INDUSTRIAL BIOSYNTHESIZER SYSTEM AND METHOD
A synthesizer system for use as either a freestanding or facility integrated device and a method of use. The system includes an inlet manifold of diaphragm valves that receives at least two liquid feeds. The streams flow either to a blending module or directly to a delivery module. From there they are delivered to a reactor for the sequential creation of desired compounds. For flow through solid phase synthesis added capability for feed recirculation and effluent detection with feedback control is included.
1 . An automated compound synthesis system comprising:
a) an inlet module featuring a manifold having an outlet and a plurality of diaphragm valves, each of said diaphragm valves having an inlet adapted to communicate with an external feed of a building block or reagent; and
b) a delivery module in communication with the outlet of the manifold of the inlet module and receiving a feed stream therefrom, said delivery module adapted to communicate with a reaction vessel to deliver the feed stream to the reaction vessel.
2 . The synthesis system of claim 1 wherein the diaphragm valves are multi-port cluster diaphragm valves.
3 . The synthesis system of claim 1 wherein the diaphragm valves are multi-port zero static diaphragm valves.
4 . The synthesis system of claim 1 further comprising a blending module in circuit between the delivery module and the reaction vessel.
5 . The synthesis system of claim 1 further comprising a flow control module in circuit between the delivery module and the reaction vessel.
6 . The synthesis system of claim 1 further comprising a PAT detection module in circuit between the delivery module and the reaction vessel.
7 . The synthesis system of claim 4 wherein the blending module includes a valve or valves.
8 . The synthesis system of claim 1 further comprising a cart provided with rollers upon which the system is mounted so that the system may be rolled across a surface.
9 . A method for providing synthesis capability to a laboratory, pilot or commercial scale system including the steps of:
a) connecting at least two liquid feeds to a synthesizer and passing them through diaphragm valves arranged in a manifold; and
b) delivering the liquid feeds from the manifold to a reaction vessel.
10 . The method of claim 9 further comprising the step of controlling the delivery of the liquid feeds to the reaction vessel by passing them through a flow control module.
11 . The method of claim 9 further comprising the step of blending the feed streams with a blending module so that a blended liquid stream of feeds is produced prior the delivery to a reaction vessel.
12 . The method of claim 9 further comprising the steps of detecting a composition of the feed liquid stream via a detection module and generating a corresponding signal and receiving the signal with the controller and controlling the inlet valve and/or delivery module with the controller based upon the received signal.
13 . The method of claim 9 wherein the reaction vessel is a flow-through reactor.
14 . The method of claim 13 further comprising the steps of
a) re-circulating of the reagents and/or reactants through the reactor;
b) receiving the effluent from the reaction vessel displaced by incoming feeds or otherwise;
c) using a post-reactor detection module to determine the completeness of reaction based on the detected signal for the reagent or reactant used in a step;
d) using a controller to determine whether to continue re-circulation, adjust the rate of re-circulation or stop the re-circulation; and
e) using the controller to determine whether to begin the next step or pause the system.
15 . The method of claim 9 wherein the synthesizer inlet valve(s) are multi-port cluster diaphragm valves.
16 . The method of claim 9 wherein the synthesizer inlet valve(s) are of a zero static design to reduce carryover and/or mixing of feed streams.
17 . The method of claim 9 wherein the synthesizer inlet valve(s) are of a zero static design connected into a low dead volume valve assembly to provide the highest level of reduced carryover and/or mixing of feed streams.