Experimental data from gas-solid fluidized reactor systems are analysed on the basis of the theoretical treatment of Parts I and II. The following systems are treated : (a) Roasting of pyrrhotite and zinc blende particles with uniform size. (b) Roasting of zinc blende concentrate with wide distribut
✦ LIBER ✦
Fluidized-solids reactors with continuous solids feed—II: Conversion for overflow and carryover particles
✍ Scribed by Sakae Yagi; Daizo Kunii
- Publisher
- Elsevier Science
- Year
- 1961
- Tongue
- English
- Weight
- 606 KB
- Volume
- 16
- Category
- Article
- ISSN
- 0009-2509
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✦ Synopsis
Based upon the simple model of particles which keep their diameters almost constant during reaction with the gas flowing in the fluidized bed, and applying the exit age-distribution functions obtained in Part I, equations for the conversion of product particles were derived.
📜 SIMILAR VOLUMES
Fluidized-solids reactors with continuou
✍
Sakae Yagi; Daizo Kunii
📂
Article
📅
1961
🏛
Elsevier Science
🌐
English
⚖ 830 KB
Fluidized-solids reactors with continuou
✍
Sakae Yagi; Daizo Kunii
📂
Article
📅
1961
🏛
Elsevier Science
🌐
English
⚖ 638 KB
The distribution of residence times of solid particles is examined in fluidized beds at steady state with continuous feed and discharge of solids, both for beds consisting of a single particle size and for beds consisting of a wide spectrum of particle sizes. The mean age (residence time in bed) of