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| Sulphuric Acid on the WebTM | Technology Manual | DKL Engineering, Inc. |
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Knowledge for
the Sulphuric Acid Industry Introduction
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All three-collection mechanisms are employed in Brownian diffusion candles but Brownian diffusion is the mechanism which allows these elements to achieve the high collection efficiencies. Brownian diffusion candles are made of glass fibres hand packed in between two metal cages or machine wound onto the inner cage with an outer cage added on top. The candles are installed in either the hanging or standing position. Design bed velocities are very low and range from 0.025 to 0.2 m/s (5 to 40 ft/min) depending on the pressure drop and collection efficiency desired. The absolute maximum gas velocity through the bed is 0.25 m/s (50 ft/min). In contrast to the other type of mist eliminators, the collection efficiency of Brownian diffusion candles increases as the gas velocity decreases. At lower velocities, the residence time of submicron mist particles in the fibre bed increases so the chance that it will be captured increases. Modern fibre bed mist eliminators use a combination of wound-on rovings and mats of various materials and grades to achieve the desired collection efficiencies with minimal pressure drop. The velocities in a Brownian diffusion candle installation are limited in order to minimize pressure drop and chance for re-entrainment of acid droplets. The approach velocity should be limited to a maximum of 15.2 m/s (50 ft/s). The exit velocity should be limited to less than 6.1 m/s (20 ft/s). These limiting velocities have an effect on the length of candle elements that can be used depending on whether they are installed in the hanging or standing position. For hanging candles, the length of the candle is limited to about 3.2 m (10.5 ft). Increasing the candle length increases the bed area and the amount of flow that can pass through the bed at the design velocity. However, all the additional flow must still pass through the central core of the element. For standing candles, the approach velocity up the core is allowed to go as high as 15.2 m/s (50 ft/s) and the height of the candle can be increased to maintain the design bed velocity. The exit velocity is limited to 6.1 m/s (20 ft/s) but this is dependent on the spacing of the candle elements on the tubesheet. The further the elements are placed apart, the lower the exit velocity. Comparison of Hanging and Standing Candle Capacities
Note 1. Based on candle elements 508 mm I.D. x 610 mm O.D.
(20 in I.D. x 24 in. O.D.) The pressure across Brownian diffusion elements varies with the design and construction of the elements. Generally, candles with higher collection efficiencies will have higher pressure drops because the supplier has increased the density of the fibres by winding or packing the glass fibres tighter. The maximum pressure drop across a candle element is about 610 mm WC (24 in. WC). Higher pressure drops can cause candle blow-out where the fibres are permanently deformed.
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2006, 2007, 2008 DKL
Engineering, Inc., All Rights Reserved |
