𝔖 Bobbio Scriptorium
✦   LIBER   ✦

Continuous shock wave reactor for chemical production and reaction studies

✍ Scribed by J.L. Lauer; M. Berchtold; J.Y. Shang


Publisher
Elsevier Science
Year
1967
Tongue
English
Weight
654 KB
Volume
22
Category
Article
ISSN
0009-2509

No coin nor oath required. For personal study only.

✦ Synopsis


A continuous shock wave reactor with a single instrumented shock tube was built, based on the concept of a disc rotating within a concentric ring about a shaft perpendicular to the disc's plane. The shock tube is a small tube having a square cross section, which is also a diameter of the disc. The ring contains ports comected in sequence to a process gas reservoir at low pressure, a driver gas reservoir at high pressure, driver gas outlets and product sample containers. Rotation of the disc results in successive opening and closing of these ports causing the charging of the tube with process gas, the generation of shock waves rapidly heating the process gas and of rarefaction waves cooling it, and removal of driver and product gases. The ability to produce relatively large quantities of reaction products and the small size of the installation give this device an advantage over the usual single-pulse shock tube, especially in the study of trace components in complex product mixtures.


πŸ“œ SIMILAR VOLUMES


ChemInform Abstract: The Shock Tube as W
✍ K. A. Bhaskaran; P. Roth πŸ“‚ Article πŸ“… 2010 πŸ› John Wiley and Sons βš– 24 KB πŸ‘ 2 views

## Abstract ChemInform is a weekly Abstracting Service, delivering concise information at a glance that was extracted from about 100 leading journals. To access a ChemInform Abstract of an article which was published elsewhere, please select a β€œFull Text” option. The original article is trackable v

Chemical reaction processes in two-phase
✍ Pierre Trambouze; M. T. Trambouze; Edgar L. Piret πŸ“‚ Article πŸ“… 1961 πŸ› American Institute of Chemical Engineers 🌐 English βš– 556 KB

## Abstract A theory of design of chemical reactors is developed for two‐phase fluid systems where the rates of chemical reaction are low relative to the rates of mass transfer. Equations are presented for batch, column, and continuous stirred tank operations. Experimental data on the continuous hy