Patent GB-486415-A (GB)
Title: Improvements in the distillation of glycerin
IPC: B01D1/04
Filed: 1936-12-01
Abstract: <PICT:0486415/III/1> <PICT:0486415/III/2> <PICT:0486415/III/3> <PICT:0486415/III/4> An apparatus for distilling glycerine and substances of similar physical properties comprises a still having closed steam heating surfaces to distil the glycerine, a boiler-condenser in which the heat of condensation of the glycerine generates steam, and means for drawing off condensed water from the closed steam heating surfaces and supplying it to the boiler.  The apparatus described is for use in carrying out the process described in Specification 486,311.  Glycerine is distilled in a still 1, Fig. 1, from which the mixed vapours of glycerine and water pass through a goose-neck 2 to a separator 3 which removes entrained liquid.  The vapours pass on through a pipe 4 to a boiler-condenser 5 in which the heat of condensation of the glycerine is used to generate steam, part of which is utilized in the still.  A pipe 6 conveys the water vapours, uncondensed glycerine and impurities to a condenser-concentrator 8, from which the water vapour and other volatile impurities are led off by a vacuum line 10.  The still 1 is heated by steam coils 11, 12, 13, 14, 15, Fig. 2, controlled by inlet valves A, B, C, D, E on a steam pipe S.  Condensed water is withdrawn through the valves a ... e and via a pressure-release trap 19, which prevents escape of steam, to a receiver 17.  The reduction in pressure at the trap 19 to a lower pressure controlled by a valve 25, causes part of the hot water to vaporize in the receiver 17, and to pass as steam to a glycerine preheater 22.  The water collecting in the receiver 17 passes through a cooler 28 to the boiler-condenser 5, whence the steam generated passes by pipe 31 to a superheater coil 16 in the still 1. High-pressure steam from the line S can also be supplied through a valve F to the coil 16, which is connected at its lower end to a ring manifold 35 carrying ejector jets 37 which cause effective circulation of the glycerine over the heating coils.  Steam from line S is also supplied to perforated rings 41, 42, 43.  The boiler-condenser, Fig. 5, is supplied with distilled water from the receiver 17 by an inlet pipe 29.  Glycerine vapours entering at 4 pass through the tubes 56 containing twisted metal baffles 57; the condensed glycerine falls into a trough 58 and thence out by the pipes 59, 72 to the receiver 7.  Uncondensed vapours pass out at 6 to the condenser-concentrator 8.  The steam generated passes out by the pipe 31 to the still; a proportion may be lead off by pipe 52 for heating the condenser-concentrator 8.  The condenser-concentrator, Fig. 6, contains banks of horizontal Field-tubes so arranged that the cooling water flows generally downward but locally upward to prevent accumulation of air in pockets.  Thus water entering by a pipe 45 flows through a Field-tube 47 back to a space 46 connecting with a second Field-tube 48, situated above the first, and from which the water passes to a connection 50 leading down to the lower of the next pair of Field-tubes underneath, and so on, until it emerges by the pipe 75.  The lowest two pipes are provided with steam from the pipe 52.  Glycerine vapours enter at the bottom and proceed upwards, condensate forming on the pipes being collected in the tank 9.