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Dry powder cells and cell culture reagents and methods of production thereof

a technology of cell culture and reagents, which is applied in the field of dry powder cell culture reagents and cell culture reagents, can solve the problems of limiting the functional life-span of culture media, reducing the number of commercial culture media available, and unable to avoid the formation of breakdown products, etc., so as to reduce the cost, reduce the cost of production, and reduce the cost of inventory, storage and labor costs

Inactive Publication Date: 2012-11-01
LIFE TECH CORP
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This approach results in stable, easily reconstituted, and cost-effective cell culture media that can be produced in large quantities, maintaining biological activity and reducing the need for specialized equipment, while ensuring sterility and consistency between batches.

Problems solved by technology

Often, particularly in complex media compositions, stability problems result in toxic products and / or lower effective concentrations of required nutrients, thereby limiting the functional life-span of the culture media.
The rate of degradation can be influenced by pH and ionic conditions but in cell culture media, formation of these breakdown products often cannot be avoided (Tritsch et al, Exp.
Since most mammalian culture media contain riboflavin, tyrosine and tryptophan, toxic photoproducts are likely produced in most cell culture media.
However, only a limited number of commercial culture media are available, except for those custom formulations supplied by the manufacturer.
Although dry powder media formulations may increase the shelf-life of some media, there are a number of problems associated with dry powdered media, especially in large scale application.
Due to the corrosive nature of dry powder media, mixing tanks must be periodically replaced.
Liquid media have the disadvantages, however, that they often do require the addition of supplements (e.g., L-glutamine, serum, extracts, cytokines, lipids, etc.) for optimal performance in cell cultivation.
Furthermore, liquid medium is often difficult to sterilize economically, since many of the components are heat labile (thus obviating the use of autoclaving, for example) and bulk liquids are not particularly amenable to penetrating sterilization methods such as gamma or ultraviolet irradiation; thus, liquid culture media are most often sterilized by filtration, which can become a time-consuming and expensive process.
Furthermore, production and storage of large batch sizes (e.g., 1000 liters or more) of liquid culture media are impractical, and the components of liquid culture media often have relatively short shelf lives.
Despite these advantages, however, concentrated liquid media still have the disadvantages of their need for the addition of supplements (e.g., FBS, L-glutamine or organ / gland extracts), and may be difficult to sterilize economically.
However, powdered media have several distinct disadvantages.
For example, some of the components of powdered media become insoluble or aggregate upon lyophilization such that resolubilization is difficult or impossible.
Furthermore, powdered media typically comprise fine dust particles which can make them particularly difficult to reconstitute without some loss of material, and which may further make them impractical for use in many biotechnology production facilities operating under GMP / GLP, USP or ISO 9000 settings.
Additionally, many of the supplements used in culture media, e.g., L-glutamine and FBS, cannot be added to the culture medium prior to lyophilization or ball-milling due to their instability or propensity to aggregate upon concentration or due to their sensitivity to shearing by processes such as ball-milling.
Finally, many of these supplements, particularly serum supplements such as FBS, show a substantial loss of activity or are rendered completely inactive if attempts are made to produce powdered supplements by processes such as lyophilization.

Method used

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  • Dry powder cells and cell culture reagents and methods of production thereof
  • Dry powder cells and cell culture reagents and methods of production thereof
  • Dry powder cells and cell culture reagents and methods of production thereof

Examples

Experimental program
Comparison scheme
Effect test

example 1

Agglomeration of Typical Dry Powder Media (DPM)

[0112]1. With a benchtop laboratory fluid bed apparatus (Stera-1; Niro, Inc. / Aeromatic-Fielder; Columbia, Md.): Place 100-500 g of DPM within the chamber. Place onto apparatus and use the lever to seal the unit.

[0113]2. Start the airflow to fluidize (levitate) the DPM. Since traditional DPM is of relatively fine particle size, setting 4-6 will be needed. Turn on the vacuum device to catch fine DPM particles, passing through the upper filters. Make sure that the fluidized powder is approximately central within the chamber with respect to the lower mesh screen and the upper filters.

[0114]3. Start the injection device (spray unit) by first plugging in the compressed air line and then by starting the pump which is connected to a water source. The goal is to admit ˜6 ml of water per minute (the flow rate for any given pump based upon RPM and tubing diameter must be known). In order to prevent clumping of DPM, alternatively add water for ˜1 m...

example 2

Addition of Sodium Bicarbonate as an Integral Part of DPM

[0145]As noted above, sodium bicarbonate is not typically added to DPM during manufacturing by ball-milling or lyophilization, due to potential off-gassing and buffering capacity complications encountered upon storage of the powdered media. This standard production process thus necessitates the addition of sodium bicarbonate, and pH adjustment, upon reconstitution of the media. With the present methods, however, these additional steps may be obviated by adding the sodium bicarbonate (or any buffering salt) directly to the powdered medium during manufacturing.

[0146]There are two ways of including sodium bicarbonate (or any buffering salt) within the DPM: (a) via the injection device and (b) as part of the DPM.

(a) Injection Device

[0147]Because of the solubility of sodium bicarbonate and the amounts that generally need to be added to a typical mammalian cell culture medium, fairly large volumes of liquid would need to be injected...

example 3

DPM that Includes Buffering Salts (e.g., Sodium Bicarbonate) and is Formulated so that pH of Reconstituted (1×) Medium is Automatically of Desired pH with No User Efforts

[0152]As noted above, all commercially available mammalian cell culture powdered media require addition of one or more buffer salts (e.g., sodium bicarbonate) when preparing 1× liquid, and then adjustment of pH, so that the solution will be at proper pH. The present methods, however, can be used to obviate both the addition of sodium bicarbonate (as described above in Example 2) and the need for pH adjustment. In this aspect of the invention, fluid bed technology is used to introduce acid or base (depending on the need) to a dry powder medium comprising one or more buffering salts. In accordance with this aspect of the invention, any buffering salts or combinations thereof, and any acid or base, may be used depending upon the desired pH and buffering capacity in the ultimately reconstituted cell culture medium.

[0153...

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Abstract

The present invention relates generally to nutritive medium, medium supplement, media subgroup and buffer formulations. Specifically, powdered nutritive medium, supplement, subgroup formulations, cell culture media comprising all of the necessary nutritive factors for in vitro cell cultivation, buffer formulations that produce particular ionic and pH conditions upon reconstitution with a solvent are provided. Particularly, methods of production of these media, supplement, subgroup, buffer formulations and kits, and methods for the cultivation of prokaryotic and eukaryotic cells using these dry powdered nutritive media, supplement, subgroup and buffer formulations are provided. Methods of producing sterile, powdered media or supplement (e.g., powdered FBS, powdered transferrin, powdered insulin, powdered organ extracts, powdered growth factors), media subgroup and buffer formulations by gamma irradiation are provided. Methods for producing dry cell powders, comprising spray-drying a cell suspension, and cells, media, media supplement, media subgroup and buffer powders produced by these methods are provided.

Description

CROSS REFERENCE TO RELATED APPLICATIONS[0001]This application claims priority to U.S. Provisional Application Nos. 60 / 040,314, filed Feb. 14, 1997, 60 / 058,716, filed Sep. 12, 1997, and 60 / 062,192, filed Oct. 16, 1997, the disclosures of which are entirely incorporated herein by reference.FIELD OF THE INVENTION[0002]The present invention relates generally to cells, nutritive media, media supplements, media subgroups and buffer formulations. Specifically, the present invention provides dry powder nutritive medium formulations, particularly cell culture medium formulations, comprising all of the necessary nutritive factors that facilitate the in vitro cultivation of cells, and methods of production of these media formulations. The invention also relates to methods of producing dry powder media supplements, such as dry powder sera (e.g., fetal bovine serum). The invention also relates to dry powder buffer formulations that produce particular ionic and pH conditions upon rehydration. The...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C12N5/02C12N1/16C12N5/07C12N5/04C12N1/00C12N1/14C12N1/20C12N5/00C12N5/074
CPCC12N1/14C12N1/16C12N5/0025C12N5/0018C12N1/20
Inventor FIKE, RICHARDWHITFORD, WILLIAMBIDDLE, WILLIAM
Owner LIFE TECH CORP