Thin channel split flow process and apparatus for particle fractionation

Claim 2

A continuous process for fractinating small particles as small as polypeptides and no larger than biological cells contained in a fluid stream comprising: a. continuously introducing two or more fluid substreams of different composition into the inlet end of a thin enclosed channel having an inlet end possessing at least two inlet means and an outlet end possessing at least two outlet means and having a thickness which is very thin compared to the other two dimensions and is less than 5 millimeters, and has a length of not more than about 20 centimeters, and bringing a substream into contact with adjacent substreams so as to collectively form a series of thin laminae flowing parallel to one another within the channel and in contact with one another over a sufficient length of channel to allow a desired level of mass transport between and through the laminae without substantial hydrodynamic mixing between the laminae, b. continuously introducing a fluid medium containing the particles to be separated by means of one of said inlet means into one or more of the fluid substreams and varying the fluid composition of the non-particle containing substreams as needed to realize separation, c. at the outlet end of the channel splitting the collective channel stream into another set of substreams so as to permit separate recovery of at least two of the substreams at separate outlet means at the outlet end of the channel, d. adjusting the flow rates at the inlet end as well as at the outlet end so as to obtain the desired separation, e. continuously removing all of the substreams being separated at least two separate outlet means at the outlet end of the channel, f. during the separation process subjecting the channel to one or more transverse driving forces or gradients having a component perpendicular to the plane of the flow stream in the channel, and being selected from the group consisting of gravitation, centrifugation, electrical, dielectrical forces, cross-flow forces, temperature gradients, density gradients and concentration gradients, and combinations thereof.

Claim 3

A process as in claim 1 wherein the thickness of the channel varies from about 0.1 mm to 2.0 mm.

Claim 4

A process as in claim 1 wherein there are two or more of such separation cells or channels joined by fluid streams in which at least one of the outlet substreams from one cell is fed to at least one of the inlet substreams of another cell or of more than one cell.

Claim 5

A process as in claim 1 wherein means are employed at the inlet end of the channel to introduce two separate substreams.

Claim 6

A process as in claim 1 wherein splitter means are employed at the outlet end of the channel to split the stream into two substreams as it reaches the end of the channel.

Claim 7

A process as in claim 1 wherein the particles are introduced through the upper inlet substream and the flow rates of all substreams introduced at the inlet end as well as the flow rates of all of the substreams at the outlet end are varied such that the ratio of the flow rates in the upper substream relative to the lower substream or substreams is greater at the outlet end than at the inlet end and thereby creating a cross-over flow of the substreams.

Claim 8

A process as in claim 1 wherein the transverse driving force or gradient is centrifugation.

Claim 9

A process as in claim 1 wherein the transverse driving force or gradient is a temperature gradient.

Claim 10

A process as in claim 1 wherein the transverse driving force or gradient is a gradient in the fluid composition or in the concentration of a modifying material, established by introducing different compositions or different concentrations of said material into different inlet substreams.

Claim 11

A process as in claim 1 wherein the transverse driving force or gradient is a cross-flow.

Claim 12

A process as in claim 1 wherein the transverse driving force or gradient is a gradient in the concentration of sample particles, leading to separation based on different diffusion rates.

Claim 13

A process as in claim 1 wherein two transverse driving forces or gradients are combined.

Claim 14

A process as in claim 1 wherein the transverse driving force or gradient is a combination of gravitation and a density gradient.

Claim 15

A process as in claim 1 wherein the transverse driving force or gradient is a combination of centrifugation and a density gradient.

Claim 16

A process as in claim 1 wherein the transverse driving force or gradient is a combination of gravitation and cross flow.

Claim 19

An apparatus as in claim 16 wherein the thickness of the channel varies from about 0.1 mm to 2.0 mm.

Claim 20

An apparatus as in claim 16 wherein there are two or more such separation cells or channels joined by fluid streams in which one or more of the outlet substreams from one cell is fed to one or more of the inlet substreams of another cell or of more than one other cell.

Claim 21

An apparatus as in claim 16 wherein the inlet end walls and the outlet end walls within the interior of the channel converge to a point to form a narrow inlet and outlet port for the substreams.

Claim 22

An apparatus as in claim 16 wherein there is a physical splitter means present at the inlet end of the channel to split the incoming stream into substreams.

Claim 23

An apparatus as in claim 16 wherein there are from 1 to 9 physical splitter means at the outlet end of the channel to split the substreams as they approach the outlet end of the channel.

Claim 24

An apparatus as in claim 16 wherein means are present to vary the flow rates of the substreams at the inlet end as well as the flow rates of the substreams at the outlet end so as to effect a cross-over flow in the channel.

Claim 25

An apparatus as in claim 16 wherein the transverse driving force or gradient is gravitation.

Claim 26

An apparatus as in claim 16 wherein the transverse driving force or gradient is a temperature gradient.

Claim 27

An apparatus as in claim 16 wherein the transverse driving force or gradient is a gradient in the fluid composition or in the concentration of a modifying material, established by introducing different compositions or different concentrations of said material into different inlet substreams.

Claim 28

An apparatus as in claim 16 wherein the transverse driving force or gradient is a combination of at least two forces or gradients selected from the group consisting of gravitation, centrifugation, dielectrical forces, cross flow forces, temperature gradients, density gradients and concentration gradients.

Claim 29

An apparatus as in claim 16 wherein the transverse driving force or gradient is a transverse flow or cross flow induced by flow across permeable or semipermeable channel walls.

Claim 30

An apparatus as in claim 16 wherein the channel is constructed as a sandwich of thin spacer elements from which the channel volume and any splitting elements are created by cutting the appropriate volume and shape out of each of said spacer elements.

Claim 31

An apparatus as in claim 28 wherein triangular shaped pieces have been removed from the ends of some of the spacers so as to permit a smooth transition from the channel flow to the inlets and outlets.

Claim 32

An apparatus as in claim 16 wherein the channel is rectangular in shape.

Claim 33

A continuous process for fractinating small particles as small as polypeptides and no larger than biological cells contained in a fluid stream comprising: a. continuously introducing two or more fluid substreams of different composition into the inlet end of a thin enclosed channel having an inlet end possessing at least two inlet means and an outlet end possessing at least two outlet means and having a thickness which is very thin compared to the other two dimensions and is less than 5 millimeter, and has a length of not more than about 20 centimeters, and bringing the substream into contact with adjacent substreams so as to collectively form a series of thin laminae flowing parallel to one another within the channel and in contact with one another over a sufficient length of channel to allow a desired level of mass transport between and through the laminae without substantial hydrodynamic mixing between the laminae, b. continuously introducing the fluid medium containing the particles to be separated by means of one of said inlet means into one or more of the fluid substreams and varying the fluid composition of the non-particle containing substreams as needed to realize separation, c. employing one or more means along the length of the channel to split the stream as it passes along the channel causing one or more of the obtained substreams to enter the following section of channel as a new substream for that section, causing other substreams to exit the channel for collection, discarding or to enter another separation channel, and to introduce new substream into the channel from outside the channel, d. at the outlet end of the channel splitting the collective channel stream into another set of substreams so as to permit separate recovery of at least two of the substreams at separate outlet means at the outlet end of the channel, e. adjusting the flow rates at the inlet end as well as at the outlet end so as to obtain the desired separation, f. continuously removing all of the substreams being separated at at least two separate outlet means at the outlet end of the channel, g. during the separation process subjecting the channel to one or more transverse driving forces or gradients having a component perpendicular to the plane of the flow stream in the channel, and being selected from the group consisting of gravitation, centrifugation, electrical, dielectrical forces, cross-flow forces, temperature gradients, density gradients and concentration gradients, and combinations thereof.

Claim 34

A continuous process for fractinating small particles as small as polypeptides and no larger than biological cells contained in a fluid stream comprising: a. continuously introducing two or more fluid substreams of different composition into the inlet end of a thin enclosed channel having an inlet end possessing at least two inlet means and an outlet end possessing at least two outlet means and having a thickness which is very thin compared to the other two dimensions and is less than 5 millimeter, and has a length of not more than about 20 centimeters, and bringing the substream into contact with adjacent substreams so as to collectively form a series of thin laminae flowing parallel to one another within the channel and in contact with one another over a sufficient length of channel to allow a desired level of mass transport between and through the laminae without substantial hydrodynamic mixing between the laminae, b. continuously introducing the fluid medium containing the particles to be separated by means of one of said inlet means into one or more of the fluid substreams and varying the fluid composition of the non-particle containing substreams as needed to realize separation, c. employing one or more means along the length of the channel to split the stream as it passes along the channel causing one or more of the obtained substreams to enter the following section of channel as a new substream for that section, causing other substreams to exit the channel for collection, discarding or to enter another separation channel, and to introduce new substream into the channel from outside the channel, d. at the outlet end of the channel splitting the collective channel stream into another set of substreams so as to permit separate recovery of at least two of the substreams at separate outlet means at the outlet end of the channel, e. adjusting the flow rates at the inlet end as well as at the outlet end so as to obtain the desired separation, f. continuously removing all of the substreams being separated at at least two separate outlet means at the outlet end of the channel, g. during the separation process subjecting the channel to one or more transverse driving forces or gradients having a component perpendicular to the plane of the flow stream in the channel, and being selected from the group consisting of gravitation, centrifugation, electrical, dielectrical forces, cross-flow forces, temperature gradients, density gradients and concentration gradients, and combinations thereof.