| INDMAX: Residue Upgradation to LPG, Light Olefins and high Octane Gasoline
|
|
Backed by a strong
R&D with state- of- the- art facilities for
characterisation and performance evaluation of FCC catalysts
and additives, IndianOil is well equipped to give precise
solutions to our customers’ requirements. The important
facilities available with us are:
| » |
Automated MAT
units |
| » |
FCC pilot
plant |
| » |
Steaming units |
| » |
Characterization equipment include ABD, PSD, SA, PV,
TA/TGA, TPD, RGA, SDA, PNA, Octane analyzer etc.
|
| » |
Kinetic based FCC process simulation model
FCCMOD. This model has been extensively used to
study the interaction among process variables in the
INDMAX process. Among other things, FCCMOD has
unique ability to predict commercial plant performance
based on the micro
reactor data
generated for any new feed or
catalyst. |
Typical IRR works out to about 17% without olefin recovery
and 35% with olefin recovery. IndianOil has put-up a
commercial plant of 100,000 TPA capacity which is under
operation and ITL can arrange visit for the prospective
customer. Typical ISBL cost of a 1MMTPA, INDMAX unit
is about US$ 50 million.
| » |
Detailed analysis of
different residue streams of the refinery and their
availability. |
| » |
Determination of the
desired product slate i.e. LPG/Gasoline ratio. |
| » |
Establishing the
requirement with down stream integration i.e. whether
the propylene/ butylenes separation to be included or
not. |
| » |
Performing a scoping
study of the project. The scoping study will include the
product yield, quality estimates and equipment required
for the entire unit. |
| » |
Preparation
of cost estimate for establishing the techno-economic
feasibility of the project. |
| » |
Preparation
of the project proposal and subsequent design
package. |
| |
|
| |
|
|
|
|
|