Method and apparatus for continuous freeze drying

• US 4,561,191 A
• Filed: 05/28/1985
• Issued: 12/31/1985
• Est. Priority Date: 05/28/1985
• Status: Expired due to Term

• Current Assignee: Martin C. Parkinson
• Original Assignee: Martin C. Parkinson
• Inventors: Parkinson, Martin C.
• Primary Examiner(s): Camby, John J.
• Application Number:
  US06/738,378
• Time in Patent Office: 217 Days
• Field of Search: 34/5, 34/92
• US Class Current: 34/290
• CPC Class Codes: A23L 3/44 Freeze-drying
• CPC Class Codes: F26B 21/083 by using sorbent or hygroscopic materials, e.g. chemical substances, molecular sieves
• CPC Class Codes: F26B 5/06 the process involving freezing

Abstract

A method and apparatus for freeze drying heat sensitive aqueous products on a continuous basis, utilizing molecular sieves to sequester the sublimating water vapor, is described. At least two beds of sieve are used sequentially, one being heat regenerated while another is actively adsorbing condensable vapors. Exotherm is controlled during freeze drying, and bed regeneration may be accomplished without the use of a purge gas. The advantages of certain types and sizes of molecular sieves, in a continuous freeze drying procedure, is discussed.

Claims

1. A freeze drying apparatus, comprising:

(A) A drying chamber means;

(B) At least two condenser means;

(C) A quantity of molecular sieve within each of said condenser means;

(D) A vacuum pump;

(E) Valving means for providing vacuum tight communication sequentially between each of said condenser means and said drying chamber means and said vacuum pump, and for opening each of said condenser means sequentially to atmospheric pressure; and

(F) Automatic control means for opening and closing valve positions in said valving means, so that during a first period of time when said vacuum pump is in operation said atmospheric pressure is reduced within said drying chamber means and the first of said condenser means, while a second condenser means is opened to said atmospheric pressure, said automatic control means further providing means for heating said molecular sieve within said second condenser means, so that vapors that have previously been adsorbed by said sieve within said second condenser means are driven out of said sieve in said second condenser means, and are expelled to the atmosphere through said opening to said atmospheric pressure in said second condenser means, said automatic control means further providing means for turning off said heating means for said sieve within said second condenser means in order to permit said sieve within said second condenser means to cool down, said automatic control means further providing, during a second period of time immediately following said first period of time, means for opening and closing valve positions in said valving means, so that when said vacuum pump is in operation, said pressure is continued to be reduced in said drying chamber, and said atmospheric pressure is reduced in said second condenser means, while said first condenser means is opened to said atmospheric pressure, said automatic control means further providing a means for heating said molecular sieve within said first condenser, so that condensable vapors that have previously been adsorbed by said sieve within said first condenser are driven out of said sieve within said first condenser, and are expelled to said atmosphere through said opening to said atmospheric pressure in said first condenser, said automatic control means further providing means for turning off said heating means for said sieve within said first condenser in order to permit said sieve within said first condenser to cool down, and then repeating, during a third period of time, the operations that occurred during said first period of time, and so on, so that adsorbable vapors diffusing from said drying chamber means are adsorbed by said molecular sieve in said condenser means on a continuous basis.

2. A freeze dry apparatus according to claim 1 wherein said drying chamber means is a manifold means.

3. A freeze dry apparatus according to claim 1 wherein said molecular sieve within said condenser means is contained in a plurality of metal holders, so that particles comprising said molecular sieve are at a maximum distance of one inch from an internal surface of said metal holders, the external surfaces of said holders having thermal contact means for providing heat transfer away from said molecular sieve, so that excessive endothermic heat build-up during freeze drying is prevented.

4. A freeze dry apparatus according to claim 3 wherein the height of each of said metal holders is no greater than ten inches, so that when said molecular sieve in said holders is heated by said heating means said condensable vapors are expelled to said atmosphere without the use of a purge gas.

5. A freeze dry apparatus according to claim 4 wherein said metal holders are fabricated in copper.

6. A freeze dry apparatus according to claim 3 wherein said vapors diffusing from said drying chamber gain entrance to each of said condenser means through an opening in each of the external surfaces of said condenser means, said opening communicating with a vapor diffusing tube containing a centrally located opening along its length, there being at least one of said vapor diffusing tubes in each of said condenser means, said vapor diffusing tube having a plurality of openings along its periphery, at least one of said peripheral openings communicating with the bottom opening of one of said metal holders, so that said vapors enter the bottom openings of a plurality of said holders in a random manner.

7. A freeze dry apparatus according to claim 3 wherein said vapors diffusing from said drying chamber means enter said condenser means, and then enter one end of the first member of a pair of said holders, and as the adsorption process goes on said vapors leave the other end of said first member, which in turn communicates with one end of the second member of said pair of said holders. through which said vapors migrate to the other end of said second member, so that said vapors migrate through a mass transfer zone at least ten inches in length.

8. A freeze dry apparatus according to claim 7 wherein said vapors migrate through a mass transfer zone of at least twenty inches in length.

9. A freeze dry apparatus according to claim 1 wherein said molecular sieve exists in the form of 1/8 inch diameter pellets.

10. A freeze dry apparatus according to claim 3 wherein said molecular sieve exists in the form of 1/8 inch diameter pellets.

11. A freeze dry apparatus according to claim 4 wherein said molecular sieve exists in the form of 1/8 inch diameter pellets.

12. A freeze dry apparatus according to claim 1 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

13. A freeze dry apparatus according to claim 3 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

14. A freeze dry apparatus according to claim 4 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

15. A freeze dry apparatus according to claim 9 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

16. A freeze dry apparatus according to claim 10 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

17. A freeze dry apparatus according to claim 11 wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and Type 4A.

18. A freeze dry apparatus according to claim 1 wherein said molecular sieve is Type 3A.

19. A freeze dry apparatus according to claim 3 wherein said molecular sieve is Type 3A.

20. A freeze dry apparatus according to claim 4 wherein said molecular sieve is Type 3A.

21. A freeze dry apparatus according to claim 9 wherein said molecular sieve is Type 3A.

22. A freeze dry apparatus according to claim 10 wherein said molecular sieve is Type 3A.

23. A freeze dry apparatus according to claim 11 wherein said molecular sieve is Type 3A.

24. A method for freeze drying heat sensitive materials on a continuous basis, which comprises the steps of:

(A) Placing frozen samples within a drying chamber means;

(B) Filling a plurality of condensing means with molecular sieve;

(C) Connecting said drying chamber means in vacuum tight engagement sequentially with said condensing means;

(D) Providing a source of vacuum for said drying chamber means and said condensing means;

(E) Reducing the pressure in said drying chamber means and in a first condensing means of said plurality of condensing means, while a second condensing means of said plurality of condensing means is at atmospheric pressure by means for opening a valve-to-atmosphere in said second condensing means;

(F) Heating said molecular sieve in said second condensing means so that condensable vapors within said molecular sieve in said second condensing means are driven off and expelled to said atmosphere by said valve-to-atmosphere means in said second condensing means;

(G) Turning off said heating of said molecular sieve in said second condensing means after said vapors in said molecular sieve in said second condensing means are expelled to said atmosphere;

(H) Permitting said molecular sieve in said second condensing means to cool down;

(I) Using means for closing said valve-to-atmosphere in said second condensing means;

(J) Connecting said second condensing means to said drying chamber means and said source of vacuum, while simultaneously raising the pressure to said atmospheric pressure by means for opening a valve-to-atmosphere in said first condensing means;

(K) Heating said molecular sieve is said first condensing means so that condensable vapors within said molecular sieve in said first condensing means are driven off and expelled to said atmosphere by means of said valve-to-atmosphere in said first condensing means;

(L) Turning off said heating of said molecular sieve in said first condensing means after said vapors in said molecular sieve in said first condensing means are expelled to said atmosphere;

(M) Permitting said molecular sieve in said first condensing means to cool down;

(N) Using means for closing said valve-to-atmosphere in said first condensing means;

(O) Connecting said first condensing means to said drying chamber means and said source of vacuum, while simultaneously raising the pressure to said atmospheric pressure by means for opening a valve-to-atmosphere in said second condensing means; and

(P) Repeating the steps of (F), (G), (H), and (I), and so on, so that condensable vapors eminating from said frozen samples within said drying chamber means are sequestered by said molecular sieve in said condensing means on a continuous basis.

25. The method as recited in claim 24, further comprising the step of filling said condensing means with molecular sieve wherein said molecular sieve is a molecular sieve selected from the group consisting of Type 3A and 4A.

26. The method as recited in claim 25, further comprising the step of filling said condensing means with molecular sieve selected from the group consisting of Type 3A and 4A, wherein said group of molecular sieves is in the form of 1/8 inch diameter pellets.

27. The method as recited in claim 24, further comprising the step of filling said condensing means with molecular sieve Type 3A.

28. The method as recited in claim 27, further comprising the step of filling said condensing means with molecular sieve Type 3A, wherein said molecular sieve is in the form of 1/8 inch diameter pellets.