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US3972849A Expired / Lapsed US ⏱️ 0.0 years remaining

Production of resins

Assignee: BASF SE
•
Filing: 1974-04-03
•
Granted: 1976-08-03
•
Expires: 1994-04-03
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Abstract

Abstract A process for the production of milled particulate resins which comprises carrying out the reaction of the resin components in a moving reaction vessel containing carrier bodies. The new process is particularly suitable for the production of pigmented resins, for example daylight fluorescent pigments.

Inventors

  • 👤 Hilmar Bruenemann
  • 👤 Guenter Stoeckelmann
  • 👤 Volker Radtke

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-29 00:12
CPC Classifications
B; B01; B01J; B01J8/00; B01J8/08; B01J8/10; C; C08; C08G; C08G63/00; C08G63/02; C08G63/12; C08G85/00; C08J; C08J3/00; C08J3/12; C08J3/20; B01J2219/00; B01J2219/18; B01J2219/182

Claims Analysis

Total Claims: 9
Claim 1
Independent Claim 165 words
A process for the production of particulate milled resins having melting points of more than about 100° C which comprises: passing the reaction components of the resin into a moving reaction vessel having an outlet for volatile reaction by-products containing grinding bodies, said grinding bodies occupying from about 20 to 60% of the volume of the reaction vessel, heating said components to their reaction temperature in the presence of said moving grinding bodies within said vessel whereby a liquid film of reactants is formed on the surface of said bodies; and cooling the formed resin while continuing to move said vessel whereby the resin in a brittle state is caused to break away from said bodies and be milled by said bodies, the ratio of the amount of the resin components (M) in grams to the surface area (O) of the grinding bodies in square centimeters conforms to the relationship: (M/O ≦ (1/5 d d being the mean diameter of a grinding body in centimeters.
Claim 2
Dependent Claim 165 words
A process for the production of particulate milled resins having melting points of more than about 100° C which comprises: passing the reaction components of the resin into a moving reaction vessel having an outlet for volatile reaction by-products containing grinding bodies, said grinding bodies occupying from about 20 to 60% of the volume of the reaction vessel, heating said components to their reaction temperature in the presence of said moving grinding bodies within said vessel whereby a liquid film of reactants is formed on the surface of said bodies; and cooling the formed resin while continuing to move said vessel whereby the resin in a brittle state is caused to break away from said bodies and be milled by said bodies, the ratio of the amount of the resin components (M) in grams to the surface area (O) of the grinding bodies in square centimeters conforms to the relationship: (M/O ≦ (1/5 d d being the mean diameter of a grinding body in centimeters.
Claim 3
Dependent Claim 28 words
A process as claimed in claim 1 wherein a dye is additionally present in the moving reaction vessel for the preparation of a resin pigmented with the dye.
Claim 4
Dependent Claim 12 words
A process as claimed in claim 2 carried out at subatmospheric pressure.
Claim 5
Dependent Claim 13 words
A process as claimed in claim 1 wherein the grinding bodies are spherical.
Claim 6
Dependent Claim 16 words
A process as claimed in claim 4 wherein aluminum oxide spheres are used as grinding bodies.
Claim 7
Dependent Claim 38 words
A process as claimed in claim 1 wherein the reaction vessel is rotated at a relatively high speed at first to effect mixing, the speed is decreased as the reaction proceeds and finally increased again to effect milling.
Claim 8
Dependent Claim 66 words
A process as claimed in claim 1 wherein the resin components comployed are components reacting together to form a cross-linked polyester resin based on an aromatic polycarboxylic acid or anhydride and a polyfunctional alcohol, an unplasticized unmodified or alcohol-modified acid amide/formaldehyde resin, an unplasticised unmodified or alcohol-modified aminotriazine/formaldehyde resin, an arylsulfonamide/acid amide/formaldehyde resin, an arylmonosulfonamide/aminotriazine/formaldehyde resin, and alkyl-, aralkyl- or aryl-sulfonamide/diisocyanate resin or a polyol/diisocyanate resin.
Claim 9
Dependent Claim 27 words
A process as claimed in claim 2 wherein the dye present is a rhodamine dye or a dye of the formula ##STR10##where X is a nitrogen heterocycle.

References Cited (Backward Citations)

US2277393A Cited
US2715117A Cited
US2779752A Cited
US3453221A Cited
US3462514A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1979-08-03 1980-02-02 1980-08-03 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1983-08-03 1984-02-02 1984-08-03 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1987-08-03 1988-02-02 1988-08-03 $7700.00 Window Closed / Lapsed

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