Boostrand ChemE
Storage Tank Selection Guide: Fixed Roof, Floating Roof, or maybe Pressure Vessel?
9:12
Boostrand ChemE
Separator Sizing Criteria: K factor and Droplet size
14:07
Boostrand ChemE
Basis and criteria of a relief system and flare header analysis
10:04
Boostrand ChemE
Automatic Depressurization Explained: API 521 & Blowdown Systems
7:43
Boostrand ChemE
Process Design Basis - From where a project starts
12:36
Boostrand ChemE
Shell and Tube Heat Exchanger Sizing & Thermal Design Parameters
21:58
Boostrand ChemE
What if a valve on pump discharge was closed by mistake? #boostrand #processengineering #pumpshutoff
0:59
Boostrand ChemE
Adjusting reboiler and tower elevations #processengineering #courses #boostrand #shorts
0:56
Boostrand ChemE
Should a Process Engineer Consider Double Jeopardy or Simultaneous Failure?
5:54
Boostrand ChemE
Avoid low flow to a fired heater! It's a large #safety concern. #process #processsafety #engineering
0:58
Boostrand ChemE
Pump isolation for #maintenance, check valves and standby #pump #processdesign #boostrand
0:45
Boostrand ChemE
Ensure reliable system protection using SIL Assessment #processdesign #boostrand #processsafety
1:00
Boostrand ChemE
Control valve P&ID isolation and maintenance considerations for #boostrand #processdesign
1:00
Boostrand ChemE
When do we need a booster #pump? Check boostrand.com/free-course #processdesign #boostrand
1:00
Boostrand ChemE
Define Separation Degree for Vessel Sizing #processdesign #boostrand #separator
1:00
Boostrand ChemE
Choosing tank type based on fluid vapor pressure #processdesign #boostrand #chemicalengineering
0:58
Boostrand ChemE
Vessel Operating Pressure design pressure & MAWP #processdesign #processsafety #boostrand
1:00
Boostrand ChemE
Process Design Stages From Conceptual Design To Startup
11:09
Boostrand ChemE
When to use compressor anti surge hot bypass. #processengineering #compressorsurge #boostrand
0:52
Boostrand ChemE
Chimney tray vs seal pan, which tower draw off to choose? #processdesign #distillation
0:38
Boostrand ChemE
Eliminate overpressure scenarios to decrease #reliefload #processdesign #psv #designpressure #safety
0:55
Boostrand ChemE
Energy Conservation Techniques in Chemical Process Design
13:43
Boostrand ChemE
Using Restriction orifice RO to adjust the flow rate #processdesign #chemicalengineering #boostrand
0:59
Boostrand ChemE
#Pump #startup using strainer, manual valves, and pressure gauges check out boostrand.com/pid
0:54
Boostrand ChemE
Process Engineering Design: Role, Activities, Documents & Career
24:10
Boostrand ChemE
Pipe Sizing 101: Criteria, Calculation, and Best Practices for Process Engineers
20:39
Boostrand ChemE
Issue with design pressure of a heat exchanger on a pump discharge - Case Study
6:42
Boostrand ChemE
Create Excel Function to calculate pipe size using VBA
30:20
Boostrand ChemE
Discover 4 Key Factors Affecting PSV Sizing & Operation
10:18
Boostrand ChemE
Process Simulation Role in Chemical Engineering Projects & Process Engineering Considerations
12:12
Boostrand ChemE
Tips to Choose the Optimum Process Control Scheme
10:52
Boostrand ChemE
Control Valve Sizing Parameters, Inherent and Installed Characteristics
17:03
Boostrand ChemE
Distillation / Absorption Tower Operation, Hydraulics and Tray Design Aspects
13:03
Boostrand ChemE
Pressure Safety Relief valves: Operation, types, and sizing procedure
11:04
Boostrand ChemE
Separator type selection, internals and design criteria
14:09
Boostrand ChemE
Process Flow Diagrams (PFDs) Explained | Key to Efficient Process Design
11:14
Boostrand ChemE
Pumped fluid density increased! What shall happen?
5:28
Boostrand ChemE
Case Study: Troubleshooting Foam Formation in Crude Oil Separators
6:37
Boostrand ChemE
Choosing the Optimum Shell and Tube Exchanger TEMA type
9:30
Boostrand ChemE
How heat transfer coefficient affects a #shellandtube #heatexchanger? #processengineering
0:57
Boostrand ChemE
Effect of liquid & gas velocities on #tower / #column #tray #hydraulics #processengineering
0:48
Boostrand ChemE
Process Design tips in Amine Gas Sweetening Units
8:28
Boostrand ChemE
How to Choose Correct Pressure Safety Valve Position in a P&ID
6:55
Boostrand ChemE
Which configuration shall we choose for a 3 phase #separator? weir or boot? #processengineering
0:44
Boostrand ChemE
Overpressure in a PSV check out boostrand.com/courses
0:56
Boostrand ChemE
Swing VS Non Slam Check Valve: Which one to Choose?
6:11
Boostrand ChemE
Typical Details in a P&ID
0:39
Boostrand ChemE
Depressurization timing check discount at boostrand.com/pid to enroll in P&ID course
0:59
Boostrand ChemE
Ensuring proper protection within a P&ID explained in P&ID course at boostrand.com/pid
1:00
Boostrand ChemE
Exchanger with removable bundle
0:15
Boostrand ChemE
Two Phase Flow Regimes check out boostrand.com/pipe-sizing
1:00
Boostrand ChemE
How to know pump operating point check out boostrand.com/pump
0:42
Boostrand ChemE
Valve Cavitation VS Flashing check out boostrand.com/control-valve
1:00
Boostrand ChemE
Hydraulics of pipes, pumps, compressors, and control valves in a process plant
2:46
Boostrand ChemE
Let's see how surge scenario happens in a compressor boostrand.com/compressor
1:00
Boostrand ChemE
Did you know? Reboiler pipe sizing can affect the whole column
3:30
Boostrand ChemE
Pump available NPSH calculation and optimization
4:49
Boostrand ChemE
Excel VBA for Chemical Engineers
3:50
Boostrand ChemE
Heat Exchanger Vs Air Cooled Exchanger: Which one to use?
6:17
Boostrand ChemE
Tips to handle Control Valves failure scenario
12:14
Boostrand ChemE
How compressor performance is affected by operating conditions and gas properties?
3:54
Boostrand ChemE
Pipe Sizing in Process Plants
3:46
Boostrand ChemE
Digital Transformation in Chemical Engineers Career
23:44