Abstract:
A process for thermal separation of a solution comprised of a thermoplastic polymer and a solvent involves heating a solvent under pressure above a critical point of the solvent; decompressing the heated solvent in a first vessel, such that a polymer-rich and a low-polymer phase form; and supplying the polymer-rich phase to a second vessel. In embodiments, on entry into the second vessel, a pressure jump occurs, the pressure jump leading to a thermal flash in the second vessel such that a polymer part of the polymer-rich phase rises to at least 70%, and a resulting polymer-rich solution is provided.
Abstract:
A catalyst loading system comprising: a vessel comprising at least one gas distribution nozzle at or near the bottom of the vessel, a top fluid distributor located at or near the top of the vessel, a catalyst inlet through which catalyst is introduced into the vessel, a first contact point at which catalyst introduced into the vessel first contacts the contents of the vessel, and a discharge outlet whereby catalyst exits the vessel. Methods of preparing catalyst slurry for introduction into a downstream reactor or in-situ activation within the vessel utilizing the catalyst loading system are also disclosed.
Abstract:
A continuous process to upgrade heavy crude oil for producing more valuable crude feedstock having high API gravity, low asphaltene content, and high middle distillate yield, low sulfur content, low nitrogen content, and low metal content without external supply of hydrogen and/or catalyst. Heavy crude oil having substantial amount of asphaltene and heavy components is mixed with highly waxy crude oil having large amount of paraffinic components and water to decompose asphaltene compounds and remove sulfur, nitrogen, and metal containing substances under supercritical conditions. Product has higher API gravity, lower asphaltene content, high middle distillate yield, lower sulfur content, lower nitrogen content, and lower metal content to be suitable for conventional petroleum refining process.
Abstract:
A reservoir is supported by a base in a vertical position. A reciprocating member is positioned in the reservoir forming an internal chamber. The chamber receives growth factor starting material through an inlet in the reciprocating member. After the inlet is sealed, the reciprocating member increases the volume of the chamber to apply negative pressure to the growth factor starting material within the chamber to produce activated growth factors. The activated growth factors are extracted from the chamber through an outlet in the reciprocating member. Optionally, the growth factor starting material is held in the chamber to separate into fractions.
Abstract:
A vacuum processing device and a vacuum processing method that strongly chuck and hold an insulating substrate when plasma processing is performed are provided. The vacuum processing device includes a vacuum chamber that is grounded; a vacuum evacuation device connected to the vacuum chamber; a chuck device arranged inside the vacuum chamber; a chuck power supply for applying an output voltage to a single-pole type electrode provided in the chuck device; a plasma generation gas introduction device for introducing a plasma generation gas into the vacuum chamber; and a plasma generation portion which converts the plasma generation gas into plasma. An object to be processed is arranged on the chuck device; and the chuck power supply applies an output voltage to the single-pole type electrode while the plasma is being generated inside the vacuum chamber; and the object to be processed is processed by the plasma while the object to be processed is being chucked by the chuck device. An insulating substrate is used as the object to be processed and the chuck power supply applies the output voltage that periodically changes between a positive voltage and a negative voltage to the single-pole type electrode.
Abstract:
Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.
Abstract:
Apparatus and methods are provided for converting methane in a feed stream to acetylene. A hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream may be treated to convert acetylene to another hydrocarbon process.
Abstract:
Apparatus and methods are provided for converting methane in a feed stream to acetylene. A supersonic reactor is used for receiving the methane feed stream and heating the methane feed stream to a pyrolysis temperature. A high temperature carrier stream passes through the reactor chamber at supersonic speeds. According to various aspects, a static mixer is provided for mixing the methane feed stream and the carrier stream.
Abstract:
Apparatus and methods are provided for converting methane in a feed stream to acetylene. A supersonic reactor is used for receiving the methane feed stream and heating the methane feed stream to a pyrolysis temperature. A high temperature carrier stream passes through the reactor chamber at supersonic speeds. According to various aspects, a static mixer is provided for mixing the methane feed stream and the carrier stream.
Abstract:
Methods and systems are provided for converting methane in a feed stream to acetylene. The method includes processing the acetylene to form a stream having acrylic acid. The hydrocarbon stream is introduced into a supersonic reactor and pyrolyzed to convert at least a portion of the methane to acetylene. The reactor effluent stream is be treated to convert acetylene to acrylic acid. The method according to certain aspects includes controlling the level of carbon monoxide to prevent undesired reactions in downstream processing units.