U.S. patents available from 1976 to present.
U.S. patent applications available from 2005 to present.

Macroporous and microporous inorganic carrier for immobilization of cells

Patent 5096814 Issued on March 17, 1992. Estimated Expiration Date: Icon_subject December 29, 2009. Estimated Expiration Date is calculated based on simple USPTO term provisions. It does not account for terminal disclaimers, term adjustments, failure to pay maintenance fees, or other factors which might affect the term of a patent.

Patent References

Support of alumina-magnesia for the adsorption of glucose isomerase enzymes
Patent #: 3992329
Issued on: 11/16/1976
Inventor: Eaton ,   et al.

High surface low volume biomass composite
Patent #: 4153510
Issued on: 05/08/1979
Inventor: Messing ,   et al.

Method for processing waste
Patent #: 4321141
Issued on: 03/23/1982
Inventor: Messing

Method of manufacturing porous sintered inorganic bodies with large open pore volume Patent #: 4588540
Issued on: 05/13/1986
Inventor: Kiefer ,   et al.

Inventors

Assignee

Application

No. 456422 filed on 12/29/1989

US Classes:

435/41, MICRO-ORGANISM, TISSUE CELL CULTURE OR ENZYME USING PROCESS TO SYNTHESIZE A DESIRED CHEMICAL COMPOUND OR COMPOSITION210/601, Treatment by living organism210/606, Adding enzyme or releasing same by treating microorganism264/43, Including vitrification or firing435/176, Enzyme or microbial cell is immobilized on or in an inorganic carrier435/395Solid support and method of culturing cells on said solid support

Examiners

Primary: Naff, David M.

Attorney, Agent or Firm

International Classes

C12P 001/00
C02N 011/14
C02N 005/00
C02F 003/00

Foreign Application Priority Data

1984-03-23 DE

Abstract

For the immobilization of micro-organisms and animal cells, in particular for anaerobic processes, such as the purification of waste water or for the biotechnological production of nutrition-essential or pharmacological substances, porous, sintered bodies are employed (inorganic carrier bodies). In particular, sintered glass in the form of Raschig rings with a double-pore structure, are employed. They have porosity-determining through-going macropores that permit a free exchange of fluid and gas from the interior of the carrier to the surroundings, and open micropores within the macropore walls, the diameter of the micropores being of the same order of magnitude as the size of the micro-organisms or cells. These carrier bodies typically have an open pore volume of 35% to 85%, 20% to 80% being accounted for by the macropores having a diameter of 20 to 500 μm, and 5%-50% by micropores having a diameter of 1-10 μm. These bodies are obtained by sintering a powder mixture comprising fine-grain material and a coarse-grain substance melting at a higher-than-sintering temperature and separable from the sintered product by allowing the latter to cool and separating (dissolving) out the soluble component.

Other References

  • Durand et al., Process Biochemistry, Sep., 1978, pp. 14-23
  • Huysman et al., "Factors Affecting the Colonization of Non Porous and Porous Packing Materials in Model Upflow Methane Reactors", Biotechnology Letters, vol. 5, No. 9, pp. 643-648 (1983
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