Development of a pellet boiler with Stirling engine for m-CHP domestic application
© Crema et al; licensee Springer. 2011
Received: 8 September 2011
Accepted: 21 November 2011
Published: 21 November 2011
A new sustainable technology has been designed by Fondazione Bruno Kessler through its unit Renewable Energies and Environmental Technologies. This technology is realized integrating in a single system (1) a Stirling engine (mRT-1K) from a pre-engineering design of Allan J. Organ; (2) a micro-heat exchanger technology, to reduce the net transfer unit deficit on the hot side of the heat engine; (3) a customized pellet boiler, able to extract electrical and thermal power; and (4) a customized hydraulic circuit, connecting the cool side of the Stirling engine and the heat generation on the second section of the pellet boiler. The objective of this paper was to present a new technology for the micro-cogeneration of energy at a distributed level able to be integrated in domestic dwellings. Most part of the available biomass is used in buildings for the generation of thermal power for indoor heating and, in minor cases, for hot sanitary water. In the Province of Trento, 88% of the biomass is used for this purpose. The full system is actually under integration for the test phase and not yet tested. The first tests on the single components have confirmed preliminary results on the Stirling engine with respect to the tolerances, pressurization, and proper integration of the electrical generator-driven control system. The pellet boiler has been tested separately, confirming an overall thermal efficiency of 90%.
Keywordsmicro-cogeneration Stirling engine pellet boiler renewable energy
The cogeneration of energy at a distributed level is one of the leading arguments in large part of energy policies related to renewable energy resources and systems. The actual marketable solar systems for domestic and distributed applications (photovoltaic [PV] and solar thermal) suffer notable limitations: (1) The low overall (electrical) efficiency of PV systems creates a small collected energy from the available space, sometimes restricted in the surface to a few square meters; (2) the stagnation temperatures on solar thermal collectors are actually limiting the diffusion of solar thermal systems; and (3) fixed and non-retrofittable systems may generate energy in an intermittent manner not aligned with the auto-consumption profile of domestic spaces.
On the other end, the growth of the distributed energy generation is far above all previsions, not only in new energy markets but even in highly industrialized countries. In Germany, more than 50% of the 43-GW installed power in 2009 is in the hands of individuals and farmers, on all sectors of solar, wind, biomass technologies . At the distributed level, an increasing number of technologies are approaching the market, such as new and efficient PV or concentrated photovoltaics ; micro-combined heat and power [m-CHP] solutions based on solar , fuel cells , or biomass; and technologies for the efficient production of thermal energy such as ground source heat pumps, air heat pumps, and solar thermal.
The development of new cogeneration systems based on non-intermittent sources able to be coupled and eventually hybridized with other sustainable technologies is highly required. A compact micro-cogeneration system based on a pellet boiler integrated with a Stirling engine is presented, realized compatibly with the market-levelized energy cost. This paper presents, for the first time, the different stages of the development of such m-CHP biomass technology.
Improvements in combustion technology allow the adaptation of a retrofitted combustion chamber with the Stirling heat exchanger in a new efficient solution, optimizing the electricity generation, the heat removal from different parts of the system at different temperatures, and the overall efficiency.
Optimized Stirling engines and new compact heat exchanger technology can reduce the costs and improve the performance of small heat engines, so they can operate with higher proportions of Carnot efficiency on the working temperatures (~600°C) from the combustion burner.
The high cost and low power efficiency of gas-fuelled m-CHP systems, combined with increases in natural gas prices, both absolute and relative to electricity prices, can undermine the financial viability of gas-fuelled m-CHP. There is an urgent need for alternative m-CHP systems, of which solar or biomass m-CHP, whether separately or as a hybrid, is an option with high potential.
Generating the electrical power only when thermal energy is required by the building
Generating the electrical power dissipating the extra thermal energy not required by the building
The first will be used in most parts of the applications where a grid connection is available, and the second will regard remote locations (mountain cottages) where the grid connection is not present. An electrical energy storage will be required to match energy generation with end-user demand of energy. In both cases, the pellet boiler will be provided with a volumetric control of the pellet in order to make the burner work at a low power (>5 kWth).
Materials and methods
Introduction to economical aspects
The biomass combustion systems (biomass boilers and stoves) are one of the most diffused and cost-effective heating systems in the Alpine region. The overall efficiency obtained by the best and state-of-the-art technologies is comparable to those on natural gas or fossil fuel boilers, with values above 80%. The m-CHP generation from a pellet or wood burner is a potential added value to the base technology.
A market analysis reveals that Italy is the first European country in the specific market sector of the pellet stoves, accounting for 800,000 domestic systems installed at 2008 and 380,000 units produced in 2006. It adds a growth of 300% in the last 5 years (2003-2008) in pellet consumption and use. To have a comparison data, in Europe, there have been 4.4 Mt produced in 2006 with respect to 8.4 Mt in 2010 . In the European energy market, biomass has a share of 51% with respect to the energy produced by renewable sources, of which 85% comes from domestic plants and about 15% from industrial plants (multistage combustion, gasification, pyrolysis processes). In addition, the direct production of thermal energy from renewable sources, about 97%, comes from biomass combustion . In addition, 97% of all direct thermal energy from renewable sources comes from biomass combustion.
A recent report from Frost and Sullivan  showed that biomass can provide a strong support to renewable energies in the European context. This source provides currently two thirds of the specific sector and has a strong growing margin since the raw material produced in the EU 25 territory is increasing. The same report underlines the biomass context, which is wrongly considered an energy resource of the past, that financing support for technological development can provide solutions for an advanced system, reduction of costs (the conversion ratio €/kW is one of the more advantageous in the market, with costs lower than 2,000 €/kWe), environmental sustainability, and lower levels of impact.
The present project aims to realize a system which is capable of covering a part of the demand for electrical energy and the demand for thermal energy for heating and hot sanitary water purposes.
There is a good match between production and demand of electrical energy since a pellet stove is mainly used during the part of the day which also has an electrical demand. For this reason, most of the electrical energy is consumed locally.
Modularity of the generation system: The system can support different demands of electrical and thermal power. The electrical conversion ratio and the thermal output can be regulated by changing the load in the combustion chamber.
The external combustion engine provides a silent, clean, and reliable system with limited cost for management and maintenance.
With an averaged electrical efficiency from a full load to a partial load of about 10%, the electrical potential production is 3 TWhe/year for the 8,400,000 tons of pellets produced yearly in Europe. Since the wood production is at least one order of magnitude higher, the whole potential electrical production is 35 TWh/year, which is roughly one tenth of the electrical production in EU from nuclear plant.
The pellet boiler m-CHP system
The pellet cogeneration boiler is based on the integration between a Stirling engine and a biomass pellet boiler. The subcomponents of the specific technology are under integration. They include a Stirling engine, the mRT-1k, pre-engineered by Allan J. Organ .
The overall system is designed as illustrated in Figure 1. The Stirling engine is integrated directly inside the combustion chamber. Its heat exchanger is immediately above the burner. The Stirling engine can start operating and generating electrical and thermal power after a transient time to keep the engine at proper working conditions (hot and cold temperatures, energy flow through the heat exchanger). A drive control electronic system activates the Stirling engine controlling the generator and making it working as a motor.
A spiral screw, electronically controlled, advances the pellet. The burner is designed to provide stoichiometric primary air to realize a flame of 18 kWth. The pellet boiler is mainly composed of (1) a burning chamber connected to primary air which is blown inside using a forced flow system; (2) an internal water circuit to remove thermal power after the Stirling engine and maintain the exhaust temperature in the range of 80°C; and (3) an external water boiler to store thermal energy for the heating of the indoor environment and the production of hot sanitary water. The hydraulic system comes from the boiler; the water is pumped inside the cold end of the Stirling engine to cool and maintain a temperature of about 45-50°C. It goes to the boiler heat remover and goes back to the water boiler at a temperature of about 75°C. The mass flow of the pellet and the water will be calibrated as a function of the energy balance able to maintain the system in a steady-state thermal condition. The electrical power is derived by the engine adapting to the specific condition of the grid connection and acting through a load management system.
The system has been provided with thermostatic control for high temperature to activate control on the combustion chamber and stop the biomass flow to the burner in case of alarm. The system first activates the water circulation through the Stirling and the water jacket; secondly, the burner is started. The control system will monitor the transient until a threshold temperature. At that condition, the Stirling engine is activated by the generator used as a motor using the drive control as the engine speed control. The rated power will be reached.
The cogeneration engine
List of symbols
Heat transfer per unit length (W/m)
Inside diameter (m)
Thermal conductivity [W/(K m)]
Dynamic viscosity (Pa s)
Mean average gas pressure (Pa)
Swept volume - expansion space (m3)
Engine cycle frequency (Hz)
Nominal Displacement (m3)
Power output of the engine (W)
Mass flow (kg/s)
Entropy generation number
Entropy generation per unit length [W/(K m)]
Fluid flow duty parameter
Volume of expansion (m3)
Volume of compression (m3)
This is a modest value surpassed in some established designs. But it should be possible to exceed that value, thereby improving on the target 1-kW rating.
Regenerator of the engine: a new technology with improved performance (under patenting process)
Heat exchanger: the application of the micro-heat exchanger fluid dynamics and realized through a selective laser melting [SLM] process (see Figure 5 for a pre-design of the heat exchanger)
Design able to realize a condition of clear surface with limited powder deposition problems
Design able to provide an easy maintenance of the system
High external surface exposed to the flame radiosity
High internal surface for efficient heat transfer to the pressurized internal gas of the Stirling
The above constraints had been taken to a proposed solution of a heat exchanger based on micro-fluid dynamics, which improve the energy density transferred through the exchanger while maintaining a lower Reynolds number and, subsequently, a limited pressure drop with respect to the convective heat transfer coefficient.
The heat exchanger design has been based on the entropy generation minimization for the internal flow of the heat exchanger, where the working fluid of the engine is located. Minimizing the entropy generations in one component is equivalent to minimizing the loss of available work. The objectives were to increase the wall fluid heat transfer without causing a damaging increase in the pumping power demanded by the forced-convection arrangement. The method combines from the start the most basic principles of thermodynamics, heat transfer, and fluid mechanics [9, 10].
The pellet boiler
The pellet is inserted by an automatic spiral screw which can be controlled with respect to the heat input by changing its velocity. The primary air is injected at the burner level and controls part of the combustion process, the flame temperature, and power; it is able to provide the correct amount of combustive agent. Depending on process thermal requirements, the power can be ranged from 18 to 5 kWth, which is the minimum power required by the Stirling engine to generate 1 kWe at the output. While the peak power will be used to take the system at the working conditions, the steady state will be maintained through the minimum power to keep the engine running and generating electrical energy at a rated power output. In such way, the system will be cogenerating energy for a larger amount of hours per year, increasing the economic benefits from the system. At the present time, it has not been possible to develop a full calorific value boiler due to potential corrosion effects at the exhaust of the system caused by particulate, sulfur, and other contaminants potentially at a dangerous concentration inside the biomass pellet.
The electrical generator and the load management system
The efficiency of these two electrical conversions are respectively 88-90% for the first stage between mechanical power and direct voltage and 90-95% for the second stage through the inverter, in the range of 1 kWe. The efficiency can increase significantly at rising power over 2-3 kWe. In a few months, the two conversions can be performed by a two-axis control drive under realization by Moog industries; this new drive control will integrate in a single unit the two previous mentioned systems and will be able to reach an overall efficiency of 92-95%, integrating a sensorless generator control.
Natural gas burner-controlled mass balance, through a mass flow controller applied to the gas duct, and energy balance, through the calculus of the energy content on the different stages, from the input gas mass flow to inside the engine and in the water external cooling circuit
On the pellet boiler, mass and energy balance at the different stages, inside the burner, in the Stirling engine and in the water circuit
The technology will be tested with respect to performance and overall efficiency, noise level and reliability, long-term tests, and mean time before fault index. The full system will then be included in a series of planned projects inside the Province of Trento, such as the 'Tomorrow's Mountain Cottages,' a territorial program launched by the Province of Trento, and the 'FBK - MIT Sustainable Connected Home', a project in cooperation between Fondazione Bruno Kessler and the Massachusetts Institute of Technology. A start-up activity has been planned for the industrialization and commercialization of the final technology. The impact at the local level can either be supported by the local Energy Agency of the Province of Trento to small-scale biomass conversion plants and installations with respect to bigger cogeneration biomass power plants. A lot of the local activities are on the way to realize a whole chain of stakeholders involved at the local level .
The authors would like to extend some acknowledgements mainly to the Editor, to Dagmar Fiedler, to Michael Narodoslawsky, and all colleagues at TU Graz and eseia [European Sustainable Energy Innovation Alliance]. Special thanks also to the Autonomous Province of Trento and to the Energy Agency of the Province of Trento for supporting the demonstration of the technology in the BioDomUs project.
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