Page 189 - Design of Simple and Robust Process Plants
P. 189

174  Chapter 5 Process Simplification and Intensification Techniques
                   Induced pulsing flow has also been applied for some time in extraction columns,
                 either by the introduction of pulsations with the feed pumps or with an external
                 pulsation device. Alternative designs applied here are the introduction of a rotating
                 disc or vertical displacement of discs which are assembled on an axis. These all have
                 the purpose of intensifying the mass transfer.
                   Currently, a supersonic, two-phase flow mixer is under development at Praxair
                 (Cheng, 1997). The concept is based on the creation of very small droplets in a gas
                 stream, through a supersonic, two-phase mixer The application area would be very
                 rapid gas-liquid reactions.

                 5.5.3
                 Benefits from Centrifugal Fields: ªHigeeº
                 Centrifugal fields have, for many years, been successfully exploited in phase separa-
                 tions. The application of cyclones in gas/solid, gas/liquid separations are well
                 known, their limitations being mainly due to particle size and scale-up (larger-scale
                 cyclones have a lower separation efficiency). Hydro-cyclones, which have found
                 application in liquid/solid separations, are very simple, robust devices and have a
                 wide field of application. Likewise, centrifugal devices are widely used for liquid/
                 solid and liquid/liquid separations. The application of multi-stage centrifuges for
                 liquid/liquid extraction is also an intense operation which is often applied where
                 there are only small differences in the density of the materials to be separated. This
                 technique is of particular interest in the pharmaceutical industry, where advantage
                 is taken of the small hold-up. Although during the past few decades several types of
                 centrifugal separation apparatus have been developed by the manufacturers, it was
                 only during the 1970s that process intensification initiatives were started, driven
                 mainly by ICI.
                  The idea was to reduce the size of equipment considerably in order to achieve
                 much lower capital costs (Ramshaw, 1987, 1995). It was concluded that the size of
                 equipment was often determined by phase separation, which in turn restricted the
                 speed at which transfer processes could be carried out. By applying a centrifugal
                 force, phase separation could be improved to provide higher processing speeds, and
                 this in turn should result in improved mass transfer. In terms of a gas/liquid col-
                 umn, the diameter should be decreased (higher velocity), but the height must also
                 be reduced by improved mass transfer and phase separation. The initial industrial
                 results for acceleration-induced gas/liquid separations were limited, and develop-
                 ments into the use of centrifugal forces over a wide range of operations continued
                 in research, especially as the potential benefits were realized and were not under
                 debate. Some details of these ongoing research efforts are summarized below.
                   Centrifugal forces have been applied for de-sorption, for example of de-aerators of
                 water streams. In the case of oil field flooding water, de-aeration vacuum towers
                 were installed. The first development of a so-called high-gravity (ªHigravº) machine
                 was at the university of Beijing, and this resulted in a range of plant-scale machines
                 that were tested successfully in the field (Zheng et al., 1997). The technique is also
                 applicable for de-aeration of boiler feed water.
   184   185   186   187   188   189   190   191   192   193   194