Methods and apparatus for continuous preparative chromatographic separation of fluid mixtures

A continuous reciprocating flow apparatus for preparative chromatographic separation of unwanted water from a volatile product comprising:

• (a) a conduit means defining an inlet and an outlet therein;
• (b) a continuous polymeric solid comprising yarns of rayon positioned throughout the interior of said conduit means;
• (c) a carrier gas supply means including an input line extending in fluid flow communication to said input of said conduit means to supply carrier gas thereto;
• (d) a mixture supply means including a mixture supply line means in fluid flow communication with said input line of said carrier gas supply means and with a reservoir containing the mixture of water and volatile product, said mixture supply means adapted to supply mixture to said input line for communication therethrough to said inlet of said conduit means, said mixture supply means comprising:
• 1. a pump means to convey the mixture through said mixture supply line;
• 2. a mixture reservoir in fluid flow communication with said pump means to supply the mixture thereto;
• 3. an injection valve means to facilitate feeding of the mixture into said carrier gas input line, said injection valve means adapted to intermittently supply charges of mixture to said input line;
• and
• 4. a capillary restriction means positioned between said injection valve means and said carrier input line to minimize back flow therethrough and to minimize volatizing of the mixture except when a charge of mixture is being fed therethrough by said injection valve means;
• (e) a product gathering means including an outlet line in fluid flow communication with said outlet of said conduit means, said product gathering means comprising:
• 1. a flow control valve means adjacent said outlet of said conduit means to control flow therethrough;
• 2. a cooling means to condense the volatilized product;
• and
• 3. a carrier gas vent to release the carrier gas after the product has been collected;
• (f) a reverse flow means adapted to selectively reverse the flow of carrier gas through said continuous polymeric solid within said conduit means to withdraw the water accumulated therein, said reverse flow means being responsive to actuate after a pre-determined time delay subsequent to the supplying of a volatilized charge of mixture wherein the delay is long enough to allow the product within the mixture charge to be gathered by said product gathering means and short enough to have the water still retained within the adsorbing continuous polymeric solid, said reverse flow means comprising:
• 1. a reverse flow line extending from said carrier gas input line to said outlet of said conduit means;
• 2. a water line in fluid flow communication with said carrier gas input line adjacent said inlet of said conduit means, said water line adapted to gather water expelled through said inlet during reverse flow through said conduit means;
• 3. a first valve means positioned within said carrier gas input line upstream of said water line, said first valve means being normally opened and adapted to close responsive to actuation of said reverse flow means;
• 4. a second valve means positioned within said reverse flow line, said second valve means being normally closed and adapted to open responsive to actuation of said reverse flow means;
• 5. a third valve means positioned within said water line, said third valve means being normally closed and adapted to open responsive to actuation of said reverse flow means;
• (g) a heating means positioned adjacent said conduit means to control the temperature thereof and positioned adjacent said carrier gas input line at the location of fluid flow connection to said mixture supply line to facilitate the volatilizing of the mixture into the carrier gas;
• and
• (h) a metal wool packing located within said carrier gas input adjacent connection to said mixture supply line to facilitate volatilizing of the mixture into the carrier gas.

A continuous reciprocating process for preparative chromatographic separation of unwanted volatile species from a volatile product comprising:

• (a) introducing a charge of mixture of volatile species and volatile product into a carrier gas supply;
• (b) volatilizing the charge of mixture, said volatilizing and said introducing comprises injecting the mixture into the carrier gas with an injection valve, said injecting being performed through a capillary tube into the carrier gas to prevent back flow and to minimize any additional volatilizing of material after the original charge has been introduced into the carrier gas;
• (c) pumping the mixture from a mixture reservoir to be introduced into the carrier gas;
• (d) passing the carrier gas through a conduit containing a continuous polymeric solid to allow the volatile species to be adsorbed to the solid and to allow the volatile product to pass therethrough much more quickly;
• (e) heating the continuous polymeric solid to control the flow rates therethrough and heating the carrier gas and the mixture to facilitate said volatilizing;
• (f) collecting the product after passage through the conduit, said collecting of the product further including cooling of the product after passing out of the conduit for condensing thereof;
• (g) collecting the volatile species expelled from the conduit including venting of the collected water to the atmospheric environment to facilitate said collecting;
• and
• (h) applying the carrier gas to the conduit in a reverse direction to expel the adsorbed volatile species therefrom back through the original direction in which the mixture passed into the conduit to make the conduit ready to receive a new charge of mixture.

A continuous flow apparatus for continuous preparative chromatographic separation of unwanted volatile species from volatile product comprising:

• (a) a conduit having a generally circular configuration and defining an inlet and an outlet;
• (b) a closed loop of continuous polymeric solid extending through said conduit, and being continuously moving therethrough;
• (c) a drive means adapted to drive said closed loop through said conduit continuously at a speed less than the migration speed of the volatile product through the polymeric solid and greater than the migration speed of the volatile species through the polymeric solid, the direction of drive of said closed loop being from said outlet toward said inlet along the flow path of product therethrough;
• (d) a mixture supply means to supply a vaporized mixture of volatile species and volatile product;
• (e) a carrier gas supply means adapted to receive the mixture from said mixture supply means, said carrier gas supply means being in fluid flow communication with said inlet with the carrier gas being movable through said conduit means to said outlet in a direction upstream counter to the movement direction of said closed loop of continuous polymeric material, said volatile product responsive to be carried by the carrier gas upstream from said inlet directly to said outlet since the migration speed thereof through said loop is greater than the speed of movement of said loop from said outlet toward said inlet;
• (f) a volatile species expelling means positioned downstream of said inlet and adapted to receive the volatile species absorbed within said moving closed loop;
• and
• (g) a product collecting means in fluid flow communication with said outlet to receive carrier gas and volatilized product therefrom.

A continuous flow apparatus for preparative chromatographic separation of unwanted volatile species from volatile product comprising:

• (a) a conduit having a generally circular configuration and defining a first open end and a second open end, said conduit also defining an inlet and an outlet;
• (b) a closed loop of continuous polymeric solid extending through said conduit and through said first open end and said second open end, said closed loop being continuously moving therethrough;
• (c) a first heating means positioned adjacent said closed loop between said inlet and said outlet to control the flow rate of volatile product therethrough;
• (d) a drive means attached with respect to said closed loop for driving thereof outside of said conduit between said first open and said second open end, said drive means being adapted to drive said closed loop through said conduit continuously at a speed less than the migration speed of the product through the polymeric solid and greater than the migration speed of the volatile species through the polymeric solid, the direction of drive of said closed loop being from said outlet toward said inlet;
• (e) a mixture supply means to supply a vaporized mixture of volatile species and volatile product, said mixture supply means comprising:
• 1. a mixture reservoir means for the supplying of charges of mixture of the volatile species and volatile product;
• 2. a pump means for withdrawing the mixture from said mixture reservoir;
• 3. an injection valve means for controlling the introduction of the pumped mixture;
• (f) a carrier gas supply means for supplying air adapted to receive the mixture from said mixture supply means, said carrier gas supply means being in fluid flow communication with said inlet with the carrier gas being movable through said conduit means to said outlet in a direction upstream counter to the movement direction of said closed loop of continuous polymeric material, said volatile product responsive to be carried by the carrier gas upstream from said inlet directly to said outlet since the migration speed thereof through said loop is greater than the speed of movement of said loop from said outlet toward said inlet;
• (g) a first constriction means located downstream of said inlet to minimize the tendency of carrier gas to flow downstream of said inlet;
• (h) a first bucking gas supply in fluid flow communication with said conduit downstream of said inlet to minimize the tendency of carrier gas to flow downstream from said inlet;
• (i) a second constriction means located upstream of said outlet to minimize the tendency of carrier gas to flow upstream of said outlet;
• (j) a second bucking gas supply located upstream of said outlet to minimize the tendency of carrier gas to flow upstream of said outlet;
• (k) a volatile species expelling means positioned downstream of said inlet and adapted to receive the volatile species adsorbed within said moving closed loop, said volatile species expelling means including a second heating means positioned adjacent said moving closed loop of continuous polymeric solid between said second bucking gas supply and said second end of said conduit, said second heating means adapted to fully vaporize the volatile species within said loop and the portion of said bucking gas supply flowing counter to the direction of movement of said loop being adapted to blow the volatile species out of said second end of said conduit into the atmosphere to ready said loop to receive a new charge of mixture;
• and
• (l) a product collecting means in fluid flow communication with said outlet to receive carrier gas and volatilized product therefrom, said product collecting means including a condenser means for condensing vaporized product and a valve means for expelling the carrier gas from the condensed product.

A continuous process for chromatographically separating unwanted water from volatile product comprising:

• (a) supplying a charge of mixture of water and volatile product into a stream of carrier gas, said supplying including pumping the mixture from a reservoir and vaporizing of the mixture by passing it through an injection valve means;
• (b) passing the carrier gas stream into the inlet of a conduit containing a closed loop of continuous polymeric solid wherein the conduit has an inlet and an outlet;
• (c) urging the carrier gas toward the outlet for expelling therethrough;
• (d) continuously moving the closed loop through the conduit in a direction from the outlet toward the inlet at a velocity greater than the migration velocity of water through the polymeric solid and less than the velocity of migration of the volatile product through the polymeric solid to cause the water to be carried from the inlet downstream with the moving loop and the carrier gas and volatile product to move upstream counter to the direction of movement of the loop and out the outlet;
• (e) constricting the conduit downstream of the inlet to encourage flow of carrier gas from the inlet toward the outlet;
• (f) applying a bucking gas supply downstream of the inlet to encourage flow of carrier gas from the inlet toward the outlet;
• (g) constricting the conduit upstream of the outlet to encourage the carrier gas to flow through the outlet;
• (h) applying a bucking gas supply upstream of the outlet to encourage the carrier gas to flow through the outlet;
• (i) expelling the water continuously at a location downstream of the inlet, said expelling including the heating of the closed loop adjacent an open end of the conduit to vaporize the water to facilitate expelling thereof;
• (j) collecting the product at the outlet of the conduit, said collecting including condensing of the volatile product and exhausting of the carrier gas;
• and
• (k) heating the closed loop of polymeric solid to control the flow of carrier gas and mixture therethrough.