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Vanadium Pentoxide
Inquiry
| Post Date: | May 02,2007 |
| Expiry Date: | Oct 29,2007 |
| Detailed Description: | Cas No. : Vanadium Pentoxide demand for v2o5 az catalyst use in sulphuric acid industr .Our technical specification of catalyst that we need is az below: Application: Oxidation of S02 to S03 for sulfuric acid production. Composition: Vanadium pentoxide and alkali metal sulfates on special silica support approx. 6% V20S approx. 7% V20S approx. 8%V20S Form: Tubular extrudates, 10 mm OD5 mmID Extruded pellets of 4, 6 and 8 mm diameter Bulk density: approx. 500 g/I (rings) approx. 600 g/I (pellets) and we expect these results from catalyst: 1) Capacity (mt/daY): 60 2) Feedstock: yes (e.g. sulfur burner): 3) Plant design: single- absorption plant 4) Type of cooling: ?indirect (heat exchangers) ?direct (e,g.air. quenchgas) ?in direct: volume of air/quenchgas efter each bed (Nm3/hr): after bed 2: 1192 Nm3 I hr after bed 3:1130 Nm3 I hr temperature of air/quenchgas after each bed :40 c composition of quench gas: 02=21% N 2=79% 5) Catalyst loading: - Total catalyst volume Installed (m3): 12 - Inside diameter of catalyst beds (m): 2.6 - Catalyst volume per bed (m3): bed 1: 2.4 bed 2: 2.5 bed 3: 2.8 bed 4: 4.3 ?Catalyst loading height per bed (cm, actual) : bed 1: 43 bed 2: 45 bed 3: 50 bed 4: 70 Actual pressure drop across the catalyst beds (mbar): bed1:20 bed2:19 bed3:18 bed4:17 6)Operating data : ?Feedgas, first bed: Flowrate (Nm3/hr):6700 m3/h Composition: So2(% vol./vol.):570 Nm3/h O2(% vol./vol.): 837 Nm3/h - Reaction temperatures: Intel:(c) outlet:(c) bed 1: 430 603 bed 2: 435 494 bed 3: 430 434 bed 4: 390 392 ?Actual S02-conversion after each bed (%): bed 1: 70 bed 2: 25 bed 3: 3 bed 4: 1.2 please tell us your price and technical specification |
| Company: | evergrand green marketing corp |
| Contact: | David Hong |
| Tel: | 0086-553-4997752 |
| Fax: | 0086-553-4997751 |
| Email: | Send Message |
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