Systems and methods for manufacturing a silk fibroin solution and powders containing silk fibroin
The disclosure relates to systems and methods for improving the manufacturing of silk solutions and powders containing silk fibroin obtained from silkworm cocoons. The methods include use of a reactor vessel to degum, rinse, and dissolve the silk fibroin protein from silk inputs to obtain a food grade silk powder. The reactor vessel may include a combination of inputs and outputs for introducing and removing different components used or generated during the process. The systems may include any combination of heat exchangers, holding tanks, filtration modules, and post-treatment equipment as necessary to obtain the silk powder. The solutions and powders can be used to improve the post-harvest preservation of perishables and to improve the performance of packaging, including biodegradable packaging.
1. A silk manufacturing system comprising:
(A) a first processing substation comprising a vessel configured to receive silk inputs, extract silk fibroin proteins therefrom, and produce a silk fibroin-based solution, such that the silk fibroin-based solution is substantially free of sericin, wherein the first processing substation is configured to extract the silk fibroin proteins via degumming, rinsing, and dissolving processes within a single vessel;
(B) a second processing substation in fluid communication with the first processing substation, the second processing substation configured to receive and purify the silk fibroin-based solution from the first processing substation, wherein the purified silk fibroin-based solution comprises less than about 650 parts per million (ppm) of one or more salts or non-organic particulates;
(C) wherein the first or second processing substation is further configured to sterilize the silk fibroin-based solution to produce a sterilized silk fibroin-based solution prior to a third processing substation; and
(D) a third processing substation in fluid communication with the second processing substation, the third processing substation is a spray dryer that is configured to receive and powderize the sterilized silk fibroin-based solution.
2. The system of claim 1 , wherein the purified silk fibroin-based solution comprises less than about 400 ppm of the one or more salts or non-organic particulates.
3. The system of claim 1 , wherein the powderized silk fibroin-based solution has a water activity level of less than 0.9.
4. The system of claim 1 , wherein the silk inputs come from a Bombyx mori silkworm.
5. The system of claim 1 further comprising:
a reservoir disposed between the first and second processing substations and configured to at least one of hold or condition the silk fibroin-based solution; and
a pump assembly disposed between the first and second processing substations and configured to transfer the silk fibroin-based solution between the first processing substation, the reservoir, and the second processing substation.
6. The system of claim 1 , wherein the second processing substation includes at least one spiral wound filtration membrane.
7. The system of claim 1 further comprising a heat exchange system configured to adjust a temperature of the silk fibroin-based solution prior to or after any one of the processing substations.
8. The system of claim 1 , wherein the second processing substation is configured to purify the silk fibroin-based solution via diafiltration.
9. The system of claim 1 , wherein the second processing substation is configured to purify the silk fibroin-based solution via tangential flow filtration.
10. The system of claim 1 , wherein the third processing substation includes a piece of agglomeration equipment.
11. The system of claim 1 , further comprising a post-treatment system configured to receive a silk fibroin powder from the third processing substation and to at least one of: condition the silk fibroin powder, test the silk fibroin powder, or package the silk fibroin powder in a food-safe container.
12. A silk manufacturing system comprising:
(A) a first processing substation comprising a vessel configured to receive silk inputs, extract silk fibroin proteins therefrom, and produce a silk fibroin-based solution, wherein the first processing substation is configured to extract the silk fibroin proteins via degumming, rinsing, and dissolving processes within a single vessel;
(B) a second processing substation in fluid communication with the first processing substation, the second processing substation configured to receive and purify the silk fibroin-based solution from the first processing substation;
(C) a third processing substation in fluid communication with the second processing substation, the third processing substation configured to receive and sterilize the purified silk fibroin-based solution; and
(D) a fourth processing substation in fluid communication with the third processing substation, the fourth processing substation configured to receive and powderize the purified silk fibroin-based solution, wherein the fourth processing substation is a spray dryer.
13. The system of claim 12 , wherein the silk inputs come from a Bombyx mori silkworm.
14. The system of claim 12 , wherein the third processing substation is configured to sterilize the purified silk fibroin-based solution to a food grade standard via microfiltration.
15. The system of claim 12 , wherein the third processing substation is configured to sterilize the purified silk fibroin-based solution to a food grade standard via pasteurization.
16. The system of claim 12 , wherein the fourth processing substation includes a piece of agglomeration equipment.
17. A silk manufacturing system comprising:
(A) a first processing substation configured to receive silk inputs, extract silk fibroin proteins therefrom, and produce a silk fibroin-based solution, wherein the first processing substation is configured to extract the silk fibroin proteins within a single vessel, the first processing substation comprising:
a reactor vessel comprising a first inlet port configured to receive the raw silk inputs and one or more compounds, a second inlet port configured to receive a solvent, and at least one outlet configured to output the silk fibroin-based solution, wherein the reactor vessel is configured to process the silk inputs by degumming, rinsing, and dissolving the silk fibroin protein from the silk inputs;
a liquid jacket disposed about the reactor vessel and configured to provide heat exchange with the vessel and its contents, wherein the liquid jacket is configured to heat the contents to a temperature of about 50° C. to about 150° C.; and
an agitation mechanism configured to agitate the contents of the reactor vessel;
(B) a second processing substation in fluid communication with the first processing substation, the second processing substation configured to receive and purify the silk fibroin-based solution from the first processing substation, wherein the second processing substation is configured to purify the silk fibroin-based solution via tangential flow filtration, the second processing substation comprising:
a filtration module housing at least one membrane, the module comprising an inlet configured to receive the silk fibroin-based solution including a compound, an outlet configured to output a purified silk fibroin-based solution with a reduced compound amount, and a waste port configured to output a portion of the compound, wherein the filtration module is configured to remove the compound from the silk fibroin-based solution by circulating the silk fibroin-based solution through the filtration module until about 1 diavolume to about at least 12 diavolumes are reached;
(C) a fourth processing substation in fluid communication with the second processing substation, the fourth processing substation configured to receive and sterilize the purified silk fibroin-based solution;
(D) the third processing substation in fluid communication with the fourth processing substation, the third processing substation configured to receive and powderize the sterilized silk fibroin-based solution, wherein the third processing substation is configured to powderize the sterilized silk fibroin-based solution via a spray dryer, and wherein the third process substation includes a piece of agglomeration equipment; and
(E) a post-treatment system configured to receive a silk fibroin powder from the third processing substation and to at least one of: condition the silk fibroin powder, test the silk fibroin powder, or package the silk fibroin powder in a food-safe container.
18. The system of claim 17 , wherein the silk inputs come from a Bombyx mori silkworm.
19. The system of claim 17 , wherein the fourth processing substation comprises a microfiltration module configured to receive the purified silk fibroin-based solution and to remove microbes and reduce turbidity from the purified silk fibroin-based solution.
20. The system of claim 19 , wherein the microfiltration module includes two filter stages, the first filter stage having a pore size between about 0.7 μm and about 5 μm and the second filter stage has a pore size between about 0.05 μm and about 0.8 μm, and the purified silk fibroin-based solution passes through the first filter stage prior to passing through the second filter stage.
21. The system of claim 20 , wherein the microfiltration module further comprises one or more pumps configured to transfer the purified silk fibroin-based solution between filter stages, between processing substations, to another process as necessary after completing the microfiltration process, or any combination thereof.
22. The system of claim 20 , wherein the microfiltration module further comprises one or more holding tanks, wherein the tanks may be configured to provide additional processing, including one or more of storing the purified silk fibroin-based solution, temperature control of the purified silk fibroin-based solution, or adjusting the purified silk fibroin-based solution concentration to address turbidity or sterility levels.
23. The system of claim 17 , wherein the reactor vessel is sized to have an aspect ratio of height to diameter as defined by a work volume of about 0.5 to about 5.0.
24. The system of claim 17 , wherein the reactor vessel is sized to have an aspect ratio of height to diameter as defined by a work volume of about 0.8 to about 2.0.
25. The system of claim 17 , wherein the reactor vessel further comprises a handling structure for controlling at least one of movement or position of the silk inputs within the vessel.
26. The system of claim 17 further comprising a pre-treatment system configured to condition the silk inputs prior to or at introduction to the first processing substation.
27. The system of claim 17 , wherein the second processing substation further comprises a heat exchange system to control a temperature of the silk fibroin-based solution or the purified silk fibroin-based solution during processing.
28. The system of claim 17 , wherein the filtration module is configured to remove a second compound from the silk fibroin-based solution by circulating the silk fibroin-based solution through the filtration module until about 5 diavolumes to about at least 8 diavolumes are reached.