Process for Producing a Powder Comprising an Extruded Carrier With an Active Compound

• US 20150031786A1
• Filed: 02/14/2013
• Published: 01/29/2015
• Est. Priority Date: 02/14/2012
• Status: Abandoned Application

• Current Assignee: Albemarle Corporation
• Original Assignee: Albemarle Corporation
• Inventors: Lambeth, Gregory H.
• Application Number:
  US14/376,796
• Publication Number:
  US 20150031786A1
• Time in Patent Office: Days
• US Class Current: 523/132
• CPC Class Codes: C05C 9/02 containing urea-formaldehyde condensates
• CPC Class Codes: C05G 3/90 for affecting the nitrification of ammonium compounds or urea in the soil
• CPC Class Codes: C05G 5/10 Solid or semi-solid fertilisers, e.g. powders layered or coated C05G5/30, incorporated into a matrix C05G5/40
• CPC Class Codes: C08K 5/5399 Phosphorus bound to nitrogen
• CPC Class Codes: C08L 61/24 with urea or thiourea
• CPC Class Codes: Y02P 60/21 Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures

Abstract

This invention provides processes for forming powders comprising at least one active compound and at least one carrier. The processes comprise (i) heating at least one active compound to at least its melting point or softening point; and (ii) in an extruder, combining at least the at least one active compound with at least one carrier, to form combined ingredients, and cooling the combined ingredients as they pass through the extruder, such that the combined ingredients exit the extruder at about ambient temperature in the form of a powder having particles sized so that about 95 wt % or more of the powder passes through a screen of about 8 standard U.S. mesh.

Claims

1. A process comprising:

(i) heating at least one active compound to at least its melting point or softening point; and

(ii) in a single screw extruder or a twin-screw extruder, combining at least the at least one active compound with at least one carrier, to form combined ingredients, and cooling the combined ingredients as they pass through the extruder, such that the combined ingredients exit the extruder at about ambient temperature in the form of a powder having particles sized so that about 95 wt % or more of the powder passes through a screen of about 8 standard U.S. mesh.

2. A process as in claim 1 wherein the active compound is selected from a group consisting of urease inhibitors, nitrification inhibitors, fungicides and insecticides.

3. A process as in claim 1 wherein the active compound is of the formula:

4. A process as in claim 1 wherein the active compound comprises N-(n-butyl)thiophosphoric triamide.

5. A process as in claim 1 wherein the carrier is selected from urea-formaldehyde polymers, thermoplastic polymers, inorganic oxides, granulated starch, and microcrystalline cellulose.

6. A process as in claim 1 wherein the carrier is at least one urea-formaldehyde polymer, and wherein the urea-formaldehyde polymer is deaerated before the combining with at least the at least one active compound.

8. A process as in claim 1 further comprising deaerating the carrier before the combining with at least the at least one active compound.

9. A process as in claim 1 wherein the active compound is employed in an amount of about 35 wt % or more relative to the total weight of the carrier and the active compound.

10. A process as in claim 1 wherein at least one stabilizer is included in the combined ingredients.

11. A process as in claim 10 wherein the stabilizer is propylene glycol or triethanolamine, and/or wherein the stabilizer is in an amount of about 5 parts or more of stabilizer per 100 parts of active compound.

13. A process as in claim 1 wherein the powder has particles sized so that about 95 wt % or more of the powder passes through a screen of about 10 standard U.S. mesh.

7. (canceled)

12. (canceled)

14. (canceled)

15. A process comprising:

(i) heating N-(n-butyl)thiophosphoric triamide to at least its melting point or softening point; and

(ii) in a single screw extruder or a twin-screw extruder, deaerating at least one solid urea-formaldehyde polymer, combining the N-(n-butyl)thiophosphoric triamide with the deaerated urea-formaldehyde polymer to form combined ingredients, and cooling the combined ingredients as they pass through the extruder such that the combined ingredients exit the extruder at about ambient temperature in the form of a powder.

17. A process as in claim 15 wherein the active compound is employed in an amount of about 35 wt % or more relative to the total weight of the carrier and the active compound.

18. A process as in claim 15 wherein at least one stabilizer is included in the combined ingredients.

19. A process as in claim 18 wherein the stabilizer is propylene glycol or triethanolamine, and/or wherein the stabilizer is in an amount of about 5 parts or more of stabilizer per 100 parts of active compound.

21. A process as in claim 15 wherein the powder has particles sized so that about 95 wt % or more of the powder passes through a screen of about 8 standard U.S. mesh.

22. A process as in claim 15 wherein the powder has particles sized so that about 95 wt % or more of the powder passes through a screen of about 10 standard U.S. mesh.

16. (canceled)

20. (canceled)

23. (canceled)

24. A powder comprising at least one active compound and at least one carrier, where the powder has particles sized so that about 95 wt % or more of the powder passes through a screen of about 10 standard U.S. mesh.

25. A powder as in claim 24 wherein the carrier is at least one urea-formaldehyde polymer and/or wherein the active compound is N-(n-butyl)thiophosphoric triamide.

27. A powder as in claim 24 wherein the powder comprises about 35 wt % or more of the active compound relative to the total weight of the carrier and the active compound.

29. A powder as in claim 24 wherein the powder has particles sized so that about 97 wt % or more of the powder passes through a screen of about 12 standard U.S. mesh.

26. (canceled)

28. (canceled)