Transformations are obtained which reduce the system of differential equations for certain types of diffusion-controlled reactions to the equation for pure diffusion.Simple relationships between the diffusion rate with and without reactions are presented for reversible unimolecular reactions, certain types of reversible bimolecular reactions, and irreversible reactions between species with equal diffusivities. It is shown that these relationships are independent of geometry, hydrodynamics, or boundary conditions, and so the mass transfer coefficient in the presence of reactions can be obtained from the coefficient in the absence of reactions without an explicit knowledge of the mass transfer mechanism.The reaction factor for irreversible reactions with equal diffusivities, obtained by others for specific mass transfer mechanisms, is found to be quite general and essentially independent of the mechanism.Some data on the absorption of sulfur dioxide in a laminar water jet is considered.The theory of simultaneous diffusion and chemical reaction is basic to the study of mass transfer in reacting systems. Although many systems are difficult to handle analytically, even when the reactions are rapid relative to the diffusion, a number can be considerably simplified by reducing them to pure diffusion problems. It will be shown that this reduction is possible for certain classes of reactions and that in these cases the effect of the chemical reaction on the transfer rate may be obtained even though the pure diffusion problem is too complicated to handle analytically.A combination of a differential material balance with Fick's law gives the equation for pure diffusion in an isothermal system (2) :The diffusion coefficient is assumed constant, and the substantial derivative is used in this and subsequent equations to account for any bulk motion superimposed on the system. If bulk motion is present, the term difusion-controlled reactions is used in a somewhat general sense to include diffusion-convection controlled reactions as well. The system is taken to be dilute enough so that the hydrodynamic velocities are independent of the diffusion, and it is assumed that there is no convection across the boundaries. Solutions of Equation (1) with the appropriate boundary conditions give the concentration profile of the diffusing species, which, upon application of Fick's first law a t the system boundaryyields the rate of transfer across the boundary.If the flow is turbulent, the equations can be considered to apply a t every instant of time, and the solutions give the instantaneous concentration and flux. Although many of the conclusions given S. H. Chiang is with Linde Company, Tonawands. New York. below are valid for turbulent flow, this paper is concerned specifically with a stagnant fluid or laminar flow.Equations (1) and (2) with the boundary conditions fix the diffusion rate and also yield the mass transfer coefficient. The two simplest solutions, which are used as models for mass transfer in systems such as packed towers...