Patent Application
20190357528
This invention relates to the stabilisation of oil-based suspension formulations of agriculturally active finely divided solids. More particularly, the invention relates to oil-based suspension formulations comprising an agriculturally active solid having improved stability.
Formulations comprising an agriculturally active solid suspended in an oil, as the primary component of the continuous phase, have been found advantageous in the treatment of agricultural substrates. Examples of such formulations have been designated by CropLife International as OD (“oil dispersion”) and OF (“oil-miscible flowable concentrate”) formulations.
Such formulations provide certain advantages to the end user. They allow the formulation of active ingredients in solid suspended form, which ingredients cannot be formulated in water because of hydrolytic instability. Also, such formulations allow oil-based adjuvants to be built-in to the formulation to enhance efficacy. Further, in many cases active ingredients have a solubility limit on the amount that can be loaded into a formulation, such as an emulsifiable concentrate formulation, and so suspension in an oil-based system can possibly lead to higher active ingredient strength formulations than would otherwise be possible.
A major limitation on an oil-based agricultural formulation, such as an OD and OF formulation, is the need to physically stabilize the formulation for potentially long periods of storage, so that it can be in a consistently useable form for later end use. Typically, an OD or OF formulation can exhibit sedimentation of the active ingredient particles over time into a hard-packed non-redispersible layer, or settling of the particles into the lower layers of the liquid column leading to the appearance of phase separation. This is what is commonly termed “syneresis”. Depending on the density of the active ingredient and that of the oil phase used, it is also possible to find the active ingredient particles migrating to the top layers of the liquid column. This is often described as “reverse” or “top” syneresis. Such physical instability can occur regardless of the presence of an oil-based surfactant dispersant, which is designed to prevent flocculation of the dispersed particles.
In order for a stabilizer to be useful in an oil-based agricultural suspension, it must provide long term physical stability across a wide temperature range, normally 0° C. to 54° C., while still maintaining a viscosity low enough to be practical for production of the formulation and its later end use. A typical viscosity required would be less than 2,000 centipoise (“cP”) and preferably, less than 1200 cP.
Various methods of stabilization of oil-based formulations are known. Typical stabilizers currently used for oil-based formulations include organically modified hectorite clay, such as the Bentone® range available from Elementis Specialties. In many of the systems that have been tested, the present inventors have found that these stabilizers do not appear to always impart stability across the desired temperature range on accelerated storage at an acceptable viscosity. Further, the thickeners used in some cases appear to inhibit some common non-aqueous dispersants used.
Hydrophobically-modified silicas are also currently used in the art. However, such stabilizers are limited in that the degree of hydrophobicity required cannot always be adequately tuned to that of the oil used. Further, such stabilizers often require the use of a small amount of hydrophilic agent, such as water, to help form a thickening structure in the oil phase. The use of water with silica in many cases negates the purpose of the formulation being anhydrous to avoid chemical degradation of the active ingredient. In many cases, the amount of silica stabilizer required to prevent undesirable sedimentation also leads to a formulation that is highly viscous and impractical to use.
Further, difficulty has been experienced in stabilizing certain active ingredients at their most desirable concentrations. Accordingly, there is a need for improved stabilizers for oil-based agricultural suspension formulations.
The use of synthetic unsaturated rubber-type copolymers, such as styrene-butadiene copolymers and styrene-polyethylene/polypropylene, as thickeners or rheology modifiers for adhesives and coatings is well known. However, to the best of the Applicant's knowledge, such polymers have not previously found practical use in agricultural oil-based suspension formulations. This is possibly because a satisfactory result has not been obtained, when such polymers have been added to oil-based suspensions in a conventional manner, such as by solid addition under high shear after the active ingredient has been dispersed and milled.
The present invention seeks to provide an improved stabilised oil-based agricultural suspension formulation and a method for producing the same. More particularly, the present invention seeks to minimize or ameliorate disadvantages and problems found in the prior art.
It has now been found, unexpectedly, that an unsaturated rubber-type copolymer based on monomers comprising, but not limited to, styrene and butadiene; styrene, ethylene and propylene; and styrene and isoprene, when formulated into a pre-mix composition according to the methods described herein, can afford greatly improved physical stability for an oil-based agricultural formulation, such as an OD or OF formulation.
According to one aspect of the present invention, there is provided an agricultural oil-based suspension formulation comprising: an active ingredient suspended in finely divided form in an oil; and at least one rubber-type copolymer or a mixture thereof, wherein the rubber-type copolymer comprises at least styrene as a residue. More preferably, the copolymer is a styrene-containing polymer selected from a styrene-butadiene copolymer, styrene-polyethylene/polypropylene or styrene-isoprene copolymer. Such copolymers may be in random, alternating or block form, or mixtures thereof.
Additional monomers may be included at levels which do not substantially change the overall form of the copolymer in oil solution or dispersion. In its most preferred form, the formulation further comprises another olefin molecule selected from butadiene, ethylene, propylene, isoprene or butylene, or mixtures thereof. Such monomers may include alpha-olefins, and vinyl olefins. Examples of such polymers include the KRATON® polymer range available from Kraton Polymers. Most preferred are the KRATON® G series polymers, such as KRATON® G-1701 polymer.
The active ingredient suitable for inclusion in an OD formulation preferably comprises at least one fungicide, insecticide, herbicide, plant growth regulator, miticide, nematocide, molluscicide, algicide, or other pesticide, or mixtures thereof. More particularly, the active ingredient is selected from, but not limited to, a fungicide, such as an alkylene bis(dithiocarbamate), such as Mancozeb (i.e. ethylenebisdithiocarbamate complex with Mg and Zn); Zineb (i.e. zinc(ethylenebis dithiocarbamate)polymer or Ziram (i.e. zinc bis(dimethyl-dithiocarbamate); Fosetyl-aluminium (i.e. aluminium tris-O-ethylphosphonate); Tebuconazole (i.e. (RS)-1-(4-chlorophenyl)-4,4-dimethyl-3-(1H-1,2,4-triazo-1-ylmethyl)-pentan-3-ol); copper hydroxide; and copper oxychloride; a phthalimide, such as Captan (i.e. N-(trichloromethylthio)-cyclohex-4-ene-1,2-dicarboximide); a herbicide, such as a sulphonyl urea, for example, Nicosulfuron (i.e. 2-[(4,6-dimethoxypyrimidin-2-ylcarbamoyl)sulfamoyl]-N,N-dimethylnicotinamide); and Azimsulfuron (i.e. 1-(4,6-dimethoxypyrimidin-2-yl)-3-[1-methyl-4-(2-methyl-2H-tetrazol-5-yl)pyrazol-5-yl sulfonyl] urea); triazolopyrimidines, such as Flumetsulam (i.e. 2′,6′-difluoro-5-methyl[1,2,4]triazolo[1,5-a]pyrimidine-2-sulfonanilide); and Penoxsulam (i.e. 2-(2,2-difluoroethoxy)-N-(5,8-dimethoxy[1,2,4]triazolo[1,5-c]pyrimidin-2-yl)-6-(trifluoro-methyl)benzenesulfonamide); a triazine, such as Atrazine (i.e. 6-chloro-N-ethyl-N′-(1-methylethyl)-1,3,5,-triazine-2,4-diamine); a phenyl urea herbicide, such as Diuron (i.e. 3-(3,4-dichlorophenyl)-1,1-dimethylurea); an insecticide, such as Aldicarb (i.e. 2-methyl-2-(methylthio)propionaldehyde-O-methylcarbamoyloxime); Carbaryl (i.e. 1-naphthyl methylcarbamate); and Diflubenzuron (i.e. N-[[(4-chlorophenyl)-amino]carbonyl]-2,6-difluorobenzamide).
The present inventors have found that the addition of certain long hydrocarbon chain organic acids or salts thereof, having C8-C20 hydrocarbyl moieties, to the above-described formulation for use in an anti-settling and physically stabilizing system produces particular advantages. Accordingly, the formulation of the present invention may further comprise at least one long hydrocarbon chain organic acid or acid salt.
The organic acid salt is preferably selected from a salt of a fatty acid; a salt of a substituted or unsubstituted linear or branched alkyl or alkenyl group; and a salt of a substituted or unsubstituted aryl group.
Where the organic acid salt comprises a fatty acid salt, the fatty acid is preferably selected from a C8-C18 fatty acid, such as oleic acid, stearic acid, myristic acid, palmitic acid, lauric acid and polyhydroxystearic acid. The salt-forming cation is selected from sodium, calcium, magnesium, potassium, aluminium, ammonium, alkylammonium, or alkanolammonium and other common monovalent, divalent and trivalent ions. The fatty acid salt is more preferably selected from sodium oleate, potassium oleate, sodium stearate, calcium dioleate, calcium distearate and calcium polyhydroxystearic acid.
Where the organic acid salt comprises a salt of an alkyl group, the hydrocarbyl moiety is preferably selected from a C10-C18 carbon chain. The alkyl group is preferably an unsubstituted linear alkyl group. The salt-forming anion of the organic acid is preferably selected from a sulphate, sulphonate, phosphate or phosphonate ion; and the salt-forming cation is preferably selected from sodium, calcium, magnesium, potassium, aluminium, ammonium, alkylammonium, or alkanolammonium and other common monovalent, divalent and trivalent ions. In one preferred embodiment, the organic acid salt is sodium lauryl sulphate.
Where the organic acid salt comprises a salt of an alkenyl group, the hydrocarbyl moiety is preferably selected from a C12-C16 carbon chain. The alkenyl group is preferably an unsubstituted linear alkenyl group. The salt-forming anion of the organic acid is preferably selected from a sulphate, sulphonate, phosphate or phosphonate ion. The salt-forming anion of the organic acid is most preferably a sulphonate ion. The salt-forming cation is preferably selected from sodium, calcium, magnesium, potassium, aluminium, ammonium, alkylammonium, or alkanolammonium and other common monovalent, divalent and trivalent ions. In another preferred embodiment, the organic salt comprising an alkenyl group is a sodium salt of an olefin sulphonate blend.
Where the organic acid salt comprises the salt of an aryl group, in one preferred form, the aryl group is preferably an alkylaryl group, wherein the alkyl chain is preferably selected from a C10-C16 carbon chain. The alkyl chain is more preferably linear. The salt-forming anion of the organic acid is preferably selected from a sulphate, sulphonate, phosphate or phosphonate ion. In yet another preferred embodiment, the organic acid salt comprising an alkylaryl group is linear alkylbenzene sulphonate.
Prior to an OD formulation being broadcast normally via foliar spray, it is diluted in water and so requires the presence of surfactant emulsifiers. However, in the case of an OF formulation, as the formulation is designed to be further diluted in an oil, surfactant emulsifiers are not required. The formulation is otherwise similar to an OD formulation. It is a requirement of an OD formulation that the active ingredient be present in a finely divided state in an oil. Suitable oil phases for OD and OF formulations include any liquid at ambient temperature, which does not dissolve the active ingredient enough to cause crystal growth or physical instability.
The oil, which is typically present in an anti-settling and physically stabilizing system may comprise, but is not limited to, a paraffin oil, such as a kerosene, for example, one of the EXXSOL® D range available from Exxon Chemical and more preferably, EXXSOL® D130; PROPAR®12 available from Caltex; and HYDROSEAL® G250H available from Total. Seed oil esters, such as methyl and ethyl oleate, methyl and ethyl soyate and their corresponding fatty acids are also suitable. Aromatic hydrocarbons, such as alkyl benzenes and alkylnaphthalenes, polyalkylene glycol ethers, fatty acid diesters, fatty alkylamides and diamides, dialkylene carbonates, ketones and alcohols may also be suitable.
The suspension formulation of the invention may comprise further additives, such as a surfactant emulsifying agent to be added once the active ingredient has been suspended in the oil; to allow the oil phase to be delivered in an emulsified form; a surfactant dispersant and physical stability agents other than those of the invention, which may function as anti-settling or anti-syneresis agents. Where present, the surfactant dispersant can be included in any suitable amount up to the level required for colloidal stabilization of the solid phase after milling.
A surfactant dispersant suitable for OD and OF formulations is preferably selected from, but is not limited to, fatty acid-polyalkylene glycol condensates, such as TERSPERSE® 2510 dispersant; polyamine-fatty acid condensates, such as TERSPERSE® 4890 dispersant; random polyester condensates, such as TERSPERSE® 2520 dispersant; and salts of polyolefin condensates, such as TERSPERSE® 2422 dispersant, which are all products of Huntsman Corporation.
The choice of emulsifiers for the OD formulation tends to be dictated by the type of oil used. Generally, surfactants with a low hydrophobe-lipophobe balance (“HLB”) are suitable. The HLB required for most oil phases used in OD or OF formulations is usually below 10. Such surfactants are preferably selected from, but are not limited to, one or more ethoxylated fatty alcohols, sorbitan esters and their corresponding ethoxylates, ethoxylated fatty acids, ethoxylated castor oil, calcium and ammonium and alkylammonium salts of alkylbenzene sulphonate, alkylsulphosuccinate salts, ethylene oxide-propylene oxide block copolymers, ethoxylated alkylamines and ethoxylated alkyl phenols.
The emulsifiers for an OD formulation comprising Mancozeb as the active ingredient, for example, can be selected from the group of castor oil ethoxylates, in particular TERMUL® 3512 emulsifier, alcohol ethoxylates in particular TERIC® 12A3, 12A4 and 17A2 fatty acid ethoxylates such as TERIC® OF6, sorbitan ester ethoxylates, such as ECOTERIC® T85, a sulphosuccinate, such as TERMUL® 3665 emulsifier, amine and calcium salts of dodecylbenzene sulphonate, such as the NANSA® EVM range of products, all of which are available from Huntsman Corporation.
Additional emulsifiers may be added as required to maintain the internal structure and viscosity of the formulation. In these circumstances, the formulation of the present invention further preferably comprises an emulsifier having a higher than usual HLB of the continuous oil phase. While uncertain as to the exact mechanism involved, the present inventors believe that the addition of a more hydrophilic molecule may assist in the internal structural reorganization of the formulation.
The additional agents are more preferably selected from one or more alkyl alkoxylates or ethylene oxide/propylene oxide diblock copolymers or alkyl initiated ethylene oxide/propylene oxide monoblock copolymers, which have an HLB exceeding the required HLB of the continuous oil phase. The agents more preferably have an HLB above about 10 and most preferably, an HLB of about 13.
The alkyl alkoxylate is preferably selected from an alcohol ethoxylate, wherein the ethoxylate is most preferably based on a fatty alcohol comprising a C10-C18 chain and wherein the number of moles of ethylene oxide added exceeds 20. In one preferred embodiment, the alkoxylate is EMPILAN® KM 20 surfactant, which is available from Huntsman Corporation.
The most preferred of the ethylene oxide/propylene oxide block copolymers is one which has a HLB above about 10 and wherein the molecular weight exceeds 2500 amu, such as for example, a diblock copolymer selected from TERIC® PE75, TERIC® PE103 and butylalkyl initiated monoblock copolymers, such as TERMUL® 5429, which are all available from Huntsman Corporation.
Further additives which may be added to the formulation include colorants, such as pigments and dyes; adjuvant surfactants; pH adjusters and other chemical stabilizers; defoamers; perfumes; odour masks; and further density-adjusting solvents. The formulation may further comprise safeners.
The scope of the present invention also extends to a premix composition comprising the unsaturated rubber-type copolymer, an oil and/or aromatic solvent, and optionally, an organic acid or organic acid salt and/or a dispersant suitable for preventing flocculation and agglomeration of an oil-based suspension formulation.
The rubber-type copolymer in the premix composition is preferably present in the range of 4-20% w/w and where an aromatic solvent is used, in the range of 10-85% w/w and most preferably, in the range of 10-50% w/w. The oil or solvent or combinations thereof is preferably present in the premix composition in the range of 80-95% of the total composition. If present, the organic acid salt in the premix composition is preferably present in the range of 0-15% w/w of the total composition and more preferably, in the range of 10-15% w/w of the total composition. The amount of surfactant dispersant in the premix composition is typically present in the range of from 0-5% w/w and preferably, in the range 2.0-3.0% w/w of the total composition.
In yet a further aspect, the scope of the present invention extends to a method of preparing an oil-based suspension formulation from an initial pre-mix composition. The pre-mix composition is preferably made by dissolving the unsaturated rubber-type copolymer of the invention in the oil by heating at high temperature, typically 70-100° C. and preferably, 80-90° C. to give a clear homogenous liquid free of gel and un-dissolved solids. It is usually the case that only efficient stirring is required to achieve this. To the oil solution, can then be added the organic acid or salt thereof, which substantially disperses or dissolves in the solution. The mixture of copolymer, organic acid or salt thereof and oil is then preferably cooled to 60° C. after which an amount of dispersant can be substantially dissolved in the premix composition. The premix composition can then be cooled to ambient temperature and stored to be used at a later date. Alternatively, the solid phase (active ingredient) can preferably be added to the premix composition upon reaching 60° C. or below.
In a still further preferred aspect, the present invention is directed to a method of preparing an oil-based agrochemical suspension formulation, such as an OD or OF formulation, comprising the steps of preparing a premix composition preferably in accordance with the method of the invention described above and then substantially dispersing the active ingredient in the premix composition without, or together with, further oil and optionally, further dispersant. Since the premix composition is typically used in the final formulation at around 10% concentration, the rubber-type copolymer is preferably present in the final formulation in the range 0.05-2% w/w and most preferably, in the range 1.0-2.0% w/w. Similarly, if present, the organic acid or salt thereof in the final formulation is preferably present in the range of 0-1.5% w/w of the total composition and more preferably, in the range of 0.4-1.0% w/w. The amount of surfactant dispersant in the final formulation is usually present in the range of from 0-10% w/w of the total composition and preferably, in the range 2.0-5% w/w. The balance of the final OD/OF formulations comprises the oil component.
The active ingredient is normally dispersed in the premix composition with high shear mixing, such as is obtained by a Silverson® mixer, and then milled under very high shear conditions, such as is obtained in a bead mill, such as a Dynomill® KDL. Milling is normally required to reduce the particle size of the active ingredient into a range suitable to prevent sedimentation within hours and also such as to provide suitable efficacy when applied. Such particle size required is normally influenced by the respective densities of the active and the oil phase; however, typically an average size of 1-10 microns and preferably, 1-3 microns is required.
The invention described herein in yet a further aspect is a method of preparing an OD formulation comprising an active ingredient comprising the steps of:
In one particularly preferred embodiment of the present invention, the active ingredient comprises Mancozeb, preferably in a concentration of greater than 400 g/L. In another preferred form, the formulation comprises Mancozeb in a concentration greater than 580 g/L. The present inventors have advantageously been able to produce a formulation comprising Mancozeb in a concentration of greater than 480 g/L, which formulation has been found to be stable long-term with no adverse effects on viscosity. In this formulation, no hard-packed layer is observed and the formulation remains fluid/pourable when stored for a time period of longer than 6 weeks at 54° C. The advantage provided by the present invention is that it achieves a superior stable high loading suspension formulation of Mancozeb, where alternative anti-settling agents, such as modified hectorite clays, appear to be ineffective.
The present inventors have found that by the use of a premix composition of the polymer stabilizer in an oil, which may or may not constitute the primary part of the dispersing medium, greatly enhanced stability in difficult OD and OF formulations tested can result. Once formulated, an OD or OF formulation produced by the method of the present invention would be expected to exhibit stability on storage at temperatures ranging from −5° C. to 54° C. for up to 2 weeks and also stability at ambient temperature for up to 2 years.
The flow curves for Examples 1 to 4 are shown in
The following description relates only to specific embodiments of the present invention and is in no way intended to limit the scope of the present invention to those specific embodiments. In particular, the following description is exemplary rather than limiting in nature. Variations and modifications to the disclosed methods may become apparent to those skilled in the art that do not necessarily depart from the essence of this invention.
The invention will now be described with reference mainly to high loading suspension formulations of Mancozeb, Diuron, Atrazine and Captan, respectively. It is anticipated that similar results can be found for suspension formulations in oil of other solid active ingredients, which are not soluble in the continuous phase.
A typical OD formulation would have a composition as described in Table 1 below.
Rheological Studies
A combination of oil and rubber-type copolymer was made without active ingredient to examine the effect of adding the organic acid salts including fatty acid salts, sulphate and sulphonate salts; high HLB non-ionic surfactants; dispersants and emulsifiers to the system. This gives a model for the later formulations which are demonstrated.
Flow and Oscillation Measurement:
Measurements have been conducted using an AR 2000ex rheometer from TA instruments.
Flow Procedure:
Cone geometry 4 cm 2°, gap 51 μm or plate geometry 4 cm, gap 150 μm; temperature 20° C.; shear rate from 0 s−1 to 100 s−1, peak hold at 100 s−1 and rate down from 100 s−1 to 0 s−1.
Temperature Sweeps:
Cone geometry 4 cm 2°, gap 51 μm or plate geometry 4 cm, gap 150 μm; temperature sweep from 5° C. to 55° C. at defined % strain within LVR and frequency of 1 Hz.
Examples 1 to 4 look at the effect of dispersants and emulsifiers on the rubber-type copolymer in oil.
Preparation of Rubber-Type Copolymer Base
To 88 parts w/w PROPAR® 12 is added 4 parts KRATON® G1701. The resultant blend is heated with stirring at 70° C. for several hours until a gel is formed. The gel formed is hereafter referred to as KRATON® base.
To 90% w/w of KRATON® G1701 base from Example 1 is added 10% w/w TERPSERSE® 2510 with heating at 40° C. until the latter is dissolved.
To 90% w/w of KRATON® G1701 base of Example 1 is added 10% of a 1:1 blend of ECOTERIC® T85 (sorbitan trioleate ethoxylate) and EMPILAN® KBE 3 (alcohol ethoxylate). The reference name of this blend is EDSA 08/09. These are typical oil in water emulsifiers that would be utilised in the emulsification of PROPAR® 12 oil.
To 90% w/w of KRATON® G1701 base of Example 1 is added 10% w/w of TERMUL® 3665 (dialkylsulphosuccinate salt in aromatic solvent); another typical emulsifier utilised in the emulsification of PROPAR® 12 type oils.
The flow curves for Examples 1 to 4 are shown in
The KRATON® G1701 polymer when present solely in PROPAR® 12 oil, as per Example 1, provides sufficient yield strength and is elastic over the applied temperature range. This shows that it is suitable as a structuring agent for OF formulations.
Addition of TERSPERSE® 2510 dispersant as per Example 2 reinforces the yield strength, but the system loses its elasticity above room temperature. This suggests TERSPERSE® 2510 provides good viscosity at room temperature, but does not afford good stabilisation at the higher temperatures of the required storage conditions for OD formulations.
The use of typical emulsifiers as per Example 3 showed inferior elasticity and hence stability below room temperature, however improvement was seemingly shown as the temperature was increased. This suggests that in the presence of the rubber-type copolymer, these emulsifiers result in lower than optimal structuring effects at lower temperatures.
The use of TERMUL® 3665 as per Example 4 was shown to destroy the yield value during the flow experiment and the elasticity over the full temperature range. Addition of this emulsifier interferes with the yield strength (flow) and the elasticity at lower temperatures. This suggests that TERMUL® 3665 in the absence of other additives inhibits the structure of the rubber-type co-polymer.
Examples 5 to 8 show the effect of adding other dispersants to the KRATON® base.
To 90% w/w of KRATON® base from Example 1 is added 10% w/w polyhydroxystearic acid with heating at 40° C. until it is dissolved.
To 90% w/w of KRATON® base from Example 1 is added 10% w/w polyethylene glycol MW 1500 (PEG 1500) with heating at 40° C. until homogeneous.
To 90% w/w of KRATON® base from Example 1 is added 10% w/w TERSPERSE® 4890 (polyamine-fatty acid condensate) and stirred until it is dissolved.
To 90% w/w of KRATON® base from Example 1 is added 10% w/w TERSPERSE® 2422 (polyolefin condensate salt) and stirred until it is dissolved.
Flow curves for Examples 5 to 8 with comparisons to Examples 1 and 2 are shown in
Addition of polyhydroxystearic acid as per Example 5, TERSPERSE® 4890 as per Example 7 and TERSPERSE® 2422 as per Example 8, displayed a detrimental effect on the structure. Addition of PEG 1500 as per Example 7 showed some beneficial effect.
These Examples suggest that TERSPERSE® 2510 is the most optimal dispersant to use with the rubber-type copolymer in the absence of any other additives.
Effect of Fatty Acid Salts on Rubber-Type Copolymer
Examples 9 to 16 show the effect of the various fatty acid salts in combination with the rubber-type copolymer in HYDROSEAL® oil. (Note: HYDROSEAL® oil is a C12-C18 hydrocarbon oil. It has a lower carbon distribution compared with PROPAR® 12 used in the previous Examples). Example 9 is hereinafter referred to as KRATON®/HYDROSEAL® base.
The rubber-type copolymer premix was prepared as described for Examples 1 and 2. The fatty acid salts were incorporated either by readily dispersing the salts, using an overhead stirrer, or where required via high shear mixing.
Compositions Used in Examples 9 to 16
Flow curves for Example 9 to 16 are shown in
Effect of Sulphate and Sulphonate Salts on the Rubber-Type Copolymer
Examples 17 and 18 show the effect of adding sulphate and sulphonate salts to the KRATON®/HYDROSEAL® base. EMPICOL® LZ/B is a sodium lauryl sulphate salt surfactant. TERWET® 1004 is an olefin sulphonate blend sodium salt surfactant. Examples were prepared in the manner described for Examples 9-16.
The flow curves for Examples 17 and 18 are shown in
The addition of EMPICOL® LZ/B is similarly beneficial toward retaining the elasticity of the structuring blend containing TERSPERSE® 2510. TERWET® 1004 also partly overcame the loss of elasticity at high temperature encountered by the use of TERSPERSE® 2510.
The conclusion is that alkyl sulphate and alkyl sulphonate salts can behave in a similar manner to fatty acid salts in further assisting the performance of the rubber-type copolymer.
Effect of Adding Higher HLB Alcohol Ethoxylates to the KRATON®/HYDROSEAL® Base
This study was conducted with HYDROSEAL® G250H. The KRATON®/HYDROSEAL® base from Example 9 was diluted with 10% HYDROSEAL® G250H and 5% TERSPERSE 2510 before measuring the rheology.
The EMPILAN® KM series are C16-C18 alcohol ethoxylates. The number following KM denotes the number of moles ethylene oxide present.
Examples 19 to 23 show the effect of adding an alcohol ethoxylate to the KRATON®/HYDROSEAL® base in the presence of TERSPERSE® 2510 dispersant.
Flow curves for Examples 19 to 23 are shown in
It can be seen from
This suggests a beneficial effect of adding an alcohol ethoxylate of an HLB of greater than 10, i.e. greater than is required to emulsify the oil, with an HLB above 13 showing the best effect.
A range of example OD formulations have been prepared using KRATON® G-1701 to determine the functional rheological effects imparted upon basis model formulations using three agricultural active ingredients. KRATON® G-1701 is used either solely as a pre-prepared gel with aromatic solvent, as a pre-prepared gel using paraffin oil, or in conjunction with various organic acid salts.
All formulations were subject to accelerated storage at 54° C. unless stated otherwise and where possible, suspensibility measurements were conducted pre-storage at 2% w/v in 20 ppm ambient water according to CIPAC MT 161. Despite such testing not being an official requirement of the Food and Agriculture Organisation (“FAO”) in relation to OD formularies, in this instance, residue suspensibilities were determined to best characterise the quality of the oil/solid dispersion once diluted.
Preparation of an OD Formulation Comprising a Bentone® Anti-Settling Agent
The formulation was prepared as follows:
The formulation was made in the manner known to those skilled in the art by dissolving the oil dispersant TERSPERSE® 2510 dispersant in 90% of the oil phase and adding the Mancozeb (85% w/w technical) powder to it with high shear mixing to form a slurry which was then milled by bead mill to produce a millbase at an average particle size (dos) of less than 5 microns (μm). To the millbase is then added the other surfactants and the Bentone® thickener with stirring.
The formulation was placed on storage at 54° C. While the emulsification of this formulation was satisfactory, after less than 5 days the formulation formed into a thick gel with a hard packed sediment layer which was not redispersible.
This formulation demonstrates that even relatively high amounts of the Bentone® thickener are not able to prevent sedimentation and also afford a satisfactory viscosity for this product.
Preparation of OD Formulations without Structuring Agent
The formulation was prepared as follows:
The formulation was prepared by adding the Diuron active to the oil and TERSPERSE® 2510 dispersant with shear mixing to make a 58% w/w premix. This premix was then milled to an average particle size of less than 2 microns to give a millbase. To the millbase was added TERMUL® 3665 emulsifier with high shear mixing (7000 rpm, 2 minutes) then further HYDROSEAL® G250H was added to volume followed by further high shear mixing until homogeneous.
The formulation was placed on storage at 54° C. and 20° C. and after 7 days, a thick hard pack layer was observed. The formulation also showed 53% syneresis.
OD Formulation Made Using Diuron 400 g/L as the Active Ingredient
The formulation was prepared as follows:
To an appropriately sized beaker, approximately 150 g/L EXXSOL® D130 was added, followed by the required amounts of TERSPERSE® 2510, TERIC® 12A3N and TERMUL® 3665. The mixture was then subject to moderate heating (approx. 30-40° C.) for several minutes, then exposed to high shear mixing to form a homogeneous pre-dispersion. Once cooled to ambient temperature, the required amount of un-milled Diuron (95% w/w technical) was dispersed and high shear mixing was continued for several minutes. The formulation was then allowed to settle, made to the required volume with further EXXSOL® D130 (if necessary), and returned to shear until homogeneous.
The formulation initially appears as a homogeneous white dispersion of relative low viscosity, that when diluted in 20 ppm ambient water emulsifies readily. Of note is the development of syneresis within several minutes. Following storage for 14 days at 54° C., it was observed that the above formulation had developed 55% syneresis in association with the presence of a permeable yet somewhat rigid gel-like matrix which upon stirring proved difficult to fluidise.
The formulation demonstrates relatively poor stability afforded by a lack of suitable rheology modifier.
OD Formulation Made Using Atrazine 400 g/L as the Active Ingredient
The formulation was prepared according to the method outlined in Example 26:
The formulation initially appears as a homogeneous white dispersion of a relative intermediate viscosity which gives suitable emulsification performance in 20 ppm ambient water. Following storage for 14 days at 54° C., the formulation displayed 48% syneresis with the bulk consisting of a homogeneous easily permeable gel-like structure that through stirring was reversible to a flowable consistency similar to its pre-storage appearance.
Preparation of an OD Formulation Using Rubber-Type Copolymer (KRATON® G-1701 Polymer) as Anti-Settling Agent Directly
KRATON® G-1701 polymer is described as a polymer of styrene and polyethylene/polypropylene as a diblock.
The following formulation was prepared in a manner similar to that used for Example 24; however, the KRATON® G-1701 polymer and the sodium oleate were added prior to milling with high shear mixing:
The formulation was placed on storage for 2 weeks at 54° C., after which time it showed a significant increase in viscosity, but no signs of a hard-pack layer of flocculation.
This formulation affords some improvement in storage stability. However, the emulsification characteristics upon dilution in water were poor.
Examples Using Structuring Agent Premix Composition Comprising Oil and Fatty Acid Salt
Preparation of the Structuring Agent Premix:
The premix composition was prepared as follows:
The total amount of oil required is heated to 80° C.-90° C. The KRATON® G-1701 polymer is added to the hot oil and using efficient stirring solubilised to give a clear, gel/bit free liquid.
The sodium oleate is then dispersed evenly in the KRATON® G-1701 polymer/oil mixture. The mixture is maintained at 80° C.-90° C. whilst being stirred until homogeneous in appearance before allowing to the mixture to cool to 60° C.
When the oil mixture reaches 60° C., TERSPERSE® 2510 dispersant is added and dispersant is fully dissolved in the oil mixture.
Once prepared, the mixture can be used at 60° C. or cooled to ambient temperature and stored for later use. The mixture remains quite stable and fluid on storage.
Preparation of a Mancozeb (480 g/L) Formulation Comprising the OD Premix Composition
The formulation was prepared as follows:
Further TERSPERSE® 2510 dispersant is added to the oil blend prepared in Example 29 together with 90% of the remaining oil required. Immediately after the TERSPERSE® 2510 dispersant has solubilised in the oil by high sheer mixing for up to 15 minutes, the Mancozeb (85% w/w technical) is added to the oil blend with continued high shear mixing. The Mancozeb pre-mix is transferred to a bead mill and milling is continued until an average particle size (dos) of less than 5 microns (μm) is obtained.
The emulsifiers are then added one at a time to the milled pre-mix under high shear mixing ensuring that each emulsifier was completely homogenised.
The final formulation is then made up to volume with further EXXSOL® D130.
The formulation was placed on storage for 2 weeks at 54° C. after which time it showed only a minor increase in viscosity and no signs of a hard-pack layer of flocculation and minimal (<1%) syneresis. The emulsion characteristics upon dilution in water in water were improved compared to previous Examples, but were still less than optimal.
Preparation of a Mancozeb (567 g/L) Formulation Comprising the OD Premix Composition
The following formulation was prepared according to the method described in Example 30:
The formulation was placed on storage for 2 weeks at 54° C. The formulation showed excellent storage stability with no increase in formulation viscosity or hard packed layer and (<1%) syneresis. The emulsion characteristics upon dilution in water were greatly improved. This formulation still showed good flowability after 6 weeks at 54° C.
Premix Comprising EXXSOL® D-130 without Fatty Acid Salt
The following structuring agent was prepared:
The total amount of oil required is heated to 80° C.-90° C. The KRATON® G-1701 polymer is added to the hot oil and using efficient stirring solubilised to give a clear, gel/bit free liquid.
The mixture is maintained at 80° C.-90° C. whilst being stirred until homogeneous in appearance before allowing to the mixture to cool to 60° C.
When the oil mixture reaches 60° C. TERSPERSE® 2510 dispersant is added and dispersant is fully dissolved in the oil mixture.
Once prepared the mixture can be used at 60° C. or cooled to ambient temperature and stored for later use. The mixture remains quite stable and fluid on storage.
Formulation made using premix of Example 32.
The following formulation was made by the method described in Example 30:
After storage at 54° C. for 2 weeks, the formulation showed a slight increase in viscosity with no signs of a hard-pack layer or flocculation. The emulsion characteristics upon dilution in water were similar to Example 30.
The following premix comprising SOLVESSO® 150 was prepared:
To an appropriate vessel, the required amount of SOLVESSO® 150 and KRATON® G-1701 are added. The resultant mixture is then heated with moderate stirring until such point that a gelatinous yet flowable homogeneous consistency is observed. On cooling, the viscosity increases further forming a workable gel, which is stored for later use.
The following OD formulation was prepared:
To an appropriately sized beaker, approximately 150 g/L EXXSOL® D130 was added, followed by the required amounts of the remaining inert components. The mixture was then subject to moderate to high heating (approx. 50-60° C.) until the structuring agent had incorporated, then high shear mixing was initiated to form a homogeneous pre-dispersion. Once cooled to ambient temperature, the required amount of un-milled Diuron (95% w/w technical) was dispersed and high shear mixing was continued for 5 minutes. The formulation was then allowed settle, made to the required volume with further EXXSOL® D130 (if necessary), and returned to shear for 10 minutes to ensure homogeneity.
The formulation initially appears as a homogeneous white dispersion of a relative intermediate viscosity. When diluted in ambient 20 ppm water, a residue suspensibility of 78.0% is observed after 30 minutes. Following storage for 7 days at ambient laboratory temperatures, 45% syneresis was observed, while the remaining settled bulk suspension displayed an easily permeable gel matrix which via stirring was reversible yielding a homogeneous fluid dispersion.
The formulation demonstrates that although initially rheology modification is observed, antagonism arises from the presence of traditional oil emulsifiers and aromatic solvent.
OF Formulations i.e. Examples without Emulsifying Agents
The following OF formulation was prepared:
The formulation was prepared by adding the Diuron active to the oil and TERSPERSE® 2510 dispersant with shear mixing to make a 58% w/w premix. This premix was then milled to an average particle size of less than 2 microns to give a millbase. To the millbase was added the structuring premix of Example 3 with high shear mixing.
The formulation was placed on storage at 54° C. and 20° C. and after 7 days, no hard pack layer was observed. The formulation also showed only 20% syneresis, which is a marked improvement over the Example without structuring agent.
The following OF formulation was prepared according to the method outlined in Example 35:
The formulation initially appears as a homogeneous white dispersion of a relative low viscosity. When diluted in ambient 20 ppm water, poor suspensibility is observed due to the lack of appropriate emulsifier. Following storage for 6 days at ambient laboratory temperatures, the formulation remained homogeneous and flowable with 7.5% syneresis. After the same period at 54° C., the formulation although flowable displayed 56.1% syneresis.
Under ambient conditions, the formulation demonstrates the expected improved performance with the exclusion of traditional oil emulsifiers in comparison to Example 35.
The following OF formulation was prepared according to the method outlined in Example 35, noting however that in this instance KRATON® G-1701 was added neat to yield a heightened use-rate:
The formulation initially appears as a homogeneous white dispersion of a relative low to intermediate viscosity. When diluted in ambient 20 ppm water, poor suspensibility is observed due to the lack of appropriate emulsifier. Following storage for 6 days at ambient laboratory temperatures, the formulation remained flowable with trace syneresis observed. After storage for the same period at 54° C., the bulk formulation remained flowable, with 55.0% syneresis observed.
The formulation highlights improved stability relating to the exclusion of antagonistic emulsifier and aromatic solvent.
Examples Using Rubber-Type Copolymer without Fatty Acid
The following OD formulation was prepared:
The formulation was prepared by making a 58% w/w millbase, as described in Example 36. To the millbase was added the structuring premix of Example 32 and TERMUL® 3665 emulsifier with high shear mixing.
The formulation was placed on storage at 54° C. and 20° C. and after 7 days, no hard pack layer was observed. The formulation showed 32% syneresis, which is still a marked improvement over the Example without structuring agent.
Further optimisation of the level of structuring premix and dispersant can be anticipated to make this formulation achieve an acceptable level of syneresis.
The following OD formulation was prepared according to the method outlined in Example 35, noting however in this instance that KRATON® G-1701 was added neat to yield a heightened use-rate:
The formulation initially appears as a homogeneous white dispersion of a relative high viscosity. When diluted in ambient 20 ppm water, a residue suspensibility of 76.2% is observed after 30 minutes. Following storage for 14 days at 54° C., 41.7% syneresis was observed, while the remaining settled bulk suspension had thickened into a non-flowable state that via stirring was reversible yielding a homogeneous fluid dispersion. After the same period at ambient laboratory temperatures, the formulation displayed the same characteristics however 32.1% syneresis was measured.
The formulation demonstrates that despite the initial high viscosity, heightened use-rate of KRATON® G-1701 does not fully overcome the antagonism afforded by the use of typical oil emulsifiers.
The following OD formulation was prepared according to the method outlined in Example 35, however only 50 g/L of EXXSOL® D130 is added initially:
The formulation initially appears as a homogeneous white dispersion of relative low to intermediate viscosity, that when diluted in 20 ppm ambient water emulsifies readily. Following storage for 14 days at 54° C., 44% syneresis had developed with the bulk consisting of a homogeneous easily permeable gel-like structure that via stirring was partly reversible to a flowable consistency. After 14 days at ambient temperature, the formulation remains flowable and displays 28% syneresis.
This formulation demonstrates improved stability via use of sodium oleate in conjunction with KRATON® G-1701, whereby the development of syneresis was inhibited. This was notable particularly both post initial preparation and within sample stored at ambient temperature.
The following premix composition comprising more fatty acid salt and SOLVESSO® 150 solvent was prepared:
To an appropriate vessel, the required amount of SOLVESSO® 150, EXXSOL® D130 and KRATON® G-1701 are added. The resultant mixture is then heated to 60° C. with moderate stirring until such point that a viscous yet homogeneous consistency is observed. Sodium oleate is then added and stirring is continued to form an opaque flowable gel. On cooling, the viscosity increases further forming a workable gel, which is stored for later use.
The following OD formulation was prepared according to the method outlined in Example 35:
The formulation initially appears as a homogeneous white dispersion of a relative low to intermediate viscosity. When diluted in ambient 20 ppm water, the formulation yields a residue suspensibility of 61.0% after 30 minutes. Following storage for 7 days at 54° C., the formulation displayed 31.7% syneresis with the bulk remaining flowable despite some thickening effects. After 7 days at ambient temperature, the formulation remains flowable and homogeneous, with 7.9% syneresis measured.
This formulation demonstrates improved syneresis at both ambient and 54° C. storage conditions, particularly the former.
The following OD formulation was prepared according to the method outlined in Example 35:
The formulation initially appears as a homogeneous white dispersion of a relative intermediate viscosity. When diluted in ambient 20 ppm water, the formulation emulsifies readily to yield a residue suspensibility of 76.7% after 30 minutes. Following storage for 5 days at 54° C., the formulation displayed only 13.8% syneresis with the bulk suspension remaining flowable. After the same period at ambient temperature, the formulation remains flowable showing only trace syneresis.
The formulation demonstrates the improved effect of using increased levels of TERSPERSE® 2510 alongside the structuring blend from Example 42 comprising KRATON® G-1701, sodium oleate, SOLVESSO® 150 and EXXSOL® D130.
The following formulation was prepared according to the method outlined in Example 35, but in this instance, an alternate polyamine-fatty acid condensate known as TERSPERSE® 4890 is used as the primary dispersant:
The formulation initially appears as a homogeneous white dispersion of a relative intermediate viscosity. When diluted in ambient 20 ppm water, the formulation emulsifies readily to yield a residue suspensibility of 71% after 30 minutes. Following storage for 2 days at 54° C., the formulation displayed 30.8% syneresis with the bulk consisting of a homogeneous easily permeable gel-like structure that through stirring was reversible to a flowable consistency similar to its pre-storage appearance. After 7 days at ambient temperature, the formulation remains flowable showing only 6.8% syneresis.
The formulation demonstrates that the structuring blend from Example 42 comprising KRATON® G-1701, sodium oleate, SOLVESSO® 150 and EXXSOL® D130 can still provide stabilising effects when used alongside and alternate dispersant.
The following formulation was prepared according to the method outlined in Example 35:
The formulation initially appears as a homogeneous white dispersion of a relative intermediate viscosity which gives suitable emulsification performance in 20 ppm ambient water. Following storage for 14 days at 54° C., the formulation displayed 25% syneresis with the bulk consisting of a homogeneous easily permeable gel-like structure that through stirring was reversible to a flowable consistency similar to its pre-storage appearance.
This formulation demonstrates marked improvement in stability particularly with regard to syneresis. This can be attributed to the use of the structuring blend outlined in Example 34 which comprises KRATON® G-1701 and SOLVESSO® 150.
Example Showing the Effect of a High Build EO/PO Block Copolymer on the Rubber-Type Copolymer
The following formulation was prepared:
To an appropriately sized beaker, 359.12 g/L of HYDROSEAL® G250H was added, followed by the required amounts of TERSPERSE® 2510, DS 10595, TERMUL® 3665 and TERIC®PE103. The mixture was then subject to moderate heating (approx. 30-40° C.) for several minutes, then exposed to high shear mixing to form a homogeneous pre-dispersion.
Once cooled to ambient temperature, the required amount of Mancozeb (85% w/w technical) was dispersed followed gradual addition of structuring blend from Example 34 comprising KRATON® G-1701 and SOLVESSO® 200. The resultant mixture was then subject to further high shear until satisfied that a homogeneous clump-free dispersion was achieved. Note in this instance that a polyalkylene glycolether fatty acid condensate blend known as DS 10595 was used as a secondary dispersant.
The formulation initially appears as a homogeneous yellow dispersion of intermediate viscosity. Upon dilution in 30° C. in 342 ppm hard water, the formulation yields a residue suspensibility of 88.1% after 30 minutes.
After storage for 14 days at 54° C., the formulation remained partly flowable and displayed 6.9% syneresis in addition to a slight increase in viscosity attributed to the presence of a weakly structured gel-matrix. Minor soft packing was also present that was easily reversible with minor stirring.
Where the terms “comprise”, “comprises”, “comprised” or “comprising” are used in this specification, they are to be interpreted as specifying the presence of the stated features, integers, steps or components referred to, but not to preclude the presence or addition of one or more other feature, integer, step, component or group thereof.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2011902298 | Jun 2011 | AU | national |
This application is a continuation application of U.S. patent application Ser. No. 14/116,392, filed Oct. 7, 2014, pending, which is the National Phase of International Application PCT/AU2012/000661 filed Jun. 8, 2012 which designated the U.S. and which claims priority to Australia Application Serial No. 2011902298 filed Jun. 10, 2011 The noted applications are incorporated herein by reference.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 14116392 | Oct 2014 | US |
| Child | 16442942 | US |
