Apparatus and method for separating heavy impurities from feed stock

Claim 2

Apparatus for removing heavy impurities from feed stock, comprising a primary classifying chamber having an upper section of circular cross section and a downwardly-converging conical lower section, a central stock outlet pipe extending upwardly through said upper section of the primary chamber and terminating in an end in the lower section thereof spaced a substantial distance from the conical section wall, an outlet in the lower end of the lower section, an inlet pipe for directing feed stock containing heavy impurities tangentially into said chamber upper section to create a vortex flow in the primary chamber, said heavy impurities being separated outwardly by centrifugal force from feed stock being directed to said outlet pipe by centripetal force, said centripetal force being minimal in the upper section and said centrifugal force being maximal in the lower section, a secondary classifying chamber connected to the lower end of said lower conical section to receive the heavy impurities with feed stock therefrom, said secondary classifying chamber having a substantially unobstructed inlet and being formed with an upper section abruptly increasing the diameter directly from said conical lower section of the primary classifying chamber in a downward and lateral direction to a maximum cross sectional area rapidly to reduce the velocity of the vortex flow of the stock and impurities therein, said upper section of the secondary classifying chamber having a substantially greater inclination from the vertical than said conical lower section of the primary classifying chamber, said upper section of the secondary classifying chamber lying at an acute angle with respect to the conical lower section of the primary classifying chamber, and a lower conical section of the secondary classifying chamber converging from said maximum cross sectional area to an outlet controlled by a valve, and means for directing a diluent tangentially into the reduced velocity stock in the secondary classifying chamber in a direction counter to the movement of said stock further to dilute the stock to assist separation of the heavy impurities by gravity and to return lighter valuable components of the stock to the primary chamber.

Claim 3

Apparatus as claimed in claim 1 comprising a reject chamber in communication with the lower conical section of the secondary chamber through the outlet thereof when the valve of the latter outlet is open, said reject chamber having an outlet controlled by a valve, and inlet means for directing a diluent into the reject chamber near the lower end thereof to flush said reject chamber and to drive any stock fibers therein back into said lower conical section.

Claim 4

Apparatus as claimed in claim 1 in which the central stock outlet pipe has a downwardly converging conical end section, said downwardly converging end section commencing in said upper section of said primary classifying chamber; and at least one opening formed in said end section.

Claim 5

Apparatus as claimed in claim 3, including flaps extending outwardly from an edge of each opening, across the respective opening.

Claim 6

Apparatus as claimed in claim 4 in which there are four openings equidistantly positioned around said end section and in which the flaps are formed by cutting out openings in the end section, shaping the cut out portions to a substantially arcuate shape and attaching each of them at one edge to an opening.

Claim 7

Apparatus as claimed in claim 1 including an inlet for directing a diluent tangentially into said lower section of the primary chamber, said inlet being elongated in the direction extending from the upper section to said secondary classifying chamber to permit the introduction of a band of lower consistency stock into said lower section; an inlet for directing a diluent tangentially into the reduced velocity stock in the secondary classifying chamber in a direction counter to the movement of said stock to assist separation of the heavy impurities by gravity and to return lighter valuable components of the stock to the primary chamber; baffles formed on said lower conical section of the secondary classifying chamber.

Claim 8

Apparatus as claimed in claim 6 in which the inlet for directing diluent tangentially into the reduced velocity stock in the secondary classifying chamber directs the diluent into the upper section of said secondary classifying chamber.

Claim 9

Apparatus as claimed in claim 6 in which the upper section of circular cross section of said primary classifying chamber is relatively elongated to provide greater dwell time for the feed stock in said upper section.

Claim 10

Apparatus as claimed in claim 1 comprising a reject chamber in communication with the lower conical section of the secondary chamber through the outlet thereof when the valve of the latter outlet is open, said reject chamber having an outlet controlled by a valve, inlet means for directing a diluent into the reject chamber near the lower end thereof to flush said reject chamber and to drive any stock fibres therein back into said lower conical section, a holding chamber having an inlet communicating with said outlet of said reject chamber and having an outlet controlled by a valve.

Claim 11

Apparatus as claimed in claim 9 in which the valve controlling the outlet of the secondary classifying chamber, the valve controlling the outlet of said reject chamber and the valve controlling the outlet of said holding chamber are interlocked so that only one of the three valves can be opened at any one time.

Claim 12

Apparatus for removing heavy impurities from feed stock, comprising a primary classifying chamber having an upper section of circular cross section and a downwardly-converging conical lower section, a central stock outlet pipe extending downwardly through said upper section of the primary chamber and terminating in an end in the lower section thereof spaced a substantial distance from the conical section wall, an outlet in the lower end of the lower section, an inlet pipe for directing feed stock containing heavy impurities tangentially into said chamber upper section to create a vortex flow in the primary chamber, said heavy impurities being separated outwardly by centrifugal force from feed stock being directed to said outlet pipe by centripetal force, said centripetal force being minimal in the upper section and said centrifugal force being maximal in the lower section, an inlet controlled by a valve for directing a diluent tangentially into said lower section of the primary chamber adjacent said end of the outlet pipe and in the direction of flow of stock in said lower section, said diluent, when said valve is open, diluting and controlling the stock consistency in said primary chamber lower section and separating relatively large particles of lighter weight from the heavy impurities and directing said separated particles into the stock flowing out through the outlet pipe, a secondary classifying chamber connected to the lower end of said lower conical section to receive the heavy impurities with feed stock therefrom, said secondary classifying chamber having a substantially unobstructed inlet and being formed with an upper section abruptly increasing in diameter directly from said outlet of the conical lower section of the primary classifying chamber in a downward and lateral direction to a maximum cross sectional area rapidly to reduce the velocity of the stock and impurities therein, said upper section of the secondary classifying chamber having a substantially greater inclination from the vertical than the conical lower section of the primary classifying chamber, said upper section of the secondary classifying chamber lying at an acute angle with respect to the conical lower section of the primary classifying chamber, and a lower conical section of the secondary classifying chamber coverging from said maximum cross sectional area to an outlet controlled by a valve, and means for directing a diluent tangentially into the reduced velocity stock in the secondary classifying chamber in a direction counter to the movement of said stock further to dilute the stock to assist separation of the heavy impurities by gravity and to return lighter valuable components of the stock to the primary chamber.

Claim 13

Apparatus for removing heavy impurities from feed stock, comprising a primary classifying chamber having an upper section of circular cross section and a downwardly-converging conical lower section, a central stock outlet pipe extending downwardly through said upper section of the primary chamber and terminating in an end in the lower section thereof spaced a substantial distance from the conical section wall, an outlet in the lower end of the lower section, an inlet pipe for directing feed stock containing heavy impurities tangentially into said chamber upper section to create a vortex flow in the primary chamber, said heavy impurities being separated outwardly by centrifugal force from feed stock being directed to said outlet pipe by centripetal force, said centripetal force being minimal in the upper section and said centrifugal force being maximal in the lower section, an inlet controlled by a valve for directing a diluent tangentially into said lower section of the primary chamber adjacent said end of the outlet pipe and in the direction of flow of stock in said lower section, said diluent, when said valve is open, diluting and controlling the stock consistency in said primary chamber lower section and separating relatively large particles of lighter weight from the heavy impurities and directing said separated particles into the stock flowing out through the outlet pipe, a secondary classifying chamber connected to the lower end of said lower conical section to receive the heavy impurities with feed stock therefrom, said secondary classifying chamber having a substantially unobstructed inlet and being formed with an upper section abruptly increasing in diameter directly from said outlet of the conical lower section of the primary classifying chamber in a downward and lateral direction to a maximum cross sectional area rapidly to reduce the velocity of the stock and impurities therein, said upper section of the secondary classifying chamber having a substantially greater inclination from the vertical than the conical lower section of the primary classifying chamber, said upper section of the secondary classifying chamber lying at an acute angle with respect to the conical lower section of the primary classifying chamber, and a lower conical section of the secondary classifying chamber coverging from said maximum cross sectional area to an outlet controlled by a valve, and means for directing a diluent tangentially into the reduced velocity stock in the secondary classifying chamber in a direction counter to the movement of said stock further to dilute the stock to assist separation of the heavy impurities by gravity and to return lighter valuable components of the stock to the primary chamber.

Claim 14

Apparatus as claimed in claim 11 comprising a reject chamber in communication with the lower conical section of the secondary chamber through the outlet thereof when the valve of the latter outlet is open, said reject chamber having an outlet controlled by a valve, and inlet means for directing a diluent into the reject chamber near the lower end thereof to flush said reject chamber and to drive any stock fibres therein back into said lower conical section.

Claim 15

A process for separating heavy impurities from feed stock, comprising the steps of introducing feed stock tangentially into a primary zone of circular cross section to create a vortex flow in said zone and thereby effect a primary classifying action by centrifugal force on the feed stock, extracting clarified stock subjected to centripetal force in the primary zone from said primary zone centrally thereof, selectively directing a diluent into the primary zone tangentially in the direction of flow of stock therein to dilute dand control the consistency of the stock and to separate relatively large but lighter particles from the heavy impurities and directing said particles out with the clarified stock, passing residual stock containing impurities through a substantially unobstructed passage into a secondary zone with a vortex flow, rapidly stopping the vortex flow of the residual stock in the secondary zone by moving the residual stock directly from said secondary zone, across a boundary which forms an acute angle and into a chamber which diverges radially at a substantially greater rate than the vortex flow, directing diluent into the residual stock in the secondary zone in a direction counter to movement of said stock to assist further reduction of the vortex flow, and continuously passing stock with the impurities therein out of the secondary chamber and into a reject zone.

Claim 16

A process for separating heavy impurities from feed stock, comprising the steps of introducing feed stock tangentially into a primary zone of circular cross section to create a vortex flow in said zone and thereby effect a primary classifying action by centrifugal force on the feed stock, extracting clarified stock subjected to centripetal force in the primary zone from said primary zone centrally thereof, selectively directing a diluent into the primary zone tangentially in the direction of flow of stock therein to dilute dand control the consistency of the stock and to separate relatively large but lighter particles from the heavy impurities and directing said particles out with the clarified stock, passing residual stock containing impurities through a substantially unobstructed passage into a secondary zone with a vortex flow, rapidly stopping the vortex flow of the residual stock in the secondary zone by moving the residual stock directly from said secondary zone, across a boundary which forms an acute angle and into a chamber which diverges radially at a substantially greater rate than the vortex flow, directing diluent into the residual stock in the secondary zone in a direction counter to movement of said stock to assist further reduction of the vortex flow, and continuously passing stock with the impurities therein out of the secondary chamber and into a reject zone.

Claim 17

A process as claimed in claim 13 comprising the additional step of directing a diluent into said reject zone near a lower end thereof to flush said zone and to drive any stock fibres therein back into the secondary zone.