WO1999018403A1 - Rapid drying oven and methods for providing rapid drying of multiple samples - Google Patents
Rapid drying oven and methods for providing rapid drying of multiple samples Download PDFInfo
- Publication number
- WO1999018403A1 WO1999018403A1 PCT/US1998/020811 US9820811W WO9918403A1 WO 1999018403 A1 WO1999018403 A1 WO 1999018403A1 US 9820811 W US9820811 W US 9820811W WO 9918403 A1 WO9918403 A1 WO 9918403A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- inert gas
- chamber
- manifold
- drying system
- supplying
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B5/00—Drying solid materials or objects by processes not involving the application of heat
- F26B5/04—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum
- F26B5/044—Drying solid materials or objects by processes not involving the application of heat by evaporation or sublimation of moisture under reduced pressure, e.g. in a vacuum for drying materials in a batch operation in an enclosure having a plurality of shelves which may be heated
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/14—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects using gases or vapours other than air or steam, e.g. inert gases
Definitions
- the present invention is related generally to drying systems and, more particularly, to drying systems which are capable of rapidly drying chemical reaction products held in cavities or wells.
- Combinatorial chemical synthesis permits the production of very large numbers of small molecule chemical compounds which may, for example, be tested for biological activity.
- One combinatorial synthesis method employs polymeric resin beads as solid phase substrates upon which small molecule compounds are formed.
- this method sometimes referred to as the "mix and split" method, a sample of beads is divided among several reaction vessels and a different reaction is performed in each vessel. The beads from all the vessels are then pooled and redivided into a second set of vessels, each of which now contains approximately equal amounts of beads carrying the products of the first set of reactions.
- each of the products of the first set of reactions acts as a substrate for a new set of reactions which produce all the possible combinations of reactants .
- Tests such as those for biological activity, are often performed upon the compounds at a different location from that where they are formed.
- samples of a variety of compounds are often placed within the wells of a plate which contains an array of wells.
- each well may contain the same compound, so that a number of tests may be conducted on the same compound simultaneously.
- Plates such as these are conventional and a number of standard arrays are available, including a ninety-six well plate. Wells within the plates are generally available in either deep or shallow configurations.
- reaction products placed within the wells are dried, by evaporating the solvents and other volatiles in which the chemical products are immersed preferably in an inert atmosphere.
- freeze drying the compounds may take several days and many times requires unwanted fillers, such as sugars. Drying by placing the compounds under a controlled vacuum may require between five and ten hours for the drying, assuming shallow well plates. A typical convection based drying oven for drying such compounds may also require on the order of ten hours for a shallow well plate and considerably more for a deep well plate.
- High vacuum ovens may provide the benefit of rapid drying, however, the solvents have been known to be susceptible to spontaneous boiling, also known as "bumping" . Bumping can be process critical as it may cause contamination and loss of compound. This is particularly true for low boiling point solvents.
- the compounds being evaporated may also include any of a number of corrosive chemicals.
- a drying system which provides rapid, inexpensive drying of chemical compounds without requiring the use of large volumes of inert gases and which can withstand exposure to corrosive chemicals would therefore be highly desirable. Additionally, it is further desirable to control temperature and pressure in a controlled manner which prevents degradation and bumping without unnecessary moving parts .
- the present invention is directed to relatively inexpensive drying systems which may be suitably employed, for example, to rapidly dry the reaction products of combinatorial chemical synthesis without oxidation.
- the invention addresses these and other problems by providing a chamber within which the temperature and pressure may be precisely controlled to facilitate rapid drying of samples placed within the chamber. Additionally, in a currently preferred embodiment, a substantially laminar flow of dry inert gas is forced across the top of sample trays or plates placed within the chamber. The inert gas flow above the plates disrupts the accumulated vapor which tends to form within individual wells containing the chemical compounds and carries away the vapor, thus accelerating the drying process without forcing large volumes of inert gas into the individual wells .
- the invention may suitably comprise a vacuum chamber with a temperature controlled heat source and an inert gas delivery system.
- the inert gas delivery system establishes a substantially laminar flow of dry inert gas over the tops of wells which contain the chemical compounds to be dried.
- the gas flow above the plates creates gas flow patterns which effectively churn the accumulated vapor of the wells.
- Shelves within the chamber provide support for the sample trays or plates which incorporate the wells containing the chemical compounds.
- the shelves are preferably located just below manifolds which are formed to supply a substantially laminar flow of inert gas across the sample trays and to evacuate the inert gas from the vacuum chamber.
- the shelves conduct heat to the trays of compounds which they support .
- two gas-supplying manifolds are included for each shelf, with one manifold located higher than the other in order to accommodate taller plates with deeper wells.
- the currently preferred manifolds contain linear arrays of circular orifices, other orifice shapes and arrangements which effectively churn out accumulated vapor utilizing inert gas flows are contemplated by the invention.
- the presently preferred laminar gas flow removes the unwanted vapor which tends to form above the tray of chemical compounds, thus accelerating the drying process.
- Fig. 1 is a perspective view of a vacuum drying system in accordance with the present invention.
- Fig. 2 is a perspective view of the interior of a vacuum chamber which may suitably be used in the new drying system of Fig. 1.
- FIGs. 3A and 3B are perspective views of the interior of a vacuum chamber illustrating the use of a stationary supplying manifold and single exhaust port, a rotating supplying manifold and a single exhaust port, and four supplying jets with a single exhaust port, respectively.
- Fig. 4 is a plan view of a stationary supplying manifold.
- Fig. 5 is a plan view of a rotating supplying manifold.
- Fig. 6 is a top plan view of the interior of a vacuum chamber which employs four supplying jets and a single exhaust port, as in the perspective view of Fig. 3C.
- Fig. 7 is a flowchart illustrating various aspects of drying methods in accordance with the present invention.
- a new drying system in accordance with the present invention will preferably provide a combination of moderate heat and reduced pressure to substantially accelerate the evaporation of liquids, typically solvents, from the wells of multi -well plates which also contain a chemical compound of interest that is to be preserved.
- a laminar flow of dry inert gas across the top of the plates rapidly removes vapors which otherwise tend to accumulate within the well.
- Shallow well plates may be dried in only four hours using the new drying system, compared to eighteen hours required for conventional convection drying. Deep well plates, which conventionally require two to three days of convection drying plus a vacuum oven finishing step, require only six hours in the new drying system.
- the new drying system virtually eliminates oxidation of the chemical products of interest, which are left behind in the wells after evaporation.
- FIG. 1 A preferred embodiment of the new drying system is illustrated in the partial sectional view of Fig. 1.
- a vacuum oven chamber 10 is connected through a vacuum line 12 to a valve system 19 which may be suitably employed to connect either a high vacuum pump 21 to the chamber 10 through a vacuum line 16, a cold trap 14, and a vacuum line 13, or a high flow capacity pump 18 through a vacuum line 15.
- a dryness sensor 17 may be included in vacuum line 15, or, alternatively in line 13. This sensor 17 may then be connected to a suitably programmed microcontroller or microprocessor 50 which in turn controls the overall operation of the system.
- the chamber 10 is preferably coated with a chemically tolerant plastic, such as TeflonTM, available from Dupont Corporation and all exposed hardware within the chamber 10 is preferably composed of titanium.
- Shelves 20 within the chamber provide support for vessels 22, such as micro well or microtiter plates, each of which contains a plurality of wells or cavities for holding compounds which are to be dried.
- An example of such a plate is a 96-well microtiter plate.
- the shelves 20 are preferably made of aluminum and are also preferably coated with a chemically tolerant plastic, such as TeflonTM. All downstream exposed parts, including plumbing, valves and the diaphragm pump 18 are preferably composed of or coated with such a chemically tolerant plastic or a combination of such plastic and ceramic.
- the chamber 10 is preferably heated by external heating elements and the shelves 20 are preferably attached to the chamber 10 so that they are efficiently heated by conduction from the chamber walls. This approach to heating provides reliable heating and, at the same time, minimizes the possibility of unwanted condensation on the interior of the chamber walls.
- An inert gas preferably nitrogen, is supplied to the chamber through a manifold 24 which is connected through tubing 26 to a nitrogen source 28.
- Nitrogen and other gases and vapors are evacuated from the chamber through an evacuation manifold or manifolds 34, illustrated in Fig. 2.
- an evacuation manifold or manifolds 34 illustrated in Fig. 2.
- the temperature of the incoming nitrogen or other inert gas can be controlled to compensate for the evaporation cooling.
- a vacuum pressure sensor 29 is preferably mounted to a wall of the chamber 10. This sensor is connected to the controller 50 which controls the pumps 18 and 21 and the valve system 19 to control the pressure in the chamber 10 during drying so as to prevent bumping as described in greater detail below.
- Multi-well plates 22 are supported within the chamber 10 upon shelves 20.
- supplying manifolds 24 provide nitrogen through .38 mm diameter circular orifices 30 which are arranged in a linear array on 12.7 mm centers.
- Two supplying manifolds are provided per shelf 20, with thirty-six orifices per manifold.
- the upper manifolds are used for deep well plates and the lower are used in conjunction with shallow well plates.
- a substantially laminar flow of nitrogen, depicted by arrows 32, is established by evacuating the nitrogen through evacuating manifolds 34 located opposite the supplying manifolds.
- the exhaust manifolds also include a linear array of orifices.
- the inside diameter of the manifolds, the number and diameter of orifices within the manifold and the plumbing connecting the manifold to the vacuum pump 18 are selected to provide adequate laminar flow of nitrogen under normal operating conditions. In the presently preferred embodiment, there are thirty four orifices measuring .813 mm in diameter. The laminar flow established in this manner provides even drying rates for all the wells within the plates 22.
- the lower supplying manifold is preferably located approximately 2.5 cm above the shelves 20, the evacuating manifold is 38 mm above the shelf 20 and the higher supplying manifolds are located approximately 5.1 cm above the shelves 20.
- Alternative inert gas supply and evacuation configurations are illustrated in the block diagrams of Figs. 3A, 3B and 3C. In Fig.
- a single rotating manifold 36 located approximately 2.5 cm above the plates 22, supplies inert gas and a single evacuation port 34 evacuates gases.
- the manifold 36 may be rotated by the reactive force established by jets of inert gas supplied by the manifold 36.
- the configuration of Fig. 3C uses a single supplying port 38 in each of the four corners of the chamber. The openings of the supplying ports are directed to establish a vortex of inert gas. At the center of the vortex a single evacuation port 40 is suspended approximately 2.5 cm above the plates 22.
- Fig. 4 provides a more detailed view of a supplying manifold 24.
- the manifold 24 preferably comprises a tube 42 composed of stainless steel and coated with a chemically resistant plastic, such as TeflonTM. Thirty six orifices 30, measuring .38 mm in diameter are evenly distributed in a linear array along the length of the tube 42. Precision machining techniques, such as laser ablation or electron deposition machining are preferably employed to insure that the orifices 30 are precisely formed to be straight and parallel to one another.
- the rotating supplying manifold 36 is depicted in greater detail in the elevation view of Fig. 5.
- the tube 42 is as previously described in relation to Fig. 4.
- the bar is suspended from a rotating fixture 48 through which inert gas may be forced.
- the jets 45 on either side of the fixture 48 are directed with their openings in opposite directions. All the jet's openings, or orifices, are directed slightly below horizontal to establish a flow of inert gas, which, in this case may be substantially turbulent, across plates 22 resting on shelves below.
- nitrogen is intermittently supplied so that accumulated vapor is removed, reforms and is removed again as the jet rotates past a given well. This approach results in a saving of nitrogen while still working quite effectively.
- FIG. 6 The top plan view of Fig. 6 illustrates the four jet arrangement of Fig. 3C in greater detail. Jets 38 and plates 22 are as described above and are situated in each of the chamber's four corners. The direction of nitrogen flow from the jets 38 is indicated by arrows.
- the evacuation port 48 is located approximately at the center of the chamber 10 about 2.5 cm above the plates 22. This configuration establishes a flow of nitrogen which accelerates drying of the contents of the plates, with the drying taking place at substantially the same rate for all the wells.
- step 101 the chamber is loaded with materials which are to be dried, such as a microtiter plate or plates containing solvents and chemical compounds of interest within small wells in the plates.
- step 104 the temperature of the chamber shelves 20 is elevated to accelerate evaporation, but only to a level that will not damage the plate materials or chemical products.
- the drying temperature is also preferably controlled to be below the boiling point of solvents within the wells.
- step 105 the chamber is evacuated to a low vacuum, one which accelerates evaporation, but does not initiate boiling of the chemical products.
- Typical operating ranges are 25° to 50° C and 400 to 200 Torr.
- step 106 a laminar flow of nitrogen across the tops of the plates is established by injecting nitrogen from the supplying manifold at a rate of approximately 22 standard cubic feet per hour (scfh) when drying four plates having ninety six wells per plate. The chamber's temperature and pressure are maintained at this level until the majority of the solvent is evaporated and the remaining volume of solvent is too low to allow boiling or "bumping" to occur.
- a timer is checked to determine whether a programmed time interval has expired. The time interval may be preset based upon measurements made with similar mixtures and quantities under laboratory conditions.
- step 109 When sufficiently dry, as indicated in the presently preferred embodiment by expiration of the time interval, in step 109, the nitrogen flow and low vacuum pump are turned off and a higher vacuum pump lowers the pressure within the chamber, typically to 5 Torr or less, to accelerate the evaporation of the remaining solvents.
- step 110 measurements are made to determine whether the materials are as dry as desired.
- the exhaust products may be tested with an appropriate sensor or sensors in the exhaust line, such as sensor 17, subject to microprocessor control.
- an actual dryness test may be employed as an alternative or in addition to the timer to control the beginning of step 109 processing.
- the process proceeds to step 112, the end.
- the dried plates may then be removed for further processing as desired.
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2000515152A JP2001519521A (en) | 1997-10-06 | 1998-10-05 | High speed dryer and method for high speed drying of multiple samples |
CA002304778A CA2304778A1 (en) | 1997-10-06 | 1998-10-05 | Rapid drying oven and methods for providing rapid drying of multiple samples |
AU96808/98A AU727658B2 (en) | 1997-10-06 | 1998-10-05 | Rapid drying oven and methods for providing rapid drying of multiple samples |
EP98950878A EP1029210A4 (en) | 1997-10-06 | 1998-10-05 | Rapid drying oven and methods for providing rapid drying of multiple samples |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US08/944,860 US5937536A (en) | 1997-10-06 | 1997-10-06 | Rapid drying oven for providing rapid drying of multiple samples |
US08/944,860 | 1997-10-06 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1999018403A1 true WO1999018403A1 (en) | 1999-04-15 |
Family
ID=25482189
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1998/020811 WO1999018403A1 (en) | 1997-10-06 | 1998-10-05 | Rapid drying oven and methods for providing rapid drying of multiple samples |
Country Status (6)
Country | Link |
---|---|
US (3) | US5937536A (en) |
EP (1) | EP1029210A4 (en) |
JP (1) | JP2001519521A (en) |
AU (1) | AU727658B2 (en) |
CA (1) | CA2304778A1 (en) |
WO (1) | WO1999018403A1 (en) |
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RU2481825C2 (en) * | 2008-01-21 | 2013-05-20 | Интервет Интернэшнл Б.В. | Method of lyophilisation of particles, which have contained in them pharmaceutical composition, and pharmaceutical package, containing such particles |
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- 1998-10-05 AU AU96808/98A patent/AU727658B2/en not_active Ceased
- 1998-10-05 EP EP98950878A patent/EP1029210A4/en not_active Withdrawn
- 1998-10-05 CA CA002304778A patent/CA2304778A1/en not_active Abandoned
- 1998-10-05 WO PCT/US1998/020811 patent/WO1999018403A1/en not_active Application Discontinuation
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1999
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
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WO2009006861A2 (en) * | 2007-07-09 | 2009-01-15 | Zentiva, A.S. | A method for isolation and purification of montelukast |
WO2009006861A3 (en) * | 2007-07-09 | 2009-05-22 | Zentiva As | A method for isolation and purification of montelukast |
EA018481B1 (en) * | 2007-07-09 | 2013-08-30 | Зентива, К.С. | A method for isolation amorphous form of montelukast sodium |
RU2481825C2 (en) * | 2008-01-21 | 2013-05-20 | Интервет Интернэшнл Б.В. | Method of lyophilisation of particles, which have contained in them pharmaceutical composition, and pharmaceutical package, containing such particles |
EP4155641A4 (en) * | 2021-03-03 | 2024-01-10 | Lg Energy Solution Ltd | Vacuum drying device for electrode in roll-to-roll state and vacuum drying method thereof |
Also Published As
Publication number | Publication date |
---|---|
CA2304778A1 (en) | 1999-04-15 |
US6058625A (en) | 2000-05-09 |
JP2001519521A (en) | 2001-10-23 |
EP1029210A4 (en) | 2001-09-12 |
AU9680898A (en) | 1999-04-27 |
EP1029210A1 (en) | 2000-08-23 |
AU727658B2 (en) | 2000-12-21 |
US5937536A (en) | 1999-08-17 |
US6158146A (en) | 2000-12-12 |
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