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WO1996003039A1 - Spherical microparticles comprising a nucleation promoter and biologically active compounds - Google Patents

Spherical microparticles comprising a nucleation promoter and biologically active compounds Download PDF

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Publication number
WO1996003039A1
WO1996003039A1 PCT/EP1995/002726 EP9502726W WO9603039A1 WO 1996003039 A1 WO1996003039 A1 WO 1996003039A1 EP 9502726 W EP9502726 W EP 9502726W WO 9603039 A1 WO9603039 A1 WO 9603039A1
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WO
WIPO (PCT)
Prior art keywords
spherical microparticles
wax
microparticles according
biologically active
active compound
Prior art date
Application number
PCT/EP1995/002726
Other languages
French (fr)
Inventor
Rudolf Nastke
Ernst Neuenschwander
Original Assignee
Ciba-Geigy Ag
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ciba-Geigy Ag filed Critical Ciba-Geigy Ag
Priority to EP95926861A priority Critical patent/EP0772393A1/en
Priority to JP8505404A priority patent/JPH11505464A/en
Priority to AU31098/95A priority patent/AU3109895A/en
Publication of WO1996003039A1 publication Critical patent/WO1996003039A1/en

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Classifications

    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01N—PRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00—Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/26—Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests in coated particulate form
    • A01N25/28—Microcapsules or nanocapsules

Definitions

  • Spherical microparticles comprising a nucleation promoter and biologically active compounds
  • the present invention relates to spherical microparticles comprising biologically active compounds and a nucleation promoter within the microparticles.
  • the invention also relates to a process for their preparation, to the use thereof for the preparation of a composition for controlling plant pests, weeds or animal parasites, and to aqueous spray mixtures containing the novel microparticles.
  • microencapsulation of active ingredients in polymeric materials with different polymers is known and can be carried out by various methods, as described for example in Encyclopedia of Polymer Science, John Wiley Sons, 1968, Vol. 8, pp. 719-736.
  • microencapsulation methods are: coacervation, interfacial polymerisation at liquid-liquid surfaces or interfacial polycondensation, for example at a solid phase boundary.
  • other suitable methods are physical methods such as the microencapsulation of aerosols.
  • Amino resins are often used as polymeric encapsulating materials for microparticles that contain agrochemical compounds. An overview of the broad field of use of these resins for microencapsulation is given, inter alia, in Acta Polymerica 40, (1989) No. 4, pp. 243-251.
  • the applied microparticles must be comparably active in field application to e.g. emulsifiable concentrates.
  • they shall release the active ingredient uniformly over an extended period of time.
  • virtually no active ingredient shall be released on skin contact, so that a high degree of handling safety is ensured.
  • the preparation and properties of microparticles prepared with self-crosslinking amino resins are described in Acta Polymerica 40, (1989) No. 5, pp. 325-331.
  • the starting materials are solid compounds which are e.g. additionally ground to give a fine dispersion in the aqueous polymer solution and are then encapsulated.
  • the drawback of this process is that the solid materials have to be ground to an average particle size of c. 10-30 ⁇ m.
  • usually large amounts of fine dust that have to be reagglomerated are formed.
  • the addition of active ingredients in the liquid, dissolved or melt state is therefore usually of interest.
  • This recrystallisation can have such a pronounced effect on the stability to hydrolysis, on the dispersing properties during the preparation of spray mixtures, on the flow properties of the microcapsules and on the release properties of the active ingredient that the microcapsules are unfit for use.
  • the microcapsules comprise, in addition to the active ingredient, a nucleation promoter that effects a rapid recrystallisation of the fused active ingredient in the microcapsule and ensures that only small microcrystallites form that remain almost wholly encapsulated by the capsule wall. Premature release of the active ingredient is thereby prevented, the handling safety is ensured, and the release properties remain effective enough to achieve sufficiently good activity. Long-term stability is good, as the recystallisation no longer occurs during storage.
  • the active ingredient is released approximately uniformly over an extended period of time from the microparticles, so that a good activity is achieved.
  • the invention relates to essentially spherical microparticles comprising a biologically active compound which is solid and crystalline at room temperatue as core substance and a polymeric capsule material, which microparticles additionally comprise a nucleation accelerator.
  • nucleation promoters are mainly linear polymers. Regardless of the active ingredient, the nucleation promoter may suitably be a polyester, a polyacrylate, a polyamide, a polyolefin, a polyvinyl alcohol, a polyvinyl pyrrolidone or a polyether. Those skilled in the an will easily find suitable combinations by simple experimentation by mixing and fusing the components as well as subsequent determination of the crystal size, conveniently by microscopy.
  • a preferred nucleation promoter is a polyethylene glycol or a polyethylene glycol which is etherified with C ⁇ -C 8 alkyl radicals at the OH end groups, a polyvinyl pyrrolidone or a polyvinyl alcohol.
  • the average molecular weight of the polyethylene glycols is preferably 10000 to 40000, most preferably 20000 to 35 000.
  • the degree of hydrolysis is preferably greater than 75 %, most preferably 95 to 100 %.
  • the average molecular weight of the polyvinyl alcohol is preferably 120000 to 200000.
  • the average molecular weight is preferably higher than 10000.
  • the polymeric nucleation promoters can be used in an amount of 0.5 to 30 % by weight, preferably of 1 to 5 % by weight, based on the weight of the active ingredient.
  • the spherical microparticles preferably have an average diameter ofl ⁇ .5 to 500 ⁇ m. More preferably the microparticles have an average diameter of 0.5 to 100 ⁇ m and, most preferably, of 0.5 to 20 ⁇ m.
  • the polymeric wall material is preferably 5 to 40 % by weight of the total weight of the microparticles.
  • the polymeric wall material may consist of a polyacrylate, a polyurea, a polyurethane, a polyester or an amino resin.
  • the polymeric wall material is preferably an amino condensation resin, most preferably a polycondensate of melamine and formaldehyde, a wholly or partially etherified melamine-formaldehyde condensate, a urea-formaldehyde condensate, a urea-glutaralde- hyde condensate or a benzoguanamine-formaldehyde condensate.
  • an amino condensation resin most preferably a polycondensate of melamine and formaldehyde, a wholly or partially etherified melamine-formaldehyde condensate, a urea-formaldehyde condensate, a urea-glutaralde- hyde condensate or a benzoguanamine-formaldehyde condensate.
  • the molar ratios of urea to formaldehyde are 1:2.5 to 1:3.5, preferably 1:2.7 to 1: 3.2. If glutaraldehyde is used instead of formaldehyde, the molar ratios may be 1:1.5 to 1:2.5, preferably 1:1.8 to 1: 2.2.
  • the molar ratios of melamine to formaldehyde can be 1:3.5 to 1:8, preferably 1:4 to 1:6.
  • the degree of etherification of these resins can be adjusted by the molar ratio of melamine to methanol and is typically c. 1:10 to 1:20, preferably c. 1:15 to 1:18.
  • Suitable amino resins for forming microparticles will be found, inter alia, in Kirk-Othmer, Encyclopedia of Chemical Technology, 3rd edition, Vol. 2, pp. 440-469.
  • the polycondensate is most preferably a melamine-formaldehyde condensate, a wholly or partially etherified melamine-formaldehyde condensate, or a urea-formaldehyde condensate.
  • the biologically active compound is preferably a pesticide or a mixture of pesticides, and is most preferably a herbicide, an insecticide, an acaricide, a nematicide, an ectoparasiti- cide, a fungicide or a mixture thereof.
  • Typical examples of pesticides are: urea derivatives, triazines, triazoles, carbamates, phosphoric acid esters, dinitroanilines, morpholines, acylalanines, pyrethroids, benzilic acid esters and polycyclic halogenated hydrocarbons.
  • pesticides suitable for use in the practice of this invention are listed hereinbelow (common names as given in The Pesticide Manual, 9th Edition, British Crop Protection Council):
  • Halogenated acetanilides Dimethachlor, alachlor, propachlor.
  • Atrazine propazine, terbuthylazine, amerryn, aziprotryne, cyromazine.
  • Triazole derivatives
  • Etaconazole 1 -[2-(2,4-dichlorophenyl)-pent- 1 -yl]- 1H- 1 ,2,4-triazole, triadimefon, difenoconazole.
  • the microparticles may additionally contain a hydrophobic wax.
  • the hydrophobic wax may be a natural wax, a modified natural wax, or a semi-synthetic or fully synthetic wax.
  • wax which is fused together with the active ingredient to form a melt which is added to the aqueous solution, has for its object to form a wax film that surrounds the active ingredient on the inner microcapsule wall. Penetration of water into the capsule core is thereby hindered, while the release properties remain effective enough to achieve sufficiently good activity.
  • the wax is preferably a vegetable wax, an animal wax, a montan wax, a paraffin wax, a polyolefin wax or an amide wax.
  • the hydrophobic wax is a macrocrystalline paraffin wax, a microcrystalline paraffin wax or a polyethylene wax.
  • the wax preferably has a melting point of 30 to 80°C.
  • the wax is used in an amount of 1 to 20 % by weight, most preferably of 5 to 15 % by weight, based on the biologically active compound or mixture thereof in the microcapsules.
  • the invention in another of its aspects, relates to a process for encapsulating biologically active compounds in the form of essentially spherical microcapsules, comprising the steps of a) preparing an aqueous solution of surfactants, catalysts and monomers, prepolymers or polymers which are suitable for forming a capsule wall, b) forming an emulsion or dispersion of the substantially water-insoluble biologically active compound or mixture thereof in the solution a) by adding said biologically active compound or mixture thereof under high shear force, and c) forming a solid capsule wall around the biologically active compound or mixture thereof, which process comprises blending the biologically active compound or mixture thereof with a nucleation promoter before forming the emulsion or dispersion b), fusing the blend and adding the melt so obained to the solution a).
  • a preferred embodiment of the process comprises fusing the the biologically active compound or mixture thereof and the nucleation promoter together and adding the co-melt to tie reaction solution a) at a temperature which is higher than that of said reaction solution a).
  • Another preferred embodiment of the process comprises dissolving the nucleation promoter in a solvent, adding the solid active ingredient and cautiously evaporating the solvent, with stirring, to give an active ingredient powder which is coated with the nucleation promoter and which can likewise be fused and added direct to the reaction solution. If a wax is used in addition to the nucleation promoter, then the active ingredient, the nucleation promoter and the wax are preferably blended, the blend is fused, and the melt so obtained is added to the reaction mixture a).
  • the aqueous solution may contain, in addition to the monomers, prepolymers or polymers that form the capsule wall, one or more than one water-soluble monomer, oligomer or polymer as emulsifier or dispersant.
  • Suitable emulsifiers or dispersants are anionic, cationic or nonionic substances.
  • the surfactants customarily used in formulation technology are described, inter alia, in the following publications:
  • the surfactants are polyethylene glycols, polyethylene glycol monoalkyl ethers, polyethylene glycol-polypropylene glycol copolymers, polyvinyl pyrrolidones and acrylic acid-acrylamide copolymers.
  • the polymers used as surfactants usually have a lower molecular weight than that of the polymers used as nucleation promoters. This applies in particular to the polyethylene glycols and polyethylene glycol ethers.
  • the invention in another of its aspects, relates to a process for controlling plant pests, weeds or animal parasites, which comprises suspending the novel microparticles in a biologically active concentration in water and applying the suspension so obtained to the pests or to the locus thereof.
  • the invention relates to the use of the novel microparticles for the preparation of a composition for controlling plant pests, weeds or animal parasites, and to water-dilutable powders, water-dispersible granules or aqueous spray mixtures containing said micropanicles.
  • Example Al Preparation of a modified melamine-formaldehyde precondensate With stirring, 28 g of melamine (0.22 mol) are added to 124 ml of a 30 % aqueous solution of formaldehyde. The reaction mixture is adjusted with 1 N aqueous NaOH to pH 9 and heated to 94°C, whereupon the melamine dissolves while reacting with the aldehyde. The reaction mixture is then cooled to 62°C and, after addition of 120 ml of methanol (3.75 mol) and 7 ml of a 15 % aqueous solution of hydrochloric acid, the reaction is carried out at 62°C for 30 minutes.
  • Example B 1 60 ml of water and 3 g of the precondensate prepared according to Example Al as well as 0.15 g of polyethylene glycol (molecular weight 300) are charged to a reactor with temperature control.
  • the reaction mixture is heated to 60°C and acidified with 2.1 ml of 2N aqueous citric acid.
  • 12.6 g of methidathion and 0.945 g (7.5 %, based on the active ingredient) of polyethylene glycol (mol wt 20000) are fused together, homogenised and heated to 60°C.
  • the melt is added rapidly to the reaction mixture, with stirring (Ultratunax, 12000 rpm), and stirred for 10 minutes at this speed.
  • Example B2 The procedure of Example B 1 is repeated, but using 0.252 g of polyethylene glycol (mol wt 20000), corresponding to 2 %, based on the active ingedient. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 ⁇ m. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • polyethylene glycol mol wt 20000
  • Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
  • Example B3 The procedure of Example Bl is repeated, but using 0.63 g of polyethylene glycol (mol wt >30000, degree of hydrolysis 95 %), corresponding to 5 %, based on the active ingedient.
  • the mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 ⁇ m.
  • the suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
  • Example B4 The procedure of Example B 1 is repeated, but using 0.63 g of polyethylene glycol (mol wt >10000), corresponding to 5 %, based on the active ingedient. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 ⁇ m. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • polyethylene glycol mol wt >10000
  • the suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
  • Example B5 The procedure of Example B 1 is repeated, but using in addition to 0.252 g of polyethylene glycol (mol wt 20000), corresponding to 2 %, based on the active ingedient, 1.26 g of paraffin wax having a melting point of >40°C. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 ⁇ m. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • polyethylene glycol mol wt 20000
  • paraffin wax having a melting point of >40°C.
  • the suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
  • Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.

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  • Life Sciences & Earth Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Pest Control & Pesticides (AREA)
  • Plant Pathology (AREA)
  • Agronomy & Crop Science (AREA)
  • Engineering & Computer Science (AREA)
  • Dentistry (AREA)
  • Wood Science & Technology (AREA)
  • Zoology (AREA)
  • Environmental Sciences (AREA)
  • Agricultural Chemicals And Associated Chemicals (AREA)
  • Manufacturing Of Micro-Capsules (AREA)

Abstract

The present invention relates to spherical microparticles comprising biologically active compounds and a nucleation promoter within the microparticles. The invention also relates to a process for their preparation, to the use thereof for the preparation of a composition for controlling plant pests, weeds or animals parasites, and to aqueous spray mixtures containing the novel microparticles.

Description

Spherical microparticles comprising a nucleation promoter and biologically active compounds
The present invention relates to spherical microparticles comprising biologically active compounds and a nucleation promoter within the microparticles. The invention also relates to a process for their preparation, to the use thereof for the preparation of a composition for controlling plant pests, weeds or animal parasites, and to aqueous spray mixtures containing the novel microparticles.
The microencapsulation of active ingredients in polymeric materials with different polymers is known and can be carried out by various methods, as described for example in Encyclopedia of Polymer Science, John Wiley Sons, 1968, Vol. 8, pp. 719-736.
Some typical microencapsulation methods are: coacervation, interfacial polymerisation at liquid-liquid surfaces or interfacial polycondensation, for example at a solid phase boundary. In addition to these chemical methods, other suitable methods are physical methods such as the microencapsulation of aerosols. Amino resins are often used as polymeric encapsulating materials for microparticles that contain agrochemical compounds. An overview of the broad field of use of these resins for microencapsulation is given, inter alia, in Acta Polymerica 40, (1989) No. 4, pp. 243-251.
Particular demands are made of the release properties of biologically active agrochemicals. On the one hand, the applied microparticles must be comparably active in field application to e.g. emulsifiable concentrates. In addition, they shall release the active ingredient uniformly over an extended period of time. On the other hand, virtually no active ingredient shall be released on skin contact, so that a high degree of handling safety is ensured.
The preparation and properties of microparticles prepared with self-crosslinking amino resins are described in Acta Polymerica 40, (1989) No. 5, pp. 325-331. In the processes referred to therein, the starting materials are solid compounds which are e.g. additionally ground to give a fine dispersion in the aqueous polymer solution and are then encapsulated. The drawback of this process is that the solid materials have to be ground to an average particle size of c. 10-30 μm. In addition, usually large amounts of fine dust that have to be reagglomerated are formed. The addition of active ingredients in the liquid, dissolved or melt state is therefore usually of interest. One problem that arises in the preparation of microcapsules from the melt or in solution is the recrystallisation of the active ingredients in the microcapsule. The active ingredient is first frozen in its liquid state, resulting in an amorphous core having different physical properties than in the crystalline state. During recrystallisation, long crystal needles or large irregularly shaped crystals may form. Some of these crystals pierce the capsule wall and thereby nullify the advantages of the microencapsulation, at least partially. This recrystallisation may also not occur until during storage.
This recrystallisation can have such a pronounced effect on the stability to hydrolysis, on the dispersing properties during the preparation of spray mixtures, on the flow properties of the microcapsules and on the release properties of the active ingredient that the microcapsules are unfit for use.
It has now been found that these drawbacks can be eliminated if the microcapsules comprise, in addition to the active ingredient, a nucleation promoter that effects a rapid recrystallisation of the fused active ingredient in the microcapsule and ensures that only small microcrystallites form that remain almost wholly encapsulated by the capsule wall. Premature release of the active ingredient is thereby prevented, the handling safety is ensured, and the release properties remain effective enough to achieve sufficiently good activity. Long-term stability is good, as the recystallisation no longer occurs during storage.
The active ingredient is released approximately uniformly over an extended period of time from the microparticles, so that a good activity is achieved.
In one of its aspects therefore the invention relates to essentially spherical microparticles comprising a biologically active compound which is solid and crystalline at room temperatue as core substance and a polymeric capsule material, which microparticles additionally comprise a nucleation accelerator.
Suitable nucleation promoters are mainly linear polymers. Regardless of the active ingredient, the nucleation promoter may suitably be a polyester, a polyacrylate, a polyamide, a polyolefin, a polyvinyl alcohol, a polyvinyl pyrrolidone or a polyether. Those skilled in the an will easily find suitable combinations by simple experimentation by mixing and fusing the components as well as subsequent determination of the crystal size, conveniently by microscopy.
A preferred nucleation promoter is a polyethylene glycol or a polyethylene glycol which is etherified with Cι-C8alkyl radicals at the OH end groups, a polyvinyl pyrrolidone or a polyvinyl alcohol.
The average molecular weight of the polyethylene glycols is preferably 10000 to 40000, most preferably 20000 to 35 000.
If a polyvinyl alcohol is used, the degree of hydrolysis is preferably greater than 75 %, most preferably 95 to 100 %.
The average molecular weight of the polyvinyl alcohol is preferably 120000 to 200000.
If a polyvinyl pyrrolidone is used, the average molecular weight is preferably higher than 10000.
The polymeric nucleation promoters can be used in an amount of 0.5 to 30 % by weight, preferably of 1 to 5 % by weight, based on the weight of the active ingredient.
The spherical microparticles preferably have an average diameter oflθ.5 to 500 μm. More preferably the microparticles have an average diameter of 0.5 to 100 μm and, most preferably, of 0.5 to 20 μm.
The polymeric wall material is preferably 5 to 40 % by weight of the total weight of the microparticles.
The polymeric wall material may consist of a polyacrylate, a polyurea, a polyurethane, a polyester or an amino resin.
The polymeric wall material is preferably an amino condensation resin, most preferably a polycondensate of melamine and formaldehyde, a wholly or partially etherified melamine-formaldehyde condensate, a urea-formaldehyde condensate, a urea-glutaralde- hyde condensate or a benzoguanamine-formaldehyde condensate.
The molar ratios of urea to formaldehyde are 1:2.5 to 1:3.5, preferably 1:2.7 to 1: 3.2. If glutaraldehyde is used instead of formaldehyde, the molar ratios may be 1:1.5 to 1:2.5, preferably 1:1.8 to 1: 2.2.
The molar ratios of melamine to formaldehyde can be 1:3.5 to 1:8, preferably 1:4 to 1:6. The degree of etherification of these resins can be adjusted by the molar ratio of melamine to methanol and is typically c. 1:10 to 1:20, preferably c. 1:15 to 1:18.
Suitable amino resins for forming microparticles will be found, inter alia, in Kirk-Othmer, Encyclopedia of Chemical Technology, 3rd edition, Vol. 2, pp. 440-469.
The polycondensate is most preferably a melamine-formaldehyde condensate, a wholly or partially etherified melamine-formaldehyde condensate, or a urea-formaldehyde condensate.
The biologically active compound is preferably a pesticide or a mixture of pesticides, and is most preferably a herbicide, an insecticide, an acaricide, a nematicide, an ectoparasiti- cide, a fungicide or a mixture thereof.
Typical examples of pesticides are: urea derivatives, triazines, triazoles, carbamates, phosphoric acid esters, dinitroanilines, morpholines, acylalanines, pyrethroids, benzilic acid esters and polycyclic halogenated hydrocarbons.
Specific examples of pesticides suitable for use in the practice of this invention are listed hereinbelow (common names as given in The Pesticide Manual, 9th Edition, British Crop Protection Council):
Urea derivatives
Chlorbromuron, chloroxuron, chlorotoluron, fluometuron, thiazafluron and triasulfuron.
Halogenated acetanilides Dimethachlor, alachlor, propachlor.
s-Triazines
Atrazine, propazine, terbuthylazine, amerryn, aziprotryne, cyromazine. Triazole derivatives
Etaconazole, 1 -[2-(2,4-dichlorophenyl)-pent- 1 -yl]- 1H- 1 ,2,4-triazole, triadimefon, difenoconazole.
Carbamates
Dioxacarb, aldicarb, benomyl.
Phosphoric acid esters
Methidathion, anilofos, azinphos methyl, fenamiphos, azamethiphos.
Dinitroanilines
Benfluralin, pendimethalin, butralin, fluchloralin.
Acylalanines
Metalaxyl, fluralaxyl, benzoylprop ethyl, flamprop methyl.
Pyrethroids
Cypermethrin, resmethrin, tetramethrin.
Benzilic acid esters
Bromopropylates, chlorobenzilates, chloropropylates.
Miscellaneous
Bromoxynil, ioxynil, oxadiazon, dicofol, fenoxycarb.
Preferred pesticides are S-2,3-dihydro-5-methoxy-2-oxo- 1,3,4 thiadiazol-3-ylmethyl O,0-dimethyl phosphorodithioate (= methidathion), 2-phenylamino-4-methyl-6-cyclopro- pylpyrimidine and 3-(3-chloro-p-tolyl)-l,l-dimethylurea = chlorotoluron.
The microparticles may additionally contain a hydrophobic wax. The hydrophobic wax may be a natural wax, a modified natural wax, or a semi-synthetic or fully synthetic wax.
The addition of wax, which is fused together with the active ingredient to form a melt which is added to the aqueous solution, has for its object to form a wax film that surrounds the active ingredient on the inner microcapsule wall. Penetration of water into the capsule core is thereby hindered, while the release properties remain effective enough to achieve sufficiently good activity.
The wax is preferably a vegetable wax, an animal wax, a montan wax, a paraffin wax, a polyolefin wax or an amide wax. Most preferably the hydrophobic wax is a macrocrystalline paraffin wax, a microcrystalline paraffin wax or a polyethylene wax.
The wax preferably has a melting point of 30 to 80°C.
In a preferred embodiment of the invention, the wax is used in an amount of 1 to 20 % by weight, most preferably of 5 to 15 % by weight, based on the biologically active compound or mixture thereof in the microcapsules.
In another of its aspects, the invention relates to a process for encapsulating biologically active compounds in the form of essentially spherical microcapsules, comprising the steps of a) preparing an aqueous solution of surfactants, catalysts and monomers, prepolymers or polymers which are suitable for forming a capsule wall, b) forming an emulsion or dispersion of the substantially water-insoluble biologically active compound or mixture thereof in the solution a) by adding said biologically active compound or mixture thereof under high shear force, and c) forming a solid capsule wall around the biologically active compound or mixture thereof, which process comprises blending the biologically active compound or mixture thereof with a nucleation promoter before forming the emulsion or dispersion b), fusing the blend and adding the melt so obained to the solution a).
A preferred embodiment of the process comprises fusing the the biologically active compound or mixture thereof and the nucleation promoter together and adding the co-melt to tie reaction solution a) at a temperature which is higher than that of said reaction solution a).
Another preferred embodiment of the process comprises dissolving the nucleation promoter in a solvent, adding the solid active ingredient and cautiously evaporating the solvent, with stirring, to give an active ingredient powder which is coated with the nucleation promoter and which can likewise be fused and added direct to the reaction solution. If a wax is used in addition to the nucleation promoter, then the active ingredient, the nucleation promoter and the wax are preferably blended, the blend is fused, and the melt so obtained is added to the reaction mixture a).
The aqueous solution may contain, in addition to the monomers, prepolymers or polymers that form the capsule wall, one or more than one water-soluble monomer, oligomer or polymer as emulsifier or dispersant. Suitable emulsifiers or dispersants are anionic, cationic or nonionic substances. The surfactants customarily used in formulation technology are described, inter alia, in the following publications:
"Mc Cutcheon's Detergents and Emulsifiers Annual", Mc Publishing Corp., Glen Rock, NJ, USA, 1988",
H. Stache, "Tensid-Taschenbuch" (Handbook ofSurfactants), 2nd edition, C. Hanser Verlag Munich, Vienna 1981,
M. and J. Ash. "Encyclopedia of Surfactants", Vol. I-ID, Chemical Publishing Co., New York, 1980-1981.
The surfactants are polyethylene glycols, polyethylene glycol monoalkyl ethers, polyethylene glycol-polypropylene glycol copolymers, polyvinyl pyrrolidones and acrylic acid-acrylamide copolymers.
The polymers used as surfactants usually have a lower molecular weight than that of the polymers used as nucleation promoters. This applies in particular to the polyethylene glycols and polyethylene glycol ethers.
Methods of producing high shear forces are known per se. It is preferred to use a high-speed impeller or a rotary homogeniser.
In another of its aspects, the invention relates to a process for controlling plant pests, weeds or animal parasites, which comprises suspending the novel microparticles in a biologically active concentration in water and applying the suspension so obtained to the pests or to the locus thereof. In yet another of its aspects, the invention relates to the use of the novel microparticles for the preparation of a composition for controlling plant pests, weeds or animal parasites, and to water-dilutable powders, water-dispersible granules or aqueous spray mixtures containing said micropanicles.
The invention is illustrated by the following Examples.
Examples for the preparation of the precondensates.
Example Al: Preparation of a modified melamine-formaldehyde precondensate With stirring, 28 g of melamine (0.22 mol) are added to 124 ml of a 30 % aqueous solution of formaldehyde. The reaction mixture is adjusted with 1 N aqueous NaOH to pH 9 and heated to 94°C, whereupon the melamine dissolves while reacting with the aldehyde. The reaction mixture is then cooled to 62°C and, after addition of 120 ml of methanol (3.75 mol) and 7 ml of a 15 % aqueous solution of hydrochloric acid, the reaction is carried out at 62°C for 30 minutes. Then 2.8 g of triethanolamine are added and the azeotropic mixture of methanol-water is distilled from the reaction mixture. After adjustment to a solids content of c. 40 to 60 % by weight, 6 g of urea are added to the solution, which is then cooled to room temperature.
Example for the preparation of the microparticles.
Example B 1 : 60 ml of water and 3 g of the precondensate prepared according to Example Al as well as 0.15 g of polyethylene glycol (molecular weight 300) are charged to a reactor with temperature control. The reaction mixture is heated to 60°C and acidified with 2.1 ml of 2N aqueous citric acid. Then 12.6 g of methidathion and 0.945 g (7.5 %, based on the active ingredient) of polyethylene glycol (mol wt 20000) are fused together, homogenised and heated to 60°C. The melt is added rapidly to the reaction mixture, with stirring (Ultratunax, 12000 rpm), and stirred for 10 minutes at this speed. Stirring is afterwards continued with a paddle agitator at 500 rpm for 120 minutes at 6O°C. The mixture is then cooled to give a suspension of fine particles having average diameters of 1 to 10 μm. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core. Example B2: The procedure of Example B 1 is repeated, but using 0.252 g of polyethylene glycol (mol wt 20000), corresponding to 2 %, based on the active ingedient. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 μm. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
Example B3: The procedure of Example Bl is repeated, but using 0.63 g of polyethylene glycol (mol wt >30000, degree of hydrolysis 95 %), corresponding to 5 %, based on the active ingedient. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 μm. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder. Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
Example B4: The procedure of Example B 1 is repeated, but using 0.63 g of polyethylene glycol (mol wt >10000), corresponding to 5 %, based on the active ingedient. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 μm. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.
Example B5: The procedure of Example B 1 is repeated, but using in addition to 0.252 g of polyethylene glycol (mol wt 20000), corresponding to 2 %, based on the active ingedient, 1.26 g of paraffin wax having a melting point of >40°C. The mixture is cooled to give a suspension of finely paniculate spherical particles having a diameter of 1 to 10 μm. The suspension can be further used direct for a formulation or the particles can be dried to give a free-flowing powder.
Thermoanalytical measurements show that the active ingredient is mainly present in microcrystalline form in the capsule core.

Claims

What is claimed is:
1. Spherical microparticles comprising a biologically active compound which is solid and crystalline at room temperatue as core substance and a polymeric capsule material, wherein the microparticles additionally comprise a nucleation accelerator.
2. Spherical microparticles according to claim 1, wherein mainly a linear polymer is used as biologically active compound.
3. Spherical microparticles according to claim 1, wherein the nucleation promoter is a polyester, a polyacrylate, a polyamide, a polyolefin, a polyvinyl alcohol, a polyvinyl pyrrolidone or a polyether.
4. Spherical microparticles according to claim 1, wherein the nucleation promoter is a polyethylene glycol or a polyethylene glycol which is etherified with Ci-Cgalkyl radicals at the OH end groups, a polyvinyl pyrrolidone or a polyvinyl alcohol.
5. Spherical microparticles according to claim 4, wherein the average molecular weight of the polyethylene glycol is 10000 to 40 000.
6. Spherical microparticles according to claim 4, wherein the average molecular weight of the polyethylene glycol is 20000 to 35 000.
7. Spherical microparticles according to claim 4, wherein the average molecular weight of the polyvinyl alcohol is 120000 to 200000.
8. Spherical microparticles according to claim 4, wherein the average molecular weight of the polyvinyl pyrrolidone is higher than 10000.
9. Spherical microparticles according to claim 1, wherein the polymeric nucleation promoter is used in an amount of 0.5 to 30 % by weight, based on the weight of the active ingredient.
10. Spherical microparticles according to claim 1, wherein the polymeric nucleation promoter is used in an amount of 1 to 5 % by weight, based on the weight of the active ingredient.
11. Spherical microparticles according to claim 1, which have an average diameter of 0.5 to 500 μm.
12. Spherical microparticles according to claim 1, which have an average diameter of 0.5 to 100 μm.
13. Spherical microparticles according to claim 1, which have an average diameter of 0.5 to 20 μm.
14. Spherical microparticles according to claim 1, wherein the polymeric wall material is 5 to 40 % of the total weight of the microparticles.
15. Spherical microparticles according to claim 1, wherein the polymeric wall material is a polyacrylate, a polyurea, a polyurethane, a polyester or an amino resin.
16. Spherical microparticles according to claim 1, wherein the polymeric wall material is an amino condensation resin.
17. Spherical microparticles according to claim 15, wherein the polycondensate is a melamine-formaldehyde condensate, a wholly or partially etherified melamine-formaldehyde condensate, a urea-formaldehyde condensate, a urea-glutaralde- hyde condensate, a benzoguanamine-formaldehyde condensate, or a urea-glyoxal condensate.
18. Spherical microparticles according to claim 16, wherein the polycondensate is a melamine-formaldehyde condensate, a wholly or partially etherified melamine-formaldehyde condensate or a urea-formaldehyde condensate.
19. Spherical microparticles according to claim 1, wherein the biologically active compound is a pesticide or a mixture of pesticides.
20. Spherical microparticles according to claim 19, wherein the biologically active compound is a herbicide, an insecticide, an acaricide, a nematicide, an ectoparasiticide, a fungicide or a mixture thereof.
21. Spherical microparticles according to claim 20, wherein the biologically active compound is selected from S-2,3-dihydro-5-methoxy-2-oxo- 1,3,4 thiadiazol-3-ylmethyl O,O-dimethyl phosphorodithioate (= methidathion), 2-phenylamino-4-methyl-6-cyclopro- pylpyrimidine and 3-(3-chloro-p-tolyl)-l,l-dimethylurea (=chlortoluron).
22. Spherical microparticles according to claim 1, which additionally comprise a natural wax, a modified natural wax, a partially synthetic or a fully synthetic wax.
23. Spherical microparticles according to claim 22, wherein the wax is a vegetable wax, an animal wax, a montan wax, a paraffin wax, a polyolefin wax or an amide wax.
24. Spherical microparticles according to claim 22, wherein the wax is a macrocrystalline paraffin wax, a microcrystalline paraffin wax or a polyethylene wax.
25. Spherical microparticles according to claim 22, wherein the wax has a melting point in the range from 30 to 80°C.
26. Spherical microparticles according to claim 22, wherein the wax is present in the capsule in an amount of 1 to 20 % by weight, based on the biologically active compound or mixture thereof.
27. Spherical microparticles according to claim 22, wherein the wax is present in the capsule in an amount of 5 to 15 % by weight, based on the biologically active compound or mixture thereof.
28. A process for encapsulating a biologically active compound in the form of essentially spherical microcapsules, comprising the steps of a) preparing an aqueous solution of surfactants, catalysts and monomers, prepolymers or polymers which are suitable for forming a capsule wall, b) forming an emulsion or dispersion of the substantially water-insoluble biologically active compound or mixture thereof in the solution a) by adding said biologically active compound or mixture thereof under high shear force, and c) forming a solid capsule wall around the biologically active compound or mixture thereof, which process comprises blending the biologically active compound or mixture thereof - 13 -
with a nucleation promoter before forming the emulsion or dispersion b), fusing the blend, and adding the melt so obained to the solution a).
29. A process according to claim 28, which comprises fusing the biologically active compound or mixture thereof and the nucleation promoter together and adding the co-melt blend to the reaction solution a) at a temperature which is higher than that of said reaction solution a).
30. A process according to claim 28, which comprises blending the active ingredient, the nucleation promoter and the wax, fusing the blend, and adding the melt so obtained to the reaction mixture a).
31. A method of controlling plant pests, weeds or animal parasites, which comprises suspending microparticles as claimed in claim 1 in a biologically active concentration in water and applying the suspension so obtained to the pests or to the locus thereof.
32. The use of microparticles as claimed in claim 1 for the preparation of a composition for controlling plant pests, weeds or animal parasites.
33. A water-dilutable powder, a water-dispersible granular formulation or an aqueous spray mixture containing microparticles as claimed in claim 1.
PCT/EP1995/002726 1994-07-22 1995-07-12 Spherical microparticles comprising a nucleation promoter and biologically active compounds WO1996003039A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP95926861A EP0772393A1 (en) 1994-07-22 1995-07-12 Spherical microparticles comprising a nucleation promoter and biologically active compounds
JP8505404A JPH11505464A (en) 1994-07-22 1995-07-12 Spherical microparticles composed of a nucleation promoter and a biologically active compound
AU31098/95A AU3109895A (en) 1994-07-22 1995-07-12 Spherical microparticles comprising a nucleation promoter and biologically active compounds

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CH233194 1994-07-22
CH2331/94-2 1994-07-22

Publications (1)

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WO1996003039A1 true WO1996003039A1 (en) 1996-02-08

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JP (1) JPH11505464A (en)
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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7691296B2 (en) 2002-11-25 2010-04-06 Amorepacific Corporation Method for stabilizing active components using polyol/polymer microcapsule, and cosmetic composition containing the microcapsule
US9138417B2 (en) 2011-03-11 2015-09-22 Osaka Gas Chemicals Co., Ltd. Controlled release particles and production method thereof

Citations (3)

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Publication number Priority date Publication date Assignee Title
FR2332053A1 (en) * 1975-11-19 1977-06-17 Bayer Ag PROCESS FOR THE PRODUCTION OF CONCENTRATED SUSPENSIONS OF PESTICIDES
JPS6413002A (en) * 1987-07-06 1989-01-17 Sumitomo Chemical Co Organic phosphorus insecticide composition for controlling insect pest in forest
EP0380325A2 (en) * 1989-01-24 1990-08-01 Griffin Corporation Microencapsulated agriculturally active material

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
FR2332053A1 (en) * 1975-11-19 1977-06-17 Bayer Ag PROCESS FOR THE PRODUCTION OF CONCENTRATED SUSPENSIONS OF PESTICIDES
JPS6413002A (en) * 1987-07-06 1989-01-17 Sumitomo Chemical Co Organic phosphorus insecticide composition for controlling insect pest in forest
EP0380325A2 (en) * 1989-01-24 1990-08-01 Griffin Corporation Microencapsulated agriculturally active material

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DATABASE WPI Section Ch Week 8908, Derwent World Patents Index; Class A97, AN 89-059198 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7691296B2 (en) 2002-11-25 2010-04-06 Amorepacific Corporation Method for stabilizing active components using polyol/polymer microcapsule, and cosmetic composition containing the microcapsule
US9138417B2 (en) 2011-03-11 2015-09-22 Osaka Gas Chemicals Co., Ltd. Controlled release particles and production method thereof

Also Published As

Publication number Publication date
AU3109895A (en) 1996-02-22
JPH11505464A (en) 1999-05-21
EP0772393A1 (en) 1997-05-14

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