Pressure Vessels

Client, Country	Year	Size	Wall Thickness (Inch)	Desig Pressure (psig)	Design Temp F (max/min)	Test Pressure (psig)	Material (Shell/Heads)	Service	Code

Nuovo Pignone, Italy	2002	24" ID x 5'-3"	1.75	2453.3	392/-36.4	3189.4	SA-516-70N	Discharge Volume Bottle 1st Stage	ASME Sec.VIII Div.1

Nuovo Pignone, Italy	2002	27" ID x 8'-10 1/2"	2	2540.3	212/-36.4	3302.5	SA-516-70N	Suction Volume Bottle 2nd Stage	ASME Sec.VIII Div.1

Nuovo Pignone, Italy	2002	23" ID x 4'-10 1/2"	2.25	3178.8	392/-36.4	4132.4	SA-516-70N	Discharge Volume Bottle 2nd Stage	ASME Sec.VIII Div.1

Nuovo Pignone, Italy	2002	22" ID x 6'-0 1/2"	1.625	2437.6	212/-36.4	3169	SA-516-70N	Suction Volume Bottle 1st Stage	ASME Sec.VIII Div.1

State Concern TurkmenGas, Turkmenistan	2001	78" ID x 20'-0"	1.375	650	150/-20	845	SA-516-70N	Inlet Separator	ASME Sec.VIII Div.1

State Concern TurkmenGas, Turkmenistan	2001	42" ID x 59'-0"	0.5	300	450/-20	390	SA-516-70N	Debutanizer Tower	ASME Sec.VIII Div.1

Combisa, Mexico	2000	42" OD x 39'-0"	0.5	155.19	200/-20	233	SA-516-70N	Sour Water Stripper	ASME Sec.VIII Div.1

Combisa, Mexico	2000	126" ID x 9'-0"	4	1332	250/10	1665	SA-516-70N	Inlet Scrubber	ASME Sec.VIII Div.2

Combisa, Mexico	2000	66" ID x 33'-0"	0.875 / 0.5	163.04	450/10	245	SA-516-70N	TEG Regenerator	ASME Sec.VIII Div.1

Combisa, Mexico	2000	66" ID x 15'-0"	0.5	164.94	250/10	247.5	SA-516-70N	TEG Surge Tank	ASME Sec.VIII Div.1

Combisa, Mexico	2000	90" OD x 20'-0"	0.625	169.56	250/10	255	SA-516-70N	TEG Condensate Separator	ASME Sec.VIII Div.1

National Iranian Gas Company, Iran	1999	102" ID x 11'-9 3/4" TAN/TAN	4	1200	194/-20	1800	SA-516-70N	Low Temperature Separator	ASME Sec.VIII Div.1

Alberta Energy Company, Canada	1998	32" ID x 47'-0"	1.75	1650	250/-20	2475	SA-516-70N	Amine Contactor	ASME Sec.VIII Div.1

Alberta Natural Gas, Canada	1998	84" ID x 40'-0"	3.25	1200	149/-49	1800	SA-516-70N	3-Phase Raw Gas Inlet Separator	ASME Sec.VIII Div.1

Orenburgneft Production Association, Russia	1998	60" ID x 20'-0"	2	970	150/-50	1455	SA-516-70N	Low Temperature Separator	ASME Sec.VIII Div.1

Orenburgneft Production Association, Russia	1998	54" ID x 14'-0"	0.75	350	149/-50	525	SA-516-70N	Deethanizer Reflux Drum	ASME Sec.VIII Div.1

Orenburgneft Production Association, Russia	1998	54" ID x 16'-0"	0.625	300	150/-50	450	SA-516-70N	High Pressure Economizer	ASME Sec.VIII Div.1

Orenburgneft Production Association, Russia	1998	18" OD x 17'-0"	0.375	50	500/-50	75	SA-333-6 / SA-516-70N	Lean Glycol Stripper	ASME Sec.VIII Div.1

Talisman Energy, Canada	1998	84" ID x 62'-0"	3	1110	149/-40	1665	SA-516-70N	Lean Oil Absorber	ASME Sec.VIII Div.1

Zielin Cychry, Poland	1998	30" ID x 35'-0"	1.25	1150	200/-20	1725	SA-516-70N	Glycol Contactor	ASME Sec.VIII Div.1 / UDT

Gulf Canada Resources, Canada	1997	16" OD x 37'-6"	0.375 / 0.500	175	375/-20	262.5	SA-106-B / SA-516-70N	Debutanizer Tower	ASME Sec.VIII Div.1

Gulf Canada Resources, Canada	1997	78" ID x 28'-0"	0.75	250	212/-20	375	SA-516-70N	Stabilizer Feed Drum	ASME Sec.VIII Div.1

Gulf Canada Resources, Canada	1997	54" OD x 20'-0"	1.75	1100	150/-49	1650	SA-516-70N	Low Temperature Separator	ASME Sec.VIII Div.1

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