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

Process for the preparation of hollow microspheres

Patent 4782097 Issued on November 1, 1988. Estimated Expiration Date: Icon_subject September 23, 2007. 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

2797201

2806509

3312632

3607169

3615972

3873475

3914360

3927181

Process for production of carbon products
Patent #: 3937775
Issued on: 02/10/1976
Inventor: Horikiri ,   et al.

Formation of hollow spherical articles
Patent #: 3975194
Issued on: 08/17/1976
Inventor: Farnand ,   et al.

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Inventors

Assignee

Application

No. 07/100090 filed on 09/23/1987

US Classes:

521/56, Particle which is expandible, process of preparing an expandible particle, or process of expanding a particle to form a cellular product521/141, Cellular vinyl alcohol polymer521/149, From oxygen containing reactant521/58, Expanding utilizing plural expansion steps521/60, Adding expanding agent subsequent to solid polymer formation521/64, Removing a liquid to form a cellular product521/87, Ingredient is aldehyde or ketone521/89, Ingredient contains a sulfur atom521/94Ingredient is a nitrogen containing compound

Examiners

Primary: Foelak, Morton

Attorney, Agent or Firm

International Classes

B01J 13/20 (20060101)
B01J 13/06 (20060101)
B01J 13/12 (20060101)
C08J 3/14 (20060101)
C08J 9/00 (20060101)
C08J 9/08 (20060101)
C08J 3/12 (20060101)

Foreign Application Priority Data

1986-10-01 CA

Abstract

A process for forming hollow microspheres containing carbon or a polymer which is a carbon precursor. The process comprises forming a solution in a liquid solvent of a polymer having the following properties (a) a molecular weight of at least 10,000 and a long chain structure; (b) an ability to be coagulated by or precipitated from the solution by a non-solvent for the polymer; (c) an ability to form a continuous stretchable film when coagulated or precipitated from solution; (d) a chemical structure which is infusible or capable of being rendered infusible, and (e) a high carbon yield of at least 30% by weight upon being carbonized in a non-reactive atmosphere. An insoluble particulate blowing agent is incorporated into the solution and the solution is then divided into droplets and the droplets are introduced into a liquid bath containing a suitable non-solvent for the polymer. The non-solvent causes the polymer to precipitate or coagulate rapidly and simultaneously the blowing agent is decomposed to generate a gas within the droplets so that hollow microspheres are formed. The microspheres are then optionally subjected to carbonization in a non-reactive atmosphere at high temperature to convert the polymer to carbon. Uniformly-sized relatively large hollow microspheres can be produced by this process.

Other References

  • Houtz, Textile Research Journal, Nov. 1950, pp. 786-801
  • Kool et al., J. Vac. Sci. Technol., 1981, 18 (3), pp. 1233-1237
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