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2nd Assignment - Furnace(1)

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PROCESS SECTION DATE NODE 100

NO PARAMETER Guide Words Deviation posssible causes possible consequences

Safe Guard/Prote ction

Action required/Recommendation

1 PRESSURE MORE - MORE - PRESSUREcontinously high flame

to the furnace.

Piping/tube thermal shock and craking lead to leakage of the heating oil to the furnace and get contact with the flame and resulting to high temperature in furnace cause cracking and Explosion

PIC 1, PT-1, PI-4, PI-5

High Alarm, High-high Alarm, fuel gas valve

malfuction - more fuel gas into the furnace

More fuel gas in the furnace, lead to high temperature in normal operation and may cause explosion during start-up.

PI 3, PI 6 & FI 3

Fuel gas control valve - fail close Interlock shut off valve Pressure Safety Valve to flare Explosion at furnace stack or Fuel gas release to

atmosphere in normal operation

PI 3, PI 6, FI 3 & AT-1

Fuel gas control valve - fail close Interlock shut off valve Pressure Safety Valve to flare Flue gas control valve,

PIC 1 malfaction - close position

High temperature of hot oil to reboiler, Distillation column experience high pressure that possible to crack and explosion.

- Pressure Safety Valve to flare Air supply to the

furnace high flow & pressure

FT 2 & PI 2 Flow Recordable Control Alarm (FRCA) link to fuel control sytem

2 PRESSURE LESS - LESS - PRESSURE

Less combustion (May caused by either less air pressure or less fuel gas)

The oil has not been heating up. The reboiler not reboil the HC, the distillation flooding, liquid HC over flow to the upper stream of distillation column.

PIC 1, PT-1, PI-4, PI-5 Pressure Low Alarm Less air pressure to

furnace for combustion

More fuel gas in the furnace, lead to explosion especially during start-up or fuel gas release to atmosphere through stack due to low combustion

FT 2 & PI 2 Additional one parallel air compressor by automatic cut in. Less fuel gas to the

furnace

The oil has not been heating up. The reboiler not reboil the HC, the distillation flooding, liquid HC over flow to the upper stream of distillation column.

FI 3, PI 3 & PI 6 and bypass valve

Flow Low alarm 3 TEMPERATURE MORE - MORE -

TEMPERATURE

High flame in the furnace (high fuel and air)

Piping/tube crack or burst due to overheating, mixture of oil burn and cause black smoke release TI 8

Automatic shut down heater on low air flow and/or low air/fuel ratio. High coke in furnace and piping, less heat transfer TI 8 Maintenance (cleaning) less hot oil flow to the

tubing (less heat transfer )

Thermal craking to the furnace - fuel gas release can cause

a jet fire FT 1 BCPS link to FT 1 and Low flow alarm

TEMPERATURE LESS - LESS - TEMPERATURE

No ignition and No flame in the furnace

High Fuel gas in the furnace - when it ignited it will exploded during start-up pilot light

Temperature alarm low, additional one pilot light , automatic cut off the fuel and air supply

No heat transfer to Hot oil - No heating to reboiler of the distalltion column, if the Feed of the distillation is liquid, the distillation will flooding

pilot light

Temperature alarm low, additional one pilot light , automatic cut off the fuel and air supply

No air Flow High Fuel gas in the furnace - when it ignited it will exploded FT 2, PI 2

Air Flow Alarm Low and automatic shut down the fuel supply on low air flow and/or low air/fuel ratio. No fuel flow

No heat transfer to Hot oil - No heating to reboiler of the distalltion column, if the Feed of the distillation is liquid, the distillation will flooding

FI 3

Fuel Flow Alarm Low and automatic shut down the air supply on low air flow and/or low air/fuel ratio.

COMPOSITION NOT CORRECT - NOT CORRECT - COMPOSITION

not corret stoikometri for perfect combustion of fuel gas

High black smoke release to Atmosphere. - Automatic shut down the heater on low air flow and/or low air/fuel ratio. Less heat transfer to the hot oil tubing/piping, less

separation in distillation column, can lead to tower flooding,

4 OTHERS

VALVE

fuel gas valve malfuction - cause leakage to furnace. un-adequate maintenance of valve and instrument

explosion when fuel gas over filling in the furnace with out combustion, and operator tried to start up the plant.

PILOT LIGHT no pilot light

un-adequate maintenance of valve and instrument

explosion when main firing started. Periodic Maintenance explosion when the enough pressure of fuel gas in the

furnace MAINTENANCE un adequate maintenance of Piping and instrumentation

Budget Control and un-aware of the risk

Instrument malfunction - lead to false reading and indication and can lead to Explosion. Piping will crack Furnace will crack

SHUT DOWN & START UP

Not follow Procedure Human Factor

Explosion can happen if not following the SU and SD procedure.

HAZOP STUDY

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

(2)

PROCESS Section

Date

NODE

200

NO PARAMETER Guide Words Deviation

FLOW

MORE - MORE - FLOW

LESS - LESS - FLOW

NO - NO - FLOW

OTHERS THAN

VALVE Valve malfuction

MAINTENANCE SHUT DOWN &

START UP Not follow Procedure

HAZOP STUDY

Air line supply to the furnace

(3)

posssible causes possible consequences Safe Guard/Protection

the valve or control valve malfuction air to fuel ratio not as per

stoikiometric, FT 2

high presure in the

furnace PT 1, PI 4 & PI 5

more gas rushing out to

atm, PIC 1

piping leaking

air to fuel ratio not as per stoikiometric, more fuel coming out from the stack can cause

detonation/explosion

FT 2 & PI 2

piping leaking

pump/compressor failure

Piping blockage/valve malfuction

un-edequate maintenance air supply to actuator block controller malfuction cost cutting

equipment malfuction and error can occurred may lead to explosion Human Factor

Explosion can happen if not following the SU and SD procedure.

HAZOP STUDY

Air line supply to the furnace

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

more fuel gas in the furnace can cause explosion

more flow or no flow of air to furnace

(4)

action required/Recommendation

Air Flow Alarm Low and automatic shut down the fuel supply or heater on low air flow and/or low air/fuel ratio.

Periodic Piping inspection, Risk based inspection (RBI)

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

Air Flow Alarm Low and automatic shut down the fuel supply or heater on

(5)

PROCESS section

date

study node

300

NO PARAMETER Guide Words Deviation

1 PRESSURE MORE - MORE - PRESSURE

LESS - LESS - PRESSURE

NO - NO -PRESSURE

3 TEMPERATURE MORE - MORE - TEMPERATURE

4 FLOW REVERSE - REVERSE - FLOW

MORE - MORE - FLOW

LESS - LESS - FLOW

NO - NO - FLOW

OTHERS THAN

VALVE Valve malfuction

MAINTENANCE SHUT DOWN &

START UP Not follow Procedure

HAZOP STUDY

Fuel gas line supply to Furnace

(6)
(7)

posssible causes possible consequences

Safe

Guard/Protectio n

Fuel gas control valve malfunction

more fuel in the furnace, can cause explosion during start-up

PI 3 & PI 6

piping leaking valve malfuction valve malfuction piping leaking

external heating cause the

gas expanded explosion when enter furnace. TI 11

Fuel gas control valve malfunction - fully open

more fuel in the furnace, can cause explosion

FI 3

piping leaking valve malfuction

un-edequate maintenance air supply to actuator block controller malfuction

cost cutting equipment malfuction and error can

occurred may lead to explosion

Human Factor Explosion can happen if not following the

SU and SD procedure.

more flow or no flow to furnace

PI 3 & PI 6

FI 3

HAZOP STUDY

Fuel gas line supply to Furnace

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

more air in the furnace, no enough heat to heat up hot oil to desired

temperature.

more air in the furnace, no enough heat to heat up hot oil to desired

(8)
(9)

Action required/Recommendation

Fuel Pressure Alarm High and automatic shut down the fuel supply or heater on low air low air/fuel ratio or high fuel supply

Automatic shut down fuel gas supply and heater

Fuel control valve - Fail close Fuel Flow Alarm High and automatic shut down the fuel supply or heater on low air

low air/fuel ratio or high fuel supply Fuel Perssure Alarm Low and automatic shut

down heater if Alarm Low Low triggered.

Fuel Flow Alarm Low

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

(10)
(11)

PROCESS section date

study node

400

NO PARAMETER Guide Words Deviation

1

PRESSURE MORE - MORE - PRESSURE

LESS - LESS - PRESSURE

NO - NO -PRESSURE

2

TEMPERATURE MORE - MORE - TEMPERATURE

3

LESS - LESS - TEMPERATURE

4

UN-EVEN TEMP

5

COMPOSITION OTHERS THEN - OTHERS THEN - COMPOSITION

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

HAZOP STUDY

(12)

FLOW LESS - LESS - FLOW

NO - NO - FLOW

OTHERS THAN

VALVE Valve malfuction

MAINTENANCE

(13)

posssible causes possible consequences Safe Guard/Protection

HC from reboiler leaking into heating oil tube

Possible fie inside the tube and lead to explosion of tube and burst heating oil burn in furnace - black smoke ,

less heating oil to reboiler - column flooding with HC

high combustion in furnace - more fuel and air

distillation column high pressure and

can cause explosion. TI 1 ~ TI 10 (exclude TI 8)

Low combustion in furnace column flooding with liquid HC TI 1 ~ TI 10 (exclude TI 8)

coking in the tubing piping craking and less flow to

reboiler TI 1 ~ TI 10 (exclude TI 8)

HC leaking to the heating oil, Reboiler crack, or tube cracking

Possible fire inside the tube and lead to explosion of tube and burst

-Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

piping leaking - in the furnace

HAZOP STUDY

(14)

High moisture content tube hammmering

-piping leaking to furnace heating oil burn in furnace - black smoke ,

coking in tubing column flooding with liquid HC

-piping leaking FT 1

pump failure

Piping blockage/valve malfuction

un-edequate maintenance air supply to actuator block controller malfuction

cost cutting equipment malfuction and error can

occurred may lead to explosion

Human Factor Explosion can happen if not following

the SU and SD procedure.

more flow or no flow of to furnace, no heating reboiler

(15)

Action required/Recom mendation Indication of pressure at tube Indication of pressure at tube Indication of pressure at tube Temperature High Alarm and automatic shut down the heater if Temperature Alarm High High Temperature Alarm Low and automatic shut down the heater if Temperature Alarm Low Low Temperature Alarm Low and automatic shut down the heater if Temperature Alarm Low Low Indication of composition at tube

Furnace/burner used to heat up using fuel oil + air Heating oil to 250 C to supply to Distillation re boiler

HAZOP STUDY

(16)

Vaporiser instalation at heating oil prior to inlet to furnace Indication of flow at exit stream of furnace Online decoking peridically Indication of flow at exit stream of furnace Standby pump, automatically cut in if another fail to function Online decoking peridically

References

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