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MerOx Sweetening Process.
Muhammad Fahad Khan
Engineer Operations
SWEETNING
 Conversion/Removal of Mercaptans (RSH), H2S
and elementary Sulfur present in Hydrocarbon
stream.
Types Of Sweetening
 Removal Process : Removal of Hazardous
Sulfur and sulfur containing compounds is called
Desulfurization.
 Conversion Process: Conversion of Mercaptans
through Oxygen is called Oxidation and the
Process is called Conversion.
Mercaptan’s Disadvantages
 Impart foul smell.
 Reduce Octane Number by reducing its
susceptibility to MMT.
 Elementary Sulfur and Presence of Mercaptans
Cause Corrosion.
 Pollute Environment.
 Dangerous to Human Health.
MerOx
 Stands for Mercaptans Oxidation.
 Mercaptans are Alkyl sulfide Halides (RSH)
 MerOx is Oxidation of Mercaptans to Alkyl
disulfides.
Types Of MerOx
 Fix Bed Process.
 Fix Bed Continuous Catalytic Process.
 Liquid/Liquid Counter Current Flow Process.
Liquid / Liquid Sweetening
 Hydro Carbon (containing Mercaptans), Air and
Caustic Containing dispersed MerOx catalyst are
simultaneously contacted in a mixer.
 Counter current flow of Caustic containing
Dispersed MerOx Catalyst (coming down) and
hydrocarbon (moving upward) in Reactor.
Fixed Bed Sweetening
 H2S free feed from Pre-Wash comes in contact
with Air in the presence of Catalyst in Reactor.
 Reactor contain Fix Bed of activated Charcoal
along with catalyst placed on Johnson Retaining
Screen.
Process
 MerOx Process completed in Three main Vessels.
 Vessel I (Pre- Wash).
 Vessel II (Reactor).
 Vessel III (Settler).
PRE-WASH (Vessel I)
 Contains Caustic Solution of Strength 3 to 5 mole
percent.
 50 to 60 percent level of Caustic Solution in Pre-
Wash.
 Product obtained from Pre-Wash, called Caustic
Washed Product.
Why to use Caustic (NaOH)???
 It has ability to dissolve low molecular weight
Mercaptans.
 It can dissolve H2S gas.
 It convert Mercaptans to Sodium Mercaptide
which is the intermediate Product.
Reactions at Pre-Wash
 RSH + NaOH NaSR + H2O
 H2S + NaOH Na2S + H2O
Na2S + H2S NaHS (Sodium Hydrosulfide)
60 % Level
3% Caustic Strength
LSRN Inlet
Caustic Washed LSRN
LSRN Distributer
Caustic/Water Inlet
Drain Point
Caustic Solution
(10 % Strength)
Pre-Wash Of LSRN
REACTOR (Vessel II)
It contain:
 Catalyst.
 Activated Charcoal.
 Bed Retaining Screen (Johnson Screen).
 Air.
Catalyst
 Metal (Iron) Chelate used as catalyst.
 Iron Chelate, catalyst to Rate of Reaction and
inhibitor to gum and peroxides formation.
 Per oxides formed due to reaction between Metals
and oxygen.
 Increase in catalyst concentration speed up the
Process.
Activated Charcoal
 It is used for bed formation.
 Iron Chelate diffuse on surface of Activated
charcoal to increase its surface area.
 Maximum exposure of Catalyst possible.
 Contact time increased.
Air (Oxygen)
 Air as a source of Oxygen.
 Air introduce at the inlet of Reactor along with
Caustic Washed Product.
 Air flow maintained according to Pre-Treatment
Graph.
Vent
Drain
Point
Caustic Washed
LSRN
Bed of MerOx
Catalyst and
Activated
Charcoal
Caustic
Circulation
Doctor Sweet
Product to
Settler
Reactor Of LSRN
Air
Reactions at Reactor
 NaSH + O2 Na2S2O3(Sodium thiosulfate)
 2NaSR + ½ O2 + H2O 2NaOH + RSSR
Caustic Regeneration
 In Reactor:
NaSR + ¼ O2 + ½ H2O NaOH + RSSR
Favorite Conditions for Regeneration of NaOH;
 High Temperature
 Increasing Amount of Air (according to Pre-Treatment Graph )
 Increasing contact time.
 Increasing catalyst concentration.
Overall Reactions
 RSH + NaOH + O2 RSSR + H2O + NaOH
 H2S + NaOH +O2 Na2S2O3 + H2O
SETTLER (Vessel III)
 Settling under gravity.
 Caustic level from 30 to 40 Percent.
 Caustic Strength from 10 to 12 mole Percent.
 Strength maintain for long because of
Regeneration of Caustic in Reactor.
Drain
Point
Doctor Sweet Product
along with Caustic from
Reactor
Caustic Level (40%)
Caustic Strength
(10%)
Caustic Circulation
Doctor Sweet Product to
Storage Tank
Settler Of LSRN
LSRN from Reformer / Storage
Doctor Sweet
ProductSettler
Caustic Circulation
Reactor
Excess Air
MerOx Catalyst
Strainer
Air
Pre-Wash
Drain Point
Dil. Caustic (3% Strength)
LSRN
Settling Tank
10% Caustic Strength
Process Flow Diagram of MerOx
Doctor Test
Take sample of sweet product in the tube.
Add approximately same amount of doctor solution
(Sodium plum bite).
Add small amount of Sulfur powder.
Shake the tube well.
If there is brownish color then the doctor test is
positive .
If the color of sulfur crystal remains unchanged then
the Test is Negative.
Steps in Case of Off Spec. Product
 Circulation of caustic from Settler to Reactor
should be carried out for at least half an hour.
 Darin exhaust Caustic from Pre-Wash and Settler
as and when required.
 If required Renew Caustic completely in both
Settler and Reactor.
 Hot Water Wash should be carried out.
 Re-Impregnation.
Thanks
Q & A

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MerOx

  • 1. MerOx Sweetening Process. Muhammad Fahad Khan Engineer Operations
  • 2. SWEETNING  Conversion/Removal of Mercaptans (RSH), H2S and elementary Sulfur present in Hydrocarbon stream.
  • 3. Types Of Sweetening  Removal Process : Removal of Hazardous Sulfur and sulfur containing compounds is called Desulfurization.  Conversion Process: Conversion of Mercaptans through Oxygen is called Oxidation and the Process is called Conversion.
  • 4. Mercaptan’s Disadvantages  Impart foul smell.  Reduce Octane Number by reducing its susceptibility to MMT.  Elementary Sulfur and Presence of Mercaptans Cause Corrosion.  Pollute Environment.  Dangerous to Human Health.
  • 5. MerOx  Stands for Mercaptans Oxidation.  Mercaptans are Alkyl sulfide Halides (RSH)  MerOx is Oxidation of Mercaptans to Alkyl disulfides.
  • 6. Types Of MerOx  Fix Bed Process.  Fix Bed Continuous Catalytic Process.  Liquid/Liquid Counter Current Flow Process.
  • 7. Liquid / Liquid Sweetening  Hydro Carbon (containing Mercaptans), Air and Caustic Containing dispersed MerOx catalyst are simultaneously contacted in a mixer.  Counter current flow of Caustic containing Dispersed MerOx Catalyst (coming down) and hydrocarbon (moving upward) in Reactor.
  • 8. Fixed Bed Sweetening  H2S free feed from Pre-Wash comes in contact with Air in the presence of Catalyst in Reactor.  Reactor contain Fix Bed of activated Charcoal along with catalyst placed on Johnson Retaining Screen.
  • 9. Process  MerOx Process completed in Three main Vessels.  Vessel I (Pre- Wash).  Vessel II (Reactor).  Vessel III (Settler).
  • 10. PRE-WASH (Vessel I)  Contains Caustic Solution of Strength 3 to 5 mole percent.  50 to 60 percent level of Caustic Solution in Pre- Wash.  Product obtained from Pre-Wash, called Caustic Washed Product.
  • 11. Why to use Caustic (NaOH)???  It has ability to dissolve low molecular weight Mercaptans.  It can dissolve H2S gas.  It convert Mercaptans to Sodium Mercaptide which is the intermediate Product.
  • 12. Reactions at Pre-Wash  RSH + NaOH NaSR + H2O  H2S + NaOH Na2S + H2O Na2S + H2S NaHS (Sodium Hydrosulfide)
  • 13. 60 % Level 3% Caustic Strength LSRN Inlet Caustic Washed LSRN LSRN Distributer Caustic/Water Inlet Drain Point Caustic Solution (10 % Strength) Pre-Wash Of LSRN
  • 14. REACTOR (Vessel II) It contain:  Catalyst.  Activated Charcoal.  Bed Retaining Screen (Johnson Screen).  Air.
  • 15. Catalyst  Metal (Iron) Chelate used as catalyst.  Iron Chelate, catalyst to Rate of Reaction and inhibitor to gum and peroxides formation.  Per oxides formed due to reaction between Metals and oxygen.  Increase in catalyst concentration speed up the Process.
  • 16. Activated Charcoal  It is used for bed formation.  Iron Chelate diffuse on surface of Activated charcoal to increase its surface area.  Maximum exposure of Catalyst possible.  Contact time increased.
  • 17. Air (Oxygen)  Air as a source of Oxygen.  Air introduce at the inlet of Reactor along with Caustic Washed Product.  Air flow maintained according to Pre-Treatment Graph.
  • 18. Vent Drain Point Caustic Washed LSRN Bed of MerOx Catalyst and Activated Charcoal Caustic Circulation Doctor Sweet Product to Settler Reactor Of LSRN Air
  • 19. Reactions at Reactor  NaSH + O2 Na2S2O3(Sodium thiosulfate)  2NaSR + ½ O2 + H2O 2NaOH + RSSR
  • 20. Caustic Regeneration  In Reactor: NaSR + ¼ O2 + ½ H2O NaOH + RSSR Favorite Conditions for Regeneration of NaOH;  High Temperature  Increasing Amount of Air (according to Pre-Treatment Graph )  Increasing contact time.  Increasing catalyst concentration.
  • 21. Overall Reactions  RSH + NaOH + O2 RSSR + H2O + NaOH  H2S + NaOH +O2 Na2S2O3 + H2O
  • 22. SETTLER (Vessel III)  Settling under gravity.  Caustic level from 30 to 40 Percent.  Caustic Strength from 10 to 12 mole Percent.  Strength maintain for long because of Regeneration of Caustic in Reactor.
  • 23. Drain Point Doctor Sweet Product along with Caustic from Reactor Caustic Level (40%) Caustic Strength (10%) Caustic Circulation Doctor Sweet Product to Storage Tank Settler Of LSRN
  • 24. LSRN from Reformer / Storage Doctor Sweet ProductSettler Caustic Circulation Reactor Excess Air MerOx Catalyst Strainer Air Pre-Wash Drain Point Dil. Caustic (3% Strength) LSRN Settling Tank 10% Caustic Strength Process Flow Diagram of MerOx
  • 25. Doctor Test Take sample of sweet product in the tube. Add approximately same amount of doctor solution (Sodium plum bite). Add small amount of Sulfur powder. Shake the tube well. If there is brownish color then the doctor test is positive . If the color of sulfur crystal remains unchanged then the Test is Negative.
  • 26. Steps in Case of Off Spec. Product  Circulation of caustic from Settler to Reactor should be carried out for at least half an hour.  Darin exhaust Caustic from Pre-Wash and Settler as and when required.  If required Renew Caustic completely in both Settler and Reactor.  Hot Water Wash should be carried out.  Re-Impregnation.