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KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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Page 1: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

KHABAROVSK REFINERYHYDROPROCESSING PROJECT

ARU / SWS – CONTROL SYSTEM and ESD

APRIL 29th – MAY 3rd 2013, MADRID, SPAIN

TRAINING COURSE

Page 2: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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CONTROL SYSTEM

The purpose of this section is to give a general explanation of how the control system works.

Process variables, that determine a good operation of the Unit, play a different role depending upon the type of operation.

Page 3: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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MAIN CONTROL LOOPS OF AMINE REGENERATOR AND SOUR WATER STRIPPER

SECTIONS

1. RICH AMINE FLASH DRUM PRESSURE2. REGENERATOR REFLUX DRUM PRESSURE3. STEAM FLOWRATE TO STRIPPER REBOILER4. SOUR WATER STRIPPER PRESSURE5. SOUR WATER STRIPPER TEMPERATURE6. SOUR WATER FEED SURGE DRUM PRESSURE

Page 4: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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RICH AMINE FLASH DRUM PRESSURE

With the purpose to avoid amine degradation caused by the oxidation of the DEA solution coming into contact with air, inert gas blanketing facilities are provided.The pressure in the drum is controlled by the pressure controller PIC-1001 acting on two control valves: vent gas valve PV-1001A and inert gas valve PV-1001B.

Page 5: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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RICH AMINE FLASH DRUM PRESSURE

Split range valves

Some control loops have two control valves controlled by one controller.A plot shows the valve position versus controller output.

Provide 5% deadband to prevent simultaneous pressuring and venting.

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REGENERATOR REFLUX DRUM PRESSUREThe pressure in the drum is controlled by the pressure controller PIC-1005 acting on two control valves:

PV-1005A located on the line that leads acid gas to SRU Section andPV-1005B located on the line to acid flare.

Page 7: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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Split range valves

Provide 5% deadband to prevent system malfunction.

REGENERATOR REFLUX DRUM PRESSURE

Page 8: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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STEAM FLOWRATE TO STRIPPER REBOILERThe higher is the flowrate of sour water fed to the stripper, the higher the saturated steam flowrate to the Reboiler must be.

The steam flow rate to the Stripper Reboiler is controlled on the basis of the measured flow of the spur water solution entering the Stripper column.

The flowrate of SW to the column is regulated by the flow controller FIC located on the discharge line of Stripper Feed Pump, that acts on the flow valve FV located on the column feed stream and that receives a signal from the level controller LIC located on Sour Water Feed Surge Drum.

The stripping steam is generated in the Stripper Reboiler by means of LP Steam, whose flow is controlled by the flow controller FIC-2019 acting on FV on the LP Steam line. The FIC-2019 set point is resetted by the signal coming from FIC-2002.

Page 9: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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SOUR WATER STRIPPER PRESSURE

The overhead pressure in the column is controlled by the pressure controller PIC-2002 acting on two control valves:

PV-2002A located on the line that leads acid gas to SRU Section and

PV-2002B located on the line to acid flare.

Page 10: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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Split range valves

Provide 5% deadband to prevent system malfunction.

SOUR WATER STRIPPER PRESSURE

Page 11: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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SOUR WATER STRIPPER TEMPERATURE

The overhead pressure in the stripper sets the stripped water temperature in the stripper bottom at the right value, so as to obtain a good performance.

The overhead temperature in the Stripper is controlled by TIC-2007, which resets the flow controller FIC-2007 acting on the flow valve FV-2007 on the delivery line of the Stripper Pumparound Pump.

Page 12: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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Split range valves

Provide 5% deadband to prevent system malfunction.

SOUR WATER STRIPPER TEMPERATURE

Page 13: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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The pressure in the drum is controlled by the pressure controller PIC-2001 acting on two control valves:

PV-2001A located on the inert gas line and PV-2001B located on the line to acid flare.

SOUR WATER FEED SURGE DRUM PRESSURE

Page 14: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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Split range valves

Provide 5% deadband to prevent simultaneous pressuring and discharging.

SOUR WATER FEED SURGE DRUM PRESSURE

Page 15: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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LOGIC SYSTEM

What is the LOGIC SYSTEM?

A Logic System is an integrated highly automated safety facility, able to perform several actions:

Handling all the start-up and shut-down phases of the Plant;

Isolate the whole plant, one unit of the plant from the other, or just a section of one unit;

Interact with the DCS system;

Keep always the Plant under safe conditions.

Page 16: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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LOGIC SYSTEM

HOW DOES IT WORK?

The working principle of a Logic System is:

INPUTINPUT: Upset signal from the Plant

OUTPUTOUTPUT: One or more actions performed automatically on valves, equipment, …

MAIN FUNCTIONS OF A LOGIC SYSTEM

Shut-Down Procedure

Start-Up Procedure

Avoid Upset conditions during normal operation that could damage the personnel or the equipment

Page 17: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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LOGIC SYSTEM

MAIN FEATURES OF LOGIC SYSTEM

All the logics are handled by a central hardware called PLC (programmable logic control)

Input/output signals of PLC are usually electrical, not digital.

PLC input signals: output signals from instrumentation installed in the plant.

PLC output signals: input signals for SD, ESD, control valves.

Page 18: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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LOGIC SYSTEM – START UP

When starting-up a section of a plant, the logic system shall strictly follow a well determined procedure.

This procedure is tied to verify the necessary conditions, in order to guarantee the safety of the operation.

These conditions are called PERMISSIVES.

Page 19: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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PERMISSIVE DURING START-UP

HOW IS A START-UP PERFORMED?

Start-up is guided and monitored by well competent operators and specialist engineers.

Start-up must be performed both from field and control room.

The operators in control room shall monitor the start-up via graphic pages.

Page 20: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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PERMISSIVE DURING START-UP

On the graphic pages, the whole plant is graphically represented:

- Equipment- Instruments- SD, ESD, control valves- Control loops- Alarms and SD causes

Furthermore, in the graphic pages the operator can check if all the logic conditions necessary for the start-up are met.

If some of the required permissives are not met, the logic system doesn’t give its permission to start-up.

Page 21: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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CAUSE & EFFECT DIAGRAM

The protective system (ESD) shall be based on the input (causes) and the output (effects) as shown in the Cause & Effect Chart

Page 22: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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ARU SECTION – ESD SYSTEM

Page 23: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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SWS SECTION – ESD SYSTEM

Page 24: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

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RomeRome

Viale Castello della Magliana 75Viale Castello della Magliana 7500148 - Italy00148 - Italy

Ph. +39 06 602161Ph. +39 06 602161Fax +39 06 65793002Fax +39 06 65793002

[email protected][email protected] – www.tecnimontkt.it

Page 25: KHABAROVSK REFINERY HYDROPROCESSING PROJECT ARU / SWS – CONTROL SYSTEM and ESD APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE

THANK YOU FOR THE ATTENTION