We deals almost all the machineries used by the Pharmaceutical Industries at the production level and also our products are used in the Chemical, Petrochemicals, Confectionary, Engineering and Process Industries. We continues upgradation of the design. We are enclosing herewith our product catalogue for your reference. We would appreciate your views and it would be of great use if you could write to us for nay further information / clarification needed by you.
Bottling / Packaging
You need one bottling / packaging machine or totally integrated systems, we are the one company that can assure you industry leading expertise in design, engineering, installation. while enquiry please mention the cap type, bottle type, speed required and pack size.
Fluid Bed Coaters: | Lab Model | Bottom Spray | Top Spray | Roto Processor
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MODELS : Different models of linear filling machine are available with combination of filling heads varying from 2 to 12 depending on the speed and the filling volume required. FUNCTIONING :
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MODELS : ROPP CAP SEALING MACHINE : Different models ranging from 4 heads to 72 heads. SCREW CAPPING MACHINE : Different models ranging from 4 heads to 72 heads. |
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| Different models of monoblock machine are available with combination of volumetric or gravimetric or vaccumetric filling with ROPP or screw capping system with filling heads varying from 4 to 72 depending on the type of the machine. |
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| Different models of labeling machine are available with either single line labeling or dual line labeling arrangement depending on the speed required which in turn depends on the label size and thickness, diameter and shape of the bottle/container to be labeled. |
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UNIVERSAL LABELING MODEL
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LABEL CODING MACHINE
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CARTON CODING MACHINE
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OPTIONAL FEATURES :
Die-Roller Design Extruder :
| The first step in pelletisation technology. It is used for converting
the powder material (which does not get sticky when mixed with binders) into
extrudes/ granules of equal diameter and fixed length. The machine is
available in various capacities for both R&D and production sizes.
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spher'oidization :
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The spher'oidization process is the extension of the extrusion process ie. It is used to convert the extrudates into pellets. It is available in the smaller sizes for R&D purpose & in larger sizes for production purpose. |
Solid Drug Layering :
| One of the processes for manufacture of pellets or loading
of the drugs on the pellets is the layering process. This process involves deposition of successive layers of an active compound onto the granules of the non pareil seeds or active compound resulting in formation of uniform sized pellets. |
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The first step in pelletisation technology. It is used for converting
the powder material (which does not get sticky when mixed with binders) into
extrudes/ granules of equal diameter. The machine is available in various
capacities for both R&D and production sizes. The main advantage of the machine vis a vis the die-roller design extruder is that it is possible to formulate pellets as fine as 0.6mm even in the production size. |
Fluid Bed Systems - Lab Model:
| The lab-model for the Fluid Bed Systems is advantageous as it has all the three attachments unlike the production models where it is not feasible to have all the three attachments. It is used for coating particles, pellets as well as loading on pellets & making pellets. All the different operations are possible using three attachments in the same machine. |
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Operations possible in WURSTER CHAMBER |
Operations possible in TOP SPRAY CHAMBER |
Operations possible in ROTO-PROCESSOR CHAMBER |
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The basic concept in Bottom spray coating, which is also
known as air suspension coating, it is to separate the particles from one
another in an air (gas) stream and spray a coating formulation on to the
particles while they are suspended.
The process takes a specially modified fluid bed that is divided into zones by a partition. The inner area is a high velocity zone that separates the particles and transports them past the spray nozzle. (Green color zone) After passing the nozzle, the particles enter the expanded area, slow down and fall back into the outer section of the fluid bed product bowl. (Red color zone) The coating dries when the particles are suspended to prevent agglomeration from occurring when they enter the tranquil part of the bed. (Blue color zone) The coated particles in the tranquil storage area remain fluidized just enough to allow them to continue moving towards the bottom of the bowl. When the particles reach the bottom of the bowl. When the particles reach the bottom they are drawn back into the high velocity air stream and the cycle is repeated. This process continues until desired level of coating has been achieved. |
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The conical shaped expansion chamber decreases the velocity of air in half form the bottom of the expansion chamber to the top. This helps to keep fine particles out of the upper filter region. Sale up from single fluid bed to utilizing multi fluid bed systems of different sizes (i.e. for development, medium scale production and large scale production) Company maintains critical scale up of factors such as average bowel geometries air velocity and air changes (quantity of air/cubic foot of product) from one unit to the next. Hence, product created in smaller size systems can be scaled to production using portionally increase air handling package. Further operating bed depth, which effects the end product coating model and density (while granulating) is also mained from one unit to the next.
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The basic concept in granulation (also known as agglomeration) involves suspending particulates in an air stream and spraying a liquid from the top down onto the fluidized bed. Particles in the path of the spray get slightly wetted and become tacky. The tacky particles collide with other particles and adhere to them to form a granule. There are two different modes of fluid bed granulation: Dry stage and Wet stage. In the dry stage granulation, the particles only require a slight wetting to become tacky and stick to each other. The granulating solution is applied at a rate less than or equal to the evaporation rate. Thus the particles remain "dry" through the entire process. In wet stage granulation, the particles require significant wetting before they become tacky enough to stick to each other. The granulating solution is applied at a rate higher than the evaporation rate until the particles build up enough moisture to granulate. The characteristics of the the particles when wet and the type of granulating solution being used will determine which mode of granulating is most appropriate. While dry stage is most common, wet stage granulating allows for denser products. Spray gun Spiral granulation use air atomized spray nozzles in single or multi-nozzle configuration. Droplet size can be varied by automation pressure and nozzle cap size. For multi-nozzle application, a high efficiency spiral pattern produces a more uniform coverage of the bed. A higher percentage of granulation solution comes in contact with the product bed as compared to cluster mounted nozzle used in a more uniform product quicker granulation time, and more efficient use of granulation solution.
To further atomize the granulation spray system the spray nozzle height can be raised or lowered automatically during the process in operation, which permits the distance between the nozzle tip and fluidized bed to be adjusted during the process to compensate for changes in the bed height during granulation.
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ROTO PROCESSOR FOR DRUG LOADING, PELLET COATING, & TABLET
COATING
Specially designed baffles, bottom plate, low speed rotation, enables it to coat pellets & tablets, also can be used for drug loading on N.P.S ROTO PROCESS FOR PELLET FORMATION High controlled speed of rotation enables pellet formation by this principle. PROCESS DESCRIPTION Fluid bed rotor process which by principle is nothing else than a horizontal Wurster process, because it fully utilizes the 3 main features below: Concurrent spraying below the product bed without premature droplet evaporation. High kinetical energy inside the product (created by the rotating disc). Additionally, the process air entering vertically the process chamber at the periphery of the rotating disc, forces the product into a helical motion, so that practically every particle is permanently rolling around its own axis. Regular statistical exposure of the particles to the spray nozzle by means of a defined disc rotation speed. Analyses have shown that due to the permanent product rolling motion under centrifugal forces the rotor film is even somewhat denser, i.e. to obtain a Wurster identical drug release profile, one would have to apply a little less coating agent with the roto process. But of course the fluid bed processing is not limited to film coating only, but permits a number of process versions: The Rotor Granulation (By spraying a suitable binder suspension powderous substances can be granulated and spher'onized by the permanent rope motion of the product. The final stage drying can be rapidly achieved as the large free area around the rotor disc allows the throughput of large air volumes. The palletizing (i.e. the production of non-paeils by |
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rapid powder and binder addition onto dummy seals through a
single, combined bottom spray nozzle (in this case tangential spray). This
process allows weight gain of approximately 250% per hour.
Unlike the Wurster process the rotor is not suited for the film coating of Powder, due to the higher kinetically energy produced by the centrifugal forces of the fast rotating disc. |
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WASHING MACHINE FOR BOTTLES / VIAL :
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1. Free flow & non free flow liquid like water, milk, Juices, Oils, Ghee, Honey, Shampoo etc. 2. Free flow & non free flow Powders like Salt, sugar, powder, chemicals etc. 3. Granules like tea, coffee, tobacco, Spices, Pan masala, chemicals etc..
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