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Chemical and Process Engineering |
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A S Jessup-Bould: Assessment of Pressure Relief Devices for Onshore and
Offshore Natural Gas Treatment Facilities |
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Project Background |
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End Client: BG, Tunisia |
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The
assessments were completed as part of a Process Safety in Design (PSiD) review of two of BG’s natural gas facilities in
Tunisia. These were for the Miskar platform and the
Hannibal gas treatment plant. The Miskar field is operated by BG Tunisia and comprises the Miskar offshore gas production complex (Miskar platform) located 120 km offshore Tunisia, a
sub-sea pipeline and the Hannibal gas treatment plant, onshore, 20 km to the
south of Sfax. Hannibal
was initially installed and commissioned in 1995 with a significant revamp in
2005 when a gas turbine driven compressor and additional production separator
were added. Further changes have since been made to maintain production
levels. |
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2013/14: |
Assessment of over-pressure and under-pressure relief devices |
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Summary
of Process |
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Miskar The Miskar offshore installation comprises 3 platforms
(production, accommodation + utilities, flare). The production platform has
three separation streams with total rated capacity of 340 MMSCFD of gas. There
is a compression train and two glycol dehydration trains. |
Photo source GM-RAM Limited |
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Hannibal The feed gas to Hannibal arrives via a 24” pipeline and is
first admitted to a slug catcher. Gas from the slug catcher is processed in
an Amine unit to remove carbon dioxide and hydrogen sulphide. The gas is
subsequently dehydrated by glycol and a molecular sieve. Nitrogen is removed
in the final stage of gas treatment prior to compression and export via
pipeline. Stabilised condensate is exported from the site via pipeline and
recovered acid gases are processed in the sulphuric acid plant or
incinerated. |
Photo source Middle East Online |
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Achievements |
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Unit Operations Pressure
vessels including slug catchers, pig launchers / receivers, separators Pumps
and compressors. Shell
and tube heat exchangers. Air
blast coolers. Compabloc heat exchangers. Fired
reboilers. Glycol
and amine contactors. Stripping
columns and fractionator. Molecular
sieves. Nitrogen
recovery towers / cold box. Gas
filters. Condensate
stabilisers Storage
tanks Plant
and instrument air Materials of Construction Carbon
steel. Documents Produced Required
relief rate calculations. Relief
device sizing calculations. Internal
notes. Overall
summary spread sheets. Final
reports. |
Over and Under Pressure
Scenarios Considered External
fire. Control
valve failure. Blocked
discharge. Thermal
expansion and vaporisation due to solar gain. Heat
exchanger tube rupture. Non-return
valve failure. Inadvertent
valve opening. Equipment
failure (eg pump/compressor) Abnormal
heating. Other
abnormal conditions. Compressor
/ pump blocked outlet. Utility
failures (coolant, instrument air, fuel gas, electricity). Tank
filling and emptying. Tank
thermal breathing. Liaison ABB
PSiD team. Client's
engineers. Standards etc. BG
standard BGA-ENG-PROC-TS-0015 “Process Engineering – Process Safety in
Design”. BG
standard BGA-ENG_PROC-TS-0003 “Relief, Blowdown and
Flaring”. API
standard 520 Part 1 “Sizing, Selection and Installation of Pressure Relieving
Devices in Refineries – Sizing and Selection”. 7th Edition. API
standard 520 Part 2 “Sizing, Selection and Installation of Pressure Relieving
Devices in Refineries – Installation”. 5th Edition. API
standard 521 “Pressure Relieving and Depressurising Systems”. 5th
Edition. API
standard 2000 “Petroleum, petrochemical and natural gas industries – Venting
of atmospheric and low-pressure storage tanks”. 6th Edition. |
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