Patent classifications
B04C7/00
Rice Input Structure of Automatic Electric Pressure Cooker
A rice input structure of an automatic electric pressure cooker that automatically adds rice and water for cooking includes a cyclone rice separator mounted on a lid and having an opening/closing hole for putting rice into an inner pot, an air intake pipe connected to one side of the cyclone rice separator and generating a intake pressure, a rice transfer pipe connected in a tangential direction of the cyclone rice separator and connected to a rice container, a valve passing through an axial direction of the cyclone rice separator to open and close the opening/closing hole, and a valve opening/closing device having a link pressing an upper end of the valve and an actuator rotating the link.
DUST SEPARATION APPARATUS AND INTELLIGENT CONTROL SYSTEM INCLUDING THE APPARATUS
The dust separation apparatus includes a dust intake unit including a blower, an inertial separation unit, a centrifugal separation unit, and a filtering separation unit. The dust intake unit, the inertial separation unit, the centrifugal separation unit, and the filtering separation unit are sequentially connected in series and together form a horizontal structure. The inertial separation unit and the centrifugal separation unit are connected in a horizontal-axis direction to form an inertial and centrifugal separation unit. A dust collection box is provided below and connected to the inertial and centrifugal separation unit. The filtering separation unit includes a dust collection barrel. The intelligent control system includes the dust separation apparatus and an intelligent control unit.
DUST COLLECTOR AND VACUUM CLEANER HAVING THE SAME
A dust collector includes a primary cyclone unit to separate dust from air introduced from outside dust collector and a secondary cyclone unit includes axial cyclones which separate fine dust from air introduced in an axial direction. The secondary cyclone unit includes a first group of axial cyclones disposed along a circumference of a first circle so as to contact an inner circumferential surface of an inner case, and formed to be partially spaced apart from the inner circumferential surface of the inner case to form first passages therebetween; and a second group of axial cyclones disposed to contact each other along a circumference of a second circle concentric with the first circle and smaller than the first circle, and formed to contact some of the first group of axial cyclones and to be spaced apart from others of the first group axial cyclones to form second passages therebetween.
DUST COLLECTOR AND VACUUM CLEANER HAVING THE SAME
The dust collector, that may be used in vacuum cleaner, includes: a primary cyclone unit separating dust from air introduced from outside the dust collector; and a secondary cyclone unit defining axial cyclone bodies separating fine dust from air introduced in an axial direction. The secondary cyclone unit includes casings having outer walls around hollow portions; and a fine dust separating member disposed on the casings to form the axial cyclones. The fine dust separating member includes vortex finders disposed in the casings; band portions enclosing an outer circumferential surface of the vortex finders at a position spaced from the vortex finders, and having a shape corresponding to the casings so as to form the axial cyclones together with the casings; and guide vanes disposed between the vortex finders and the band portions and extending in a spiral direction to induce a rotational flow of air.
Apparatus and method to clean particle loaded fluid using low energy multi-flow splitter technology requiring no filter media
The present invention relates to an apparatus and a method of cleaning particle loaded “dirty” air using a multi flow-splitter technology in combination with at least one cyclone system which requires minimal energy to operate due to low pressure drops used to generate the fluid flows whilst allowing to exert high centrifugal or G-Force on the infeed fluid stream. This further allows to operate the particle removal process such that conventional additional filter media become optional, such that the technology may operate a significantly reduced or even without the need for maintenance and/or repair. Low internal air turbulence ensures a very high separation efficiency. Optionally adding additional explosion safe low-energy down-stream filtration stages with variable speed system fan provides optimal operational performance and operational flexibility.
Systems and methods for removing contaminants from surfaces of solid material
Systems and methods for removing contaminants from surfaces of a solid material using a flow of compressible fluid to draw incompressible fluid through pathways between fragments of the solid material. At least one method includes introducing solid material into a processing chamber, concurrently directing compressible fluid and incompressible fluid into the processing chamber via the inlet fluid distribution manifold, and operating a vacuum pump to maintain a pressure at a discharge outlet of the processing chamber sufficient to promote the compressible and incompressible fluids each achieving a velocity of at least 10 meters per second within the processing chamber.
Systems and methods for removing contaminants from surfaces of solid material
Systems and methods for removing contaminants from surfaces of a solid material using a flow of compressible fluid to draw incompressible fluid through pathways between fragments of the solid material. At least one method includes introducing solid material into a processing chamber, concurrently directing compressible fluid and incompressible fluid into the processing chamber via the inlet fluid distribution manifold, and operating a vacuum pump to maintain a pressure at a discharge outlet of the processing chamber sufficient to promote the compressible and incompressible fluids each achieving a velocity of at least 10 meters per second within the processing chamber.
Librixer Comminutor and Particle Air Classifier System
A discharge arrangement (120) for a comminution reactor assembly (100). The discharge arrangement (120) comprises a main chamber (202) extending along a main axis (124). The main chamber has an inlet (121) arranged to be fluidly connected to a comminution reactor (110) and an outlet (122) arranged opposite from the inlet (121) along the main axis (124) and closeable by a common material take-out valve (204). The main chamber (202) is arranged to support a fluid-material stream (123) along a helical path about the main axis (124) from the inlet (121) towards the outlet (122). The discharge arrangement (120) further comprises an airduct (206) arranged extending into the main chamber (202) at an acute angle (a) with respect to the main axis (124). The airduct (206) comprises an aperture arranged facing the outlet (122). Thereby, a portion (125) of the fluid-material stream (123) changes direction from the helical fluid-material stream (123) about the main axis (124) from the inlet (121) towards the outlet (122) to a helical flow inside the airduct (206).
SYSTEMS AND METHODS FOR REMOVING CONTAMINANTS FROM SURFACES OF SOLID MATERIAL
Systems and methods for removing contaminants from surfaces of a solid material using a flow of compressible fluid to draw incompressible fluid through pathways between fragments of the solid material. At least one method includes introducing solid material into a processing chamber, concurrently directing compressible fluid and incompressible fluid into the processing chamber via the inlet fluid distribution manifold, and operating a vacuum pump to maintain a pressure at a discharge outlet of the processing chamber sufficient to promote the compressible and incompressible fluids each achieving a velocity of at least 10 meters per second within the processing chamber.
SYSTEMS AND METHODS FOR REMOVING CONTAMINANTS FROM SURFACES OF SOLID MATERIAL
Systems and methods for removing contaminants from surfaces of a solid material using a flow of compressible fluid to draw incompressible fluid through pathways between fragments of the solid material. At least one method includes introducing solid material into a processing chamber, concurrently directing compressible fluid and incompressible fluid into the processing chamber via the inlet fluid distribution manifold, and operating a vacuum pump to maintain a pressure at a discharge outlet of the processing chamber sufficient to promote the compressible and incompressible fluids each achieving a velocity of at least 10 meters per second within the processing chamber.