A cyclonic chiller-separator, including a vertically oriented treatment tower defining an interior space and having an exhaust inlet disposed in an upper portion, and a chimney with an exhaust outlet; an exhaust stream conduit in fluid communication with said interior volume of said treatment tower through said exhaust inlet, wherein said exhaust inlet is configured to induce cyclonic fluid motion in an exhaust stream entering said interior volume; a coolant water source; and a plurality of nozzles disposed about interior walls of said treatment tower and in fluid communication with said coolant water source for spraying cooling water into said interior volume above and into an exhaust stream introduced into said interior volume so as to cool, condense, and precipitate volatile organic compounds and organic acids, and to entrain and remove particulates from the exhaust stream.

This disclosure provides a two-phase separator device for separating condensate or particulate from a gas stream. In some implementations, the separator device removes water from air and may operate under micro-gravity conditions. The gas stream flows through the two-phase separator device and passes through a rotatable vane assembly along a flow path without being redirected in another flow path. Condensate or particulate in the gas stream is impacted by a plurality of vanes of the rotatable vane assembly, and the condensate is captured by features formed within the plurality of vanes. The captured condensate is accelerated radially outwardly along the each of the plurality of vanes towards a sloped inner wall, and further moved along the sloped inner wall in a direction against the flow path of the gas stream during rotation.

This disclosure provides a two-phase separator device for separating condensate or particulate from a gas stream. In some implementations, the separator device removes water from air and may operate under micro-gravity conditions. The gas stream flows through the two-phase separator device and passes through a rotatable vane assembly along a flow path without being redirected in another flow path. Condensate or particulate in the gas stream is impacted by a plurality of vanes of the rotatable vane assembly, and the condensate is captured by features formed within the plurality of vanes. The captured condensate is accelerated radially outwardly along the each of the plurality of vanes towards a sloped inner wall, and further moved along the sloped inner wall in a direction against the flow path of the gas stream during rotation.

An apparatus and a method for separating glue particles from a glue aerosol are described. Accordingly, the device comprises a cyclone separator and a collection container arranged underneath for collecting glue particles running down from the cyclone separator. Due to the fact that the device further comprises a discharge line which is connected in a gas-tight manner to the cyclone separator and which projects downwards into the collection container in order to hydrostatically seal the cyclone separator at the discharge end by means of a solvent held in the collection container, separated particles can be continuously dissolved in the solvent and discharged by replacing the solvent without interruption of the cyclonic flow prevailing in the cyclone separator.

An apparatus and a method for separating glue particles from a glue aerosol are described. Accordingly, the device comprises a cyclone separator and a collection container arranged underneath for collecting glue particles running down from the cyclone separator. Due to the fact that the device further comprises a discharge line which is connected in a gas-tight manner to the cyclone separator and which projects downwards into the collection container in order to hydrostatically seal the cyclone separator at the discharge end by means of a solvent held in the collection container, separated particles can be continuously dissolved in the solvent and discharged by replacing the solvent without interruption of the cyclonic flow prevailing in the cyclone separator.

A method of centrifugal separation of particles, comprising providing a gas flow containing the particles, charging the particles in the gas flow, generating an aerosol of polar liquid droplets introducing the aerosol into the gas flow for attracting the charged particles by the polar liquid droplets, and separating the liquid droplets comprising the attracted particles from the gas flow by the centrifugal separation.

A method of centrifugal separation of particles, comprising providing a gas flow containing the particles, charging the particles in the gas flow, generating an aerosol of polar liquid droplets introducing the aerosol into the gas flow for attracting the charged particles by the polar liquid droplets, and separating the liquid droplets comprising the attracted particles from the gas flow by the centrifugal separation.

Vibrator is used to move circular strings in a harp-like screen to achieve frequencies corresponding with one of the natural frequencies of the strings as well as with the frequencies of gas vortices shedding off the strings in order to more efficiently: a) scrub particulates/droplets (solid or liquid) from the gas, b) exchange and utilize energy between the oncoming cold or hot gas and a liquid flowing down the screens in order to heat or cool the liquid, and c) agitate and, without clogging, more efficiently remove the liquid film streaming down the strings, i.e., to increase the sliding efficiency of the liquid flowing down the strings. With the strings vibrating in the resonant regime, particulate capture and energy and mass transfer are substantially enhanced compared to non-resonant, passive systems in which strings do not vibrate, or where vibrations are induced solely by the gas flow.

Vibrator is used to move circular strings in a harp-like screen to achieve frequencies corresponding with one of the natural frequencies of the strings as well as with the frequencies of gas vortices shedding off the strings in order to more efficiently: a) scrub particulates/droplets (solid or liquid) from the gas, b) exchange and utilize energy between the oncoming cold or hot gas and a liquid flowing down the screens in order to heat or cool the liquid, and c) agitate and, without clogging, more efficiently remove the liquid film streaming down the strings, i.e., to increase the sliding efficiency of the liquid flowing down the strings. With the strings vibrating in the resonant regime, particulate capture and energy and mass transfer are substantially enhanced compared to non-resonant, passive systems in which strings do not vibrate, or where vibrations are induced solely by the gas flow.

A wet scrubber apparatus has a housing with access doors and guides that allow for the installation of self-contained baffle modules. Selected baffle modules can to be inserted, exchanged, removed or left blank (no baffles) within the wet scrubber housing, depending on the desired process. The wet scrubber allows for variable performance and feature-enhancing for a target efficiency and effectiveness. The wet scrubber can incorporate a pump and pipe manifold “fluidizer” design that can spray water or fluid up onto the modules during operation of the wet scrubber to keep collected material off the baffles. Water can be sprayed throughout the modules onto the baffles during operation, or when the scrubber is offline, isolated from the gas to be scrubbed, during a cleaning operation. This water or fluid can come from an outside source or can be piped and valved to recirculate existing scrub water or fluid.