Skip to main content
Log in

Ethylene–air mixtures under flowing conditions: a model-based approach to explosion conditions

  • Original Paper
  • Published:
Clean Technologies and Environmental Policy Aims and scope Submit manuscript

Abstract

Propylene oxide, ethylene oxide (EO), methanol, and phthalic anhydride are examples of versatile, widely applied chemical intermediates, produced at elevated temperature and pressure conditions, demanding rigorous safety considerations. Well-known industrial applications in which ethylene at the vapour phase is oxidized with oxygen are the manufactures of vinyl acetate and of EO. Partial oxidation of ethylene is usually performed at elevated temperature and pressure in multitubular cooled reactors where the application of explosive limits experimentally obtained under stagnant conditions could entail a not justified economical handicap. Bearing in mind these considerations, in this paper, we developed a novel physical–mathematical model to predict the ignition and flame-propagation phenomena in the presence of gaseous explosive mixtures. The explicit formulae for the ignition condition and the transition from local reaction to the fully developed explosion were obtained by exploring a broad range of operative conditions. A fairly good agreement was found between the predictions in this study of the oxygen critical concentration corresponding to the explosion point and the results of previous experimental studies performed by different researchers.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5

Similar content being viewed by others

Abbreviations

a:

Parameter defined by Eq. (34) [m−1]

cp :

Specific heat capacity [J/(kg K)]

C:

Molar concentration (mol/m3)

δ:

Distance defined by Eq. (15) [m]

D:

Tube diameter (m)

H:

Enthalpy flow (W)

k:

Thermal conductivity [W/(m K)]

Kt :

Heat-transfer coefficient [W/(mK)]

m:

Mass flux [kg/(m2 s)]

M:

Molar mass [kg/kmol]

p:

Pressure (Pa)

Q:

Heat release rate (W/m)

R:

Ideal gas constant 8.314 [J/(mol K)]

r:

Radial coordinate (m)

Re:

Reynolds number

ℜ:

Reaction rate [mol/(m3 s)]

T:

Temperature (K)

u:

Flow velocity (m/s)

V:

Volume (m3)

X:

Conversion

y:

Molar fraction

z:

Vertical axial coordinate (m)

c:

Flame heating step

e:

In-coming

ei:

at Te and zi

eth:

Ethylene

ew:

at Te and zw

f:

Flame

i:

Ignition

iw:

at Ti and zw

m:

Average

oxy:

Oxygen

p:

Flame propagating

w:

Wire

References

  • Bernardo P, Clarizia G (2012) Integrated membrane operations in the ethylene oxide production. Clean Technol Environ Policy 14:475–485

    Article  CAS  Google Scholar 

  • Bielert U, Sichel M (1998) Numerical simulation of premixed combustion processes in closed tubes. Combust Flame 114:397–419

    Article  CAS  Google Scholar 

  • Bird RB, Stewart WE, Lightfoot EN (2007) Transport Phenomena, 2nd edn. Wiley, New York

    Google Scholar 

  • Bolk JW, Westerterp KR (1999) Influence of hydrodynamics on the upper explosion limit of ethene-air-nitrogen mixtures. AIChE J 45:124–144

    Article  CAS  Google Scholar 

  • De Rademaeker E, Suter G, Pasman HJ, Fabiano B (2014) A review of the past, present and future of the European loss prevention and safety promotion in the process industries. Process Saf Environ Prot 92(4):280–291

    Article  Google Scholar 

  • Fabiano B, Currò F (2012) From a survey on accidents in the downstream oil industry to the development of a detailed near-miss reporting system. Process Saf Environ Prot 90:357–367

    Article  CAS  Google Scholar 

  • Fabiano B, Cermelli D, Pastorino R, van den Hoogenband V, van den Hengel E (2010) Influence of flow rate and pressure on the upper explosion limit of ethene-air mixture. 13th Loss Prevention Symposium 2, 491–494, Technologisch Institut vzw, Brugge, BE

  • Fabiano B, Reverberi AP, Del Borghi A, Dovì VG (2012) Biodiesel production via transesterification: process safety insights from kinetic modeling. Theor Found Chem Eng 46(6):673–680. doi:10.1134/S0040579512060097

    Article  CAS  Google Scholar 

  • Fabiano B, Kersten RJA, Barbucci A, Boers MN (2013) Experimental and theoretical approach to the assessment of stability criteria for safe transport of ammonium nitrate based emulsions. Chem Biochem Eng Q 27(3):307–317

    CAS  Google Scholar 

  • Glasar JA (2014) Good chemical manufacturing process criteria. Clean Technol Environ Policy 16:217–223

    Article  Google Scholar 

  • Günther RM, Schöneberger JC, Thielert H, Wozny G (2014) Process development and catalyst testing under industrial conditions. Clean Technol Environ Policy 16:1307–1317

    Article  Google Scholar 

  • IHS (2013) Ethylene Oxide. www.ihs.com/products/ethylene-oxide-chemical-economics-handbook.html. Accessed on 17th March 2015

  • Klemesˇ JJ, Varbanov PS (2012) Efficient and clean production of fuels and biofuels: a summary. Clean Technol Environ Policy 14:371–375

    Article  Google Scholar 

  • Klemesˇ JJ, Varbanov PS (2013) Process intensification and integration: an assessment. Clean Technol Environ Policy 15(3):417–422

    Article  Google Scholar 

  • Lou HH, Martin CB, Chen D, Li X, Li K, Vaid H, Kumar AT, Singh KD, Bean DP Jr (2012) A reduced reaction mechanism for the simulation in ethylene flare combustion. Clean Technol Environ Policy 14:229–239

    Article  CAS  Google Scholar 

  • Milazzo MF, Aven T (2012) An extended risk assessment approach for chemical plants applied to a study related to pipe ruptures. Reliab Eng Syst Saf 99:183–192

    Article  Google Scholar 

  • Palazzi E, Fabiano B (2012) Analytical modelling of hydrocarbon pool fires: conservative evaluation of flame temperature and thermal power. Process Saf Environ Prot 90:121–128

    Article  CAS  Google Scholar 

  • Palazzi E, Currò F, Fabiano B (2013) Accidental continuous releases from coal processing in semi-confined environment. Energies 6:5003–5022

    Article  CAS  Google Scholar 

  • Palazzi E, Currò F, Reverberi A, Fabiano B (2014a) Development of a theoretical framework for the evaluation of risk connected to accidental oxygen releases. Process Saf Environ Prot 92(4):357–367

    Article  CAS  Google Scholar 

  • Palazzi E, Pistritto F, Reverberi A, Fabiano B (2014b) Modelling approach to the evaluation of explosion limits of ethylene-air mixtures at flowing conditions for industrial process optimisation. Chem Eng Trans 39:829–834. doi:10.3303/CET1439139

    Google Scholar 

  • Park O, Veloo PS, Egolfopoulos FN (2013) Flame studies of C2 hydrocarbons. Proc Comb Inst 34:711–718

  • Petrochemicals Europe (2015) http://www.petrochemistry.eu. Accessed on 15th April 2015

  • Reverberi AP, Fabiano B, Dovì VG (2013) Use of inverse modelling techniques for the estimation of heat transfer coefficients to fluids in cylindrical conduits. Int Commun Heat Mass Transf 42:25–31

    Article  Google Scholar 

  • Shariff AM, Zaini D (2013) Using integrated toxic release consequences analysis tool for inherently safer design of process plant at preliminary design stage. Clean Technol Environ Policy 15:851–858

    Article  Google Scholar 

  • Siccama NB, Westerterp KR (1993) The explosion region becomes smaller under flow conditions: the Ignition of ethylene-air mixtures with a hot surface. Ind Eng Chem Res 32:1304–1314

    Article  CAS  Google Scholar 

  • Skjoldi T, Arntzen BJ, Hansen OR, Taraldset OJ, Storvik IE, Eckhoff RK (2005) Simulating dust explosion with the first version of DESC. Process Saf Environ Prot 83:151–160

    Article  Google Scholar 

  • Testa E, Giammusso C, Bruno M, Maggiore P (2014) Analysis of environmental benefits resulting from use of hydrogen technology in handling operations at airports. Clean Technol Environ Policy 16:875–890

    Article  CAS  Google Scholar 

  • True WR (2013) Global ethylene capacity poised for major expansion. Oil Gas J 111:90–95

    Google Scholar 

  • Varbanov PS, Seferlis P (2014) Process innovation through Integration approaches at multiple scales: a perspective. Clean Technol Environ Policy 16:1229–1234

    Article  Google Scholar 

  • Westbrook C, Dryer F (1981) Simplified reaction mechanisms for the oxidation of hydrocarbon fuels in flames. Combust Sci Technol 31:2429–2436

    Google Scholar 

  • Wu M, Burke MP, Son SF, Yetter RA (2007) Flame acceleration and the transition to detonation of stoichiometric ethylene/oxygen in microscale tubes. Proc Combust Inst 31:2429–2436

    Article  Google Scholar 

Download references

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Bruno Fabiano.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Fabiano, B., Pistritto, F., Reverberi, A. et al. Ethylene–air mixtures under flowing conditions: a model-based approach to explosion conditions. Clean Techn Environ Policy 17, 1261–1270 (2015). https://doi.org/10.1007/s10098-015-0966-1

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s10098-015-0966-1

Keywords

Navigation