Property

NameEndpoint Distance
Codeede
Symbold<sub>e</sub>
TypeConsequence (Plant Unit)
Data TypeNumeric
Unitm
View Order17
Please enter a message.Please enter an endpoint distance.
Invalid MessageInvalid endpoint distance.
Validation Rule
[x] >= 0
AccessPublic
Created: Serkan GIRGIN, 2012/08/17 07:40:13

Property Estimators

NoNameValueValidity Conditions
1.Distance to 1 psi overpressure for VCE (TNT-equivalency method)ƒ(fyield, Qfuel, ∆Hc0mSubstance Type: Flammable; VCMmodel: TNT Equivalency; Fire/Explosion Event: Vapor Cloud Explosion; Δp: 1 psi---
2.Distance to endpoint for no firemSubstance Type: Flammable; Fire/Explosion Event: No Fire---
3.Distance to endpoint for no releasemPrelease: 0%---
4.Distance to endpoint for no releasemQreleased: 0 kg---
5.Distance to endpoint for no releasemqrelease: 0 kg/min---
6.Distance to endpoint for non-hazardous substancesmSubstance Type: Non-hazardous---
7.Distance to endpoint thermal dose for BLEVE (Hymes point-source model)ƒ(τa, R, ∆Hc0, Qfuel, DT, tcmSubstance Type: Flammable; Fire/Explosion Event: BLEVE---
8.Distance to endpoint thermal dose for pool fire (3 kW/m2 INERIS correlation)ƒ(lpoolmSubstance Type: Flammable; lpool: < 300 m; Fire/Explosion Event: Pool Fire; qR: 3 kW/m2---
9.Distance to endpoint thermal dose for pool fire (5 kW/m2 INERIS correlation)ƒ(lpoolmSubstance Type: Flammable; lpool: < 300 m; Fire/Explosion Event: Pool Fire; qR: 5 kW/m2---
10.Distance to endpoint thermal dose for pool fire (8 kW/m2 INERIS correlation)ƒ(lpoolmSubstance Type: Flammable; lpool: < 300 m; Fire/Explosion Event: Pool Fire; qR: 8 kW/m2---
11.Distance to endpoint thermal dose for pool fire (TNO point model)ƒ(R, qc, ∆Hc0, τa, qRmSubstance Type: Flammable; Fire/Explosion Event: Pool Fire; Pool Fire Model: Point Source---
12.Distance to endpoint thermal dose for pool fire (TNO Solid Surface Model)ƒ(qR, SEP, dpool, hflame, Θ, PwatermSubstance Type: Flammable; Fire/Explosion Event: Pool Fire; Pool Fire Model: Solid Surface-5-
13.Distance to lower flammability limit (LFL) from RMP reference table (dense plume)ƒ(RTRMP, LFL, MW, qgas, reducedmileqgas: > 0 kg/min; RTRMP: Table 28, Table 29---
14.Distance to lower flammability limit (LFL) from RMP reference table (neutrally buoyant plume)ƒ(LFL, MW, qgas, reduced, RTRMPmileqgas: > 0 kg/min; RTRMP: Table 26, Table 27---
15.Distance to peak overpressure for VCE (TNT-equivalency method)ƒ(fyield, Qfuel, ∆Hc0, ΔpmSubstance Type: Flammable; VCMmodel: TNT Equivalency; Fire/Explosion Event: Vapor Cloud Explosion; Δp 1 psi---
16.Distance to second-degree burns for pool fire from RMP Pool Fire Factorƒ(PFFRMP, ApoolftSubstance Type: Flammable; Fire/Explosion Event: Pool Fire; Pool Fire Model: RMP pool fire model---
17.Endpoint Distance calculated by ADAMƒ(deADAMmADAM: On-1-
18.Endpoint distance for confined vapor cloud explosion (Multi-energy model)ƒ(Vcloud, obstructed, Δp, PAmSubstance Type: Flammable; VCMmodel: Multienergy; Fire/Explosion Event: Vapor Cloud Explosion---
19.Endpoint distance for unconfined vapor cloud explosion (Multi-energy model)ƒ(Vcloud, Δp, PAmObstruction Class: Unobstructed; VCMmodel: Multienergy; Fire/Explosion Event: Vapor Cloud Explosion---
20.Endpoint distance from RMP reference table (dense gas)ƒ(TEPRMP, qgas, reduced, RTRMPmileqgas: > 0 kg/min; Fire/Explosion Event: No Fire, Vapor Cloud Fire; RTRMP: Table 5, Table 6, Table 7, Table 8, Table 18, Table 19, Table 20, Table 21-3-
21.Endpoint distance from RMP reference table (neutrally buoyant plume)ƒ(qgas, reduced, TEPRMP, RTRMPmileqgas: > 0 kg/min; RTRMP: Table 1, Table 2, Table 3, Table 4, Table 14, Table 15, Table 16, Table 17---
22.Endpoint distance from RMP reference table (substance-specific)ƒ(RTRMP, qgas, reduced, TOPOmileqgas: > 0 kg/min; RTRMP: Table 9, Table 10, Table 11, Table 12, Table 22, Table 23, Table 24, Table 25---
23.Selection of manually-inserted endpoint distance for Maltaƒ(EPDMImSubstance Type: Flammable; EPDMI: > 0 m1--

Risk Assessment

Natural Hazards

Industrial Plants

Scientific

Users