Patent classifications
B01J2219/0218
Reduction of SiCl4 in the presence of BCl3
The present invention relates, in general, to the purification of boron trichloride (BCl.sub.3). More particularly, the invention relates to a process for minimizing silicon tetrachloride (SiCl.sub.4) formation in BCl.sub.3 production and/or the removal of SiCl.sub.4 in BCl.sub.3 product stream by preventing/minimizing the silicon source in the reaction chambers. In addition, a hydride material may be used to convert any SiCl.sub.4 present to SiH.sub.4 which is easier to remove. Lastly freeze separation would replace fractional distillation to remove SiCl.sub.4 from BCl.sub.3 that has been partially purified to remove light boilers.
Reactor and agitator useful in a process for making 1-chloro-3,3,3-trifluoropropene
Disclosed are a reactor and agitator useful in a high pressure process for making 1-chloro-3,3,3-trifluoropropene (1233zd) from the reaction of 1,1,1,3,3-pentachloropropane (240fa) and HF, wherein the agitator includes one or more of the following design improvements: (a) double mechanical seals with an inert barrier fluid or a single seal; (b) ceramics on the rotating faces of the seal; (c) ceramics on the static faces of seal; (d) wetted o-rings constructed of spring-energized Teflon and PTFE wedge or dynamic o-ring designs; and (e) wetted metal surfaces of the agitator constructed of a corrosion resistant alloy.
Processes for increasing bioalcohol yield from biomass
A process for increasing alcohol yield from biomass (the form or agro- or forest residue, grains, hops, etc.), involving multiple hydrodynamic cavitation treatments of biomass filtrateboth before and after fermentation. Carbohydrates extracted from biomass are subjected to a first cavitation treatment to promote additional conversion into carbohydrates. The carbohydrates are then combined with bacterial species and nutrients, and allowed to ferment. The fermentation product is subjected to a second hydrodynamic cavitation treatment to promote further conversion of carbohydrates into bioalcohol. After distillation, the bioalcohol is subjected to a second hydrodynamic cavitation treatment to increase its purity.
DEVICE FOR PRODUCING METHANE GAS AND USE OF SUCH A DEVICE
The invention relates to a device for producing methane gas including a chamber, means for conveying the product in the chamber which comprise a screw mounted to turn in the chamber along a geometric axis of rotation, Joule-effect heating means of the screw, a removal unit for removing impurities present in the gas coming from the thermal treatment of the product, said unit being connected to a high outlet of the chamber, and a purification system for purifying the gas at the outlet of the removal unit.
CRACKING FURNACE
The invention relates to a cracking furnace containing a tubular vertical chamber which comprises an inlet for introducing a gas to be treated and an outlet for removing said gas from the chamber, means for heating said gas which include a heating tube extending vertically inside the chamber and coaxial with the chamber, the heating tube being shaped in such a way as to have a closed lower end and being arranged in such a way that the lower end thereof is arranged in the chamber and such that the upper end thereof is connected to a burner of the heating means arranged outside the chamber. The invention also relates to an assembly comprising such a cracking furnace and a device for thermal treatment of biomass and/or waste, an outlet of which is connected to the inlet of said cracking furnace.
REACTOR COMPONENT PLACEMENT INSIDE LINER WALL
Reaction chamber liners for use in a fluidized bed reactor for production of polysilicon-coated granulate material are disclosed. The liners include an aperture and a cavity configured to receive a reactor component, such as a probe, a sensor, a nozzle, a feed line, a sampling line, a heating/cooling component, or the like. In some embodiments, the liner is a segmented liner comprised of vertically stacked or laterally joined segments, wherein at least one segment includes an aperture and a cavity configured to receive a reactor component.
Reactor component placement inside liner wall
Reaction chamber liners for use in a fluidized bed reactor for production of polysilicon-coated granulate material are disclosed. The liners include an aperture and a cavity configured to receive a reactor component, such as a probe, a sensor, a nozzle, a feed line, a sampling line, a heating/cooling component, or the like. In some embodiments, the liner is a segmented liner comprised of vertically stacked or laterally joined segments, wherein at least one segment includes an aperture and a cavity configured to receive a reactor component.
FLUIDIZED BED REACTOR FOR PREPARING CHLOROSILANES
The lifetime of a fluidized bed reactor containing silicon particles, for the production of chlorosilanes is greatly extended by armoring at least a portion of the reactor shell interior wall with expanded metal coated with a cement containing ceramic particles.
Processes for increasing bioalcohol yield from biomass
A process for increasing alcohol yield from biomass (the form or agro- or forest residue, grains, hops, etc.), involving multiple hydrodynamic cavitation treatments of biomass filtrateboth before and after fermentation. Carbohydrates extracted from biomass are subjected to a first cavitation treatment to promote additional conversion into carbohydrates. The carbohydrates are then combined with bacterial species and nutrients, and allowed to ferment. The fermentation product is subjected to a second hydrodynamic cavitation treatment to promote further conversion of carbohydrates into bioalcohol. After distillation, the bioalcohol is subjected to a second hydrodynamic cavitation treatment to increase its purity.
FLUIDIZED BED REACTOR INCLUDING LINER
A fluidized bed reactor includes a reactor core and a stack of liner segments. The stack includes a first liner segment and a second liner segment. The first liner segment includes a first edge having a base surface and an angled surface. The base surface and the angled surface form an obtuse angle. The second liner segment includes a second edge. The first edge and the second edge form a shiplap joint to connect the first liner segment to the second liner segment.