Modelling of a side reactor configuration combining reaction and distillation

Author:

Jakobsson Kaj,Pyhälahti Antti,Pakkanen Sini,Keskinen Kari,Aittamaa Juhani

Publisher

Elsevier BV

Subject

Applied Mathematics,Industrial and Manufacturing Engineering,General Chemical Engineering,General Chemistry

Reference19 articles.

1. Multistaged separators with nonstandard specifications solved by Newton–Raphson method;Buzzi Ferraris;A.I.Ch.E. Journal,1981

2. A modified Naphtali–Sandholm method for general systems of interlinked, multistage separators;Hofeling;A.I.Ch.E. Journal,1978

3. Jakkula, J., Järvelin, H., & Kivi, J. (1994). The production of TAME and heavier ethers to achieve higher oxygen and lower olefins content in motor gasoline, new fuels and lubricants. Stavanger: World Petroleum Congress.

4. Järvelin, H., Tamminen, E., & Ewy, G. (1996). NexTAME process operating experiences from a commercial unit and some economical considerations. NPRA annual meeting, March 17–19, San Antonio, TX.

5. Calculation of multistage countercurrent separation processes—II;Jelı́nek;Chemical Engineering Science,1973

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