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Multiple steady states are established. The situation always results in reduced cooling performance, a very wide residence time spectrum, and in many cases, a higher pressure drop than calculated originally. The design of multitube equipment for viscous cooling or polymerization reaction involving increasing viscosity requires thorough analysis of the rate of viscosity increase versus the ow rate. In many cases, very high pressure drop becomes necessary to avoid creation of a multiple steady-state situation. A single ow channel is highly desirable for heat transfer/reaction processes with steeply increasing viscosity. Isolated ow paths are avoided and radial exchange of material ensures uniform product treatment. This is achieved in the monotube SMX, SMXL, or KMS heat exchanger, but only at small throughput, due to limited availability of the heat transfer surface. At high throughput, special features such as those provided by the SMR design are required. 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