| dc.contributor.author | A. W., NurSulihatimarsyila | |
| dc.contributor.author | T. G., Chuah Abdullah, Dr. | |
| dc.contributor.author | Choong, Thomas Shean Yaw, Assoc. Prof. Dr. Ir. | |
| dc.contributor.author | B., Thayananthan | |
| dc.date.accessioned | 2011-08-12T05:51:07Z | |
| dc.date.available | 2011-08-12T05:51:07Z | |
| dc.date.issued | 2005-12 | |
| dc.identifier.citation | The Journal of the Institution of Engineers, Malaysia, vol. 66(4), 2005, pages 61-64 | en_US |
| dc.identifier.issn | 0126-513X | |
| dc.identifier.uri | http://www.myiem.org.my/content/iem_journal_2005-176.aspx | |
| dc.identifier.uri | http://dspace.unimap.edu.my/123456789/13545 | |
| dc.description | Link to publisher's homepage at http://www.myiem.org.my/ | en_US |
| dc.description.abstract | This paper illustrates design aspects of a shallow bed reactor involving a very rapid reaction, which is a diffusion controlled
reaction. The design of the bed composed of a small number of catalyst screens, is normally based on past experience, scaleup
on the basis of equal velocity, and careful planning for good distribution. Methods needed to estimate the number of
meshes, diameter, height and volume of catalyst bed are discussed. This design method can be useful for economic or
operating studies. | en_US |
| dc.language.iso | en | en_US |
| dc.publisher | The Institution of Engineers, Malaysia | en_US |
| dc.subject | Ammonia oxidation | en_US |
| dc.subject | Gauze | en_US |
| dc.subject | Kinetic | en_US |
| dc.subject | Nitric acid | en_US |
| dc.subject | Shallow bed reactor | en_US |
| dc.title | Estimation of platinum gauzes catalyst for ammonia oxidation in nitric acid production | en_US |
| dc.type | Book | en_US |
