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1.5.2. Catalyst regeneration ................................................................................................................ 21
1.6.
E
FFLUENTS CHARACTERIZATION
.................................................................................................... 22
1.6.1. Normal operations ..................................................................................................................... 23
1.6.2. Intermittent operations ............................................................................................................. 24
1.6.3. Solid wastes ................................................................................................................................ 24
1.7.
E
MISSIONS REDUCTION PROPOSALS
............................................................................................... 25
2.
N
APHTHA ISOMERISATION
.............................................................................................................. 25
2.1.
P
URPOSE OF THE UNIT
..................................................................................................................... 25
2.2.
R
AW MATERIALS AND RESOURCES INPUT CHARACTERISTICS
........................................................ 25
2.2.1. Naphtha feeds ............................................................................................................................ 25
2.2.2. Hydrogen .................................................................................................................................... 26
2.2.3. Catalyst ....................................................................................................................................... 26
2.2.4. Dryers molecular sieves ............................................................................................................ 26
2.3.
P
RODUCTS CHARACTERISTICS
........................................................................................................ 26
2.4.
N
ORMAL OPERATIONS
.................................................................................................................... 26
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