Vanadium Pentoxide
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Post Date:
May 02,2007
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Expiry Date:
Oct 29,2007
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Detailed Description:
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
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Company:
evergrand green marketing corp
[ China ]
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Contact:
David Hong
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Tel:
0086-553-4997752
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Fax:
0086-553-4997751
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Email:
yxchemic@hotmail.com
Inquiry