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  2. Flash evaporation - Wikipedia

    en.wikipedia.org/wiki/Flash_evaporation

    The water is heated and then routed into a reduced-pressure flash evaporation "stage" where some of the water flashes into steam. This steam is subsequently condensed into salt-free water. The residual salty liquid from that first stage is introduced into a second flash evaporation stage at a pressure lower than the first stage pressure.

  3. Circulation evaporator - Wikipedia

    en.wikipedia.org/wiki/Circulation_evaporator

    The general steps in design are as follows, [2] [3] and would be carried out in excel for ease of calculation. Other design software such as Aspen Plus could also be used with built in functions for process equipment. 1) Estimate temperature distribution in the evaporator, taking into account boiling-point elevations.

  4. Multiple-effect evaporator - Wikipedia

    en.wikipedia.org/wiki/Multiple-effect_evaporator

    Condensing vapors from flash tank B1 heat evaporator A2. •1=feed •2=product •3=steam •4=vapors. In chemical engineering, a multiple-effect evaporator is an apparatus for efficiently using the heat from steam to evaporate water. [1] Water is boiled in a sequence of vessels, each held at a lower pressure than the last.

  5. Thermal expansion valve - Wikipedia

    en.wikipedia.org/wiki/Thermal_expansion_valve

    Externally equalized thermostatic expansion valves compensate for any pressure drop through the evaporator. [3] For internally equalised valves a pressure drop in the evaporator will have the effect of increasing the superheat. Internally equalized valves can be used on single circuit evaporator coils having low-pressure drop.

  6. Kozeny–Carman equation - Wikipedia

    en.wikipedia.org/wiki/Kozeny–Carman_equation

    The Kozeny–Carman equation (or Carman–Kozeny equation or Kozeny equation) is a relation used in the field of fluid dynamics to calculate the pressure drop of a fluid flowing through a packed bed of solids. It is named after Josef Kozeny and Philip C. Carman.

  7. Pressure drop - Wikipedia

    en.wikipedia.org/wiki/Pressure_drop

    Pressure drop (often abbreviated as "dP" or "ΔP") [1] is defined as the difference in total pressure between two points of a fluid carrying network. A pressure drop occurs when frictional forces, caused by the resistance to flow, act on a fluid as it flows through a conduit (such as a channel, pipe , or tube ).

  8. Hagen–Poiseuille equation - Wikipedia

    en.wikipedia.org/wiki/Hagen–Poiseuille_equation

    In non ideal fluid dynamics, the Hagen–Poiseuille equation, also known as the Hagen–Poiseuille law, Poiseuille law or Poiseuille equation, is a physical law that gives the pressure drop in an incompressible and Newtonian fluid in laminar flow flowing through a long cylindrical pipe of constant cross section.

  9. Flow distribution in manifolds - Wikipedia

    en.wikipedia.org/wiki/Flow_distribution_in_manifolds

    [1] [2] [3] A key question is the uniformity of the flow distribution and pressure drop. Fig. 1. Manifold arrangement for flow distribution. Traditionally, most of theoretical models are based on Bernoulli equation after taking the frictional losses into account using a control volume (Fig. 2).