Ampholyte separation method and apparatus

Claim 2

An ampholyte separation apparatus comprising: a lower base plate; an upper base plate; at least two transversely extending barriers positioned between said upper and lower base plates and defining at least one transversely extending channel therebetween; a first semipermeable membrane abutting one end of each of said at least two transverse barriers; a second semipermeable membrane adjacent to and spaced-apart from the other end of each of said at least two transverse barriers so as to define a sample flow channel therebetween in fluid communication with said at least one transversely extending channel; a first electrode adjacent to said first semipermeable membrane and separated from said transversely extending barriers by said first semipermeable membrane; a second electrode adjacent to said second semipermeable membrane and separated from said sample flow channel by said second permeable membrane; a first temperature controllable thermal mass positioned in proximity to said first electrode; and a second temperature controllable thermal mass positioned in proximity to said second electrode; whereby an electric field and a pH gradient may be established along the length of said at least two transverse barriers so as to cause ampholytes flowing through said sample flow channel to be forced into said at least one transversely extending channel to differential positions corresponding to the isoelectric points of the ampholytes.

Claim 3

An apparatus according to claim 1 wherein said upper and lower base plates, said at least two transverse barriers and said thermal masses comprise copper.

Claim 4

An apparatus according to claim 2 wherein said upper and lower base plates, said at least two transverse barriers and said thermal masses are coated with polyethylene.

Claim 5

An apparatus according to claim 3 wherein acrylamide is grafted onto said polyethylene coating.

Claim 6

An apparatus according to claim 1 wherein said semipermeable membranes comprise cellulose acetate.

Claim 7

An apparatus according to claim 1 wherein said first electrode is a cathode and said second electrode is an anode.

Claim 8

An apparatus according to claim 6 wherein said electrodes comprise platinum.

Claim 9

An ampholyte separation apparatus comprising: a lower copper base plate; an upper copper base plate; a plurality of transversely extending copper barriers positioned between said upper and lower base plates and defining a plurality of transversely extending channels therebetween; a first semipermeable membrane of cellulose acetate extending along the length of said base plates and abutting one end of each of said transverse barriers; a second semipermeable membrane of cellulose acetate extending along the length of said base plates and being spaced-apart from the other end of each of said transverse barriers so as to define a sample flow channel therebetween in fluid communication with said transversely extending channels; a platinum cathode extending along and parallel to said first semi-permeable membrane and being separated from said transverse barriers by said first semi-permeable membrane; a platinum anode extending along and parallel to said second semi-permeable membrane and being separated from said flow channel by said second semi-permeable membrane; a first copper thermal mass positioned adjacent said cathode, said first copper thermal mass having an independent temperature control means; and a second copper thermal mass positioned adjacent said anode, said second copper thermal mass having an independent temperature control means; whereby an electric field and a pH gradient may be established along the length of said transverse barriers so as to cause ampholytes traveling through said flow channel to be forced into said transversely extending channels to differential positions corresponding to the isoelectric points of the ampholytes.

Claim 10

An ampholyte separation apparatus comprising: a lower copper base plate; an upper copper base plate; a plurality of transversely extending copper barriers positioned between said upper and lower base plates and defining a plurality of transversely extending channels therebetween; a first semipermeable membrane of cellulose acetate extending along the length of said base plates and abutting one end of each of said transverse barriers; a second semipermeable membrane of cellulose acetate extending along the length of said base plates and being spaced-apart from the other end of each of said transverse barriers so as to define a sample flow channel therebetween in fluid communication with said transversely extending channels; a platinum cathode extending along and parallel to said first semi-permeable membrane and being separated from said transverse barriers by said first semi-permeable membrane; a platinum anode extending along and parallel to said second semi-permeable membrane and being separated from said flow channel by said second semi-permeable membrane; a first copper thermal mass positioned adjacent said cathode, said first copper thermal mass having an independent temperature control means; and a second copper thermal mass positioned adjacent said anode, said second copper thermal mass having an independent temperature control means; whereby an electric field and a pH gradient may be established along the length of said transverse barriers so as to cause ampholytes traveling through said flow channel to be forced into said transversely extending channels to differential positions corresponding to the isoelectric points of the ampholytes.

Claim 11

An ampholyte separation apparatus comprising: at least two elongate barriers defining at least one elongate channel therebetween; a first semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to one end of each of said at least two elongate barriers; a second semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to the other end of each of said at least two elongate barriers; means for creating an electric field along the length of said at least two elongate barriers, said means for creating an electric field being positioned adjacent to said semi-permeable membranes so as to be separated from said elongate barriers by said semi-permeable membranes; and at least one flow channel extending substantially parallel to said semi-permeable membranes and substantially transverse to said at least two elongate barriers.

Claim 12

An ampholyte separation apparatus comprising: at least two elongate barriers defining at least one elongate channel therebetween; a first semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to one end of each of said at least two elongate barriers; a second semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to the other end of each of said at least two elongate barriers; means for creating an electric field along the length of said at least two elongate barriers, said means for creating an electric field being positioned adjacent to said semi-permeable membranes so as to be separated from said elongate barriers by said semi-permeable membranes; and at least one flow channel extending substantially parallel to said semi-permeable membranes and substantially transverse to said at least two elongate barriers.

Claim 13

An ampholyte separation apparatus comprising: at least two elongate barriers defining at least one elongate channel therebetween; a first semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to one end of each of said at least two elongate barriers; a second semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to the other end of each of said at least two elongate barriers; means for creating an electric field along the length of said at least two elongate barriers, said means for creating an electric field being positioned adjacent to said semi-permeable membranes so as to be separated from said elongate barriers by said said semi-permeable membranes; at least one flow channel extending substantially parallel to said semi-permeable membranes and substantially transverse to said at least two elongate barriers; and means for thermally establishing and controlling a pH gradient along the length of said at least two elongate barriers.

Claim 14

An ampholyte separation apparatus comprising: at least two elongate barriers defining at least one elongate channel therebetween; a first semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to one end of each of said at least two elongate barriers; a second semi-permeable membrane positioned transverse to said at least two elongate barriers and adjacent to the other end of each of said at least two elongate barriers; means for creating an electric field along the length of said at least two elongate barriers, said means for creating an electric field being positioned adjacent to said semi-permeable membranes so as to be separated from said elongate barriers by said said semi-permeable membranes; at least one flow channel extending substantially parallel to said semi-permeable membranes and substantially transverse to said at least two elongate barriers; and means for thermally establishing and controlling a pH gradient along the length of said at least two elongate barriers.

Claim 15

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through a flow channel which is transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte; and altering the pH gradient so as to cause the at least one ampholyte stabilized in said at least one elongate channel to reenter said flow channel and to be eluted and separately collected.

Claim 16

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through a flow channel which is transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte; and altering the pH gradient so as to cause the at least one ampholyte stabilized in said at least one elongate channel to reenter said flow channel and to be eluted and separately collected.

Claim 17

A process according to claim 11 wherein the pH gradient is thermally engendered so as to cause all of the ampholytes in solution to migrate into said at least one elongate channel and to stabilize at positions corresponding to their isoelectric points and wherein the pH gradient is altered so as to cause the ampholytes to reenter said flow channel at different times and to be separately eluted and collected.

Claim 18

A process according to claim 11 wherein the pH gradient is thermally engendered so as to cause one or more selected ampholytes to migrate into said at least one elongate channel and stabilize at positions corresponding to their isoelectric points while the other ampholytes remain in said flow channel so as to be eluted, and wherein the pH gradient is altered so as to cause the one or more selected ampholytes to reenter said flow channel at different times and to be separately eluted and collected.

Claim 19

A process for separating ampholytes comprising: directing a solution containing two or more ampholytes through a flow channel which is transverse to a plurality of elongate barriers, said elongate barriers defining a plurality of elongate channels; providing a first electrode adjacent one end of the transverse barriers and extending in the direction of the flow channel, said first electrode being separated from the transverse barriers by a first semi-permeable membrane which abuts the one end of said transverse barriers; providing a second electrode spaced-apart from the other end of the transverse barriers and extending in the direction of the flow channel, said second electrode being separated from the transverse barriers by a second semi-permeable membrane which is also spaced-apart from the other end of the transverse barriers and is adjacent to the flow channel; generating an electric field along the length of the transverse barriers with the first and second electrodes; providing a first temperature controllable thermal mass adjacent to said first electrode so that said first electrode is positioned between said first semi-permeable membrane and said first thermal mass; providing a second temperature controllable thermal mass adjacent to said second electrode so that said second electrode is positioned between said second semi-permeable membrane and said second thermal mass; thermally engendering a pH gradient along the transverse barriers with the first and second thermal masses so as to cause at least one of the ampholytes to migrate from the flow channel into the elongate channels and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte; and altering the pH gradient so as to cause the at least one ampholyte stabilized in the elongate channels to reenter the flow channel and to be eluted and separately collected.

Claim 20

A process for separating ampholytes comprising: directing a solution containing two or more ampholytes through a flow channel which is transverse to a plurality of elongate barriers, said elongate barriers defining a plurality of elongate channels; providing a first electrode adjacent one end of the transverse barriers and extending in the direction of the flow channel, said first electrode being separated from the transverse barriers by a first semi-permeable membrane which abuts the one end of said transverse barriers; providing a second electrode spaced-apart from the other end of the transverse barriers and extending in the direction of the flow channel, said second electrode being separated from the transverse barriers by a second semi-permeable membrane which is also spaced-apart from the other end of the transverse barriers and is adjacent to the flow channel; generating an electric field along the length of the transverse barriers with the first and second electrodes; providing a first temperature controllable thermal mass adjacent to said first electrode so that said first electrode is positioned between said first semi-permeable membrane and said first thermal mass; providing a second temperature controllable thermal mass adjacent to said second electrode so that said second electrode is positioned between said second semi-permeable membrane and said second thermal mass; thermally engendering a pH gradient along the transverse barriers with the first and second thermal masses so as to cause at least one of the ampholytes to migrate from the flow channel into the elongate channels and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte; and altering the pH gradient so as to cause the at least one ampholyte stabilized in the elongate channels to reenter the flow channel and to be eluted and separately collected.

Claim 21

A process according to claim 14 wherein said flow channel, said transverse barriers and said thermal masses comprise copper.

Claim 22

A process according to claim 15 wherein said flow channel, said transverse barriers and said thermal masses are coated with polyethylene.

Claim 23

A process according to claim 16 wherein acrylamide is grafted onto said polyethylene coating.

Claim 24

A process according to claim 14 wherein the semi-permeable membranes comprise cellulose acetate.

Claim 25

A process according to claim 14 wherein the first electrode is a cathode and the second electrode is an anode.

Claim 26

A process according to claim 19 wherein the electrodes comprise platinum.

Claim 27

A process according to claim 14 wherein the pH gradient is thermally engendered so as to cause all of the ampholytes contained in the solution to migrate into the elongate channels and stabilize at positions corresponding to their isoelectric points and wherein the pH gradient is altered so as to cause the ampholytes to reenter the flow channel at different times and to be separately eluted and collected.

Claim 28

A process according to claim 14 wherein the pH is thermally engendered so as to cause one or more selected ampholytes to migrate into the elongate channels and stabilize at positions corresponding to their isoelectric points while the other ampholytes remain in the flow channel so as to be eluted and wherein the pH gradient is altered so as to cause the one or more selected ampholytes to reenter the flow channel at different times and to be separately eluted and collected.

Claim 29

A process for separating ampholytes comprising: directing a solution containing two or more ampholytes with at least two of the ampholytes having identical isoelectric points but different mobilities through a flow channel which is transverse to a plurality of elongate barriers defining a plurality of elongate channels; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into the elongate channels and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte and so as to cause the at least two ampholytes having identical isoelectric points but different mobilities to migrate into different elongate channels due to the different mobilities of the at least two ampholytes; and altering the pH gradient so as to cause the at least one ampholyte to reenter the flow channel and to be separately eluted and collected and so as to cause the at least two ampholytes having identical isoelectric points to reenter the flow channel at different positions along the flow channel due to their location in different elongate channels and to also be separately eluted and collected.

Claim 30

A process for separating ampholytes comprising: directing a solution containing two or more ampholytes with at least two of the ampholytes having identical isoelectric points but different mobilities through a flow channel which is transverse to a plurality of elongate barriers defining a plurality of elongate channels; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into the elongate channels and stabilize at a position corresponding to the isoelectric point of the at least one ampholyte and so as to cause the at least two ampholytes having identical isoelectric points but different mobilities to migrate into different elongate channels due to the different mobilities of the at least two ampholytes; and altering the pH gradient so as to cause the at least one ampholyte to reenter the flow channel and to be separately eluted and collected and so as to cause the at least two ampholytes having identical isoelectric points to reenter the flow channel at different positions along the flow channel due to their location in different elongate channels and to also be separately eluted and collected.

Claim 31

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers which define at least one elongate channel between said barriers; establishing an electric field along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate at a speed according to its electrophoretic mobility from said one of one or more flow channels through said at least one elongate channel and into one of the one or more flow channels to be eluted and separately collected.

Claim 32

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers which define at least one elongate channel between said barriers; establishing an electric field along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate at a speed according to its electrophoretic mobility from said one of one or more flow channels through said at least one elongate channel and into one of the one or more flow channels to be eluted and separately collected.

Claim 33

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel; and altering the pH gradient so as to cause the at least one ampholyte in said elongate channel to enter one of said one or more flow channels and to be eluted and separately collected.

Claim 34

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engendering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel; and altering the pH gradient so as to cause the at least one ampholyte in said elongate channel to enter one of said one or more flow channels and to be eluted and separately collected.

Claim 35

A process for separating ampholytes comprising: directing a first solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engineering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel; and flushing a second solution through the transverse channels so as to cause the at least one ampholyte in said elongate channel to enter one of said one or more flow channels and to be eluted and separately collected.

Claim 36

A process for separating ampholytes comprising: directing a first solution containing one or more ampholytes through one of one or more flow channels which are transverse to at least two elongate barriers defining at least one elongate channel therebetween; establishing an electric field along the length of said elongate barriers; thermally engineering a pH gradient along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel; and flushing a second solution through the transverse channels so as to cause the at least one ampholyte in said elongate channel to enter one of said one or more flow channels and to be eluted and separately collected.

Claim 37

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through a flow channel which is transverse to at least two elongate barriers defining at least one elongate channel therebetween, said two elongate barriers having a semi-permeable membrane abutting the ends of said elongate barriers opposite said flow channel; establishing an electric field along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel and stabilize at the boundary defined by said semipermeable membrane; and reversing the electric filed so as to cause the at least one ampholyte stabilized at said boundary to migrate through said at least one elongate channel towards said flow channel at a speed according to the electrophoretic mobility of the ampholyte and to reenter said flow channel to be eluted and separately collected.

Claim 38

A process for separating ampholytes comprising: directing a solution containing one or more ampholytes through a flow channel which is transverse to at least two elongate barriers defining at least one elongate channel therebetween, said two elongate barriers having a semi-permeable membrane abutting the ends of said elongate barriers opposite said flow channel; establishing an electric field along the length of said elongate barriers so as to cause at least one of the ampholytes to migrate from the flow channel into said at least one elongate channel and stabilize at the boundary defined by said semipermeable membrane; and reversing the electric filed so as to cause the at least one ampholyte stabilized at said boundary to migrate through said at least one elongate channel towards said flow channel at a speed according to the electrophoretic mobility of the ampholyte and to reenter said flow channel to be eluted and separately collected.