Bepex International, LLC

Other

Hosokawa Bepex Corporation

Bepex Corporation

Gregory J Kimball

David L Phillips

Ilya Pikus

Peter M Koenig

David Lonnie Phillips

Hanford N Lockwood, Jr

Peder K Langsetmo

Richard W Ozer

Joseph Merwyn Bonem

Charles L Stock

Extraction of bitumen from oil sands may generate oil sands tailings mixed with a liquid. Systems may be used to separate the liquid from the tailings so the tailings can be disposed or otherwise reclaimed. In some examples, a system includes a primary separation vessel configured to receive oil sands tailings mixed with water and to separate the oil sands tailings into a plurality of layers, where at least one of the plurality of layers includes a mature fines tailing material. The system may include an apparatus configured to receive the mature fines tailing material from the primary separation vessel and to mechanically separate a portion of the water in the mature fine tailings material. The system may also include an apparatus configured to receive a concentrated oil sands tailings material and to thermally evaporate water from the concentrated oil sands tailings materials, thereby producing trafficable dried oil sands tailings.

System and method for the treatment of oil sands

Systems and processes may be used for continuously processing a solid material at a non-atmospheric pressure. In some examples, the material is delivered to a process vessel at substantially the same non-atmospheric pressure condition as the process vessel so as to avoid shearing the material. In some examples, the solid material is continuously fed into a process vessel, continuously processed in the process vessel, and continuously discharged from the process vessel.

System and method for the continuous treatment of solids at non-atmospheric pressure

Systems and processes may be used for continuously processing a solid material such as a solid starch-bearing material at a non-atmospheric pressure. In some examples, the material is delivered to a process vessel at substantially the same non-atmospheric pressure condition as the process vessel so as to avoid shearing the material. In some examples, the solid material is continuously fed into a process vessel, continuously processed in the process vessel, and continuously discharged from the process vessel.

A continuous gravity flow apparatus for heating and/or drying of particulate material is vertically disposed and is provided with an inlet at the top and an outlet at the bottom. The apparatus includes a flow passage for the particulate material which is defined between an outer housing and an inner housing. Each of the outer and inner housing defines perforated wall sections allowing for the flow of hot gas through the wall of one housing, into contact with the particulate material, and then out through the wall of the other housing. Manifolds are associated with the outer and inner housings to provide for uniform flow of the gas through the material. The perforated wall sections are positioned and designed to enhance particle-to-particle movement of the material to thereby avoid particle sticking and bridging problems.

Heating and drying apparatus for particulate material

A method for thermally processing polyester pellets by crystallization and polymerization in the solid state which comprises providing a confined processing unit. The pellets are introduced to said unit along with a liquid medium. The combination of pellets and liquid medium is agitated to achieve mixing and the temperature of the agitated mixture is controlled to achieve treating of the polyester pellets in the agitated heating liquid medium at a temperature slightly below the sticking temperature of the polyester. The treatment is continued for a period sufficient to substantially increase the crystallinity and molecular weight of the polyester.

Method for thermally processing polyester pellets

A system for material drying comprising a pulse combustor and an associated combustion chamber whereby a pulsating flow of hot gases are generated. A tail pipe is connected to the outlet of the combustion chamber for receiving the pulsating flow of hot gases and a material introduction chamber is connected at the outlet of the tail pipe. A drying chamber is connected at the outlet of the material introduction chamber. The hot pulse combustion exhaust gases are cooled to control the temperature of the gases issuing from the outlet of the tail pipe and entering the material introduction chamber. This control is accomplished with a cool air stream issuing into the pulse combustion mixing chamber along with the hot gases from the pulse combustion tail pipe for mixing with and cooling of the hot gases. A separate diluent air stream may be employed for contact with material issuing from the introduction chamber and passing into the drying chamber. This separate diluent air stream will urge material already present in the drying chamber away from the entry location of new material into the drying chamber. The tail pipe may be provided with an inlet end of restricted dimension to act as a venturi with respect to the pulsating stream of hot gases entering the tail pipe from the combustion chamber thereby increasing the sound levels measured at the pulse combustion discharge.

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Blaine, MN, United States of America

Gregory J Kimball