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Chemical plant design & operations

ChemEngSquirrel
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Flare Design for Air Failure
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0
Views
66
ChemEngSquirrel
ChemEngSquirrel
jamesbanda
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Distillation Column Sump Residence Time Basis
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2
Views
566
sshep
sshep
mvelez
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Gear Pump supplier 1
Replies
5
Views
155
SNORGY
SNORGY
Bambie
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REGULATOR FAIL OPEN CAPACITY PER ASTM F1795
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14
Views
338
Bambie
Bambie
mamed
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Dynamic depressurization in Hysys 2
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11
Views
478
OldDoc
OldDoc
ysrawat1990
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Inclined Nozzles on all Equipment
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3
Views
160
MJCronin
MJCronin
Chem2020
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Line Sizing 3
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5
Views
542
moltenmetal
moltenmetal
landrover77
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API 661 Condenser
Replies
3
Views
153
SNORGY
SNORGY
lukman143
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How to Remove Foam from Cooling Water Surface
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6
Views
340
thorium1
thorium1
ysrawat1990
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Flow element in Vertical ? 1
Replies
11
Views
336
thorium1
thorium1
mEng123
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Tank level Calculation 1
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3
Views
139
chicopee
chicopee
Tariqi
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Introducing liquid propane in ethane vapor environment 1
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11
Views
214
sshep
sshep
silebi66
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  • Question
Why is the suction pressure to be zero for the submerge pit pump? 1
Replies
6
Views
437
bimr
bimr
Berenger
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PIPE SIZING (DIAMETER)
Replies
4
Views
523
racookpe1978
racookpe1978
HubertChen
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material for dual wiper secondary seal
Replies
1
Views
100
IFRs
IFRs
remy1234
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  • Question
Chemical Plants
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4
Views
252
Latexman
Latexman
ananya2011
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Deaerator level control
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9
Views
860
thorium1
thorium1
ziptron
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Venting Water Storage Tank 2
Replies
4
Views
246
lukman143
lukman143
Chem2020
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Depressurizing time calculation
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3
Views
146
sshep
sshep
LiamNolan27
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  • Question
Licht, W. H. Koch, "New design approach boosts cyclone efficiency", Chemical Egineering, N
Replies
2
Views
346
bimr
bimr
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