IP Library › Granted Patent US 11,702,625
Granted Patent B2
US 11,702,625 · App. 17/376,439 · Granted Jul 18, 2023

System and method for production of on-demand proteins in a portable unit for point of care delivery

Inventors: Govind Rao (Ellicott city, MD); Yordan Kostov (Columbia, MD); Leah Tolosa (Columbia, MD); Xudong Ge (Woodstock, MD); Douglas Frey (Ellicott City, MD)
Assignee: University of Maryland, Baltimore County
C12M47/10C12M41/12C12M47/12
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Quick Facts
Patent No.
US 11,702,625
App. No.
17/376,439
Granted
Jul 18, 2023
Kind
B2
Abstract

A portable and mobile bioprocessing system and method for protein manufacturing that is compact, integrated and suited for on-demand production of any type of proteins and for delivery of the produced proteins to patients or for assay purposes. The portable system and method can also be used for efficient on-demand production of any type of protein with point-of-care delivery.

Claims (28)

1. A method of stimulating production of granulocytes in a patient undergoing cancer therapy, said method comprising administering a Granulocyte Colony Stimulating Factor (G-CSF) protein to the patient, wherein the G-CSF is synthesized on-demand in a bioprocessing system using cell-free protein expression, said bioprocessing system comprising:

a production module for producing non-purified G-CSF protein, and

a purification module for receiving the non-purified G-CSF protein from the production module and for purifying the G-CSF protein.

2. The method of claim 1 , wherein the G-CSF protein can be administered continuously or as a bolus to the patient.

3. The method of claim 1 , wherein the purification module comprises:

a chromatography component for receiving the non-purified G-CSF protein from the production module and for outputting purified G-CSF protein; and

a diafiltration component for receiving the purified G-CSF protein from the chromatography component and for outputting further purified G-CSF protein, wherein the diafiltration component comprises a product section for receiving the purified G-CSF protein from the chromatography component and a buffer section for receiving a buffer solution.

4. The method of claim 3 , wherein the buffer solution is free of dithiothreitol (DTT).

5. The method of claim 1 , wherein the production module comprises a reaction mixture comprising a nucleotide template for production of the G-CSF protein, monomers for the G-CSF protein to be synthesized, co-factors, enzymes and reagents that are necessary for the synthesis.

6. The method of claim 5 , wherein the enzymes and reagents that are necessary for the synthesis are ribosomes, tRNA, polymerases and transcriptional factors.

7. The method of claim 1 , wherein the production module comprises a bioreactor for cell-free G-CSF protein expression.

8. The method of claim 3 , wherein the diafiltration component further comprises: a first substrate; a second substrate; and a diafiltration membrane positioned between the first and second substrates.

9. The method of claim 8 , wherein the diafiltration component comprises a flow cell.

10. The method of claim 1 , wherein the production module comprises at least one sensor for monitoring at least one of conductivity, temperature, pH, oxygen and CO 2 .

11. The method of claim 1 , wherein the production module and purification module each comprise a heating and cooling element for controlling the temperature of solution inside the production module and purification module.

12. The method of claim 1 , wherein the bioprocessing system further comprises a fluid storage and dispensing module for storing solutions used by the production module for G-CSF protein expression, for storing waste product produced by the purification module, and for storing G-CSF protein output by the purification module.

13. The method of claim 1 , wherein the bioprocessing system further comprises a processor for controlling and/or monitoring at least one of the production module and the purification module.

14. The method of claim 1 , wherein a therapeutic dose and potency/activity of the G-CSF protein is determined by expression time in the production module.

15. The method of claim 1 , wherein the G-CSF protein is delivered directly to the patient.

16. The method of claim 1 , wherein a therapeutic dose and potency/activity of the G-CSF protein is determined by holding time in the production module.

17. The method of claim 1 , wherein potency/activity of the purified G-CSF protein is at least 55% or more of the initial activity for at least 3 days at temperature from above 0° C. to about 30° C.

18. The method of claim 1 , wherein the cancer therapy comprises drugs that cause low white blood cell counts in the patient.

19. A method of treating anemia in a patient in need thereof, said method comprising administering Erythropoetin (EPO) to the patient, wherein the EPO is synthesized on-demand in a bioprocessing system using cell-free protein expression, said bioprocessing system comprising:

a production module for producing non-purified EPO protein, and

a purification module for receiving the non-purified EPO protein from the production module and for purifying the EPO protein.

20. A method of treating a clot or achieving thrombolysis in a patient in need thereof, said method comprising administering Streptokinase to the patient, wherein the Streptokinase is synthesized on-demand in a bioprocessing system using cell-free protein expression, said bioprocessing system comprising:

a production module for producing non-purified Streptokinase protein, and

a purification module for receiving the non-purified Streptokinase protein from the production module and for purifying the Streptokinase protein.

Continuity (6)
Division 16506079 · Jul 9, 2019
Division 15966609 · Apr 30, 2018
Continuation 15095305 · Apr 11, 2016
Continuation In Part 13823911
Provisional Application 61450191 · Mar 8, 2011
Related Publication 20210340488A1 · Nov 4, 2021
Cited By (1)
US 12,221,603