System for controlling and optimizing reactions in solid phase synthesis of small molecules

• US 9,069,358 B2
• Filed: 06/24/2013
• Issued: 06/30/2015
• Est. Priority Date: 06/24/2013
• Status: Active Grant

• Current Assignee: Biolytic Lab Performance, Inc.
• Original Assignee: Biolytic Lab Performance, Inc.
• Inventors: Demmitt, Thomas J.
• Primary Examiner(s): Griffin, Walter D
• Assistant Examiner(s): NGUYEN, HUY TRAM
• Application Number:
  US13/925,642
• Publication Number:
  US 20140377134A1
• Time in Patent Office: 736 Days
• Field of Search: 422/64, 422/63, 422/131, 422/136, 422/134, 422/112, 422/114, 137/1
• US Class Current: 1/1
• CPC Class Codes: B01J 19/0046 Sequential or parallel reactions, e.g. for the synthesis of polypeptides or polynucleotides; Apparatus and devices for combinatorial chemistry or for making molecular arrays synthesis methods per se C40B50/00
• CPC Class Codes: B01J 2219/00286 Reactor vessels with top and bottom openings
• CPC Class Codes: B01J 2219/00308 interchangeably mounted in racks or blocks
• CPC Class Codes: B01J 2219/00326 Movement by rotation
• CPC Class Codes: B01J 2219/0036 Nozzles
• CPC Class Codes: B01J 2219/00389 Feeding through valves
• CPC Class Codes: B01J 2219/00418 using pressure
• CPC Class Codes: B01J 3/042 in the form of a tube
• CPC Class Codes: C07K 1/00 General methods for the preparation of peptides , i.e. processes for the organic chemical preparation of peptides or proteins of any length
• CPC Class Codes: G01N 35/00 Automatic analysis not limited to methods or materials provided for in any single one of groups G01N1/00 - G01N33/00; Handling materials therefor
• CPC Class Codes: G01N 35/10 Devices for transferring samples or any liquids to, in, or from, the analysis apparatus, e.g. suction devices, injection devices G01N35/0099 takes precedence
• CPC Class Codes: G05D 7/0605 specially adapted for solid materials
• CPC Class Codes: Y10T 137/0318 Processes

Abstract

A instrument for performing synthesis of small molecules such as Oligos and Peptides when using solid phase synthesis techniques to synthesize small molecules. The system and methods include a mechanism for controlling the pressure differential across the reaction vessels that contain the solid support used in solid phase synthesis. Reaction vessels are held in a holder that provides a sealable chamber at the outlet ends of the reaction vessels. The rotor containing the reaction vessels is placed within a sealable chamber. The sealable chamber is fitted with a means for engaging the rotor and draining the reaction vessels to waste. The sealable chamber is also fitted with a means for engaging the rotor to drain the reaction vessels at a slower, variable rate.

Claims

1. A solid phase synthesizer reaction system, of a type utilizing a plurality of flow through reaction vessels, each reaction vessel having an open top to allow introduction of reagents through said reaction vessel, an open bottom of each reaction vessel to allow liquid to flow from said reaction vessel and a solid phase reaction material within each of said reaction vessel between said open top end and open bottom end, said system comprising:

a rotor configured to hold a plurality of reaction vessels;

a cover positioned above said rotor;

an upper sealable chamber on said rotor, said reaction vessel open tops within said upper sealable chamber;

a lower sealable chamber within said rotor, said reaction vessel open bottoms within said lower sealable chamber;

a controllable pressure regulation pathway between said upper sealable chamber and said lower sealable chamber, said controllable pressure regulation pathway allowing equalization of pressure between said upper chamber and said lower chamber without requiring that gas pass through said reaction vessels.

2. The system of claim 1, wherein said lower sealable chamber includes a plurality of lower sealable chambers, each lower chamber including a plurality of reaction vessel open bottoms.

3. The system of claim 1, wherein said rotor includes a priming port.

4. The system of claim 1, further including a first drain system positioned on said rotor to drain liquid and gasses flowing through said reaction vessels into said lower sealable chamber and a second drain system connectable to said lower sealable chamber, said second drain system allowing draining gas only and allowing draining at a selectable flow rate.

5. The system of claim 1, further including a plurality of reagent dispense nozzles on said cover, and a motor mounted to said rotor to allow rotational positioning of said rotor such that a dispense nozzle can be selectively positioned above an open top of a reaction vessel.

6. The system of claim 1, further including a motor to turn said rotor and a motor mount onto which said motor is mounted, said motor mount having a spill channel to collect spilled waste and a drain to drain said spill channel.

7. The system of claim 4, wherein said second drain system in said lower sealed chamber includes a manifold, at least a first and a second calibration tube receiving gas flow from said manifold, and at least a first and a second valve regulating flow through respectively through said first and second calibration tube.

8. The system of claim 4, wherein said first drain system includes a ball check valve.

9. The system of claim 1, further including a central spacer on said rotor, said spacer located on a top, central position on said rotor just below said cover, said spacer limiting a gas volume in said upper sealable chamber.

10. A solid phase synthesizer reaction system, of a type utilizing a plurality of flow through reaction vessels, each reaction vessel having an open top to allow introduction of reagents through said reaction vessel, an open bottom of each reaction vessel to allow liquid to flow from said reaction vessel and a solid phase reaction material within each of said reaction vessel between said open top end and open bottom end, said system comprising:

a rotor configured to hold a plurality of reaction vessels;

a cover positioned above said rotor;

a sealable chamber within said rotor, said reaction vessel open bottoms within said sealable chamber;

a first drain connectable to said lower sealed chamber, configured to allow only gas flow from said lower sealable chamber and having a controllable flow rate regulation system;

a first drain control valve, configured to open or close flow through said first drain;

a second drain positioned within said lower sealable chamber such that it drains both gas and liquid from said chamber; and

a second drain control valve configured to open or close flow through said second drain.

11. The system of claim 10, wherein said first drain includes a drain pipe, a manifold joined to said drain pipe and a plurality of calibration tubes receiving flow from said manifold, each calibration tube having an associated valve that controls flow through each of said calibration tube.

12. The system of claim 10, wherein said second drain has a drain rate between 2 and 100 times greater than said first drain.

13. The system of claim 10, wherein said second drain control valve is a ball check valve.

14. The system of claim 10, wherein said first drain includes an initial outflow passageway from said sealable chamber that is out of line with a longitudinal axis of reaction vessels held on said rotor.

15. A method for control of flow through reaction vessels during solid phase synthesis reaction, wherein said reaction vessels each have an open top end, an open bottom, said reaction vessels positioned on a rotor such that said open bottom end is enclosed in a sealable chamber within said rotor, said method comprising:

equalizing a pressure utilizing a passageway that connects between an area holding said reaction vessel open top and said sealable chamber without flow through said reaction vessel, thereby limiting flow through said reaction vessel; and

Opening a variable flow rate gas drain to controllably drive fluid flow through said reaction vessels.

16. The method of claim 15, further including sealing said variable flow rate gas drain to seal said sealable chamber.

17. The method of claim 15, further including a further step of opening a second drain in said sealable chamber, said second drain providing flow draining of liquid and gas from said sealable chamber at a flow rate higher than a flow rate of said variable flow rate gas drain.