An applicable technologies for indirect
heat transfer use tubes (shell-and-tube
exchangers) or flat surfaces (plate exchangers). Their goal is to exchange the maximum amount of heat per unit area by generating as much
turbulence as possible below given
pumping power limits. Typical approaches to achieve this consist of corrugating the tubes or plates or extending their surface with
fins. However, these geometry conformation technologies, the calculation of optimum
mass flows and other turbulence related factors become diminished when
fouling appears, obliging designers to fit significantly larger heat transfer areas. There are several types of fouling, including particulate accumulation,
precipitation (
crystallization),
sedimentation, generation of
ice layers, etc. Another factor posing difficulties to heat transfer is
viscosity. Highly viscous fluids tend to generate deep
laminar flow, a condition with very poor
heat transfer rates and high
pressure losses involving a considerable pumping power, often exceeding the exchanger design limits. This problem becomes worsened frequently when processing
non-newtonian fluids. The DSSHE has been designed to face the aforementioned problems. They increase heat transfer by: removing the fouling layers, increasing turbulence in case of high viscosity flow, and avoiding the generation of ice and other process by-products. == Description ==