User:Milton Beychok/Image Gallery2: Difference between revisions
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== | ==17 Images== | ||
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|[[Image:Industrial piping.jpg|300px]]<BR><BR>'''Large-scale industrial piping'''||[[Image:Visbreaker.png|300px]]<BR><BR>'''Schematic diagram of the visbreaking process''' | |[[Image:Industrial piping.jpg|300px]]<BR><BR>'''Large-scale industrial piping'''||[[Image:Visbreaker.png|300px]]<BR><BR>'''Schematic diagram of the visbreaking process''' | ||
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|[[Image:Natural Gas Condensate.png|298px]]<BR><BR>'''Schematic flow diagram of a typical facility for separating and recovering liquid condensate from raw natural gas'''] | |||
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Revision as of 13:39, 5 September 2008
17 Images
Schematic diagram of a typical packed bed absorption column |
Structured packing used in packed beds |
Schematic diagram of a Claus sulfur recovery plant |
Randomly dumped packing material used in packed beds |
Randomly dumped packing material used in packed beds |
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Drawing of Henri Giffard's Injector A- Steam from boiler, B- Needle valve, C- Needle valve handle, D- Steam and water combine, E- Water feed, F- Combining cone, G- Delivery nozzle and cone, H- delivery chamber and pipe, K- Check valve |
A gas flare as used in the process industries |
File:Centrigugal Pump.png Cut-away view of a centrifugal pump |
A lobe pump with three-lobe rotors |
A hand-operated pump |
Schematic diagram of a conventional spring-loaded pressure relief valve |
A typical control valve with pneumatic actuator and a positioner |
Schematic diagram of conventional control valve with a pneumatic actuator |
Large-scale industrial piping |
Schematic diagram of the visbreaking process |
Schematic flow diagram of a typical facility for separating and recovering liquid condensate from raw natural gas] |