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"Study of Heat Transfer from Buried Pipelines", value 6,95,108
(US$ 15,798) consultancy project, Mangalore Refinery & Petrochemicals Ltd.
(Subsidiary of ONGC Ltd.)
"Spent Catalyst Reused / Disposal", in collaboration with PDIL, Noida, Value 2,00,00,000
(US$ 44, 4,445). Department of Fertilizer, Ministry of Chemicals and Fertilizers, GOI.
"Literature survey on Supersonic Burners", Value 1,08,000 (US$2,400) consultancy
project, Petroleum Conservation Research Association, Ministry of Petrolium and
Natural Gas, GOI.
"Scale up and Design of Trickle Bed Reactors-Phase III, Ministry of Petroleum and
Natural Gas, GOI, Value INR 1.35 Crores (US$3,00,000), Association with EIL and IOC Ltd.,
(2002-2004)
The aim and scope of the work is to design a Trickle Bed reactor of 1 meter diameter
and prepare experimental data base. Test the model which has already been developed
during the phase I and Phase II study. The attempts will also be made to develop the
CFD codes.
"Pilot Plant Study on Coiled Flow Inverters as a Heat Exchanger" Value INR 2,46,00,000
(US$ 54,8,000); March 2001 to March 2005.
This concept introduces a new and more effective device for flow inversion, which is
achieved by changing the direction of centrifugal force in helically -coiled tubes.
Advantages offered by the proposed device over any other known or conventional
methods used in the industry.
"Pilot Plant Study on Innovative Heat Exchanger - Phase II" Value
INR 1,10,00,000; April 2005 to March 2007. -
"Extraction of Oil from Jojoba Seed" value INR 5,90,000 (US$13, 111); duration June
2001 to September 2002 sponsored by National Oil Seeds and Vegetable Oils,
Development Board, Gurgaon.
Design of the low cost oil extractor for the extraction of oil under cold conditions.
Commercially Jojoba oil can be used as lubricant for break oil, gear oil, engine oil and
grinding oil etc. It can also be used in cosmetics such as lipstick, face cream, skin
freshner, winter care lotion, shampoo, moisturizer, soap and medicine etc.
"Radioisotope Tracer Studies for Modelling and Simulation of Multiphase Reactors at
Elevated Pressures" Value INR 13,85,200 (US$ 30,782), Department of Atomic Energy,
Board of Research in Nuclear Sciences, April 2000 to March 2002.
The major processes carried out in trickle-bed reactors are hydrotreating,
hydrocracking, hydrodemetallisation and hydrofinishing. Trickle-bed reactors are also
find applications in chemical and biochemical industries. Vast literature is available in
trickle-bed reactors based on experiments conducted at atmospheric pressure at
ambient temperature where as commercial trickle-bed reactors operate in the range of
25-40 MPa. At eleveated pressure the physical properties of the liquid changes
considerably and hydrodynamics of the reactor changes drastically. Therefore the
validity of using the correlations & models developed at atmosphere pressure in the
design of trickle-bed reactor is in doubt. In this present study the aim is to carry out
residence distribution studies in trickle-bed reactor at elaveted pressure using porous
particles as packing.
"Technology Development: Hydrodynamics and Cold Flow Studies in Trickle Bed
Reactor - Phase-II" in collaboration with EIL and IOC, Value INR 3,59,062,000 (US$
79,79,155); August 1997 to June 2001.
The aim is to design and scale up of trickle bed reactor employing semi-theoretical
modeling approach, study of various hydrodynamic parameters and liquid distribution in
the catalytic bed and demarcation of flow regimes at high pressures. The reactors used
are 6" and 12" diameters and operating pressure is 1-20 bar (A).
"Technology Development: Hydrodynamics and Cold Flow Studies in Trickle Bed
Reactor -Phase - I and Phase-II" in collaboration with EIL and IOC, Value INR
5,000,000(US$ 1,11,111) ; August 1997 to March 2002.
Trickle Bed Reactors belong to the most widely used multiphase reactors and are
applied on a large scale particularly for hydrotreatment of medium heavy and heavy oil
fractions in the hydrocarbon processing industry. Importance of Trickle Bed Reactors is
increasing, mainly in hydroprocessing of oil fractions- due to more environmental
restrictions and high demand of middle distillate. At present all refineries have already
installed HDS unit for kerosene and diesel and are going to install Hydrocracker. The
aim of this project is to design and scale up trickle bed reactors using these
hydrodynamic tools which are evaluated at higher pressure. Here the reactor sizes are
1" and 2" diameters and operating pressure is 1-25 bar(A).
"Radioisotope Tracer Study to Investigate the Mixing Characteristics of Chemical
Reactor" Value INR 8,01,000 (US$ 17,800); July 1996 to March 1999. Department of Atomic
Energy, Board of Research in Nuclear Sciences.
The importance of trickle bed reactor is increasing. Residence time distribution studies
were carried out in trickle bed reactors using radioisotope tracer technique to
investigate the flow pattern of the phases, and liquid saturation.
"Radioisotope Tracer Studies for Modelling and Simulation of Multiphase Reactors at
Elevated Pressures" Value INR 13,85,200 (US$ 30,782), Department of Atomic Energy,
Board of Research in Nuclear Sciences, April 2000 to March 2002.
The major processes carried out in trickle-bed reactors are hydrotreating,
hydrocracking, hydrodemetallisation and hydrofinishing. Trickle-bed reactors are also
find applications in chemical and biochemical industries. Vast literature is available in
trickle-bed reactors based on experiments conducted at atmospheric pressure at
ambient temperature where as commercial trickle-bed reactors operate in the range of
25-40 MPa. At eleveated pressure the physical properties of the liquid changes
considerably and hydrodynamics of the reactor changes drastically. Therefore the
validity of using the correlations & models developed at atmosphere pressure in the
design of trickle-bed reactor is in doubt. In this present study the aim is to carry out
residence distribution studies in trickle-bed reactor at elaveted pressure using porous
particles as packing.
"Development of Drag Reducers for Petroleum Industry " Duration 1 year (1995 - 96 )
Fee INR 100,000 (US$ 2, 222); Vam Organics Ltd. Delhi. (Consultancy)
"Studies on Multiphase Reactors" with Prof. W. D. Deckwer, University of Oldenburg,
FR Germany, AvH Foundation, 1989, Value DM 49, 000.
A three-phase fluidized bed is formed when solid particles are fluidized with cocurrent
upward gas and liquid flows. Mass transfer and effective shear rate in the three-phase
fluidized bed were investigated experimentally. A uniform correlation was developed for
the liquid phase volumetric mass transfer coefficient in the three-phase fluidized bed
with viscous liquids.
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