CATALYTIC OXIDATION OF 1-BUTENE TO MALEIC ANHYDRIDE IN A FLUIDIZED BED REACTOR

Q: How can I download an article?

To download an article from SID, first log in to the site, search for the article title, and click on the 'Download Article' option.

Q: How can I download an ISI article?

To download an ISI article on SID, enter the keyword or article title in the search bar, view the relevant results, click on the desired article, and select the 'Download Article' option.

Q: How can I access the SID database?

To access the SID database, visit SID.ir, create an account, and log in to access scientific resources.

Q: Is downloading articles from SID free?

Some articles on SID are available for free, while others require payment. Details are specified on the article's page.

ALAVI M.; SHAHHOSSEINI S.; DELDARY H.

مرکز اطلاعات علمی Scientific Information Database (SID) - Trusted Source for Research and Academic Resources

Journal Paper

Paper Information

Journal: INTERNATIONAL JOURNAL OF INDUSTRIAL ENGINEERING AND PRODUCTION MANAGEMENT (IJIE) (INTERNATIONAL JOURNAL OF ENGINEERING SCIENCE) (PERSIAN) Year:2003 | Volume:14 | Issue:4 Page(s): 59-73

Download Full-Text

Persian Verion

View:

1,709

Download:

Cites:

Information Journal Paper

Title

CATALYTIC OXIDATION OF 1-BUTENE TO MALEIC ANHYDRIDE IN A FLUIDIZED BED REACTOR

Author(s)

ALAVI M. | SHAHHOSSEINI S. | DELDARY H. | Issue Writer Certificate

Keywords

Not Registered.

Abstract

One of industrial applications of fluidized bed reactors is the production of maleic anhydride on Vanadium Phosphorus Oxide (VPO) catalyst. Synthesis of maleic anhydride from a feed containing 1% v/v of 1-Butene in the air have been investigated in a fluidized bed reactor at various bed temperatures and different gas velocities. The best selectivity and reaction yield obtained when temperature was approximately 395°C and gas velocity was three fold of the minimum velocity for fluidization (U=3Umf). The comparison between experimentally measured selectivity with model predictions showed that the models of K&L and Grace predicted the fluidized bed performance better than others. This is due to the more realistic assumptions of these models indicating the right image of the physical and chemical processes, which happen in the bed.

Cites

No record.

References

No record.

Cite

APA: Copy

ALAVI, M., SHAHHOSSEINI, S., & DELDARY, H.. (2003). CATALYTIC OXIDATION OF 1-BUTENE TO MALEIC ANHYDRIDE IN A FLUIDIZED BED REACTOR. INTERNATIONAL JOURNAL OF INDUSTRIAL ENGINEERING AND PRODUCTION MANAGEMENT (IJIE) (INTERNATIONAL JOURNAL OF ENGINEERING SCIENCE) (PERSIAN), 14(4), 59-73. SID. https://sid.ir/paper/65715/en

Vancouver: Copy

ALAVI M., SHAHHOSSEINI S., DELDARY H.. CATALYTIC OXIDATION OF 1-BUTENE TO MALEIC ANHYDRIDE IN A FLUIDIZED BED REACTOR. INTERNATIONAL JOURNAL OF INDUSTRIAL ENGINEERING AND PRODUCTION MANAGEMENT (IJIE) (INTERNATIONAL JOURNAL OF ENGINEERING SCIENCE) (PERSIAN)[Internet]. 2003;14(4):59-73. Available from: https://sid.ir/paper/65715/en

IEEE: Copy

M. ALAVI, S. SHAHHOSSEINI, and H. DELDARY, “CATALYTIC OXIDATION OF 1-BUTENE TO MALEIC ANHYDRIDE IN A FLUIDIZED BED REACTOR,” INTERNATIONAL JOURNAL OF INDUSTRIAL ENGINEERING AND PRODUCTION MANAGEMENT (IJIE) (INTERNATIONAL JOURNAL OF ENGINEERING SCIENCE) (PERSIAN), vol. 14, no. 4, pp. 59–73, 2003, [Online]. Available: https://sid.ir/paper/65715/en

Related Journal Papers