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A fluidized bed reactor with one or more stages each stage having a heating section located below a reacting section and a mechanism that pulses granules back and forth between the heating and reacting sections, separate injectors for silicon containing gases non silicon containing gases, heaters to

A fluidized bed reactor with one or more stages each stage having a heating section located below a reacting section and a mechanism that pulses granules back and forth between the heating and reacting sections, separate injectors for silicon containing gases non silicon containing gases, heaters to heat the non silicon containing gases above the reaction temperature and the silicon containing gases to a temperature just below their decomposition temperature. The heater for the silicon containing gases controls the condensing vapor of a heat transfer fluid to a temperature below the decomposition temperature of the silicon containing gases. An enclosed noncontaminating sieving device selectively removes product and recycles undersize material. A weigh cell with frequency analysis capability provides information on the weight of the reactor and the force exerted by the pulsing action of the granules.

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1. A machine for Production of Granular Silicon comprising:a heating section located below a reacting section; where said heating section comprises one or more tubes heated by one or more heatersa mechanism that pulses silicon granules back and forth between the heating and reacting sections wherein

1. A machine for Production of Granular Silicon comprising:a heating section located below a reacting section; where said heating section comprises one or more tubes heated by one or more heatersa mechanism that pulses silicon granules back and forth between the heating and reacting sections wherein the mechanism includes at least one separate injection means for injection non silicon containing gases into the heating section;separate injection means for injecting silicon containing gases into the reaction section;a heating means to heat the non silicon containing gases above a reaction temperature. 2. A machine of claim 1 further including at least one additional stage connected above the reacting section and containing a second reacting section, a heating means, and one or more gas injecting means. 3. A machine of claim 2, where high purity hydrogen is used for the non silicon containing gas to the first stage and silane is injected via the separate injection means for silicon containing gas in all the stages. 4. A machine of claim 2, where; high purity hydrogen is injected in the first and subsequent stages, a silicon containing gas selected from a first group consisting of trichlorosilane, dichlorosilane, tribromosilane, dibromosilane, triodosilane, diiodosilane and mixtures thereof is injected via the separate injection means for silicon containing gas in the first stage and further comprising a final feedstock recovery system where a silicon tetrahalide selected from a second group consisting of silicon tetrachloride, silicon tetrabromide and silicon tretraiodine is injected, mixed with the reactor effluent then quenched at an optimal temperature to recover gases from the first group, residual silicon tetrahalides from the prior second group and hydrogen. 5. A machine of claim 2 where at least one of the at least one additional stage contains some residual silicon dust and/or silicon containing gases. 6. A machine of claim 1 further comprising a means for recovering heat from the granules by direct contact with a high purity gas, which has carbon and oxygen containing contaminants below 1 ppmv, parts per million by volume, and which can be selected either from a first group consisting of hydrogen, helium, argon, nitrogen and mixtures thereof, or from a second group consisting of helium, argon, nitrogen, silicon tetrachloride, silicon tetrabromide and mixtures thereof. 7. A machine of claim 1 further comprising a heat exchanger in which one or more containment means for the silicon containing gases are heated by hot liquid or condensing vapor maintained within a temperature range which cannot cause decomposition of the gases; which temperature range is about 200-400° C. 8. A machine of claim 7 where the location of the one or more flow control means for the silicon containing gas is upstream of the heat exchanger. 9. A machine of claim 1 further comprising a sieving device, operated either continuously or in batches, by which the silicon granules are sieved using one or more sieves manufactured from non contaminating sieve material selected from the group consisting of single crystal silicon, polycrystalline silicon, silicon oxide, silicon nitride, silicon oxynitride, silicon carbide and mixtures thereof where the contaminants in the abradable surfaces is less than about 1000 ppmwt. 10. A machine of claim 1 further comprising a feedstock recovery section; where hydrogen is injected in the heating section, a silicon containing gas selected from a first group, consisting of trichlorosilane dichlorosilane, tribromosilane, dibromosilane, triodosilane, diiodosilane and mixtures thereof is injected via the separate injection means for silicon containing gas in the reacting section and a silicon tetrahalide selected from a second group, consisting of silicon tetrachloride, silicon tetrabromide and silicon tetraiodide is injected after the reactor section, mixed with the reactor effluent then quenched at an optimal temperat ure to recover hydrohalosilanes selected from the first group, residual silicon tetrahalides selected from the second group and hydrogen. 11. A machine of claim 10 where a cyclone is used after the injection of the silicon tetrahalide to remove silicon dust and to provide residence time for the mixing and reaction of the silicon tetrahalide with the reactor effluent and the silicon dust to improve the recovery of the said silicon hydrohalosilanes and tetrahalides. 12. A machine of claim 1 further comprising one or more cooled joints between external equipment and the reactor which transmit hot gases or solids and which are cooled using, one or more, microchannels positioned to primarily cool the immediate area around the connection to the reactor and/or the seal area of the connection to the external equipment. 13. A machine of claim 1 further comprising an external flow control means for controlling flow to each of said injection means, selected from a group consisting of: a means for direct flow control of each said injection means a means of indirect flow control by a flow distribution device or a combination of the two where some of the said injection means are ganged in groups. 14. A machine of claim 1 where the instantaneous flow of gases into the reactor through one or more of the injection means is varied periodically and/or the distribution of flow between said injection means is adjusted to control the generation of new particles without changing the total flow averaged over 1 minute. 15. A machine of claim 1 where the heating section is of smaller diameter than the reacting section above it and connected by a tapered section, angle of said tapered section to be between 10 and 80 degrees from the vertical. 16. A machine of claim 1 where the heaters used in the heating sections are selected from the group consisting of resistance heaters, inductive RF heaters, microwave heaters, lamp heaters or lasers. 17. A machine of claim 1 further including a means of supplying a silicon etching gas which is injected through one or more of the injection means for the purpose of etching wall deposits from all or part of the reactor, where the gas is selected from the group consisting of chloride, bromine, iodine, hydrogen chloride, hydrogen bromide, hydrogen iodide, a mixture of hydrogen and silicon tetrachloride, a mixture of hydrogen and silicon tetrabromide, a mixture of hydrogen and silicon tetraiodide and mixtures thereof. 18. A machine of claim 1 where the reactor is supported upon a weigh cell, capable of both weighing the reactor and its contents and of measuring the intermittent force exerted by the pulsing granules and where the connections to and from the reactor are flexible enough to allow the movement required by the weigh cell and the thermal expansion of the reactor relative to the support structure, said movement to be less than 1″ (25 mm). 19. A machine of claim 1 where all or a portion of the non silicon containing gases are heated to a temperature below the reaction temperature outside the heating section then heated to a temperature above the reaction temperature inside the heating section prior to entry to the reacting section.