Liquefied Natural Gas (LNG) & Liquefied Petroleum Gas (LPG)

CFD Modeling of LNG Spreading and Atmospheric Dispersion

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
April 27, 2015
LNG release, spreading and vaporization lead to the formation of a flammable vapor cloud with high VCE risk. NFPA 59A Standard for the Production,...

Integrated LNG and NGL Production

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
April 27, 2015
Cryogenic NGL extraction plants from natural gas offer an attractive opportunity for LNG production as a side stream. Cold gas is tapped from the...

Handling LPG Components In LNG Plants

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 14, 2011
Natural Gas Liquid (NGL) recovery is an inherent part of most Liquefied Natural Gas (LNG) production trains. The requirement serves many purposes,...

Uncertainties in Modeling LNG Vapor Dispersion with CFD Codes

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 23, 2010
Computational fluid dynamics (CFD) models have been widely proposed and developed to predict LNG vapor dispersion behavior and to determine safe...

Advances in LNG Expander Technology

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 22, 2010
The first use of cryogenic liquefied gas expanders dates back to the late nineties. The proven advantages of incorporating liquid expanders in the...

Flare Minimization at LNG Receiving Terminal

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 22, 2010
The LNG (liquefied natural gas) receiving terminal is an important sector of the entire LNG value chain. The handling of boil-off gas (BOG) during...

Liquid Density By Eos

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 29, 2017
Liquid Density by EOS Yoshitsugi Kikkawa, Kikkawa Giken, Yokohama Japan, yoshikikkawa@yahoo.co.jp David Hill Manager of Technical Support,...

Mid-Scale LNG Processes

Archived Webinar
Oct 16, 2013
This Webinar presents the need for natural gas liquefaction (LNG), the LNG value chain, and compares several technologies such as the PRICO® single mixed refrigerant process.

The Past, Present and Future of LNG

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
April 2, 2014
In one decade, the gas prospects in North America have gone from dire to exceptional. In 2004, we were scrambling to build import capacity for gas as...

Star LNG: a Family of Small-to-Mid-Scale LNG Processes

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
March 31, 2014
Linde Engineering has successfully developed and marketed a range of processes, which cover the range between 50 t/d and 5,000 t/d LNG product. These...

QRA Method for Liquified Natural Gas (LNG) Filling Stations

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
May 1, 2013
Summary This paper describes a method to calculate risks generated by liquefied natural gas (LNG) filling stations for road trucks. An increasing...

Constructability Issues for FLNG

Conference Presentation
AIChE Spring Meeting and Global Congress on Process Safety
April 30, 2013
Constructability issues shall be reviewed and incorporated in the Project Development Plan and Design of the FLNG. This paper addresses important...

CEP: Process Safety Beacon - An LPG Tragedy

November
2014
Process Safety Beacon
At about 5:30 a.m. on Nov. 19, 1984, there was a major fire and a series of explosions at a liquefied petroleum gas (LPG) storage and distribution terminal at San Juan Ixhuatepec, Mexico City, Mexico. There were over 500 fatalities, about 7,000 injuries, 200,000 people were evacuated, and the terminal was destroyed. The blasts were recorded on a seismometer 20 km (12.4 miles) away. Most of the injuries and fatalities were in the surrounding community — people were living as close as 130 m (425 ft) from the terminal. The cause of the accident could not be definitively established because of the destruction of the facilities and absence of witness reports.
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