Method and apparatus for controlling the effect of the centrifugal force on the stock in pulp defibrating apparatus

Claim 2

In the method of refining pulp stock in which the pulp material is ground in a grinding space defined between a pair of grinding discs having ridges and grooves providing opposing grinding surfaces, which discs rotate relative to one another in an environment of a fluid medium under superatmospheric pressure and correspondingly elevated temperature in a housing, and in which grinding space the pulp material is accelerated from a central portion outwards towards a peripheral portion by the centrifugal force generated by the relative rotational movement of the discs, the improvement for controlling the effect of the centrifugal force on the pulp, comprising: axially inclining the peripheral portion of the grinding space to form an inner passage extending from said central portion and an outer axially inclined passage having a peripherally outer stationary grinding surface facing an inner rotating grinding surface, the length of said inner passage and the angle of inclination of said outer passage being calculated in accordance with the pulp material and the equipment used to maximize the effect of the centrifugal force exerted on the pulp material in the direction of flow through said inner passage and split the centrifugal force exerted on the pulp material in said outer passage into two force vectors, the vector perpendicular to the direction of flow being greater than the vector in the axial direction of flow, to thereby reduce the outwardly accelerating force.

Claim 3

Method according to claim 1, in which the effect of the centrifugal force is additionally controlled by arranging the ridges and intervening grooves of the opposing grinding surfaces in the inclined portion of the grinding space so as to regulate the rate of flow of pulp stock in response to variables of the pulping process.

Claim 4

The method according to claim 1, comprising further inclining a portion of the inclined grinding space at an angle thereto to generate a force vector substantially neutralizing the effect of the centrifugal force in said further inclined portion.

Claim 5

The method according to claim 1, comprising further inclining a portion of the inclined grinding space to generate a centrifugal force vector opposing the direction of flow of pulp stock in said further inclined portion.

Claim 6

The method according to claim 2, in which the effect of the centrifugal force is additionally controlled by varying the angle between the ridges and grooves of the opposing grinding discs relative to a generatrix of the inclined portion of the grinding space to regulate the rate of flow of the pulp stock therethrough.

Claim 7

The method according to claim 1, in which the inclined passage of the grinding space extends at an angle of at least 45° to the radial portion of the grinding space.

Claim 8

The method according to claim 1, in which the inclined passage of the grinding space extends at an angle to the radial portion ranging between 45° and 90°.

Claim 9

In a pulp defibrating apparatus in which the pulp stock is ground in a grinding space defined between a pair of grinding discs having ridges and grooves providing opposing grinding surfaces, which discs rotate relative to one another in an environment of a fluid medium under superatmospheric pressure and correspondingly elevated temperature in a housing, and in which grinding space the pulp material is accelerated from a central portion outwards and towards a peripheral portion by the centrifugal force generated by the relative rotational movement of the discs; the improvement for controlling the effect of the centrifugal force on the pulp stock in the grinding space, comprising: (a) an inner portion of said grinding space extending peripherally outward from said central portion; (b) an axially inclined portion extending from the peripherally outward end of said inner portion forming a peripherally inner inclined rotating grinding surface facing an outer stationary grinding surface; (c) the length of said inner portion and the angle of said inclined portion relative to said inner portion being calculated in accordance with the pulp material to be ground and the equipment used to maximize the effect of the centrifugal force exerted in the direction of flow through said inner portion and split the centrifugal force exerted on the pulp material in said outer portion into two vector forces, the vector perpendicular to the direction of flow being greater than the vector in the axial direction of flow, to thereby reduce the outwardly accelerating force.

Claim 10

In a pulp defibrating apparatus in which the pulp stock is ground in a grinding space defined between a pair of grinding discs having ridges and grooves providing opposing grinding surfaces, which discs rotate relative to one another in an environment of a fluid medium under superatmospheric pressure and correspondingly elevated temperature in a housing, and in which grinding space the pulp material is accelerated from a central portion outwards and towards a peripheral portion by the centrifugal force generated by the relative rotational movement of the discs; the improvement for controlling the effect of the centrifugal force on the pulp stock in the grinding space, comprising: (a) an inner portion of said grinding space extending peripherally outward from said central portion; (b) an axially inclined portion extending from the peripherally outward end of said inner portion forming a peripherally inner inclined rotating grinding surface facing an outer stationary grinding surface; (c) the length of said inner portion and the angle of said inclined portion relative to said inner portion being calculated in accordance with the pulp material to be ground and the equipment used to maximize the effect of the centrifugal force exerted in the direction of flow through said inner portion and split the centrifugal force exerted on the pulp material in said outer portion into two vector forces, the vector perpendicular to the direction of flow being greater than the vector in the axial direction of flow, to thereby reduce the outwardly accelerating force.

Claim 11

The improvement according to claim 8, in which said inclined portion comprises grinding surfaces in which the opposing ridges and grooves are arranged to additionaly control the effect of the centrifugal force on the pulp stock to regulate its rate of flow through the grinding space in response to variables of the pulping process.

Claim 12

The improvement according to claim 9, in which the ridges and grooves of the opposing discs in the inclined portion of the grinding space are disposed at an angle relative to a generatrix of the inclined portion.

Claim 13

The improvement according to claim 8, in which the inclined portion of the grinding space extends at an angle of at least 45° to the inner portion.

Claim 14

The improvement according to claim 8, in which the inclined portion extends at an angle to the inner portion, ranging between 45° and 90°.

Claim 15

The improvement according to claim 8, in which the inclined portion extends at an angle to the inner portion effective to substantially neutralize the effect of the centrifugal force in the inclined portion.

Claim 16

The improvement according to claim 8, in which the center of gravity of the rotating discs is located in the central plane through a carrier disc supporting the inner grinding surface of the inclined grinding space.