p - trap is the pressure above the filter ( assume downstream pressure remains constant ) as the run progressed . flow 2 is the na flow rate and the v reactor shows when the product was made . at t = 8420 , sodium flow was initiated to the trap . trap pressure remained relatively constant as the na flowed through the clean filter ( 125 micron ) until the reactor valve was opened and started to build cake . the cake dp grew in a linear fashion until t = 8520 when the reaction rate began to slow because of nozzle plugging due to subsonic operation of the nozzle . the cake thickness after distillation was measured to be on average 5 to 6 inches . the bottom of the cake appeared less dense than the top of the cake and measurements of the cake density showed a density in the top of the cake of 1 . 1 g / cc and in the bottom of the cake 0 . 73 g / cc . it is believed that the bottom was less dense because it was formed at a lower pressure . for example , the dp is determined by the flow rate ; for this run the flow rate was 30 kg / min . also , after product production was terminated and na flow continued , the cake appeared to compact further ( see pressure increase while flow decreased after t = 8550 ). prior to na flow shutdown , dp was up to 22 psig versus 18 psig when significant product production ended , see fig1 and 2 . heat was applied to the cake area and vapor was removed to a primary condenser out the top side of the trap and to a secondary condenser by distilling through the wedge wire filter . during the distillation , a total of 5 . 9 kg of na was removed from the cake which weighed 3 . 4 kg after the distill . 3 . 8 kg of the 5 . 9 kg was found to have condensed in the secondary condenser , see fig3 . in another nutsche run , the trap was designed to allow distillation through the filter into the bottom of the trap to utilize the full trap diameter for vapor movement . the trap also had the standard 1 ″ line to a primary condenser , see fig4 . heat was concentrated on the cake area while the bottom of the trap was maintained cool to support condensation of the na . after distillation , 1 . 6 kg of na went to the primary condenser and 1 . 3 kg . of na distilled into the bottom of the trap leaving a 3 . 1 kg . cake of titanium and nacl . however , it has been found that breaking the filter cake drastically reduces the distillation times and rates for the distillation of the liquid metal , such as sodium . using a breaker bar or some other mechanical means such as moving fingers or a mixer has significantly reduced the first portion of the vacuum distill from 40 , 000 - 50 , 000 seconds ( 11 - 14 hours ) to 20 , 000 to 30 , 000 ( between about 6 and 8 hours ). the second portion of the distill , that is the decreasing temperature and pressure portion referred to as the tail was not affected by breaking the filter cake . it has also been discovered that using a sweep of inert gas such as argon heated , preferably in the range of from about 500 ° c . to about 800 ° c . during the second distill or tail portion reduced the amount of time necessary to distill the reductant metal ( sodium ) from about 40 , 000 - 50 , 000 seconds to about 10 , 000 seconds ( about 3 hours .). this is a significant improvement over the prior method . by using either one of the methods or a combination of breaking the filter cake combined with an inert gas sweep , the distillation times can be decreased from about ( 22 or 28 ) hours to about ( 9 to 11 ) hours . this is of significant importance in the design of plants by simplifying designs , reducing collection tanks , valves , piping and other associated equipment . after vacuum distillation is apparently complete , any remaining trapped reductant metal ( sodium ) becomes impractical to remove . while it seems obvious to introduce the filter cake into water to wash the residual salt ( nacl ) from the titanium powder , the problem exists of trapped reductant metal ( sodium ) in the filter cake which when combined with water could produce a significant explosion . it is a fact that the mixture of sodium liquid and water will provide an explosion having energy greater than the equivalent amount of tnt . it has been found in the production of ti by the subsurface reduction of ticl 4 by na that crumbling the filter cake into small quantities , such as less than about five centimeters in diameter and preferably in the range of from about two to about five centimeters in diameter , during or subsequent to the distillation of sodium apparently makes particles or clumps small enough that any trapped na is manageable without significant damage to equipment or harm to personnel , if proper care is taken in equipment design and with appropriate safety precautions . after distillation , the filter cake is friable and easily crumbled . to the extent that large quantities of crumbled filter cake can be water washed without fear of explosion significantly reduces the distillation times required in the production of the various elemental material and alloys described in the above - referenced patents , particularly where sodium or other alkaline metal is used as a reductant . alternatively , it has been found that the entire distillation can be accomplished at positive pressure , such as , but not limited to , psig with a heated or hot inert gas , such as but not limited to ar at about 500 ° c . to about 800 ° c . followed by cooling to condense the vaporized liquid metal , such as but not limited to na . thereafter , the cooled liquid metal will be returned for additional use . summarizing this invention relates to mechanism and methods for decreasing the distillation time of a filter cake produced by the process described in the above - referenced patents . the filter cake can be broken such as by vibration or moving mechanism in the filter cake area or by stationery mechanical bars or members in the filter cake area or other suitable mechanism . an inert sweep gas with or without vacuum can be used alone or in combination with the above described methods breaking the filter cake during the distillation in order significantly to reduce the distillation time of the liquid metal in the filter cake . while there has been disclosed what is considered to be the preferred embodiment of the present invention , it is understood that various changes in the details may be made without departing from the spirit , or sacrificing any of the advantages of the present invention .