Couette membrane filtration apparatus for separating suspended components in a fluid medium using high shear

Claim 3

A method according to claim 1 wherein the speed of rotation and local radii of the facing surfaces are selected to provide a uniform ratio of local gap thickness to local fluid suspension viscosity to maintain said constant value of shear stress.

Claim 4

A method according to claim 2 wherein the fluid is withdrawn at a rate such that the rate of withdrawal of the fluid does not exceed predetermined filtration velocities on the surface of the membrane.

Claim 5

A method according to claim 3 including the step of supporting the membrane by means of a plurality of ribs and channels incorporated into each surface upon which a membrane is mounted.

Claim 6

A method according to claim 4 wherein the fluid suspension is whole blood and the shear stress is maintained below the value at which significant hemolysis occurs.

Claim 7

A method according to claim 5 including the step of maintaining the gap at a predetermined minima along the path of the fluid and maintaining the speed of rotation of the surfaces relative to each other such that the shear stress to which the blood is subject does not exceed 1500 dynes/cm 2 .

Claim 8

A method according to claim 5 wherein the dimension and geometry of the gap, the flow rates and the angular velocity are maintained in a predetermined relation such that the variation of the Taylor number for whole blood is maintained at a minimum over the entire longitudinal extent of the membrane.

Claim 9

In the method of operating filter apparatus to separate blood components in a fluid suspension, including: (a) a first surface of revolution; (b) a membrane having a plurality of pores therethrough, the membrane defining a second surface of revolution spaced from and facing the first surface and defining therewith a shear gap of predetermined radial dimensions which are non-uniform in the axial length direction of the membrane, said first and second surfaces extending coaxially, (c) inlet means for introducing the fluid suspension into the gap; (d) means for rotating one of said surfaces about its axis of revolution relative to the other surface and at an angular velocity such that shear stress is imposed on the fluid suspension in the gap and laminar flow of the fluid suspension in the gap is created whereby fluid is separated from the fluid suspension and passes through the membrane pores; and (e) first outlet means for removal of fluid passing through the membrane pores, and other outlet means for removing fluid from the gap remotely from the inlet means, the steps that include: (f) introducing the fluid suspension into the gap between the first and second surfaces; (g) operating said means for rotating one surface relative to the other; and (h) controlling the speed of said relative rotation, whereby fluid passage through the pores of the membrane is maintained along the length of the membrane, said suspension consisting of blood from which fluid plasma is to be separated, the blood filling the gap, and including the steps, (i) producing laminar flow regions adjacent the pores and producing Taylor vortices in the gap, adjacent said laminar flow regions, with Taylor number maintained essentially constant over the length of the membrane, (j) and increasing the thickness of the gap between said surfaces, along length of the membrane between the inlet means and the other outlet means and in a direction toward said other outlet means to compensate for changes in fluid viscosity such that the shear stress imparted to the fluid suspension in and along the gap region adjacent the membrane pores is maintained substantially constant and below a level at which a component of the blood in the suspension would otherwise be damaged.

Claim 10

In the method of operating filter apparatus to separate blood components in a fluid suspension, including: (a) a first surface of revolution; (b) a membrane having a plurality of pores therethrough, the membrane defining a second surface of revolution spaced from and facing the first surface and defining therewith a shear gap of predetermined radial dimensions which are non-uniform in the axial length direction of the membrane, said first and second surfaces extending coaxially, (c) inlet means for introducing the fluid suspension into the gap; (d) means for rotating one of said surfaces about its axis of revolution relative to the other surface and at an angular velocity such that shear stress is imposed on the fluid suspension in the gap and laminar flow of the fluid suspension in the gap is created whereby fluid is separated from the fluid suspension and passes through the membrane pores; and (e) first outlet means for removal of fluid passing through the membrane pores, and other outlet means for removing fluid from the gap remotely from the inlet means, the steps that include: (f) introducing the fluid suspension into the gap between the first and second surfaces; (g) operating said means for rotating one surface relative to the other; and (h) controlling the speed of said relative rotation, whereby fluid passage through the pores of the membrane is maintained along the length of the membrane, said suspension consisting of blood from which fluid plasma is to be separated, the blood filling the gap, and including the steps, (i) producing laminar flow regions adjacent the pores and producing Taylor vortices in the gap, adjacent said laminar flow regions, with Taylor number maintained essentially constant over the length of the membrane, (j) and increasing the thickness of the gap between said surfaces, along length of the membrane between the inlet means and the other outlet means and in a direction toward said other outlet means to compensate for changes in fluid viscosity such that the shear stress imparted to the fluid suspension in and along the gap region adjacent the membrane pores is maintained substantially constant and below a level at which a component of the blood in the suspension would otherwise be damaged.

Claim 11

A method according to claim 8 wherein the apparatus is vertically oriented and the fluid suspension in the gap flows from the inlet means to said other outlet means under the influence of differential pressure and gravity.

Claim 12

A method according to claim 9 wherein the fluid suspension is whole blood, the fluid extracted from the suspension via the membrane pores is plasma, and the remaining portion of the fluid contains concentrated red blood cells and other blood particulate matter.

Claim 13

A method according to claim 8 wherein gap dimensions are selected at predetermined minimum values and the angular velocity of the one surface is controlled such that the blood is subjected to shear stress slightly less than the shear stress at which significant hemolysis begins to occur.

Claim 14

A method according to claim 11 wherein the angular velocity is selected such that the Taylor number for the blood in the gap does not exceed 1000.

Claim 15

A method according to claim 11 wherein the shear stress to which the blood is subjected does not exceed 1500 dynes/cm 2 .

Claim 16

A method according to claim 8 including varying the resistance to flow of fluid passing through the membrane such that resistance to such flow increases at locations corresponding to locations of gap increasing radial dimensions.

Claim 17

A method according to claim 8 including the step of controlling the speed of rotation such that the Taylor number for the blood in the gap does not exceed 1000.

Claim 18

A method according to claim 8 including the steps of maintaining the gap dimension, flow rate, trans-membrane pressure and angular velocity at values such that the rate of withdrawal of fluid via membrane pores does not exceed the critical filtration velocity for blood anywhere on the surface of the membrane.