9results about "Flat flow vortex" patented technology

A dust separator including a top member having a top member having an inlet port arranged to supply dust-laden air and an outlet port arranged to remove clean air, the top member having a lower portion configured as a lip and having a radius which equals diameter of the inlet port, and a dust separator plate, housed within the lip, having a passage with at least one opening arranged to remove the dust from within the top member.

A cyclonic particle separator includes a first member having an arcuate outer wall and an inlet port having a diameter d1 extending from the outer wall in a first direction and an outlet port extending from the wall in a second direction, the first direction being different than the second direction; a separator plate in communication with the first member; and a cyclonic chamber defined by the separator plate and the outer wall, the cyclonic chamber, the separator plate, and the outlet port having a common central axis.

Separator apparatuses of various examples include a container and a lid for the container. The lid includes a cyclone separation device comprising a cyclone chamber for processing fluid and separating solids from the fluid, a cover portion disposed over an end of the cyclone chamber, a first, inlet channel through the cover portion for communicating fluid into the cyclone chamber, a second, outlet channel through the cover portion for communicating fluid out of the cyclone chamber. Separated solids can be received in a receiving region from a distal end or opening of the cyclone separation device, and fluid connection provided between the receiving region and the outlet channel or an outside of the container for removing fluid from the receiving region to the outlet channel or the outside of the container. The separation device can include wear detector means. A method of fluid processing includes using the separator apparatus.

The invention relates to a method and a plant (2) for carrying out this method for processing a target sorting fraction (1) with a polyolefin content of at least 80 m%, in particular of at least 90 m%, from a waste fraction (3) for further chemical and / or mechanical recycling of the target sorting fraction (1). The method comprises feeding a first mixed plastics fraction (4) and optionally additionally a second mixed plastics fraction (5) to a comminution device (7) and comminuting or homogenising said fraction(s) by means of a comminution device. The method further comprises the metal separation (12) of ferrous impurities (13) and / or magnetisable impurities (16), the impurity separation (19) of a first heavy fraction (20) and the fine separation (26) of a second heavy fraction (27), wherein the plant (2) comprises corresponding plant components for carrying out the method.

Separator apparatuses of various examples include a container and a lid for the container. The lid includes a cyclone separation device comprising a cyclone chamber for processing fluid and separating solids from the fluid, a cover portion disposed over an end of the cyclone chamber, a first, inlet channel through the cover portion for communicating fluid into the cyclone chamber, a second, outlet channel through the cover portion for communicating fluid out of the cyclone chamber. Separated solids can be received in a receiving region from a distal end or opening of the cyclone separation device, and fluid connection provided between the receiving region and the outlet channel or an outside of the container for removing fluid from the receiving region to the outlet channel or the outside of the container. The separation device can include wear detector means. A method of fluid processing includes using the separator apparatus.

The invention relates to a device for separating a liquid from a feedstock, in particular material to be ground or granulate of plastic, having a screen drum (1) comprising a screen drum base (2), a screen drum wall (3) and an outlet side (4) opposite the screen drum base (2), having a feed device (15) for feeding the feedstock into the screen drum (1) and having a discharge device (9) arranged on the outlet side (4) of the screen drum (1) for discharging the feedstock separated from liquid, wherein the screen drum (1) rotates about its centre longitudinal axis (5) and guides off the liquid, characterised in that the feed device (15) has a feed opening arranged on the screen drum base (2) and that a conveying device with at least one conveying element (16) for conveying the feedstock to the outlet side is arranged in the screen drum (1). The method also relates to a method for separating a liquid from a feedstock.

According to one aspect of the present invention, a filtration device includes a tank portion including a first tank to which a liquid containing foreign matters flows, and a pump provided at a central portion of the first tank to discharge the liquid stored in the first tank. The first tank includes a bottom surface, four side surfaces connected to the bottom surface, four corners to which the bottom surface and two of the four side surfaces are connected, and four inclined surfaces covering the four corners. The four inclined surfaces are inclined to be close to the bottom surface from a connecting portion to which the two side surfaces are connected toward the central portion.

A cyclonic particle separator may include a housing including a cylindrical sidewall having a plurality of flow entry ports. A cover member closes a first end of the cylindrical sidewall, and a mounting member having a flow exit opening defined therethrough is at a second end of the cylindrical sidewall. At least one particle exit passage is defined in the housing. Each of the plurality of flow entry ports includes a flow directing surface angled to direct a gas flow from upstream of the housing to enter the housing in a tangential direction relative to the cylindrical sidewall, causing a cyclone vortex. The cyclone vortex acts to separate particles from the gas flow. The cylindrical sidewall may have a first diameter, and the flow exit opening may have a second diameter, where a difference between the first diameter and the second diameter is greater than 12.5 millimeters.