The present invention provides a filling nozzle obtained by using a resin selected from a cycloolefin polymer and a cycloolefin copolymer, or a filling nozzle including a tubular passage for supplying a pharmaceutical solution, and a filling port disposed at a lower end of the tubular passage, in which the tubular passage and the filling port have a circular peripheral cross-section, and an inner diameter of the passage of the filling port is larger than an inner diameter of the tubular passage disposed on an upstream side.

A reactor for converting hydrogen sulfide into hydrogen gas and sulfur.

The present disclosure provides device comprising a cylindrical reaction vessel having one or more permeable cylindrical membranes disposed therein separating the cylindrical reaction vessel into at least a first portion and a second portion, wherein the one or more permeable cylindrical membranes are configured to permit first reactants from a first solution in the first portion or reactants from a second solution in the second portion to percolate or seep to a reaction zone proximate a surface of the one or more cylindrical membranes. A lifting device (mechanism) located above the first portion of the cylindrical reaction vessel configured to continuously draw a preform two-dimensional polymer tube formed by continuous reaction of the first and second reactants out from the reaction zone.

Devices, systems, and methods are provided that cause plasma-based chemical reactions. An example plasma-based reactor system includes a reactor chamber and an inlet port configured to provide an entry point for one or more reagents to enter the reactor chamber. The reactor system also includes an outlet port configured to provide an exit point for one or more chemical products to exit the reactor chamber. The reactor system also includes a resonator disposed within the reactor chamber and configured to provide a low-temperature coronal plasma when excited at a resonant wavelength. The low-temperature coronal plasma is configured to chemically modify at least a portion of the one or more reagents so as to form one or more chemical products.

A device for continuously producing hydrogen from polyester plastics by photocatalytic degradation is provided, including: a machine housing; a feeding mechanism provided at one side of the machine housing, a bottom of the feeding mechanism is in communication with a dissolving mechanism for transporting waste plastics to the dissolving mechanism; a dissolving mechanism provided inside the machine housing and configured for hydrolyzing the waste plastics into a solution containing small molecule monomers by means of a dissolving solution, the dissolving mechanism transports the solution to a photocatalytic reactor through a solution circulation pipeline; the solution circulation pipeline provided at the other side of the machine housing, two ends of the solution circulation pipeline are respectively connected to the dissolving mechanism and the photocatalytic reactor; the photocatalytic reactor provided above the dissolving mechanism and configured for degrading plastics in the solution to collect a reaction solution and hydrogen.

A device and method for producing a fluid product, such as a fluid reaction product, are provided. The device includes a reaction chamber and a reception chamber and a control unit configured to control the flow of fluid into the reaction chamber through the one or more fluid connections. The device also includes a first and second amount sensor arranged to determine an amount of fluidic component(s) of the reaction chamber and reception chamber continuously or at least quasi-continuously at least during the introduction of fluidic component(s).

A method of operating a dump tank of a polymer production process by transferring all or a portion of a content of a polymerization reactor into the dump tank, wherein the reactor contents comprise solid polymer, and liquid and gaseous non-product components, and removing at least a portion of the liquid and gaseous non-product components from the dump tank by: reducing a pressure of the dump tank, subjecting the solid polymer to a first cleaning stage comprising heating the solid polymer by introducing a first heated treatment gas into the dump tank, and subjecting the solid polymer to a second cleaning stage comprising purging the solid polymer by introducing a second heated treatment gas into the dump tank.

A reactive process for converting hydrogen sulfide into hydrogen gas and sulfur and a reactor for effecting such process.

Processes and apparatus for preparing bimodal polymers are provided. In some embodiments, processes include introducing a monomer, a first diluent, a catalyst, hydrogen, at a first hydrogen concentration, and optional comonomer, to a first loop reactor to produce, under polymerization conditions, a first slurry of polymer solids. Processes may also include continuously discharging the first slurry of polymer solids from the loop reactor as a first polymerization effluent to a first flash tank; separating the first polymerization effluent in the first flash tank to provide a first concentrated polymer slurry with significantly lower hydrogen concentration; and transferring the first concentrated polymer slurry from the flash tank to a re-slurry mixer. Processes may further include introducing a re-slurry mixer diluent to the first concentrated polymer slurry to form a second concentrated polymer slurry in the re-slurry mixer that can be pumped to a second slurry loop reactor.

Disclosed are a method and system for propylene polymerization utilizing a loop slurry reactor. The method can include polymerizing propylene in a loop slurry reactor under bulk polymerization conditions to produce polypropylene. The propylene polymerization system can include i) a loop slurry reactor and a heat exchange system that is configured to cool the legs of the loop slurry reactor and/or ii) an inlet manifold that is configured to connect flashline heaters to a separator.