Fertilizer coating applied in the reduction of caking and moisture adsorption
11739033 · 2023-08-29
Assignee
Inventors
Cpc classification
C09D123/00
CHEMISTRY; METALLURGY
C05G5/30
CHEMISTRY; METALLURGY
C09D133/02
CHEMISTRY; METALLURGY
C08F210/14
CHEMISTRY; METALLURGY
C05G3/30
CHEMISTRY; METALLURGY
C09D191/00
CHEMISTRY; METALLURGY
International classification
C05G5/30
CHEMISTRY; METALLURGY
C05G3/30
CHEMISTRY; METALLURGY
C08F210/14
CHEMISTRY; METALLURGY
C08L91/00
CHEMISTRY; METALLURGY
C09D123/00
CHEMISTRY; METALLURGY
Abstract
An active chemistry capable of being combined with a carrier to produce a coating for fertilizer or other granular or compacted products, where the coating is capable of being applied at ambient temperature and is capable of reducing moisture adsorption and caking of the granular product. The active chemistry may be a functionalized polymer such as maleic anhydride/acid (from maleic anhydride), itaconic acid, diisobutylene, methacrylic acid, alkyl acrylates (i.e. butyl acrylate), hydroxyl ethyl methacrylate, 2-acrylamido-2-methyl propane sulfonic acid, 3-allyloxy-1,2-propanediol acrylic acid, acrylamide, or a combination thereof.
Claims
1. A coating for granular products, the coating comprising: a functionalized polymer, where the functionalized polymer is a solution and where the functionalized polymer comprises maleic anhydride/acid and diisobutylene; and a carrier, where the carrier is paraffin oil, raffene oil, bright stock, rerefined base oil, base oil, petroleum-based oil, or a combination thereof; where the coating is pumpable at ambient temperature.
2. The coating of claim 1 where the functionalized polymer is a copolymer or block polymer.
3. The coating of claim 1 where the functionalized polymer is a tertpolymer.
4. The coating of claim 1 where the functionalized polymer is combined with the carrier at a concentration of 10-30%.
5. The coating of claim 1 where the molecular weight of the functionalized polymer is 2000 to 500,000 Daltons.
6. A method of reducing moisture adsorption in a granular or compacted product, the method comprising: combining a functionalized polymer with a carrier to produce a coating, where the functionalized polymer is a solution; the functionalized polymer comprises maleic anhydride/acid and diisobutylene; and the carrier is paraffin oil, raffene oil, bright stock, rerefined base oil, base oil, petroleum-based oil, or a combination thereof and where the coating is pumpable at ambient temperature; and coating a granular or compacted product with the coating, where the coating is not heated prior to coating the granular or compacted product with the coating.
7. The method of claim 6 where the functionalized polymer is a copolymer.
8. The method of claim 6 where the functionalized polymer is a tertpolymer.
9. The method of claim 6 where the functionalized polymer is combined with the carrier at a concentration of 10-30%.
10. The method of claim 6 where the molecular weight of the functionalized polymer is 2000 to 500,000 Daltons.
11. The method of claim 6 where the granular product is fertilizer.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
(1)
(2)
(3)
(4) Other advantages and features will be apparent from the following description and from the claims.
DETAILED DESCRIPTION OF THE INVENTION
(5) The devices and methods discussed herein are merely illustrative of specific manners in which to make and use this invention and are not to be interpreted as limiting in scope.
(6) While the devices and methods have been described with a certain degree of particularity, it is to be noted that many modifications may be made in the details of the construction and the arrangement of the devices and components without departing from the spirit and scope of this disclosure. It is understood that the devices and methods are not limited to the embodiments set forth herein for purposes of exemplification.
(7) In general, in a first aspect, the invention relates to an active chemistry for a coating for fertilizer or other granular or compacted products that can be applied at room temperature, that reduces moisture adsorption, and that reduces caking of the product.
(8) The active chemistry may be a polymeric dispersant and/or antiscalent-type chemistry. The functionalized polymer may be used alone or in combination with one or more traditional anticaking chemistries, including but not limited to stearyl amines, stearic acid, phosphate esters, etc. The traditional anticaking chemistries may be alkyl or alkoxylated phosphate esters, fatty carboxylic acid, fatty amines, or combinations thereof. The dispersants/antiscalents may be polymer in nature and at least a copolymer, if not a tertpolymer. This polymer may be a solution, an emulsion, or neat. The base chemistry of the polymer may be either one or a combination of maleic anhydride/acid (from maleic anhydride), itaconic acid, diisobutylene, methacrylic acid, alkyl acrylates (i.e. butyl acrylate), hydroxyl ethyl methacrylate, 2-acrylamido-2-methyl propane sulfonic acid, 3-allyloxy-1,2-propanediol acrylic acid, acrylamide, styrene, acrylic acid, ethyl acrylate, and salts of acids such as ammonium, sodium, potassium, calcium, etc.
(9) The active chemistry may be combined with any traditional or nontraditional carrier to produce the coating. The carrier may include, but is not limited to, paraffin wax, paraffin oil, raffene oil, bright stock, rerefined base oils, base oils, or petroleum-based oils. The molecular weight of the active chemistry may be 2000 to around 500,000 Daltons, preferably 15,000 to 30,000 Daltons.
(10) The combination of the active chemistry with the carrier may provide a novel solution to the reduction of moisture adsorption by hygroscopic granules or hygroscopic compacted products, such as those found in fertilizers and LDAN. It is able to do so without the requirement of heating the coating, which is an industrial need. Based on what is known in the industry, this should have a significantly favorable impact on the caking tendencies of the fertilizer.
EXAMPLE
(11) A polymer chemistry consisting of maleic anhydride/acid and diisobutylene at a molecular weight of 17,000 Daltons was combined at a concentration of 15% with a carrier consisting of 77% rerefined base oil and 23% bright stock (ASC1-D). The resulting stable coating was easily pumpable at ambient temperature. A second coating was prepared by combining 15% of a polymer chemistry consisting of acrylic acid and methacrylic acid at a molecular weight of 4500 Daltons with a carrier consisting of 77% rerefined base oil and 23% bright stock (ASC2-D). The resulting stable coating was likewise easily pumpable at ambient temperature.
(12) During testing, calcium nitrate coated with ASC1-D was able to reduce moisture uptake by 43% and maintain the resistance to moisture uptake to a minimum of 34% for the course of five hours, relative to uncoated fertilizer. This material also reduced the clumping or caking tendencies of the calcium nitrate.
Example 1
(13) Following the below temp/humidity profile, ASC1-D yielded a 41% reduction in moisture uptake within the first hour, thus preventing the dissolution or moisture contamination of the calcium nitrate granule. ASC2-D also yielded a reduction in moisture uptake, but only 6% during the one hour.
(14) Conditions:
(15) TABLE-US-00001 Relative Humidity 42% Temperature 30° C. Coating Rate 2 kg/MT
(16) Results:
(17) TABLE-US-00002 Moisture Reduction (%) Time (h) ASC1-D ASC2-D 0 0.00 0.00 1 −41.38 −6.00 2 −43.10 −3.44 3 −40.53 3.50 5 −33.89 13.37
Example 2
(18) Following the same temp/humidity profile, two variations were also prepared of an active pack blend with steryl acid and steryl amine with the polymer chemistry. In this case, the new products yielded significant moisture uptake, which was 654% and 710% moisture gain at its highest. This adds mass and dilutes the calcium nitrate components. However, these components also disrupted the recrystallization process more effectively, thus reducing the caking by 72 and 74%, which is quite significant. A 10.3% reduction is observed with the ASC1-D. So, this combination of coatings will allow for a blender to decide if moisture gain, and thus nutrient dilution, is more important, or if caking is more important.
(19) Conditions:
(20) TABLE-US-00003 Relative Humidity 42% Temperature 30° C. Coating Rate 2 kg/MT
(21) Results:
(22) TABLE-US-00004 Moisture Reduction (%) Time (h) SA-ASC1-D SA-ASC2-D 0 0 0 1 531.8 556.6 2 596.0 620.0 3 630.6 671.2 4 654.0 709.9
(23) Whereas, the devices and methods have been described in relation to the drawings and claims, it should be understood that other and further modifications, apart from those shown or suggested herein, may be made within the spirit and scope of this invention.