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Transcript of HAZOP
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From Chemical Dosing Tank (F100) to the Flash Separator (K200), passing through Pump J100
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Mixing
Agitator failure (1)
Temperature rise; salt’s properties alteration; vortex formation; paddle stirrers corrosion and/or erosion
Speed indicator (SIC100); mixing motor (M100); hand switch (HS100) (2)
Send a specialist to fix the motor in order to control the agitator’s velocity (3)
Low Mixing
As for (1); paddle stirrers corrosion and/or erosion
Desired homogeneity not achieved; pump’s erosion
As for (2) As for (3)
High Level
High feed rate to dosing tank (F100)
Flooding; pressure surges (4) Level transmitter (L100); manual drain connected to a valve (V100) (5)
Install a high level alarm; automatic switch of valve (V100) connected to level transmitter (L100)
Pump (J100) or valve (V101) failure
As for (4) As for (5); Flow controller (FC102); hand switch (HS102) (6)
Pump and valve regular maintenance; install a speed frequency controller (7)
Low Level
Low feed rate to dosing tank (F100)
Paddle stirrers corrosion; sludge formation (8)
Level transmitter (L100) Install a low level alarm
Pump (J100) racing As for (8) As for (6) As for (7)
High Flow
Pump (J100) racing Dosing tank (F100) pressure lost; flash separator (K200) pressure gain; low level on dosing tank; high level on flash separator (K200); pump (J100) cavitation
As for (6); valve (V103) and manual drain point – valve (V100)
Install a flow transmitter (9); pump regular maintenance (10)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Flow Pump (J100) racing; pump (J100) cavitation;
High level on dosing tank(F100); low level on flash separator (K200); dosing tank pressure gain; flash separator pressure lost (11)
As for (6) As for (9); as for (10)
Manual drain point failure (valve V100 failure : opened all time);
As for (11) As for (6) As for (9); valve regular maintenance (12)
Valve (V101,V102,NRV201) failure: obstructed route
As for (11) As for (6) As for (9); as for (12)
No Flow Pump (J100) failure As for (11); As for (6); manual drain point from valve (V100) (13)
As for (9);
Commissioning Wrong installation of an equipment or instrument such as a mixing motor, a pump or a valve
Dosing tank (F100) mixing motor failure; Pump (J100) failure; valve (V100, V101, V102, NRV201) failure
Chemical dosing tank mixing motor controller (SIC100)
Install a motor controller on pump J100; pump and valve regular maintenance (14)
Contaminants Paddle stirrers corrosion; pump (J100) corrosion; pump (J100) erosion;
Contaminate the solution; change solution’s properties;
No safeguards As for (14)
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From Pump J100 to the Pump J101 passing through the Feed Tank (F101)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Level Increase in the input flow on the feed tank (F101) due to the higher pump (J100) race
Flooding; pressure surges Hand switch on pump J100 (HS102); flow controller on pump J100 (FC102) (1); manual drain connected to a valve (V107); manual drain connected to a valve (V109) (2)
Install a level transmitter; install a high level alarm on the feed tank F101 (3); pump regular maintenance (4)
Pump (J101) or valve (V108) failure
Flooding; pressure surges As for (2); feed pump (J101) over temperature; feed pump (J101) motor controller
As for (3); install an automatic switch of valve (V107,V109) connected to level transmitter; as for (4); valve regular maintenance (5)
Low Level Low feed rate on the feed tank (F101) due to a failure on pump J100
Process inefficiency since the feed tank F101 is the mainly tank in the system (6)
As for (1); level switch indicating the feed tank F101 low level (LSL101) (7)
Increase the inlet flow of reagents (8)
Pump J101 failure As for (6) As for (7); feed pump (J101) over temperature; feed pump (J101) motor controller
As for (8)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Flow Pump (J100) racing Feed tank (F101) pressure gain; high level on feed tank (F101); pump (J101) cavitation
As for (1); manual drain connected to a valve (V107); manual drain connected to a valve (V109);
Install a flow transmitter
Low Flow Pump (J100) racing; valve V103 failure; pump (J100) cavitation
Feed tank (F101) pressure lost; low level on feed tank (F101) (9)
As for (1); Level switch indicating the feed tank F101 low level (LSL101) (10)
Pump and valve regular maintenance (11)
No Flow Pump (J100) failure; closed valve
As for (9) As for (10) As for (11)
High Concentration Pump J100 racing (12) Flash separator inefficiency (13)
Valve V103 and flow controller FC102 (14)
Install a flow transmitter before entering the feed tank (15)
Low Concentration
As for (12) As for (13) As for (14) As for (15)
Commissioning Wrong installation of an equipment such as a pump or a valve
Pump (J100,J101) failure; valve failure (V103,V107,V108,V109)
Feed pump (J101) over temperature alarm (TSH101)
As for (11)
Contaminants Pump (J100) corrosion; pump (J100) erosion; valve (V103,V108) corrosion due mechanical friction
Contaminate the solution; change solution’s properties
No safeguards As for (11)
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject Feed recycle loop from the Pump J101 back to the Feed Tank (F101)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Flow Pump (J101) racing Increase in the recycle flow (1) Feed pump (J101) over temperature sensor (TE101), feed pump (J101) motor controller (SIC101) and feed pump (J101) over temperature alarm (TSH101) (2)
Install a flow transmitter (3); pump regular maintenance (4)
Valve (V111,V112) failure: opened route
As for (1) The valve type can be considered a safeguard since a globe valve uses a plug closing against the flow being good for regulating flow while the ball valve has a gate that closes across the flow that is better for on/off control without pressure drop (5)
As for (3); valve regular maintenance (6)
Low Flow Pump (J101) racing; pump (J101) cavitation
Decrease in the recycle flow (6)
As for (2) As for (3)
Valve (V111, V112) failure: obstructed route
As for (6) As for (5) As for (4)
No Flow Pump (J101) or valve (V111,V112) failure
No recycle loop back to the feed tank (F101)
As for (2); as for (5)
Pump and valve maintenance (7)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Commissioning Wrong installation of an equipment such as a pump or a valve
Pump (J101) failure; valve failure (V111,V112)
As for (2) As for (7)
Contaminants Pump (J101) corrosion; pump (J101) erosion; valve (V111,V112) corrosion due mechanical friction
Contaminate the solution; change in solution’s properties
No safeguards As for (7)
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject Feed line from the Pump (J101) up to the Flash Separator (K200)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Flow Pump (J101) racing Feed tank (F101) pressure lost, flash separator (K200) pressure gain, low level on feed tank, high level on flash separator (K200) and pump (J101) cavitation (1)
Feed pump (J101) over temperature sensor (TE101), feed pump (J101) motor controller (SIC101) and feed pump (J101) over temperature alarm (TSH101) (2)
Install a flow controller, install a flow transmitter and pump regular maintenance (3)
Valve (V113, NRV200) failure: opened route
As for (1) No safeguards Install a flow controller; install a flow transmitter; valve regular maintenance (4)
Low Flow Pump (J101) racing; pump (J101) cavitation
Feed tank (F101) pressure gain, flash separator (K200) pressure lost, high level on feed tank and low level on flash separator (K200) (7)
As for (2) As for (3)
Valve (V113, NRV200) failure: obstructed route
As for (7) No safeguards As for (4)
No Flow Pump (J101) failure As for (7) As for (2) As for (3)
Valve (V113,NRV200) failure
As for (7) No safeguards As for (4)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From Storage Tank (R500) to the Feed Tank (F101)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Level (R500) Failure of pump J400 Flooding; high pressure on storage tank (R500)
Valve leaving the storage tank Install a level transmitter and controller on storage tank (R500), connected to pump J500
Low Level (F101) Failure of pump J500 (1) Inefficiency of the process since feed tank (F101) must always have a minimum level
Level control with pump J101 Install a level transmitter and controller on feed tank (F101), connected to pump J500 as a second alternative
High Flow As for (1) Level rise on feed tank (F101) and level drop on storage tank (R500)
Valves installed before and after pump J500 allow regular maintenance of the pump; flow transmitter (FT101) (2)
Regular maintenance of the pump (3)
Low Flow
As for (1) Failure to increase the level on feed tank (F101) and/or failure to decrease the level on storage tank (R500)
As for (2) As for (3)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Contaminants Corrosion/erosion of pump J500 and/or corrosion/erosion of valve leaving the storage tank (R500) and valve V106
Inefficiency of the process since it won’t have pure MEG
Valves installed before and after pump J500 allow regular maintenance of the pump
Regular maintenance of the valves and the pump
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From the Flash Separator (K200) to Valves V200, V201 and V203
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Temperature Failure in communication between controllers of the flash separator with controllers of the heat exchanger (H300) (1); overheat in the flash separator due to: heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212, TZAH212 malfunction
Change in solution and salt crystals properties; MEG degradation
Valve V204; instruments HS204, TT211, TIR211, TSH212, temperature sensors (TE211,TE212), high temperature alarm (TZAH212) and communication between controllers of the flash separator with controllers of the heat exchanger (H300); temperature sensor TE202 and transmitter TT202 could predict this outcome
Decrease the temperature by less steam input into the heat exchanger (H300); maintenance and, if that is the case, fixing of the pipelines
Low Temperature
As for (1); heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212, TZAH212 malfunction; malfunction of valves V309 and/or V310, PCV300
Inefficient MEG separation; lower salt concentration due to the higher presence of MEG, leading to a salt solution provided by the pipe containing the valve V203 with less salt than expected for the heating recycle flow, and probably more water and MEG
Instruments HS204, TT211, TIR211, TSH212; temperature sensors (TE211,TE212) and communication between controllers of the flash separator with controllers of the heat exchanger (H300)
Increase the temperature by more steam input on heat exchanger H300; maintenance and, if that is the case, fixing of the pipelines
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Pressure Failure of the vacuum system; high flow into the flash separator (K200) from heat exchanger (H300) and from the feed and dosing tank (F101 and F100 respectively) combined or not with failure (not opening) of the valves V200, V201, V202, V203 (2); malfunction of the safeguards related to pressure, temperature and level (3)
A flammable atmosphere at a temperature above the flash point may be created in the gas space within the Flash Separator, which can result in explosions
Valve V222; pressure instruments PI202, PT203, PIR203 and PIC203 connected to the pressure control valve PCV203; level instruments LT200, LTC200, LR200 and level controller LTC200 connected with heat exchanger (H300) controllers (4)
Use the valve V222 and the vacuum system, always avoiding sources of ignition anywhere within the flash separator (K200)
High Level As for (2); as for (3)
Can lead to a high pressure problem, as stated above; flooding
As for (4); valve V200 leading to a manual bleed point; flow transmitter FT200 and controller FCT200
Maintenance of the valves of the MEG Rig plant
Low Level
As for (3); pump racing (J300); low flow into the flash separator (K200) from heat exchanger (H300) and from the feed and dosing tank (F101 and F100 respectively) combined or not with failure (not closing) of the valves V200, V201, V202, V203, V302, V303, V305; failure (closure) of valve NRV200
Vortex breaker connected with valve V202 may not deliver the correct amount and concentration of solution for the heating recycle flow; corrosion of equipment
As for (4); flow transmitter FT200 and controller FCT200
Maintenance of the valves of the MEG Rig plant; fix the pump J300
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Static Build-up Presence of salts and variations in pressure, temperature and composition of liquid/gas
Source of ignition Instruments CT200, TI200, TIR200, CI200, CIR200
Correct concentration of salts into the solution
High Mixing Vortex formation due to vortex breaker malfunction
Vapour may go into the liquid, which make the separation process not as efficient as it would and should be
Vortex breaker located inside the Flash Separator (K200)
Maintenance and fixing of the vortex breaker
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From the Valve V202 to the Heat Exchanger (H300)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Temperature Overheat in the flash separator due to: heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212, TZAH212 malfunction; failure in communication between Controllers of the flash separator with controllers of the heat exchanger (H300) (1)
Change in solution and salt crystals properties; MEG degradation (2)
Valve V204; hand switch HS204; temperature instruments TT211, TIR211, TSH212; temperature sensors (TE211,TE212); communication between controllers of the flash separator with controllers of the heat exchanger (H300); high temperature alarm (TZAH212)
Decrease the temperature by less steam input into the heat exchanger (H300); maintenance and, if that is the case, fixing of the pipelines (3)
The overheat in flash separator (K200) leads to a high temperature liquid arriving into the recycle pump
As for (2) Temperature Instruments TE315, TSH315 and high temperature alarm (TZAH315)
As for (3)
Recycle pump (J300) racing (4)
High flow of a liquid with higher temperature
Temperature instruments TW322, TE322, TIR320, TDIR321, TIR322 and temperature controller TDCR321 (5)
Fix the recycle pump
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Temperature As for (1); heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212 malfunction; malfunction of valves V309 and/or V310, PCV300
Inefficient MEG separation; lower salt concentration due to the higher presence of MEG, leading to a salt solution provided by the pipe containing the valve V203 with less salt than expected for the heating recycle flow, and probably more water and MEG
As for (4); As for (5); temperature sensor (TE315)
Increase the temperature by more steam input on heat exchanger H300; maintenance and, if that is the case, fixing of the pipelines
High Flow As for (4) High flow into the heat exchanger (H300) may lead to an insufficient heating of the solution
Flow control instruments SIC300, SIR300, HS304, FT302, DIR302, FIR302, TIR323 (6); valves V303, V305 (leading to a manual drain point)
Maintenance and fixing of the pump, the last one only if it’s necessary
Low Flow
Low Level in Flash Separator (K200)
Pump failure As for (6); level controllers connected to the flash separator vessel (K200)
Look for problems related to the level of solution inside the flash
Recycle pump (J300) failure related to poor suction conditions
Cavitation; low flow into the heat exchanger (H300) may lead to a solution overheated; cavitation inside the recycle pump (J300)
As for (6) Maintenance and fixing of the pump, the last one only if it’s necessary
Drain leaking; valve jammed
Low flow into the heat exchanger (H300) may lead to a solution overheated; cavitation inside the recycle pump (J300)
As for (6) Maintenance of the pipeline, paying special attention to the valves V303 and V305, that shouldn’t be always opened, and the valve V302 that mustn’t be always jammed or closed
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Flow High concentration of salt due to low level inside the flash or errors related to the concentration of salt given by the dosing tank
Blockage of pump and/or valves; low flow into the heat exchanger (H300) may lead to a solution overheated; cavitation inside the recycle pump (J300)
As for (6) Maintenance of the system and attention to the concentration of salt measured in the bottom part of the flash separator
No Flow Recycle pump (J300) failure
Failure of all the heating system of the flash
As for (6) Fix the pump
Valve V302 jammed and not opening at all
Failure of all the heating system of the flash
As for (6) Change or maintenance of the valve V302
Gas locking due to presence of gas if the vortex breaker doesn’t work properly
Heating system inefficient As for (6) Maintenance of the vortex breaker
Reverse Flow Recycle pump (J300) failure (pump reversed)
Failure of all the heating system of the flash
As for (6) Fix the recycle pump (J300)
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From the Heat Exchanger (H300) to the Flash Separator (K200)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Temperature
Overheat in the flash separator due to: heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212, TZAH212 malfunction
Change in solution and salt crystals properties; MEG degradation; If the fluid is overheated, the flash separator (K200) may have its temperature risen, which can cause high pressure problems into the vessel
Valve V204; hand switch HS204; temperature instruments TT211, TIR211, TSH212; temperature sensors (TE211,TE212) (1); high temperature alarm (TZAH212); communication between controllers of the flash separator with controllers of the heat exchanger (H300) (2) temperature instruments TE315, TSH315, TW322, TE322, TIR320, TDIR321, TIR322, TW320, TE320, TW319, TE319, TSH319 and temperature controller TDCR321 (3); high temperature alarm TZAH315; high temperature alarm TZAH319; valve V205
Decrease the temperature by less steam input into the heat exchanger (H300); maintenance and, if that is the case, fixing of the pipelines
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Temperature Failure of communication among the following controllers: TDCR321, LTC200 and PCV300 (4)
If the fluid is overheated, the flash separator (K200) may have its temperature risen, which can degrade MEG and cause high pressure problems into the flash vessel as well (5)
Temperature controller TDCR321, temperature instruments TIR320, TDIR321, TIR322, TW320, TE320, TW319, TE319, TSH319 (6); high temperature alarm TZAH319 (7); valve V205 (8)
Maintenance and if it is necessary, change or fix the controllers
Failure (not opening) of valves V311, V312 and V313
As for (5) As for (6); as for (8)
Maintenance and if it is necessary, change of fix the valves
Low Temperature
As for (4) If the fluid is not hot enough, the flash separator (K200) may not be efficient to vaporize the MEG/water mixture (9)
Temperature instruments TW322, TE322, TIR320, TDIR321, TIR322, TW320, TE320, TW319, TE319, temperature controllers TDCR321 (10)
Maintenance and if it is necessary, change or fix the controllers
Failure (not closing) of valves V311, V312 and V313
As for (9) As for (10) Maintenance and if it is necessary, change of fix the valves
Not enough steam from building supply into the heat exchanger (H300) due to: pressure indicator PI204 malfunction; valves V309 and/or V310 jammed or fail to open
As for (9) As for (10); pressure indicator PI204
Maintenance and if it is necessary, change or fix the controllers and valves
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Temperature Heat exchanger (H300) and/or HS204, TE211, TT211, TIR211, TE212, TSH212, TZAH212 malfunction
Inefficient MEG separation; lower salt concentration due to the higher presence of MEG, leading to a salt solution provided by the pipe containing the valve V203 with less salt than expected for the heating recycle flow, and probably more water and MEG
As for (1); as for (2); as for (3)
Increase the temperature by more steam input on heat exchanger H300; maintenance and, if that is the case, fixing of the pipelines
High Flow Leak in heat exchanger (H300), promoting steam and solution mixture
Solution overheated, composition changed, ingress of steam can lead to presence of contaminants that can react with the solution or equipment, damaging the operation
Pressure indicator PI204; speed viewing device SG301; temperature instruments TE320, TW320, TW319, TE319, TSH319; high temperature alarm TZAH319; valve V205
Fix the heat exchanger
Recycle pump (J300) racing
As for (9); high flow into the heat exchanger (H300) may lead to an insufficient heating of the solution
As for (10); speed/frequency instruments SIC300, SIR300, hand switch HS304 and flow control instruments FT302, DIR302, FIR302, TIR323 (11); valves V303, V305 (leading to a manual drain point)
Maintenance and fixing of the pump, the last one only if it’s necessary
Low Flow
Low level in flash separator (K200)
Pump failure As for (11); level controllers connected to the flash separator Vessel (K200)
Look for problems related to the level of solution inside the flash
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Flow Recycle pump (J300) failure related to poor suction conditions
As for (5); cavitation; low flow into the heat exchanger (H300) may lead to a solution overheated, which can rise the pressure in the flash vessel (K200); cavitation inside the recycle pump (J300)
As for (6); as for (7); as for (11)
Maintenance and fixing of the pump, the last one only if it’s necessary
High concentration of salt due to low level inside the flash or errors related to the concentration of salt given by the dosing tank
As for (5); blockage of pump and/or valves; low flow into the heat exchanger (H300) may lead to a solution overheated, which can rise the pressure in the flash vessel (K200)
As for (6); as for (7); as for (11)
Maintenance of the system and attention to the concentration of salt measured in the bottom part of the flash separator
Valve V205 malfunction, half or completely opened when it shouldn’t be
Less volume of heated solution into the flash vessel can lead to an inefficient separation of MEG/water from salt
Level controller LTC200 and level recorder LR200 (12)
Maintenance and if it is necessary, fix the valve
Drain leaking
As for (5); low flow into the heat exchanger (H300) may lead to a solution overheated, which can rise the pressure in the flash vessel (K200);
Flow control instruments FT302, DIR302, FIR302, TIR323
Check valves V303 and V305
No Flow Valve V302, V304 or V204 jammed and not opening at all
Failure of all the heating system of the flash (13)
As for (11) Change or maintenance of the valve V302
Gas locking due to presence of gas if the vortex breaker doesn’t work properly
As for (13) As for (11) Maintenance of the vortex breaker
Heat exchanger (H300) leaking all the fluid outside the system
As for (13) As for (12) Fix or change the heat exchanger (H300)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Reverse Flow
Recycle pump (J300) reversed
As for (13) As for (12) Maintenance of the plant
High Pressure
High temperature Rise of pressure in the flash separator (K200)
As for (6); as for (7); as for (8)
Use valve V222 and check possible problems in the plant that led to high temperature
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From the Separation Column (E200) to the Bleed Down (R403) and the Sampling Receiver (R404)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High temperature Overheat in the flash separator
Change in solution and salt crystals properties; MEG degradation
Temperature sensors (TE306,TE308,TE310,TE312); high temperature alarms (TZAH306,TZAH308,TZAH310, 312)
Decrease the temperature by less steam input on heat exchanger H300
Low temperature Flash separator temperature under set point
Inefficient MEG separation; lower salt concentration due to the higher presence of MEG
Temperature sensors (TE306,308,310,312); sampling receiver (R404)
Increase the temperature by more steam input on heat exchanger H300
High level Blockage in separation column due to incrustation and/or salt accumulation
Flooding; corrosion; erosion; break of salt loop operation.
Bleed down (R403); high level alarms (LZAH300, LZAH301,LZAH302,LZAH303)
Regular maintenance of the separation column (E200)
High pressure testing Failure in vacuum pump (J200); failure in valves V409 and/or V411
No testing (no sample collection due to the lack of pressure difference). The separation column (E200) will be at the same pressure as the bleed down (R403) and the sampling receiver (R404)
Pressure indicators (PI400,PI401,PI402,PI403).
Install high pressure alarms; vacuum pump (J200) regular maintenance; valves V409 and V411 regular maintenance
High speed Motor malfunction (M300,301,302,303) (1)
Motor temperature rise; vortex formation
Temperature controllers (TIC305,307,309,311); hand switches (HS300,HS301,HS302,HS303)
Motor (M300,M301,M302, M303) regular maintenance (2)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low speed As for (1) Insufficient wash of the MEG residue from the salts
Conductivity transmitters (CT300,CT301,CT302, CT303,CT304); sampling receiver (R404) to analyse MEG concentration
As for (2)
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject Salt loop (from R400 to R401 and back to R400)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
No Flow No feed to salt tank
No production of brine (1); column full of salt
Conductivity control in the column
Install level alarm on R400 (2)
Pump J401 failure
As for (1)
Speed frequency control, temperature control and pressure control in the pump
As for (2); regular maintenance in the pump
No water feed into the brine tank; valve V428 closed in error
As for (1); high salt concentration in the stream
Flow rate transmitters (FT400,401,402)
Regular maintenance in the valve (3); install level alarm on R401; composition transmitter in pipelines
Line blockage/closed valve
As for (1); overload of the pump J401
Temperature sensor (TE403); FT400,FT401,FT402
Regular maintenance in the valves
Line fracture As for (1); leakage
FT400,FT401,FT402 Regular inspection in the lines
High Flow Pump J401 racing Low level of salt tank; high pressure stream in brine tank; low pressure in salt tank; pump temperature rise
Speed frequency control, temperature control and pressure control in the pump; manual drain; FT400,FT401,FT402
Regular maintenance in the pump (4); open valves V416, V419 or V420
Low Flow Pump J401 failure
Low production of brine (5)
Speed frequency control, temperature control, pressure control in the pump; FT400,FT401,FT402
As for (4)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Flow Sedimentation of salts in pipes
As for (5); line blockage; change in desired fluid properties and concentration
FT400,FT401,FT402 Regular inspection in the lines; install composition transmitter in pipelines
Low water influx to R401
As for (5) Flow transmitter (FT402) Increase water feed
High Concentration Low water feed to R401
As for (5) FT402 Increase water feed; install composition transmitter in pipelines
Low Concentration High water feed to R401
Change in desired fluid properties (6)
FT402 Decrease water feed
J401 failure
As for (5); as for (6)
Speed frequency control; temperature control; pressure control in the pump
As for (4)
High Level (R400) High feed to R400 from the column
Flooding in R400 (7) Conductivity control in the column; manual drain point (V416)
Install high level alarm in R400 (8); open drain point
High feed from brine tank
As for (7)
FT400; Manual drain point (V416)
As for (8); open drain point
J401 failure
As for (7)
Speed frequency control, temperature control and pressure control in the pump; manual drain point (V416 and V419)
As for (4); as for (8); open drain point
Line blockage As for (7) FT400,FT401,FT402; manual drain point (V416, V419 and V420)
As for (8); regular inspection in the lines; open drain point
High Level (R401)
High water feed
Flooding in R401 and change in brine composition (9)
FT402; manual drain point (V425); valves V428 and V429
Install high level alarm in R401 (10); open drain point; close V428 or V429
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Level (R401) High feed from salt tank (J401 racing)
As for (9); pump temperature rise
Speed frequency control, temperature control, pressure control in the pump; manual drain point (V425); valve V417
As for (4); as for (10); close V417; open drain point
Low Level (R400) Low feed from the column
Change in brine composition (11)
Conductivity control in the column; level switches in column
Install low level alarm in R400 (12)
Low feed from brine tank
As for (11)
FT400
As for (12)
J401 racing
As for (11); pump temperature rise
Speed frequency control, temperature control, pressure control in the pump
As for (12)
Low Level (R401) Low water feed
As for (11); accumulation of salt in pipelines
FT402
As for (12); increase water feed
Low feed from salt tank (J401 failure)
As for (11) Speed frequency control, temperature control and pressure control in the pump
As for (12); regular maintenance in the pump
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From the Flash Separator (K200), to the Condensate Separator Tank (K300) passing through condenser C201 and sub-cooler C301
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Flow
Pump (J200) racing Inefficient process of condensation in condenser C201 and sub-cooler C301 (1); leak in condenser C201 and sub-cooler C301; flash separator (K200) pressure loss
Hand switch (HS200); vacuum control valve PCV203 (2)
Install a speed frequency controller in pump J200 and a flow transmitter (3)
Low Flow Pump (J200) failure Flash separator (K200) pressure gain; cavitation in pipelines; presence of foreign body from corrosion; sedimentation; leak in condenser C201 and sub-cooler C301
As for (2) As for (3); regular maintenance of condensers
High Temperature Low/no flow of chilled water input on condenser C201 and sub-cooler C301; valves jammed (V221 and V306)
As for (1); change in solution properties (4)
Flow indicators (FI202,301); temperature sensors (TE204,205,316,317), transmitters (TT204,205,316,317) and indicators & recorders (TIR204,205,316,317) (5)
Install a flow controller in the chilled water feed associated with the temperature indicators & recorders (TIR204,316) (6)
Low temperature High flow of chilled water input on condenser C201 and sub-cooler C301
As for (4) As for (5)
As for (6)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Pressure Failure of condenser C201 and/or sub-cooler C301 in cooling the solution of MEG/water
Insufficient MEG/water solution recovered; high pressure in condensate separator tank (K300)
No safeguards Install a high pressure alarm; install a pressure indicator on K300
HAZOP RECORD FORM Facility/Project MEG Reclamation Pilot Plant
Drawing No./Procedure 26164_P&ID_001
Subject From Condenser 201 to Storage Tank (R500), passing through Vacuum Trap (K201), Vacuum Receiver (K202) and Condensate Separator Tank (K300)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Temperature No ventilation around the J200 pump
Pump damage and/or malfunction (1)
Ventilated place without hot surfaces for the J200 pump work
Install temperature indicator in the pump (2)
No ventilation around the J400 pump
As for (1) Ventilated place without hot surfaces for the J400 pump work
As for (2)
Failure of sub-cooler C301, leading J400 pump to heat
As for (1) Temperature indicators TW318, TE318, TT318, TIR318, valve V431
Regular maintenance of sub-cooler C301
Low Temperature Cold fluid entrance in J200 pump
J200 pump damage, condensing fluid
Presence of vacuum trap K200 and receiver K201
Temperature control of the air entering the pump
High Pressure Obstruction in the line connected to the J200 pump
Pump damage; failure of J200 to provide vacuum
Valves V213 and V214,; vacuum trap K200 and receiver K201 (3)
Install relief valve downstream from the pump (4)
Liquid entrance in the J200
J200 pump damage, lubrication oil compromised
As for (3) Install extra pressure indicator/controller
Water vapour entrance above J200 pump capacity
Condensing fluid dissolves in pump oil; pump corrosion
As for (3) No action
Obstruction in the line connected to the J400 pump
Pump damage; failure of J400 to drive the MEG/water liquid mixture
No safeguards
As for (4)
Date 10/12/2014
Team Members Ana Carmem G. B.; Ana Maria G. L.; Bernardo de Sa R.; Gabriel V. S.; Gabriela F. F.; Maximiano K. F.; Raphael de Souza R.
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Low Pressure
Narrow diameter pipes Low flow and poor efficiency of J200
Vacuum control valve PCV203 Correct dimensioned pipes
High flow in J400 pump, stoking so fast that the fluid can’t be pulled or sucked into the chamber as fast as the diaphragm is withdrawing, lowering pressure
Risk of J400 pump to air suction; cavitation
Hand switch HS400 Regular maintenance (5)
Failure of Vent Failure of vent to drive the output of J200 pump
Rise in J200 pump temperature and pressure
Vent to a safe location As for (5)
Failure of Power Electrical failure of hand switch HS200
Failure of J200 to provide vacuum and drive the MEG/water mixture (6)
Computer monitoring of the hand switch
Install backup generator; check the connection between the switch and the J200 pump
Electrical failure of hand switch HS400
Failure of J400 to drive the MEG/water mixture (7)
Computer monitoring of the hand switch
Install backup generator; check the connection between the switch and the J400 pump
Failure of Vacuum Internal/component problem of J200 pump
As for (6) Respect the working conditions, lifetime and lubrication of the pump
Regular maintenance, testing and lubrication
Obstruction in line near J200 pump
As for (6) No safeguards
As for (4)
Failure of valves V411 or V409
Failure of J200 to provide vacuum to bleed down R403 and sampling receiver R404
Pressure indicators PI400, PI401, PI402, PI403
As for (5)
Reverse Flow
Failure of J400 diaphragm pump internal check valves
As for (7)
No safeguards Install check valve before the entrance of the J400 pump
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
Reverse Flow Sudden power cut to J200 pump leads to low inertial force of rotating parts, that can’t overcome system head (blowback)
As for (6)
No safeguards Install check valve before the entrance of J200
No Flow Overpressure in pipeline; failure of vacuum
As for (6) As for (3) Install extra pressure indicator/controller
Line blockage near J200 pump
As for (6) As for (3) As for (4)
Line blockage near J400 pump
Danger to the process stability and continuation, as it stops the MEG/water drive
No safeguards As for (4)
Vapour appearance near J400 pump, cavitation
Pump damage, stop to the process
Speed indicator controller SIC400 (8)
Install temperature indicator
High Flow Failure of valve V222 Vacuum control valve PCV203 won’t control the adequate level of vacuum (9)
Hand switch HS200 (10) Install flow rate controller/transmitter (11)
Failure of vacuum control valve PCV203
As for (9) As for (10) As for (11)
Failure of speed indicator controller SIC400
Risk of J400 pump to air suction, cavitation
Hand switch HS400 As for (5)
Low Flow Partial blockage near J200 pump
As for (6) Vacuum control valve PCV203 As for (11)
J200 pump malfunction As for (6) Vacuum control valve PCV203 As for (11)
Partial blockage near J400 pump
As for (7) As (8) As for (5)
J400 pump malfunction As for (7) As (8) As for (5)
Failure of speed indicator controller SIC400 (jammed low)
Low J400 pump efficiency No safeguards As for (5)
DEVIATION CAUSE EFFECT SAFEGUARDS ACTION
Contaminants Failure of sintered filter Z203, allowing contaminated air to enter the vacuum system
As for (1)
Valve V205
As for (5)
Water or any other liquid entering the pump J200
As for (1) As for (3) As for (5)
Contaminant in the oil lubricant of the J200 pump
As for (1) Check lubricant and clean filters regularly, replace when necessary
As for (5)
Contaminant in the oil lubricant of the J400 pump
As for (1) Check oil level and clean filters regularly, replace when necessary
As for (5)
Corrosion of vessels or instrument near J400 pump, contaminating fluid
As for (1)
Valve V205
As for (5)
High Concentration Condenser C201, flash separator K200 or mixing tank F101 failure
High concentration of MEG/water vapour (>90%) causes J200 pump to fail to drive the mixture
Temperature indicators and transmitters in the condenser C201 and flash separator K200 (12)
As for (5)
Low Concentration Condenser C201, flash separator K200 or mixing tank F101 failure
Low concentration of MEG/water vapour (<20%) causes J200 pump to fail to drive the mixture
As for (12) As for (5)
High Level Failure of valve V213 to open
High level of liquid in K201 vacuum trap, danger to J200 pump
Valve V205; vacuum control valve PCV203 (13)
Install level indicator (14)
Failure of valve V214 to open
High level of liquid in K202 vacuum receiver, danger to J200 pump
As for (13) As for (14)
Failure of valve V412 to open
High level in R403 bleed down, unable to take sample
Valves V408 and V433 As for (14)
DEVIATION
CAUSE EFFECT SAFEGUARDS ACTION
High Level Failure of valve V413 to open
High level in R404 sampling receiver unable to take sample
Valves V410 and V434 As for (14)
Failure of speed indicator controller SIC400, lowering speed of J400 pump
High level in condensate separator tank K300
Valve V307; level indicators LSL305 and LSL306
As for (5)
Failure of discharge valve after storage tank R500
High level in storage tank R500
Valves V431 and V432 As for (14)