Hydrotreating/ Hydrodeoxygenation reactor
Isomeri s ation/selective/ Hydrocracking reactor
Make - up hydrogen
Fractionator
Amine
LPG
PSA
Product stripper
Green n aphtha
Fuel gas
Fuel gas
Air
CO r ich stream
Air
Green j et fuel
Ogas
Green d iesel
Air cooler
Chemical injection
Waste water Feed: Fats, vegetable oils
Waste water
This section process layout is licensor dependent
Pretreating
Waste water
Fuel gas
Air
Heavies
Figure 3 Due to feedstock variations, exotherm variations, and accuracy requirements for accurate reporting of yields, utility usage and raw materials, Coriolis meters are recommended for green diesel production flow measurement control
damage to the catalyst bed. Therefore, Coriolis meters are recommended for the reactor feed to recycle ratio and purge rate controls. Coriolis meters are also recommended for control of pre-feed treatment operations to remove contaminants that could harm catalysts in the reactor section. The pre-feed treatment operations mirror food and beverage manufacturing more so than traditional refining.
design. These variations result in inaccuracies impacting the unit mass balance, meeting production targets, and reactor control. The reactor control is especially important because the hydrodeoxygenation reaction is highly exothermic, and the exotherm varies based on feedstock, so accurate control of the target recycle to fresh feed ratio and the purge rates are critical to prevent temperature excursions and
Flaring 2.5%
Sulphur plant 1.8% H plant 5.8%
CRU c oke burn-o 0.36%
Delayed coking 0.21%
Fluid/exi-coking units 0.60%
FCC u nit c oke burn-o 23.5%
Coke calcining 0.101%
Asphalt blowing 0.94%
Other 3.1%
Combustion 63.3%
Blowdown 0.167%
Wastewater treatment 0.40% Storage tanks 0.30%
Cooling towers 0.002% Equipment leaks 0.013%
Figure 4 Contribution of different emission sources to the CO 2 equivalent GHG emission from petroleum refineries (Source: www.epa.gov/sites/production/files/2015-12/documents/refineries.pdf)
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