Process Reactors in Palghar (प्रोसेस रिएक्टर, पालघर)

Chemical Reactor: Material of Construction (MOC): Available in SS304, SS316, SS316L, Carbon Steel, Hastelloy, Alloy-20, or as per client requirement. Design Options: Jacketed, Limpet coil, Half-pipe coil, or Plain reactors. Capacity Range: From 50 liters to 50,000 liters. Agitation System: Customizable high-speed or low-speed agitators, anchor, paddle, turbine, or helical ribbon type impellers. Heating Cooling: Steam, hot oil, electrical heating, or chilled water cooling arrangements. Pressure Rating: Full vacuum to 25 bar (or higher on request). Surface Finish: Mirror finish (pharma-grade), matt finish, or chemical-grade internal external polish. Sealing Options: Gland packing, mechanical seal (single/double), or magnetic drive. Applications: Reaction, mixing, and blending of chemicals. Polymerization, hydrogenation, and crystallization. Fermentation and biochemical processes. Heat transfer, dissolution, and emulsification. Value Proposition: Optimized design for high efficiency uniform mixing. Enhanced safety and reliability with pressure/vacuum tested vessels. Long service life due to corrosion-resistant materials. Tailor-made solutions to match exact process conditions industry norms. Backed by installation, commissioning, and after-sales support.

UMA CHEM PHARMA MACHINERIES design and manufactures Reactor / Reaction Vessel. They are mainly use in chemical, pharmaceutical, API/Drugs paint and Colour Industries. These are available in 50ltrs to 25KL Capacity. We have made the Jacket Reactor Vessel as a standard apparatus in the chemical industry and its basic work is for mixing processes and for chemical reactions in the liquid phase. The vessel can be easily operated in batch mode with temperature going up to 150*C To 500 C Depending on the requests of the process the agitated vessel consists of unalloyed or alloyed steel. Jacket Reactor Vessel consists of a cylindrical vertical shell with standard Torispherical/ Ellipsoidal dish on both ends. A Jacket is provided on the Outside of the shell for Heating Cooling Stiffener Rings are provided on shell in between the shell and jacket to give uniform circulation of the heating or cooling media and to intensify the vessel. MOC: SS 304 SS 316 Hastelloy Titanium Nickel (As per customer requirement) ADVANTAGE : We follow ASME Section VIII Div-I or Designing of vessels and section IX for welding qualification procedure, electrode selection for all the application. Different types of Agitators such as Anchor, Turbine, Mig, Hydrofoil, Propeller, Helical and Contra Mixer etc.

Features: Superb performanceDurabilityRobust design

Top Open Reactor/Kettle

Enzymes are biomolecules that catalyze (i.e. increase the rates of) chemical reactions. Almost all enzymes are proteins. Like all catalysts, enzymes work by lowering the activation energy for a reaction, thus dramatically increasing the rate of the reaction. Most enzyme reaction rates are millions of times faster than those of comparable un-catalyzed reactions. As with all catalysts, enzymes are not consumed by the reactions they catalyze, nor do they alter the equilibrium of these reactionsAdding free enzyme to a batch reactor is practical only when the value of the enzyme is relatively low. With expensive enzymes, reuse by retaining the enzyme with some type of support makes great economic sense. As some activity is usually lost in tethering the enzyme and the additional operations cost money, stability is very important. However, many enzymes are stabilized by immobilization; thus, many reuses may be possible. Methods of immobilization have already been discussed, and various reactor configurations are possible. An enzyme immobilized on beads of a support material or captured in a gel droplet is essentially a catalytic particle. Mounted in a packed column, there may be upflow or downflow of the feed solution, and a fluidized bed may be feasible except that particle collision often endangers stability of the enzyme. A serious problem is growth of microorganisms on the particles because enzymes are proteins that are nutritious. As immobilized enzymes often have more thermal stability than do free enzymes, the columns can be run at elevated temperatures (50 to 65 C, or 122 to 149 F) to improve reaction rate and to inhibit most but not all contaminating organisms. Sterile feed solutions and aseptic technique can minimize contamination, but, more commonly, antiseptics are added to the feed, and there is occasional treatment with a toxic chemical to wash organisms from the column. Particles with immobilized enzymes are sometimes added to a reactor and recovered later by filtration or by some trick such as using magnets to collect enzymes attached to iron. Cellulose is hydrolyzed by a complex of several enzymes. The mix of enzyme activities produced by mold cultures can have insufficient amounts of the enzyme beta-glucosidase to maintain a commercially acceptable hydrolysis rate. This enzyme can be produced with a different microbial culture and used to supplement the original enzyme mix, but the cost is high. It is logical to immobilize the betaglucosidase for multiple use. Handling is minimized by circulating fluid from the main reactor through an external packed column of immobilized enzyme. Enzymes can be immobilized in sheets. One design had discs of enzymes fastened to a rotating shaft to improve mass transfer, and an alternate design had the feed stream flowing back and forth through sandwiches of sheets with enzyme. However, volumetric efficiency of such reactors is low because sheets with finite spacing offer less area than that of packed particles. It is possible to add free enzyme and recover it by ultrafiltration, but sufficient membrane surface to get good rates and the required auxiliary equipment are expensive. A hollow fiber device packs a vast amount of membrane area into a small volume. Enzyme may be immobilized inside or outside of the fiber, and it is easy to flush and replace the enzyme. Drawbacks to this design are: