Process for expanding microspheres

• US 4,513,106 A
• Filed: 11/22/1983
• Issued: 04/23/1985
• Est. Priority Date: 11/26/1982
• Status: Expired due to Fees

• Current Assignee: Kemanord AB
• Original Assignee: Kemanord AB
• Inventors: Soderberg, Jan, Edgren, Anders, Bergstrom, Bengt
• Primary Examiner(s): Foelak, Morton
• Application Number:
  US06/554,313
• Time in Patent Office: 518 Days
• Field of Search: 521/56, 521/58, 521/60, 264/DIG. 9, 264/53
• US Class Current: 521/58
• CPC Class Codes: B01J 19/20 in the form of helices, e.g. screw reactors
• CPC Class Codes: C08J 9/228 Forming foamed products
• CPC Class Codes: C08J 9/32 from compositions containing microballoons, e.g. syntactic foams
• CPC Class Codes: Y10S 264/09 Pre-expansion of foamed polystyrene

Abstract

A process for expanding expandable thermoplastic microspheres containing a blowing agent which will be volatilized at heating. A slurry of the unexpanded spheres is fed to a pressure zone together with steam whereby volatilization of the blowing agent occurs in the zone and the expanded microspheres are then allowed to leave the zone at a considerable pressure drop.

Claims

1. A method for expanding expandable organic thermoplastic microspheres containing a blowing agent, able to be vaporized upon heating, comprising the steps of

(a) providing a pumpable slurry of the unexpanded microspheres in an inert liquid,

(b) feeding the slurry into a pressure zone in which a pressure above the surrounding pressure is maintained,

(c) feeding to the pressure zone steam of a temperature and in an amount sufficient for heating the microspheres above the vaporization temperature of the blowing agent, at the pressure in the pressure zone, to thereby partially expand the microspheres,

(d) allowing the partially expanded microspheres to leave the pressure zone under a pressure drop whereby the spheres are further expanded and accelerated into a stream with a velocity of at least 1 meter per second,

(e) injecting the accelerated stream into gas volume whereby the stream is disintegrated and cooled, and

(f) separating essentially uniformly expanded and non-agglomerated spheres from the gas.

2. The method of claim 1 wherein the pressure drop at the outflow of the slurry exceeds 0.05 MPa.

3. The method of claim 1 wherein the pressure drop at the outflow of the slurry exceeds 0.1 MPa.

4. The method of claim 1 wherein the content of microspheres in the slurry fed to the pressure zone is between 5 and 45 percent by weight.

5. The method of claim 4 wherein the content of microspheres is between 5 and 45 percent by weight.

6. The method of claim 1 wherein the initial dry content and the amount of steam are selected to give a microspheres content in the outgoing mixture exceeding 10 percent by weight.

7. The method of claim 6 wherein the microsphere content in the outgoing mixture exceeds 15 percent by weight.

8. The method of claim 1 wherein an inert gas is fed into the pressure zone.