Abstract: A spray gun (1) forms a desired spray pattern by atomizing by means of atomizing air (A) a spray liquid which is sprayed from a liquid ejection port (44) opened/closed by a needle valve (4), and jetting pattern air (P) to the flow of spray mist of the atomized spray liquid. A nozzle taper angle (?1) is set in a range of 5° to 15°, and a cap taper angle (?2) is set in a range of 20° to 40°. Atomizing air (A) is jetted from a nozzle insertion hole (58) toward the center of a nozzle (3). Pattern air (P) is jetted in a spreading suppressed region (R) wherein the flow of the spray mist does not spread over an area greater than or equal to a predetermined cross-sectional area, to the flow of spray mist, and as a result, the spray mist is more uniformly sprayed over a wide range.

Abstract: A spray gun (1) forms a desired spray pattern by atomizing by means of atomizing air (A) a spray liquid which is sprayed from a liquid ejection port (44) opened/closed by a needle valve (4), and jetting pattern air (P) to the flow of spray mist of the atomized spray liquid. A nozzle taper angle (?1) is set in a range of 5° to 15°, and a cap taper angle (?2) is set in a range of 20° to 40°. Atomizing air (A) is jetted from a nozzle insertion hole (58) toward the center of a nozzle (3). Pattern air (P) is jetted in a spreading suppressed region (R) wherein the flow of the spray mist does not spread over an area greater than or equal to a predetermined cross-sectional area, to the flow of spray mist, and as a result, the spray mist is more uniformly sprayed over a wide range.

Abstract: Processing vessel (1) is formed by overlaying a filter casing (2), a spray casing (3), a material container (4) and an air supply unit (5). Airtightnesses between respective units are maintained by airtight junctions (61 to 63). In the airtight junction (61), two seal portions (91 and 92) are radially provided, and U-seals (64 and 65) are contained. The U-seals (64 and 65) vertically move within seal grooves (67 and 68) through supply and exhaust of air to/from cylinder chambers (69 and 71), to thereby attain close contact with or detachment from flange (74). During particulate material processing, the airtightness of the seal portion (91) is maintained by the U-seal (64). During processing vessel washing, the airtightness of the seal portion (92) is maintained by the U-seal (65), to thereby prevent exposure thereof. Simultaneously, the U-seal (64) is raised, to thereby attain washing of the seal portion (S1) during the particulate processing.

Abstract: A cartridge filter 7 is vertically movably placed in a processing vessel 1 having a cylindrical profile. An ultrasonic washer 55 is fitted to the lateral wall 3a of the spray casing of the processing vessel 1. Washing liquid 56 is injected into the processing vessel 1 and the filter 7 is moved downward and immersed in the washing liquid 56. The washer 55 is activated under this condition to wash the filter 7. Since the washer 55 is arranged near the filter 7, the ultrasonic oscillation is easily transmitted to the filter 7 to efficiently remove the foreign objects adhering to the filter 7. Thus, with this arrangement, it is possible to wash the filter 7 in the processing vessel 1 without removing the filter 7 from a fluidized bed apparatus. In a filter washing apparatus 101, a cartridge filter 103 is contained in a processing vessel 102 and immersed in washing liquid 110.

Abstract: A rotating drum 3 has ventilation sections 6 that can ventilate the inside of the drum and the outside of the drum in the coating processing. To the ventilation sections 6, a panel unit 41 having arranged therein plural hollow pipes 42 through which cold water passes is attached. The hollow pipes 42 are fixed to a base plate 44 in parallel with each other, and a gap “G” is provided between the adjacent pipes. The base plate 44 is provided with a communication hole 45, and the hollow pipes 42 are so arranged as to face the communication hole 45. To both ends of the hollow pipes 42, charge/discharge collecting pipes 46a and 46b are fixed. In the coating processing, cold water is arbitrarily supplied to the hollow pipes 42 through the charge/discharge collecting pipe 46a to cool the drum 3 so as to bring about the temperature difference between the inside of the drum and processing objects, which can prevent coating base materials from adhering to the inside of the drum.

Abstract: A powder and particle processing apparatus comprising multifunctional baffle devices is capable of not only mixing and stirring powders and particles but also ventilating and cooling a processing container by itself. The boot-shaped baffle devices 22 are arranged in the granulation/coating apparatus 1 having a rotary drum 2. Each of the baffle devices 22 has a hollow baffle main body 24 provided with ventilating holes 32, a ventilating pipe 35 held in communication with the internal space 31 of the body 24, cooling tubes 34 arranged at the body 24 so as to allow a cooling medium 33 to flow through them and a cooling medium supply/discharge pipe 36 held in communication with the tubes 34. The baffle devices 22 are adapted to mix/stir the powders and particles in the drum 2, exhaust air from the body 24 by way of the holes 34 and the pipes 35 and cool the body 24 by means of the tubes 32 and the pipes 36.

Abstract: A seamless capsule manufacturing device comprises a multiple nozzle 7 for ejecting liquid drops into hardening liquid 10 and a flow passage tube 11 for containing hardening liquid 10. The flow passage tube 11 has a deformation section 28 that includes an inlet part 25 and a formation tube part 28b showing a cross sectional area smaller than the inlet part 25. The liquid drops ejected from the multiple nozzle 7 into the hardening liquid 10 are once made to become spherical liquid drops 26 in a sol state at the inlet part 25. The liquid drops 26b are introduced from the inlet part 25 into the deformation section 28 while they are still in a sol state. As hardening liquid 10 is introduced from the inlet part 25 into the formation tube part 28b, its flow rate is changed and the liquid drops 26 are deformed due to the change in the flow rate to produce nonspherical seamless capsules SC.

Abstract: Under the granulating section 10a for performing fluidized-bed granulation coating of powder grains, a drying section 20a for drying powder grains granulated is provided. A drying section 30a for drying the powder grains that are not sufficiently dried is provided under the drying section 20a. A product discharging section 40a for discharging a dried product is provided under the drying section 30a. A fluidized-bed forming-gas is supplied downward to upward, and granulation and dryness are continuously performed by the fluidized-bed forming-gas, and the powder grains moved from the granulating section to the drying section located immediately thereunder are pneumatic classified.

Abstract: An upper processing section 10 is provided by evenly spacing out functional stations 13 having respective functions of steps constituting a fluidized bed granulation coating process, on circumferential points. An intermediate storing section 20 is provided under the upper processing section 10 by evenly spacing out powder grain storing vessels 22 corresponding to the plurality of functional stations 13, on circumferential points. A lower gas supply section 30 is provided under the intermediate storing section 20 by evenly spacing out gas supply stations 31 corresponding to the plurality of powder grain storing vessels 22. The powder grain storing vessels 22 storing powder grains sequentially proceed to the respective functional stations 13 to execute respective processes to the powder grains, and thereby granulation coating of the powder grains is performed in a batch type and a continuous type.

Abstract: Under the granulating section 10a for performing fluidized-bed granulation coating of powder grains, a drying section 20a for drying powder grains granulated is provided. A drying section 30a for drying the powder grains that are not sufficiently dried is provided under the drying section 20a. A product discharging section 40a for discharging a dried product is provided under the drying section 30a. A fluidized-bed forming-gas is supplied downward to upward, and granulation and dryness are continuously performed by the fluidized-bed forming-gas, and the powder grains moved from the granulating section to the drying section located immediately thereunder are pneumatic classified.

Abstract: An upper processing section 10 is provided by evenly spacing out functional stations 13 having respective functions of steps constituting a fluidized bed granulation coating process, on circumferential points. An intermediate storing section 20 is provided under the upper processing section 10 by evenly spacing out powder grain storing vessels 22 corresponding to the plurality of functional stations 13, on circumferential points. A lower gas supply section 30 is provided under the intermediate storing section 20 by evenly spacing out gas supply stations 31 corresponding to the plurality of powder grain storing vessels 22. The powder grain storing vessels 22 storing powder grains sequentially proceed to the respective functional stations 13 to execute respective processes to the powder grains, and thereby granulation coating of the powder grains is performed in a batch type and a continuous type.

Abstract: A powder grain processing apparatus is provided such that both agitation and mixture of powder grains can be performed efficiently.

Abstract: This is a granulating-coating apparatus comprising: a spraying means for spraying a binder liquid or a coating liquid onto articles to be processed, which are received in a rotary drum; a brush provided in a manner to be movable relatively to the spraying means in the rotary drum, for contacting a spray gun formed in the spraying means and removing adhered articles on the spray gun; and an adhered article sucking device provided in the vicinity of the brush, for receiving the removed adhered articles. With this arrangement, the adhered articles on spraying openings of the spraying means can be removed completely without contamination of the articles to be processed with the removed adhered articles.

Abstract: An apparatus for applying a coating to a powdery or granular material has a rotary drum 20 including a tubular portion 21 formed with air holes 27 and hollow shaft portions 23 and 24 provided at opposite end portions in the axial direction. A coating chamber 26 is defined inside the rotary drum 20. Liquid is sprayed from a nozzle 32 onto an accumulated layer 33 of a powdery or granular material in the coating chamber 26. Drying gas supplied from an air supply duct 45 is introduced into the rotary drum 20 from one of the two hollow shaft portions 23 and 24. A plurality of axially extending air ducts 34 are provided on the outer periphery of the rotary drum 20. When an air duct is positioned downwardly it is communicated with an air exhaust duct 41 through a distributor 35. Air introduced from the air supply duct 45 is biased toward the accumulated layer 33 by louvers 48.

Abstract: A method of and an apparatus for sugar coating, the apparatus comprising: a rotatable vessel for containing a material to be coated; a baffle 9 movable independently of the rotatable vessel; a baffle mounting shaft 10 having a bent construction, for mounting the baffle 9 thereon; and a hydraulic cylinder for rocking the baffle mounting shaft 10 to displace the baffle 9. Load cells 17a and 17b for detecting the position of the baffle 9 relative to an accumulated layer M of a material to be coated are provided on the baffle 9. The load cells 17a and 17b serves for holding the position of the baffle 9 relative to the accumulated layer M of the material to be coated at all times, on the basis of a load imposed due to the presence of the contact with the material to be coated.

Abstract: A prolonged release dosage form of drug made by coating a surface of an ungranulated medicinal particle with a water-insoluble material which is physiologically acceptable and does not dissolve in water and gastric juice; and then, granulating or tableting the coated medicinal particles.

Abstract: A method of performing granulating, coating, drying of a powdry or granular material having a relatively minute particle diameter and an apparatus therefor. A nozzle for supplying the powdery or granular material and a nozzle for supplying a coating liquid are parallelly provided at adjacent positions where air streams dispersed from the both nozzles are not in contact with each other and directed to the interior of a processing cylinder. The two nozzles are connected to compressed air sources independently of each other. Drying air-stream blow-in openings are provided on the way from collision of the powdery or granular material and the coating material to catching thereof. Drying air streams are supplied from a direction tangent to the processing cylinder having a circular section.

Abstract: A granulating and coating method using the drying air streams to effectuate granulating, coating and drying and apparatus therefore wherein:a nozzle for supplying an article to be coated and another nozzle for supplying a coating material are provided at such positions that the article to be coated and the coating material collide with each other before the article to be coated and the coating material are dispersed by the drying air streams.

Abstract: A granulating and coating apparatus comprising a rotary drum to be charged therein a powdery or granular material, and a baffle plate provided in the rotary drum and not rotatable together with the rotary drum. The rotary drum is formed to be a polygonal shape. This polygonal shape may be, for example, a pentagon, a hexagon, an octagon or a decagon. The baffle plate may be positionally fixedly supported. Or, the baffle plate can be made to change a position in a rocking direction, a position of the rotary drum in the axial direction, a depth of insertion into a layer of a powdery or granular material or an angle of insertion by use of plurality of actuators.