Home |
Search |
Today's Posts |
|
#1
![]() |
|||
|
|||
![]() Nav wrote: I think it's also pretty sloppy to call the inlet prssure to a turbine a vacuum. Don't you guys traditionally use mmHg for near vacuum pressures? We sometimes us inHg and sometimes we use psia, depends on the shipbuilder and machinery supplier. It is reasonable to assume a metric ship displays mmHg ... makes no matter as far as operation is concerned. It is hardly "sloppy" to call inlet pressure the condenser a vacuum. It is engine exhasut and as long as it is less than atmospheric it is a vacuum. Condenser pressure is engine exhaust pressure for engineering purposes. We determine condensate depression and other operational factors by calculating condenser vacuum based on exhaust temperature. Rick |
#2
![]() |
|||
|
|||
![]()
Rick wrote:
We determine condensate depression and other operational factors by calculating condenser vacuum based on exhaust temperature. Here's a good homework question for Navvie/Navjax/Navsprit: Define "condensate depression" and explain it's significance in steam plant operations. DSK |
#3
![]() |
|||
|
|||
![]() DSK wrote: Rick wrote: We determine condensate depression and other operational factors by calculating condenser vacuum based on exhaust temperature. Here's a good homework question for Navvie/Navjax/Navsprit: Define "condensate depression" and explain it's significance in steam plant operations. Good lord. How childish. No wait, it's a genuine question right? Well Doug, it's a temperature difference that is impoertant to overall thermodynamic efficiency which can be defined as P/Qh-Qc. For a steam plant, the steam temperature and it's dryness fraction times the mass flow rate determine heat fluxes in that equation. Yes Doug, I did freshman thermodynamics. Did you? Cheers |
#4
![]() |
|||
|
|||
![]()
Nav wrote:
Good lord. That may not be the response you were looking for ... You guys have fun, it is time to bow out of this one. Rick USCG Chief Engineer Steam/motor/gas turbine |
#5
![]() |
|||
|
|||
![]()
Define "condensate depression" and explain it's significance in steam
plant operations. Nav wrote: Good lord. How childish. No wait, it's a genuine question right? Well Doug, it's a temperature difference Right. Where? I mean, between which two points in the steam cycle? ... that is impoertant to overall thermodynamic efficiency which can be defined as P/Qh-Qc. How else could it be defined, in more everyday terms? ... For a steam plant, the steam temperature and it's dryness fraction times the mass flow rate determine heat fluxes in that equation. Yes Doug, I did freshman thermodynamics. Did you? Yep. But your answer is mostly gobbledy gook to me. What's a dryness fraction? Are you saying that condensate depression relates to degree of superheat? Rick can you make any sense of this? DSK |
#6
![]() |
|||
|
|||
![]()
DSK wrote:
Yep. But your answer is mostly gobbledy gook to me. What's a dryness fraction? Are you saying that condensate depression relates to degree of superheat? Rick can you make any sense of this? You both have really muddled and overcomplicated the issue. Condensate depression is simply the difference in temperature between the temperature at which steam will condense at the pressure existing in the condenser and the temperature of the condensate in the hotwell. Too much cooling (beyond about 10* below condensation temperature) means that BTU's are needlessly tossed overboard and must be replaced by burning expensive fuel. Rick |
#7
![]() |
|||
|
|||
![]()
Rick wrote:
You both have really muddled and overcomplicated the issue. All I did was ask the question. Condensate depression is simply the difference in temperature between the temperature at which steam will condense at the pressure existing in the condenser and the temperature of the condensate in the hotwell. Absolutely & precisely correct. Too much cooling (beyond about 10* below condensation temperature) means that BTU's are needlessly tossed overboard and must be replaced by burning expensive fuel. Yes.... although the Navy cares less than they should about fuel economy. We used to shoot for 5 degrees. Here's a fun thought... let's list all the unexpected things found in main condenser headers. How about a case of beer (unfortunately mangled & empty)? Fresh Steam Doug King |
#8
![]() |
|||
|
|||
![]() Rick wrote: DSK wrote: Yep. But your answer is mostly gobbledy gook to me. What's a dryness fraction? Are you saying that condensate depression relates to degree of superheat? Rick can you make any sense of this? You both have really muddled and overcomplicated the issue. It's Dougs fault. He always does this (asking ever more arcane irrelevant questions) when when he's painted himself into his corner of ignorance. He goes on and on until he finds something that you can't be bothered to answer and then he'll jump around the playground claiming he scored some point. I can see he's trying to do it to you now... Cheers |
#9
![]() |
|||
|
|||
![]() DSK wrote: ... For a steam plant, the steam temperature and it's dryness fraction times the mass flow rate determine heat fluxes in that equation. Yes Doug, I did freshman thermodynamics. Did you? Yep. But your answer is mostly gobbledy gook to me. What's a dryness fraction? Are you saying that condensate depression relates to degree of superheat? You claim to have done freshman thermodynamics in engineering and you don't know what the dryness fraction is? How strange. Perhaps you had better look it up -'cos I know nothing! Try a google and you'll learn some freshman engineering on steam plants. Cheers |