Marcos Buenijo wrote:
r john wrote:Marcos
If your talking thermal efficiency thats a total different ball game. Most CHP plants run at 80 to 90 per cent efficiency its just how you split between electric and heat that is the difference.
http://www.bios-bioenergy.at/en/electricity-from-biomass/screw-type-engine.html
OK, so we've cleared things up - these engines do not (indeed, cannot) have the extremely high thermal efficiency suggested in your previous posts. Thermal efficiency is what fundamentally distinguishes/differentiates one heat engine from another. When people consider the "efficiency" of a heat engine, then it is thermal efficiency that is generally considered. Hence, you can understand my consternation at your claim of "50% electrical efficiency" (BTW, the only way I know to interpret this claim is that 50% of the heat provided to the system is converted to electricity, and this implies a thermal efficiency so high as to be unbelievable).
The engine in the link you provided lists "Electric efficiency at nominal load operation of 12,6 %" using steam at 500F and about 360 psig. This is very good efficiency for a once through expander at these parameters, especially with the fairly high exhaust pressure. In particular, the high condenser pressure/temperature makes for excellent use of the heat in cogeneration applications. I agree that these seem to be great for combined heat and power purposes. However, they really should be made much smaller for real impact.
r john wrote:Marcos
I think you need to understand how steam efficiencies are calculated. The efficiency is a function of the temperatures used with the limiting factor being the strength of stainless steel at high temperatures. If you use power station temperatures in a screw expander you will get power station efficiencies in fact a screw expander can be used at higher temperatures as the stainless steel deteriorates more in a blade than a screw.
Marcos Buenijo wrote:
r john wrote:Marcos
I think you need to understand how steam efficiencies are calculated. The efficiency is a function of the temperatures used with the limiting factor being the strength of stainless steel at high temperatures. If you use power station temperatures in a screw expander you will get power station efficiencies in fact a screw expander can be used at higher temperatures as the stainless steel deteriorates more in a blade than a screw.
R John, if you can provide resources that demonstrate an engine using screw expanders and achieving a net thermal efficiency higher than conventional modern steam power plants, then please do so. Personally, I have strong doubts that this has been done, but I would love to learn otherwise.
...actually, I'm interested to know about any such system over 20% as well.
r john wrote:
Marcos
As I said its very important to understand steam cycles when it comes to power station efficiencies. At present conventional steam power stations have an upper temperature limit imposed due to the type of metal used in the turbine blade and a lower limit set at approx 350C due to water droplets eroding the turbine blades. To overcome this MHD technology is used for the higher temperature phase the output of which produces a conventional steam phase with a lower temperature ORC phase recovering the heat below 350C. Its this lower phase where twin screw technology is being used very effectively.
As for discrimination between technologies of twin screw expanders and turbines both have similar usage maps its just twin screws will tolerate wet steam whereas turbines certainly wont.
http://www.engineering.zhaw.ch/fileadmin/user_upload/engineering/_Institute_und_Zentren/IEFE/Kompetenzen/ORC_Final_Paper_WEC2011_2011-07-30.pdf
The other high thermal efficiency option is the DICE using coal or charcoal slurry but with ORC capture of waste heat from the exhaust and cooling systems.
r john wrote:Marcos
Given your background I am very surprised you have been arguing down the thermal efficiency road. Turbines are normally rated on isentropic efficiency hence the figures quoted by Kobelco for there steamstar.
As regards small steam power plants theres plenty on the market but the price makes them uneconomic. This article gives an insight at the low end of the market
http://peer.ccsd.cnrs.fr/docs/00/78/98/84/PDF/PEER_stage2_10.1016%252Fj.applthermaleng.2011.06.008.pdf
Marcos Buenijo wrote:
r john wrote:Marcos
Given your background I am very surprised you have been arguing down the thermal efficiency road. Turbines are normally rated on isentropic efficiency hence the figures quoted by Kobelco for there steamstar.
As regards small steam power plants theres plenty on the market but the price makes them uneconomic. This article gives an insight at the low end of the market
http://peer.ccsd.cnrs.fr/docs/00/78/98/84/PDF/PEER_stage2_10.1016%252Fj.applthermaleng.2011.06.008.pdf
My emphasis on thermal efficiency has a simple explanation. I consider the primary purpose of this forum as a resource for education. There is a lot of nonsense circulating on the net about steam engine systems, and I like to clear things up whenever I have an opportunity. The "thermal efficiency road" is exactly the one that most readers take when a discussion of "efficiency" in heat engines is made. Your previous claims on the "efficiency" of steam engine systems could easily lead many to believe that the thermal efficiency of steam engine systems are much higher than in reality. Therefore, my purpose in replying to your claims was to provide clarification for the casual reader.
The article you linked discusses possibilities for expanders in micro organic rankine cycle engines. I'm aware of all these possibilities. Unfortunately, it provides no information on actual products available for purchase. I am particularly interested in micro systems (under 10 hp) as I believe these would be best suited for the residential scale. Also, I am particularly interested in steam systems vs. ORC mainly because steam will more easily provide higher condenser temperatures that make additional heating applications possible. If you know of any such systems, then please let us know.
r john wrote:What nonsense on steam engines am I accused of writing. I point out good steam systems can achieve over 50% electrical efficiency and 90% overall thermal efficiency which is conservative to what current generating plants are achieving with existing technology going beyond 60 percent (GE claim for there systems).
http://www.ge-energy.com/products_and_services/products/gas_turbines_heavy_duty/flexefficiency_50_combined_cycle_power_plant.js
I provide articles which show steam conversion efficiencies of 50 to 60 percent at various points on the steam cycle. What you then do is ridicule steam performance because you isolate such a small element of the steam cycle for a particular technology Ie screw expander when in reality compound engines are always far more efficient using a greater part of the steam cycle. Typical compound would be HP piston, LP Piston, Turbine, Screw Expander.
Obviously achieving even in excess of 40% electrical efficiency on sub 1MW systems is not easy but can be done with a Jenbacher gas engine with exhaust heat recovery steam turbine and cooling system recovery screw expander. Alternatively a Capstone Gas Turbine , HP & LP Piston Steam Engine, LP Turbine and Screw Expander.
If you want a residential system then look at the Otag Lion which uses a linear generator (Linator) and was well ahead of its time but I believe went into receivership over patent arguments.
As for products for purchase if you look up the individual company websites in the article they do have a range of products to purchase but you will need to email the companies to obtain prices. Normally in the £1-2k per KW generated for plant in the 10KW to 250KW range.
Those who hammer their swords into plows will plow for those who don't!
Marcos Buenijo wrote:Just sharing one of my wacky ideas. I like the idea of using a modernized piston steam engine with good thermal efficiency and fueled by biomass as an off grid power plant. One of the main benefits of a piston steam engine in this setting is the ability to operate at very low power for extended periods while providing heat in a convenient package. Steam is an excellent heat transfer medium. Unfortunately, these systems are not available. So, I considered, why not a biomass fueled steam generator for heating applications? Furthermore, since my recent research shows that charcoal gasifiers can power very small engines cleanly and with impressive energy density, then how about a system that chars wood chips at a controlled rate while generating steam on demand? The charcoal produced from the system can then be stored for use as required in fueling small engines.
I'll describe a basic configuration to get the reader thinking on the topic. Particulate biomass like wood chips is gravity fed through a vertical pipe section. A hopper is connected to the top. A lower section of the pipe is surrounded by a combustion chamber fueled by pyrolysis gases generated from the heated wood chips. A key point to consider is that pyrolysis occurs at a rate directly proportional to the rate at which the biomass feeds through the system (within limits). So, it's possible to govern the steam rate with a motorized auger tha removes charcoal from the base of the system. A steam generator tubing coil is placed above the combustion chamber in the annular space between the pipe and exterior shroud used to form the combustion chamber. The draft draws air into the base of the system to cool the lower pipe (and charcoal within) and combust the pyrolysis gases escaping from a ring of holes in the inner pipe at the base of the combustion chamber. These hot combustion gases pass over the steam generator coil before heating the hopper that contains the fuel (thereby drying and/or preheating the fuel before it enters the pipe).
The steam generated is sent through an insulated line to a high point in the system, then distributed to various heating applications. This is controlled in two ways. First, each load has a valve to control flow. Second, the final pass of the steam/condensate is through an insulated water storage tank. The temperature of the water in this tank is used as a control for the auger motor.
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