Liquid substances freeze-drying systems and methods

• US 5,208,998 A
• Filed: 10/03/1991
• Issued: 05/11/1993
• Est. Priority Date: 02/25/1991
• Status: Expired due to Fees

• Current Assignee: James R. Oyler Jr
• Original Assignee: James R. Oyler Jr
• Inventors: Oyler, James R. Jr.
• Primary Examiner(s): Bennet, Henry A.
• Assistant Examiner(s): ESQUIVEL, DENISE LYNNE
• Application Number:
  US07/770,456
• Time in Patent Office: 586 Days
• Field of Search: 34/5, 34/92, 34/15, 34/17, 34/60, 34/57 R, 34/35, 34/86, 159/4.01, 159/DIG. 5
• US Class Current: 34/288
• CPC Class Codes: F26B 3/12 in the form of a spray , i.e. sprayed or dispersed emulsions or suspensions spray drying of solutions B01D1/18
• CPC Class Codes: F26B 5/065 the product to be freeze-dried being sprayed, dispersed or pulverised

Abstract

Spray-freeze-drying systems and methods are disclosed for converting a wide variety of liquid substances into dry powder that may be reconstituted into the original substance by addition of water or other liquid that had been removed therefrom. Such systems and methods involve repetitive cycles of four operational steps, i.e., freezing, drying, defrosting and resetting and are characterized by: spraying the liquid substance downwardly in a vessel while surrounding the spray with a downward flow of process gas during the freezing step and by utilizing a heat pump for energy recapture to increase efficiency of operation.

Claims

1. In a system for the spray-freeze-drying of a fluid substance having a substantial content of solids dissolved in a liquid that includes a vertically elongated vessel having top, bottom and central portions, atomizing means including a nozzle positioned centrally in said vessel adjacent said top portion to deliver atomized particles of said fluid substance into said vessel, fluidizing means in said bottom portion to fluidize particles of frozen product formed in said vessel by upward flow of process gas into said vessel including a bottom opening in said bottom portion, cooling means to cool gas circulating in said system, heating means to heat gas circulating in said system and gas circulation means for introducing and withdrawing process gas into and from said vessel, the improvement which comprises:

a top opening in said top portion of said vessel,

said gas circulation means comprising conduit means connecting said top opening to said bottom opening,

pump means associated with said conduit means to move said process gas thorough said conduit means,

a heat pump including a hot side and a cold side,

a hot tank connected to said hot side,

a cold tank connected to said cold side,

first plumbing means connecting said hot tank to said heating means for circulation of heat exchange fluid between said hot tank and said heating means, and

second plumbing means connecting said cold tank to said cooling means for circulation of heat exchange fluid between said cold tank and said cooling means.

2. The system of claim 1 wherein said conduit means includes a first conduit connecting said top opening to said pump means and a second conduit serving to connect said bottom opening to said pump means.

3. The system of claim 1 wherein said atomizing means comprises a canopy surrounding said nozzle.

4. The system of claim 3 wherein said conduit means includes a third conduit which enters into said vessel through a wall thereof and connects to said canopy to flow a portion of said process gas around said nozzle.

5. The system of claim 4 wherein said conduit means further comprises at least one proportioning valve.

6. The system of claim 5 wherein said proportioning valve controls flow of process gas through said third conduit.

7. The system of claim 6 wherein said conduit means passes process gas through said heating means and said heating means is positioned downstream of said pump means.

8. The system of claim 7 wherein said conduit means passes process gas through said cooling means and said cooling means is positioned downstream of said pump means.

9. The system of claim 1 which further comprises means to deliver said fluid substance in cooled condition and under pressure to said atomizing means nozzle.

10. The system of claim 1 wherein said fluidizing means further comprises a grid positioned in said conduit means below said bottom opening at an angle relative to the horizontal creating a higher portion and a lower portion in said grid.

11. The system of claim 10 wherein discharge means having an upper end and a lower end is associated with said grid to receive particulate material discharged from said lower portion of said grid into said upper end.

12. The system of claim 11 wherein flow of particulate material into said discharge means is controlled by a value positioned at said upper end of said discharge means.

13. The system of claim 12 which further comprises a canister for connection to said lower end of said discharge means.

14. The system of claim 1 wherein said bottom portion of said vessel is separable from said central and top portions permitting said vessel to be accessed for internal cleaning of said vessel by external cleansing equipment.

15. In a system for the spray-freeze-drying of a fluid substance having a substantial content of solids dissolved in a liquid that includes a vertically elongated vessel having top, bottom and central portions, atomizing means including a nozzle positioned centrally in said vessel adjacent said top portion to deliver atomized particles of said fluid substance into said vessel, fluidizing means in said bottom portion to fluidize particles of frozen product formed in said vessel by upward flow of process gas into said vessel including a bottom opening in said bottom portion, cooling means to cool gas circulating in said system, heating means to heat gas circulating in said system and gas circulation means for introducing and withdrawing process gas into and from said vessel, the improvement which comprises:

a top opening in said top portion of said vessel,

process gas flow control means to cause a portion of said process gas to pass downwardly in said vessel around said nozzle

conduit means to remove process gas from said top opening and convey a first portion thereof to said bottom opening and a second portion thereof to said flow control means, and

valve means associated with said conduit means to vary the volumes of said first and second portions of said process gas.

16. The system of claim 15 wherein said flow control means comprises a canopy surrounding said nozzle.

17. In a method for the spray-freeze-drying of a fluid substance having a substantial content of solids dissolved in a liquid in a processing system including the steps of (a) spraying said fluid substance as a downwardly projected spray into a vertically elongated zone defined by boundary walls and including a top, central and bottom portions, (b) freezing said atomized particles by contact with chilled gas circulated within said zone, (c) fluidizing a bed of said frozen particles within said bottom portion by upward passage of gas through said bed, (d) drying said frozen particles in said fluidized bed by subliming said liquid therefrom to produce dried particles consisting essentially of said solids content and (e) removing said dried particles from said zone, the improvement which comprises:

maintaining said system at essentially atmospheric pressure throughout the course of said method,

exhausting gas from said top portion of said zone throughout the course of said method,

injecting gas into said bottom portion of said zone throughout the course of said method, and

during said spraying step, surrounding said projected spray with a downwardly flow of gas.

18. The method of claim 17 which includes the additional steps of:

collecting a major portion of said sublimed liquid as frozen liquid within said system, and

after said drying step and said dried particles removing step,

defrosting said system by passing gas through said system having a temperature sufficiently high to melt said frozen liquid into melt liquid.

19. The method of claim 18 which further comprises removing said melt liquid from said system.

20. The method of claim 19 wherein, following said removal of said melt liquid, said zone is purged by drawing a vacuum thereon and refilling it with dry process gas.

21. The method of claim 17 wherein the flow rate F_P of said fluid substance relative to said downwardly flow of gas F_G around said downwardly projected spray is controlled according to the following equations:

space="preserve" listing-type="equation">Q.sub.P =Q.sub.G

space="preserve" listing-type="equation">where Q.sub.P =F.sub.P (H.sub.VP Δ

T.sub.P +H.sub.FP)

space="preserve" listing-type="equation">Q.sub.G =F.sub.G (H.sub.VG)Δ

T.sub.G

and

Q=heat flux (heat per unit time)

F=flow rate (volume per unit time)

H_V =heat content per unit volume per degree

H_F =heat of fusion per unit volume

Δ

T=temperature change.

22. The method of claim 17 wherein said downwardly flow of gas ceases during said drying step.

23. The method of claim 17 wherein said fluid substance is precooled outside said zone before said spraying thereof.

24. The method of claim 17 wherein said gas exhausted from said top portion is contacted with a heat exchanger and then recycled back into said zone.

25. In a method for the spray-freeze-drying of a fluid substance having a substantial content of solids dissolved in a liquid including the steps of (a) spraying said fluid substance into a vertically elongated zone defined by boundary walls and including a top, central and bottom portions, (b) freezing sprayed particles of said fluid substance by contact with chilled process gas circulated within said zone, (c) fluidizing a bed of frozen particles of said substance within said bottom portion by upward passage of process gas through said bed, (d) drying said frozen particles in said fluidized bed at essentially atmospheric pressure by subliming said liquid therefrom to produce dried particles consisting essentially of said solids content and (e) removing said dried particles from said zone, the improvement which comprises:

providing a first quantity and a second quantity of heat exchange liquid,

withdrawing heat from said first quantity to reduce the temperature thereof to below the freezing point of said substance,

heating said second quantity at least partially with heat withdrawn from said first quantity,

during said freezing step, using said first quantity to chill said process gas and said zone and

during said drying step, using said second quantity to heat said process gas.

26. The method of claim 25 wherein further during said drying step said first quantity is used to cool a portion of said zone.

27. The method of claim 25 wherein a heat pump is used to withdraw heat from said first quantity and to heat said second quantity.