Page 168 - Process Equipment and Plant Design Principles and Practices by Subhabrata Ray Gargi Das
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166    Chapter 6 Evaporators




             6.3.1 Types of continuous evaporators
             Continuous evaporators are further classified based on (i) the method of agitation or the nature of liquid
             circulation over the heating surface, (ii) movement of the evaporating film, (iii) type of heat transfer
             surface.
                Evaporators may be divided into three main types on the basis of nature of circulation:

             (a) Natural circulation units
             (b) Forced circulation units
             (c) Film-type units
                In natural-circulation evaporators, the circulation of the liquid is effected by employing a short
             length of the tube. These evaporators are further classified as horizontal tube and vertical tube type.
                Horizontal tube evaporators (Fig. 6.6A) have the tube bundle fitted horizontally into the lower
                                        part of the body. Above the heating section is a cylindrical portion in
                                        which vapor-liquid separation takes place. Some form of de-
                                        entraining device is usually fitted (not shown in the diagram) to
                 Horizontal tube Evaporator
                                        prevent carryover of liquid droplets with the vapor stream. The
                                        horizontal tube evaporator is the only type with the heating medium
                                        inside the tubes. Steam is fed to one steam chest wherefrom it enters
             the tubes and reaches the opposite chest. From here, the condensate leaves through a steam trap (not
             shown). A small vent is provided at the top location of the opposite chest to bleed out any condensable
             component accompanying the condensing vapor/steam. Horizontal tube evaporators are relatively
             cheap and easy to install, require low headroom, and are suitable for handling liquors that do not
             crystallize. They can be used either as batch or as continuous units. Typically, the shell diameter is in
             the range 1e3.5 m and the height is 2.5e4 m. These units are not used for viscous liquors as the natural
             recirculation rate is poor. Difficulty in cleaning the outer surfaces of the tubes render this design
             unsuitable for liquids that form scales or deposit salts.
                        (A)                        (B)
                                                                          Vapour







                                                   Vent
                                               Feed

                                                                            Steam



                                                  Steam
                                                condensate
                                                                            Thick liquor
             FIGURE 6.6
             Natural circulation evaporator with (A) horizontal tubes, (B) vertical tubes.
                     From Richardson, J.F., Harker, J.H., & Backhurst, J.R. Particle technology & separation processes (5th ed.). Coulson and
                                                     Richardson’s chemical engineering (Vol. 2). Butterworth-Heinemann.
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