LCWS10 Final Plenary ILC CONVENTIONAL FACILITIES AND SITING GROUP
Siting and Safe Operation of Liquefied Natural Gas Facilities
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Transcript of Siting and Safe Operation of Liquefied Natural Gas Facilities
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R egulations require facilities to usecomputer simulations to modelpotential fire and explosion hazards
from accidental liquefied natural gas (LNG)releases. This has required the run of severalseparate computer models and manual trans-fer of data among the models, which is atime-consuming process prone to errors.
The Code of Federal Regulations (49 CFR193) defines safety standards for LNG facili-ties covered by federal pipeline safety laws. Itaddresses protection in the vicinity of LNGstorage and transfer systems by specifying themodels used to calculate exclusion zones forthermal and vapor hazards. The models spec-ified are LNGFIRE3 for thermal radiationprotection and DEGADIS for air dispersioncalculations. The Gas Technology Institute(GTI) sponsored development of the LNG-FIRE3 model as well as the LNG-specificSOURCE5 model that predicts the spreadand vaporization rate of LNG spills. Outputfrom the SOURCE5 model is compatiblewith DEGADIS, making the combination of the two models useful for ensuring compliance with 49 CFR 193. SOURCE5,DEGADIS and LNGFIRE3 can be run ontypical personal computers.
SOURCE5In developing SOURCE5, GTI examinedfield and laboratory experiments and selectedthe best-in-class model that simulated LNGspread and vaporization rates for each of thefollowing release types:
• instantaneous confined spills on land;• continuous confined spills on land;• instantaneous unconfined land spills;• continuous unconfined water spills; and
• instantaneous unconfined water spills.SOURCE5 allows the user to specify
the size and shape of fuel impound-ment basins, material properties of theimpoundment structure (dike) and LNGchemical properties. The main outputs fromSOURCE5 are the LNG vaporization andspread rates, and a comparison of the volumeof a specified impoundment basin with vol-umes as specified in 49 CFR 193 (Figure 1,Table 1).
DEGADIS49 CFR 193 specifiesDEGADIS as an accept-able model for determiningthe downwind distances toflammability limits. Theprogram originally wasdeveloped for the U.S.Coast Guard and GTI withthe primary objective ofsimulating dispersion ofcryogenic flammable gases.DEGADIS has been usedfor a number of years in industry and iswidely accepted. When modeling air disper-sion from LNG releases, DEGADIS canaccept predicted vaporization and spreadingrates, such as those produced by SOURCE5(Figure 2).
LNGFIRE349 CFR 193 specifies LNGFIRE3 as anacceptable model for determining thermalexclusion areas surrounding LNG fires.LNGFIRE3 is a set of three fire models thatcalculates the thermal exclusion distances for
Winter 2005 • GasTIPS 27
LNG FACILITIES
by Dr. Erwin T. Prater,Trinity ConsultantsSiting and Safe Operation of
Liquefied Natural Gas FacilitiesSafety is a prime consideration in the placement and design of liquefied natural gas facilities.
Figure 1. SOURCE5 input screen.
Figure 2. Typical DEGADIS output screen from a liquefied nat-ural gas release scenario.
Table 1. Key SOURCE5 Input and Output Parameters.Input Parameters Output ParametersType of LNG release (5) Construction material of impoundment basinRelease duration DEGADIS-compatible LNG vaporization
and spreading ratesRelease amount LNG chemical propertiesSize, shape of impoundment basin Comparison of impoundment basin volume
with specifications in CFR 49 193
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unconfined pool fires, confined pool fires andjet fires (Figure 3). It calculates radiant fluxlevels at user-defined points downwind of an LNG fire. Meteorological information,including wind speed, wind direction andhumidity as well as parameters that describethe LNG release are specified through a seriesof input screens. The model for pool fires simulates flame as a cylinder or a paral-lelepiped, depending upon the geometry of the impoundment areas. Wind-inducedflame drag and tilt also are accounted for inthe models.
An integrated approachThe commercial product BREEZE LFGFire/Risk from Trinity Consultants combinesSOURCE5, DEGADIS and LNGFIRE3into one package, allowing the analyst to effi-ciently simulate a broad set of potential haz-ards associated with LNG process operations(Table 2). The product also contains an addi-
tional U.S. Environmental Protection Agency-approved model for simulating the exclusiondistance for boiling liquid expanding vaporexplosions. Input parameters are sharedamong the programs, eliminating redundantdata entry while saving time and increasingefficiency. Output is available in tabular andgraphical forms, giving the user several differ-ent ways to display and analyze results. Outputalso can be imported into other programs,such as Microsoft Word, Excel andPowerPoint, aiding preparation of reports andpresentations. For more information, visitwww.breeze-software.com
Scenario analysisLFG Fire/Risk recently was used to deter-mine exclusion distances for various acciden-tal release scenarios for an LNG terminal.These hazards included releases from tankergrounding, LNG transfer, LNG off-loading,re-gasification, and failure of tanks and pip-
ing. One scenario involved an LNG storagetank dike fire that occurred when a tank wasdamaged and its contents were released intoa circular containment structure. Figure 4features a plot of thermal exclusion distancesand a graph of thermal flux as a function ofdistance, which are useful for determiningthe proper siting for an LNG facility.
Another scenario involved the release ofLNG from a 1.64-ft (0.5-m) diameter hole inan LNG tanker resulting from its accidentalgrounding. This is an unlikely scenario giventhe procedures and technology used to guidetankers during docking and unloading. Figure5 shows the results from running SOURCE5and DEGADIS from within LFG Fire/Risk.The vapor exclusion distances were calculatedto 2.5% methane concentration.
As economic conditions continue to makeLNG import, processing and storage moreattractive, robust analytical capabilities associ-ated with potential hazards are becoming moreimportant. Integrated, productivity-enhancingsoftware that facilitates these analyses will makeproject planning for LNG operations easier.
For more information about hazardousrelease analysis, contact Dr. Erwin Prater,senior product specialist for TrinityConsultants, at (972) 661-8881 or [email protected]
Reference documents are GRI-92/0534 forSOURCE5; GTI-04/0049 for DEGADISand GTI-04/0032 for LNGFIRE3; and are available on GTI’s Web site atwww.gastechnology.org ✧
28 GasTIPS • Winter 2005
LNG FACILITIES
Table 2. Features in BREEZE LFG/Fire Risk.LNG-specific SOURCE5 model Extensive database of industrial chemical propertiesUser-specified LNG containment basin Flexible and user-friendly MS-Windows interfacesize, shape and composition materialSeamless integration of results from LNGFIRE3 fire modelsSOURCE5 into DEGADIS dense-gas air dispersion modelChoice of tabular and graphical Environmental Protection Agency boiling liquid output expanding vapor explosions modelOutput compatibility with common Ability to animate results from DEGADIS MS-Office applicationsImport map images in popular formats, Ability to overlay thermal and vapor exclusion areas including DXF, BMP, and JPEG on maps, plots and drawings
Figure 3. LNGFIRE3 output screen. Figure 5. LFG Fire/Risk output screen.Figure 4. Results from LFG Fire/Risk featur-ing a plot of thermal exclusion distancesand thermal flux.