Intensifying Heat/Mass Transfer and Plant Design Layout Process intensification in heat and mass transfer is achieved particularly in chemical systems by optimizing molecular energy in gases and liquids involved in the reaction and heat transfer processes. This process focuses on key different components that play specific roles in mass and heat transfer in these systems. These include methods such as absorption, mist disengagement, filtration, dust disengagement, electrolysis, and distillation among others. The buoyancy of fluids is used for mass transfer intensification and bears a general relationship defined by the equation, Δρg. These variables affect the interfacial shear characteristic of liquid droplets directly influencing the flow of heat in a system. On the other hand, electrical bulbs, waxes, and similar sources of heat and light depend on variables such as the diameter of the electric valve and the diameter of wax globules (Kearney, 1999). The behavior of these devices may be inferior leading to poor heat transfer and larger heat losses. On the other hand, the intensification of heat transfer relies on various mechanisms involved in the process. This intensification correlates with the nature of the fluid stream and the method through which heat is transferred within the system. Generally, when fluid turbulence is high, higher shear forces result, influencing values of heat transfer coefficients. This is well illustrated in the following expressions. These values can be manipulated to optimize mass and heat transfer. Nu = 1 Re0.8 Pr0.33 3.1 Sh = 2 Re0.8 Sc0.33 3.2 Nu = Nusselt number; Re = Reynolds number; Pr = Prandtl number; Sh = Sherwood number. The film transfer coefficient can be obtained by integrating these items in the calculation process. In these expressions, d is the diameter of the fluid and v is the propagation velocity. Increasing the pumping velocities may lay severe penalties on the piping system and other system components. That may adversely affect process intensification since every element incorporated in the process need to withstand all operating conditions. On the other side, the benefits of mass transfer intensification can be realized by compounding smaller diameter pipes, manipulating the geometry of the internal surface of the pipe and the geometry of the surface in contact with the fluid. Enhanced heat transfer within systems comes with a number of benefits. Heat transfer intensifications, therefore, are in two categories. The passive category focuses on the external powers of systems while the active category emphasizes rotational effects. Passive techniques incorporate the host equipment enhancement techniques. These techniques include coating surfaces, surface catalysis, and porous structures, among others (Kearney, 1999). Passive enactments are characterized by the coatings that are applied to surfaces to promote transformations of fluids to liquid or steam. In addition to that, it has been demonstrated that dropwise condensation of fluids comes with positive benefits overall. It sustains endothermic processes within these systems and leads to optimum heat intensifications. In addition to that, coating