Chemical Reactors Dealers in Delhi

Jacketed Reaction Vessel consist of a Cylindrical vertical shell with standard torospherical dish on both ends. A jacket is provided on the Outside of the shell for Heating the reactor by passing steam or thermic oil or Cooling the reactor by passing cooling media. 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. Agitator assembly mounted on the Top dish of Reactor consists of Shaft supported by Lantern Assembly on the Top End containing Bearing Housing with Tapered roller bearing and Ball bearing to withstand impact load and vibratory load ensuring smooth rotation of the Shaft. On the other end of the shaft Blade is fitted of different types as per the need of the Process viz. Single Anchor, Double Anchor, Turbine & Propeller types. Baffles are also provided inside the shell as per the requirement. Top Dish of the Reactor is provided with various Nozzles viz. Manhole, Light Glass, Sight glass, Vapour, Addition, Reflux, Thermowell etc. Bottom Dish of the Reactor is provided with an Outlet nozzle where valve is fitted. Specifications: 50 Ltrs, 100 Ltrs, 150 Ltrs, 200 Ltrs, 250 Ltrs , 300 Ltrs, 350 Ltrs, 400 Ltrs, 500 Ltrs, 600 Ltrs, 700 Ltrs, 750 Ltrs, 800 Ltrs 1 KL,1.2 KL, 1.6 KL, 2 KL, 2.5 KL, 3 KL, 3.5 KL, 4 KL, 4.5 KL, 5 KL, 6 KL, 7 KL, 7.5 KL, 8 KL, 9 KL, 10 KL, 12 KL, 15 KL, 20 KL. Available in GMP model and NGMP model, MS Jacket and SS 304 Cladding, SS 304 Jacket and SS 304 Cladding, Limpet Coil, Insulation. Available with Anchor agitator, PBT agitator, Propeller agitator, Hydrofoil agitator.SS 316, SS 304 and MS.

Indvacuum offer high pressure reactors. High pressure reactors product description this product applies when handing chemical, chemical reaction temperature, need to add an inert gas, stress, and the conductance, ph value, redox reaction of precision chemical synthesis via the experiment. Application: catalytic synthesis, high temperature and high pressure, kinetics, fischer - tropsch, hydrogenation reaction.

We are engaged in the manufacturing, exporting and supplying premium Chemical Reactor in the market. Chemical Reactor, offered by us, is used in vessels in Pharmaceutical industry and Chemical industry. We offer a range of Chemical Reactors in several grades such as C.S., M.S., S.S. 316L, S.S. 304 and S.S.316. Furthermore, our Chemical Reactors are available with limpet for heating and also a jacket. Specialties Of Our Chemical Reactor Available in seeral gradeslawlessly designedDurable Cost-effective

Volume: 20ml to 10liters. Inner Ø from1/8" to 5" Working temperature:  up to 900°C. Working pressure: 10 to 1000 bar.

We are offering pressure reactors. Plant scale high pressure reactors size 50 to 1000 ltrs. Moc : ss-316, 316l, hastelloy b/c, monel inconel, nickel, titanium etc. Fabricated with dished ends & jacketed / electrically heated. Zero leakage magnetic drive coupling from 200-900 kgcm torque capacity. Max. Working pressure: upto 70 kg/cm2 (1000psi) max. Working temperature : 350c. Gas induction impeller, pitch blade turbine, anchor etc. 50-500 rpm infinite variable speed. Temp., pressure, rpm control & optional datalogging on pc. Internal cooling coil, sparger, vent valve, liquid / powder charging vave, flush bottom valve, baffles, light & sight glass, manhol. Optional autocooling, liquid charging, condensor, reflux condensor, metering pump, chainpulley lifting system. All designs as per asme codes.

We are offering industrial reactor, based in delhi. The reactors are provided with various types of agitators such turbine, anchor, propeller or any special type as per requirement of the process. The industrial reactor may be provided with internal cooling coils if needed. Reactors for various industries can be manufactured, as per process need such resin plant, basic drug plant, bioreactor, open reactors etc. The s.s. Reactor can be availed either in mirror finish or aluminum finish as per requirement of the requirement of the customer. available in : reactors of capacities varying from 50l to 1,20,000l in various materials of constructions such as stainless steels gr. 304 / gr.316 / m.s. Etc.

High Pressure Reactors, Bellows Hbr Gas Generator

Agitator Reactors, Pressure Vessels, Heat Exchangers, Silo Storag

Eco Process SBR Sequencing Batch Reactor, Waste Water Treatment Plant

ACSION SAFF (Submerged Aerobic Fixed Film Reactor ) In ACSION SAFF processes, the microorganisms responsible for the conversation of organic material nutrients are attached to an inter packing material and nutrients are removed from the waste water flowing past the attached growth also known as a biofilm liquid layer. The most common aerobic attached growth process used is the trickling filter in which waste water is distributed over the top area of a vessel containing non submerged packing material. Historically, rock was used most commonly as the packing material for trickling filters, with typical depths ranging from 1.25 to 2 m (4 to 6 ft). Most modern trickling filters vary in height from 5 to 10 m (16 to 33 ft) and are packed with a plastic packing material for biofilm attachment. The plastic packing material is designed such that about 90 to 95 percent of the volume in the tower consists of void space. Air circulation in the void space, by either natural draft or blowers, provides oxygen for the microorganisms growing as an attachment biofilm. Influent wastewater is distributed over the packing and flows as a non uniform liquid film over the attached biofilm. Excess biomass sloughs from the attached growth periodically and clarification is required for liquid/solids separation to provide an effluent with an acceptable suspended solids concentration. The solids are collected at the bottom of the clarifier and removed for waste-water sludge processing. BIOLOGICAL NITRIFICATION Nitrification is term used to describe the two-step biological process in which ammonia (nh4 –n) is oxidized to nitrite (no2-n) nitrite is oxidized to nitrite (no3-n). the need for nitrification in wastewater treatment arises from water quality cancers over (1) the effect of ammonia on receiving water with respect to do concentrations and fish toxicity, (2) the need to provide nitrogen removal to control eutrophication, and (3) the need to provide nitrogen control for water-reuse applications including groundwater recharge. For reference, the current (2001) drinking water maximum contaminant level (MCL) for nitrate nitrogen is 45 mg/l as nitrate or 10mg/l as nitrogen. the total concentration of organic and ammonia nitrogen concentration in municipal wastewater is typically in the range from 25 to 45 mg/l as nitrogen based on a flow rate of 450l/capited.d (120gal/capita.d). In many parts of the world with limited water supplies, total concentrations in excess of 200 mg/l as and have been measured in domestic wastewater. PROCESS DESCRIPTION As with BOD removal, nitrification can be accomplished in both suspended growth and attached growth biological processes. For suspended growth processes, a more common approach is to achieve nitrification along with BOD removal in the same single-sludge process, consisting of an aeration tank, clarifier, and sludge recycle system. In case where there is a significant potential for toxic and inhibitory substances in the wastewater, a two-sludge suspended growth system may be considered fibers in series with the first aeration tank/clarifier unit operated at a short SRT for BOD removal. The BOD and toxic substances are removed in the first unit, so that nitrification can proceed unhindered in the second. A portion of influent wastewater usually has to be bypassed to the second sludge system to provide a sufficient amount of solids for efficient solids flocculation and clarification. Because the bacteria responsible for nitrification grow much more slowly than heterotrophic bacteria, systems designed for nitrification generally have much longer hydraulic and solids retention times than those for systems designed only for BOD removal. In SAFF systems used for nitrification, most of the BOD must be removed before nitrifying organisms can be established. The heterotrophic bacteria have a higher biomass yield and thus can establish. The heterotrophic bacteria have a higher biomass yield and thus can dominate the surface area of fixed-film systems over nitrifying bacteria. Nitrification is accomplished in an attached growth reactor BOD removal or in a separate attached growth systems designed specifically for nitrification. The placement of packing material in the aeration tank of the activated-sludge process dates back to the 1940s with the Hays and Griffith processes (WEF, 2000). Present day designs use more engineered packing and include the use of packing materials tat are suspended in the aeration tank with mixed liquor, fixed packing material placed in portions of the aeration tank, as well as submerged RBC. The advantages claimed for these activated sludge process enhancements are as follows : Increased treatment capacityGreater process stabilityReduced sludge productionEnhanced sludge settles abilityReduced solids loadings on the secondary clarifierNo increase in operation and maintenance costs MICROBIOLOGY Aerobic autotrophic bacteria are responsible for nitrification in activated sludge and biofilm processes. Nitrification, as noted above is a two step process involving two groups of bacteria. In the first stage, ammonia is oxidized to nitrite by one group of autographic bacteria. In the second stage, nitrate is oxidized to nitrate by another group of autotrophic bacteria. It should be noted that the two groups of autographic bacteria are distinctly different. Starting with classical experiments on nitrification by Winogradsky (1891), the bacteria genera commonly noted for nitrification in wastewater treatment are the autotrophic bacteria Nitrosamines and Nitrobacter, which oxidize ammonia to nitrate and then to nitrate, respectively. Other autotrophic bacteria where were identified as being capable of oxidation ammonia to nitrate (prefix with Nitroso-) are Nitrosococcus, Nitrosospira, Nitrosolobus, and nitrosorobrio (printer, 1970). It should be noted that during the 1990, many more autotrophic bacteria were identified as being capable of oxidizing ammonia. Besides Nitrobacter, nitrite can also be oxidized by other autotrophic bacteria (nitro-) genera: Nitrosococcus, Nitrosospira, Nitrospina and Nitroeystis. Using oligonucleotied probes for ammonia oxidizing bacteria, Wagner et al. (1995) showed that nitrosomonas was common in activated-sludge systems. For nitrate oxidation in activated sludge, Teske et al. (1994) found that Nitrococcus was quite prevalent. Whether different growth conditions can select for different genera of nitrifying bacteria or if their nitrification kinetics are significantly different is unknown at present. ACSION has developed this technique in a most modern way of versatile design and has supplied many such plants to meet the requirement of our valued customers.

Internal Cooling Coil, Sparger, Vent Valve, Liquid Powder Charging Vave, Flush Bottom Valve, Baffles, Light & Sight Glass, Manhol.

High Pressure Reactor, Filter Testing Equipment, Membrane Testing Equipment

Moving Bed Biofilm Reactors, Electro Chlorinator, Chlorine Dosing Syste

Reactor, Agitator, Condenser, Industrial Conveyor, Screw Conveyo

Ultraviolet Reacto

Stainless Steel Reactor, Pharmaceutical Plants, Pharmaceutical Machiner

Chemical Reactors, Chemical Blenders, Pressure Vessel

Chemical Reactors, Roasters, Safety Gloves, Safety Helmet, Safety Product

Line Reactor, Resistive Load Bank, D.C. Filter Chok

Chemical Reactors, Process Tank

Reactor, Storage Tanks, Laboratory Fermenter, Chimney, Ventury Injecto