details are reproduced in the contents of Monod's collected papers. These references identify contemporary publications without establishing priority between them. ^[ref]. ^[ref].