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

Fluidized bed cellulation process

Patent 4769057 Issued on September 6, 1988. Estimated Expiration Date: Icon_subject May 12, 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

2691248

3163512

3441396

3532480

Process for the preparation of expansible beads
Patent #: 4059423
Issued on: 11/22/1977
Inventor: De Vos ,   et al.

Method for forming coated cellular glass pellets
Patent #: 4081259
Issued on: 03/28/1978
Inventor: Bassin ,   et al.

Fluidized bed calcining system
Patent #: 4161389
Issued on: 07/17/1979
Inventor: Staffin ,   et al.

Process of making cellulated glass beads
Patent #: 4234330
Issued on: 11/18/1980
Inventor: Taupin ,   et al.

Centrifuge apparatus and method for producing hollow microspheres
Patent #: 4303433
Issued on: 12/01/1981
Inventor: Torobin

In-mold process for fabrication of molded plastic printed circuit boards
Patent #: 4584767
Issued on: 04/29/1986
Inventor: Gregory

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Inventors

Assignee

Application

No. 07/048656 filed on 05/12/1987

US Classes:

65/21.3, Spheroidizing or rounding of solid glass particles431/3, Decarbonizing, cleaning or purging431/8, Flame shaping, or distributing components in combustion zone65/22With pore forming in situ

Examiners

Primary: Lindsay, Robert L.

Attorney, Agent or Firm

International Classes

C03B 19/08 (20060101)
C03B 19/00 (20060101)
C03B 19/10 (20060101)

Abstract

Sintered particles of pulverulant glass and cellulating agent are coated with a parting agent and introduced into a fluidizing vessel. Gas is passed upwardly through the fluidizing vessel at a velocity sufficient to form a fluidized bed of these sintered particles within the fluidizing vessel. The gas and fluidized bed of sintered particles are heated within the fluidizing vessel to a cellulation temperature of the sintered particles to cause the sintered particles within the fluidized bed to form discrete cellular glass nodules of uniform size. The cellular glass nodules formed within the fluidized bed of sintered particles, having a density less than the density of the sintered particles, migrate to the top of the fluidized bed to float on the top surface of the fluidized bed. The discrete cellular glass nodules floating on the top surface of the fluidized bed are withdrawn from the fluidizing vessel.

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