Increasing pressure loss alone does not increase output, it only allows you to do other things in the design that may. One way to look at HRSG efficiency is by looking at gas outlet temperature. This can be limited by pinch, but there are also ways around this. This article by Ganapathy may...
Ed is correct, heat transfer in an HRSG is usually gas-side limiting, so a well designed unit is designed to use the maximum pressure loss that the GT can handle. If a higher pressure loss is available for the design, it can be used to make the HRSG smaller which should result in lower cost.
Cold end corrosion is primarily dependent on the sulfur content of the fuel and the temperature of the cold surface. For example in boilers, raising combustion temperature doesn't mitigate it much since the temperature of the tube metal is primarily dependent on water temperature. So you should...
The thought process is likely that for low air flows, the on/off-controlled fan is off and the VFD-controlled fan provides adjustment. For higher air flows, the on/off-controlled fan is on and the VFD-controlled fan provides adjustment. As to whether this would provide the desired results would...
I'll put in a second vote for Trello. We used it for almost exactly what you are describing. Can use it from the desktop (browser-based), or mobile app. Typically we would have a Board for each person and "To Do", "Doing", and "Done" lists on each person's board. Its easy to move items...
I would expect valves car sealed for safety to have some sort of administrative procedure to document that the process was in a safe condition for the valve to be operated when the car seal is removed. We do not use this term specifically, but we do identify valves on the P&ID that are car...
The above link is not the type of toroidal ring you need. Vent stack toroidal rings are essentially a small (1/2" to 1") diameter piece of SS tubing bent into a circle (ends welded together) with the same center line diameter as the vent stack pipe and welded to the end of the vent stack. A...
In the refining industry I have seen it both excluded and added as a percentage of the equipment area (e.g. an additional 10-20%) but more often excluded. This can be interrelated with how the company handles calculation of the heat of vaporization and the confidence level in the description of...
API 2000 does not in all cases give absolute requirements on which potential causes of overpressure are applicable to a particular tank. This may require evaluation based on the particulars of the tank. It's good to have a sound engineering basis for determining applicability of scenarios and...
We have had the scenario hageye describes actually happen. We considered this a very serious near-miss. As a result, in pilot operated RVs that could encounter water (from the process or steaming) we have changed the soft goods to withstand higher temperatures and have added steam tracing and...
Instead of
integer, parameter :: dbl = selected_real_kind(p=7)
Try
integer, parameter :: dbl = selected_real_kind(1.D0)
and specify all real constants like 0.1 as 0.1_dbl
For liquid coolers, see API STD521 (5th ed) section 5.15.7.4. It becomes a question of whether your solid floors qualify as a "surface at which a major fire could be sustained". If so then it requires relief. If your floors are designed so that the drainage is adequate then it does not.
If...
We use Farris valves extensively, mainly the 2600 series you are referring to. No specific experience with the super capacity valves, but the main drawback I see is weight. Those things are heavy! Otherwise, they are built to ASME Section VIII and capacity certified. Acceptability beyond...
