Hydrocyclone separator arrangement

Claim 1

A hydrocyclone separator including a body having a wall defining an elongated chamber of generally circular cross-section and shaped such that it decreases in cross-sectional size from a large end to a smaller apex end, a reject outlet at the apex end and an accept outlet at the large end, both being located in axial alignment with said chamber, and means for feeding a liquid suspension generally tangentially into said chamber whereby to form a liquid vortex in said chamber surrounding a central air core extending longitudinally of the chamber, the feeding means including guide vane means defining channel means for the flow of said suspension therethrough, and wherein said accept outlet comprises an elongated tubular member defining an annular region between itself and the wall of said chamber with said guide vane means being located in the annular region and extending between said tubular member and the wall of the chamber such that the channel means has a width determined by the distance from said tubular member to said wall of said chamber throughout the length thereof, said guide vane means defining: (a) a transition section wherein the guide vane means are disposed at a shallow angle to the longitudinal axis of the chamber at the large end thereof to initially receive the feed suspension in a path of travel directed generally longitudinally of the chamber with such angle gradually increasing so as to gradually swing said suspension from motion in the generally longitudinal direction to motion in the form of a spiral around the longitudinal axis of said chamber, said channel means also being of gradually decreasing cross-sectional area along the length thereof to effect gradual acceleration of the suspension in said transition section, and (b) a helical section of constant lead smoothly connected to said transition section, wherein said channel means defined by the guide vane means in said helical section is of substantially constant cross-sectional area along the length thereof, to cause the accelerated suspension to rotate around the chamber axis to impart centrifugal and shear forces thereto and to effect partial separation of the suspension prior to entry of the suspension into the separation chamber across substantially the full width of the annular region between said tubular member and the wall of the chamber.

Claim 9

A method of separating suspensions in a hydrocyclone separator including a body having a wall defining an elongated chamber of generally circular cross-section and shaped such that it decreases in cross-sectional size from a large end to a smaller apex end with a reject outlet for heavier portions of the suspension at the apex end and a tubular accept outlet for lighter portions of the suspension at the large end, both being located in axial alignment with said chamber, the accept outlet defining an annular region between itself and the chamber wall and having guide vane means in said annular region defining a transition section wherein the guide vane means are initially at a shallow angle to the longitudinal axis of the chamber and a helical section of constant lead smoothly connected to said transition section, the method including feeding a liquid suspension into said chamber whereby to form a liquid vortex in said chamber surrounding a central air core extending longitudinally of the chamber, said step of feeding the liquid suspension including passing the feed suspension into the separator via the full area of the annular region defined between the accept outlet and the chamber wall and in a path of travel initially directed generally longitudinally of the chamber in the transition section and then gradually swinging said suspension from motion in the generally longitudinal direction to motion in the form of a spiral path around the longitudinal axis of the chamber while gradually accelerating the suspension by way of a gradual reduction in the cross-sectional area of the flow path of the suspension along its length as it travels along the transition section, the width of said path being at all times equal to the distance between the tubular accept outlet and the chamber outlet and the chamber wall, and then causing the suspension to enter the helical section and to rotate around the chamber axis while travelling in a flow path of substantially constant cross-sectional area to impart centrifugal forces thereto so as to induce heavier particles in the suspension to move radially outwardly to the wall of the chamber before the suspension enters into the separation chamber and feeding the suspension generally tangentially into the separation chamber in a path whose width is defined by the distance between said tubular accept outlet and the chamber wall.

Claim 10

A method of separating suspensions in a hydrocyclone separator including a body having a wall defining an elongated chamber of generally circular cross-section and shaped such that it decreases in cross-sectional size from a large end to a smaller apex end with a reject outlet for heavier portions of the suspension at the apex end and a tubular accept outlet for lighter portions of the suspension at the large end, both being located in axial alignment with said chamber, the accept outlet defining an annular region between itself and the chamber wall and having guide vane means in said annular region defining a transition section wherein the guide vane means are initially at a shallow angle to the longitudinal axis of the chamber and a helical section of constant lead smoothly connected to said transition section, the method including feeding a liquid suspension into said chamber whereby to form a liquid vortex in said chamber surrounding a central air core extending longitudinally of the chamber, said step of feeding the liquid suspension including passing the feed suspension into the separator via the full area of the annular region defined between the accept outlet and the chamber wall and in a path of travel initially directed generally longitudinally of the chamber in the transition section and then gradually swinging said suspension from motion in the generally longitudinal direction to motion in the form of a spiral path around the longitudinal axis of the chamber while gradually accelerating the suspension by way of a gradual reduction in the cross-sectional area of the flow path of the suspension along its length as it travels along the transition section, the width of said path being at all times equal to the distance between the tubular accept outlet and the chamber outlet and the chamber wall, and then causing the suspension to enter the helical section and to rotate around the chamber axis while travelling in a flow path of substantially constant cross-sectional area to impart centrifugal forces thereto so as to induce heavier particles in the suspension to move radially outwardly to the wall of the chamber before the suspension enters into the separation chamber and feeding the suspension generally tangentially into the separation chamber in a path whose width is defined by the distance between said tubular accept outlet and the chamber wall.