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Solutions : Blending optimization
Technology Summary
The blending optimization loop
begins with measurement. We accurately and efficiently measure
properties in real-time, on-line and/or off-line, using Near
Infra-Red analyzers and Topnir models (See Topnir Technology).The solution provides the End User with the
facility to efficiently prepare and run the operation with full
confidence all along the blend.
Our solution is compliant with any existing
facilities and has been interfaced with most of the DCS, Regulatory
blend controlers and blending optimizers.
Blend
Preparation
The first step consists in measuring the
destination tank heel and blending components quality using Topnir
model implemented off-line (less than 1 minute per product are
required to output the full suite of properties). The blending
optimizer uses this fresh and
accurate quality information to output the best achievable recipe.
Note that we can either provide our own
optimizer (Optiblend) or interface Topnir to the existing
optimization system.
Blend
Operation
Topnir implemented on line provides every 1 minute all the properties required by the blender header (No limitation of number of properties). The
information is transferred to the DCS and allows maximizing the
blending optimizer efficiency.For complex blending process, where no intermediate
component tanks are being used, our technology allows to monitor on-line
multiple streams (components and blender headers) using a single
analyzer
Typical savingsGive away minimization
Key advantages
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| KEROSENE | GASOIL | |||
| True Values | Blending Indices | True Values | Blending Indices | |
| Density @15 | 0.795 | 0.795 | 0.845 | 0.845 |
| Cloud point | -45 | -35 | -5 | 0 |
| Flash point | 38 | 33 | 65 | 70 |
| Cetane Index | 43 | 40 | 50 | 55 |
| Diesel Blending | Cetane Number, Cetane Index, Cloud Point, CFPP, Pour Point, Flash Point, Viscosity, Density, ASTM Distillation D86, Aromatics ,... |
| Gasoline Blending | RON, MON, RVP, DVPE, %Aromatics, % Benzene, %Olefins, % Naphtene, % Parafins, MTBE, ETBE, Oxygenate, ASTM Distillation D86, Density,... |
Typical profits :
Between 1 to 5 MUS$ per year depending on refinery throughput.
| Item | Yearly savings ($) |
| Give away minimization (0.3 on Octane and 4 KPa on RVP) | 2.9 M $ |
| Re-blend rate minimization (from 20% to 7%) | 1.3 M $ |
| Sampling and laboratory cost minimization | not estimated |
| Maintenance cost reduction | not estimated |
| Yearly Global Saving | 4.2 M $ |
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