Abstract: The present invention provides a stable agrochemical composition including a dispersed phase comprising an anilide herbicide; a continuous aqueous phase; and at least one anionic surfactant. The present invention also provides a process of preparing stable agrochemical compositions and methods of application thereof.

Abstract: The present invention provides a co-crystal of sulfentrazone and a triazinone herbicide and process for preparation thereof. The present invention also provides an agrochemical composition comprising said co-crystal and process of preparation of an agrochemical composition and method of controlling weeds with said compositions.

Abstract: The present invention provides a stable agrochemical composition including a dispersed phase comprising an anilide herbicide; a continuous aqueous phase; and at least one anionic surfactant. The present invention also provides a process of preparing stable agrochemical compositions and methods of application thereof.

Abstract: The present invention relates to an herbicidal composition particularly stable at lower temperatures. The present invention provides a stable herbicidal composition comprising at least one pesticide in its salt form and a crystal habit modifying system comprising an alkoxylated alcohol and a polymer. Further the invention relates to a stable herbicidal composition comprising at least two pesticides in their salt form and a crystal habit modifying system comprising an alkoxylated alcohol and a polymer.

Abstract: Disclosed are beads comprising endothall, its salts or derivatives entrapped in an alginate complex. The disclosure further relates to a process for preparing herbicidal alginate bead compositions and a method of controlling algae and aquatic weeds using the same. Further, a safe delivery system of herbicides, for aquatic weed control, comprising the bead composition is also provided.

Abstract: Described herein are aqueous homogeneous herbicide compositions including electrolytic herbicides and a multipart amine component, wherein the multipart amine component includes at least one tertiary amine having an alkyl group of at least 8 carbon atoms.

Abstract: The present invention relates to novel agrochemical compositions with enhanced bio-efficacy comprising at least one agrochemical active ingredient and an adjuvant composition.

Abstract: The present invention relates to an herbicidal composition particularly stable at lower temperatures. The present invention provides a stable herbicidal composition comprising at least one pesticide in its salt form and a crystal habit modifying system comprising an alkoxylated alcohol and a polymer. Further the invention relates to a stable herbicidal composition comprising at least two pesticides in their salt form and a crystal habit modifying system comprising an alkoxylated alcohol and a polymer.

Abstract: The present invention relates to novel agrochemical compositions with enhanced bio-efficacy comprising at least one agrochemical active ingredient and an adjuvant composition.

Abstract: The present invention provides a stable aqueous pesticide bifenthrin formulation having reduced toxicity and liquid fertilizer compatibility.

Abstract: The present invention provides a stable aqueous pesticide bifenthrin formulation having reduced toxicity and liquid fertilizer compatibility.

Abstract: Dry flow, low compact, dust free, soluble granules of phosphoroamidothioates, preferably acephate, are produced by the process of 1) pre-mixing technical grade phosphoroamidothioate with specified adjuvants and other inert ingredients; 2) grinding to produce a ground product having a preferred particle size of 5 microns to 10 microns; 3) post-mixing; 4) granulating; 5) drying; 6) sizing to required length, preferably 1.5 to 3.0 mm; 7) and sieving to remove the fines to get the desired dust free soluble granule.

Abstract: Dry flow, low compact, dust free, soluble granules of phosphoroamidothioates, preferably acephate, are produced by the process of 1) pre-mixing technical grade phosphoroamidothioate with specified adjuvants and other inert ingredients; 2) grinding to produce a ground product having a preferred particle size of 5 microns to 10 microns; 3) post-mixing; 4) granulating; 5) drying; 6) sizing to required length, preferably 1.5 to 3.0 mm; 7) and sieving to remove the fines to get the desired dust free soluble granule.

Abstract: Uniformly sized granules are formed using the present extruder and granulation process. The extruder contains a spiral worm screw for guiding a granulation material to an apertured plate. The spiral worm screw is rotated within a chamber and is formed from a guiding slant which terminates at a blunt edge near the apertured plate. The blunt edge rubs the granulation material against the apertured plate which softens the material forming a semi-solid material. The semi-solid material is then gently pushed through the apertured plate using just the required pressure. The granules are formed when the semi-solid material hardens after exiting the apertured plate.

Abstract: Uniformly sized granules are formed using the present extruder and granulation process. The extruder contains a spiral worm screw for guiding a granulation material to an apertured plate. The spiral worm screw is rotated within a chamber and is formed from a guiding slant which terminates at a blunt edge near the apertured plate. The blunt edge rubs the granulation material against the apertured plate which softens the material foming a semi-solid material. The semi-solid material is then gently pushed through the apertured plate using just the required pressure. The granules are formed when the semi-solid material hardens after exiting the apertured plate.

Abstract: Dry flow, low compact, dust free, soluble granules of phosphoroamidothioates, preferably acephate, are produced by the process of 1) pre-mixing technical grade phosphoroamidothioate with specified adjuvants and other inert ingredients; 2) grinding to produce a ground product having a preferred particle size of 5 microns to 10 microns; 3) post-mixing; 4) granulating; 5) drying; 6) sizing to required length, preferably 1.5 to 3.0 mm; 7) and sieving to remove the fines to get the desired dust free soluble granule.