Patrick James Harder - Midland MI, US Arthur James Tselepis - Midland MI, US
International Classification:
C01B 33/107
US Classification:
423342
Abstract:
A process for reducing waste and increasing yield of chlorosilane monomers is performed by cracking polychlorosiloxane and polychlorosilane by-products generated during production of trichlorosilane useful for the manufacture of polycrystalline silicon.
Process For Preparing Silicon Carbide Powder From Vaporized Polysiloxanes
William H. Atwell - Midland MI Donald M. Bartos - Midland MI Patrick J. Harder - Bay City MI Jonathan Lipowitz - Midland MI Chandan K. Saha - Midland MI
Assignee:
Dow Corning Corporation - Midland MI
International Classification:
C04B 35571
US Classification:
501 88
Abstract:
Disclosed is a process for the formation of silicon carbide powder in which vaporized polysiloxanes are reacted and pyrolyzed in a single heating step to form the silicon carbide powder. The process is simple and inexpensive and yields powder having desirable characteristics.
Richard A. Burgie - Midland MI Patrick J. Harder - Bay City MI David H. Sawyer - Midland MI
Assignee:
Hemlock Semiconductor Corporation - Hemlock MI
International Classification:
C01B 33107
US Classification:
423342
Abstract:
An improved process for contacting hydrogen gas and tetrachlorosilane in a reactor comprising a pressurizable shell having located therein a reaction vessel forming a substantially closed inner chamber for reacting the hydrogen gas with the tetrachlorosilane. The improvement comprises feeding to an outer chamber between the pressurizable shell and the reaction vessel a gas or gaseous mixture having a chlorine to silicon molar ratio greater than about 3. 5. The improvement reduces the concentration of hydrogen and tetrachlorosilane in the outer chamber that results from leakage of these gases from the substantially closed inner chamber and the detrimental reactions associated with such leakage on structural elements and performance of the reactor.
Tapered Fluidized Bed Reactor And Process For Its Use
- Hemlock MI, US Raymond Anthony Cocco - Elmhurst IL, US Max E. Dehtiar - Saginaw MI, US Patrick J. Harder - Saginaw MI, US Ted M. Knowlton - Willowbrook, US Michael J. Molnar - Freeland MI, US
A fluidized bed reactor includes a gas distributor, a tapered section above the gas distributor, and an expanded head above the tapered section. The gas distributor defines a plurality of inlets surrounding a product withdrawal tube, which extends away from the fluidized bed reactor. The fluidized bed reactor is useful in a process for fluidizing relatively large particles, such as Geldart Group B particles and/or Geldart Group D particles, where said particles are in a bubbling fluidized bed residing, in whole or in part, in the tapered section. The fluidized bed reactor and process may be used for manufacturing polycrystalline silicon.
Method For Fluidizing Copper Silicide And Process For Preparing A Halosilane Using The Method
- Midland MI, US Aaron Coppernoll - Crestwood KY, US Patrick James Harder - Midland MI, US Dimitris Katsoulis - Midland MI, US Vladimir Pushkarev - Midland MI, US
Assignee:
Dow Corning Corporation - Midland MI
International Classification:
B01J 8/18 C01B 33/06 C01B 33/107
Abstract:
A method is useful for maintaining a uniformly fluidized bed in a fluidized bed apparatus. The method includes the steps of charging a mixture of particles including copper silicide particles and fluidization additive particles into the fluidized bed apparatus, and uniformly fluidizing the particles at a temperature of at least 400 C. in the fluidized bed apparatus.
Taper Fluidized Bed Reactor And Process For Its Use
- Hemlock MI, US Raymond Anthony Cocco - Elmhurst IL, US Max E. Dehtiar - Saginaw MI, US Patrick J. Harder - Saginaw MI, US Ted M. Knowlton - Willowbrook IL, US Michael J. Molnar - Freeland MI, US
International Classification:
B01J 8/24 C01B 33/03 G01N 15/02 B01J 8/18
Abstract:
A fluidized bed reactor includes a gas distributor, a tapered section above the gas distributor, and an expanded head above the tapered section. The gas distributor defines a plurality of inlets surrounding a product withdrawal tube, which extends away from the fluidized bed reactor. The fluidized bed reactor is useful in a process for fluidizing relatively large particles, such as Geldart Group B particles and/or Geldart Group D particles, where said particles are in a bubbling fluidized bed residing, in whole or in part, in the tapered section. The fluidized bed reactor and process may be used for manufacturing polycrystalline silicon.
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