The present invention relates to a device according to the introductory part of claim 1.
The use of firewood in stoves for heating is widespread in Norway and represents an energy contribution of approximately 7 TWh/year 2002). In the time period between 1990 and 1999 the use of firewood in stoves increased by 11 percent The effluents from uncombusted components in stoves come particles (PM10), carbon monoxide (CO) and uncombed hydrocarbons (UHC) in gaseous phase. These emissions are caused by a combination of poor air diffusion in the stove and too low temperatures. It has been established that these emissions are significant on a national scale, and particle emissions from stove heating constitute 60 percent of the total national particle emissions, and 40 percent of the particle emissions of the larger towns, the other major source being traffic fumes. It is largely the older stoves that are responsible for the large emissions. Data from the National Bureau of Statistics of Norway show that 97 percent of all particle emissions from stoves in Norway come from closed stoves dang from before 1998.
The first stoves with catalysts reducing the amount of uncombusted components in smoke were available on the market towards the end of the 1980s. Other solutions comprising a vault and pre-heated secondary air underneath the vault, also contributing to significantly reduced emissions, appeared later on. Both these conceptual solutions were named clean-burning stoves. Today's requirements on new (clean-burning) stoves are a maximum particle content of 5 g per kilo of combustibles for catalyst stoves and a maximum of 10 g per kilo of combustibles for vault solutions. For traditional wood-burning stoves and closed stoves the particle average (calculated mean over the entire load range) emission factor has been calculated to be 40 g per kilo of combustibles. The requirements are specified in the Technical Regulation of the Planning and Construction Act (the National Technical Construction Department 2000). The current requirements are given in Norwegian Standard NS3059 (Norwegian Standardisation Association 1994).
The emissions of uncombusted components depends on the heating intensity and increase radically at low intensities (loading). Norwegian Standard takes this into account by weighing the emissions at different loading, and two classes have been defined: stoves that burn cleanly with a minimum fuel consumption of less than 0.8 kg/h (class 1) and those that burn cleanly with less than 1.25 kg combustibles per hour (class 2). Problems relating to emissions from traditional stoves are highly significant in an international context as well. Stoves with corresponding technical constructions exist in Europe, the US and Canada. This issue is particularly relevant in Austria, Germany, the northern part of the US and all of Canada, as well as in the Nordic countries. Problems relating to emissions of uncombusted components are also an issue in China, but then with coal instead of firewood as fuel. Problems relating to incomplete combustion are significant in a number of developing countries, for instance in India where an estimated number of 300 million small stoves do not let the smoke out above roof level, mainly discharging it inside buildings. This is one of the greatest health problems in India and in many other countries, inter alia in African countries.
There are a number of different stoves on the market both in Norway and other countries. Typical for most of these traditional stoves, is that air is supplied through an air inlet 8 in the front of the stove, see
The so-called clean-burning stoves of the vault type (no catalyst) dominate the Norwegian market today.
Normally, there is not sufficient air at the right places in the traditional stoves. While secondary air devices constitute an integrated part of the stove construction itself in clean-burning stoves, no solution exists to improve the combustion of uncombusted components in older, traditional stoves.
The present invention provides an afterburner which can be installed in already existing traditional stoves, and which ensures that the right amount of preheated air is supplied at the right place in the stove and is characterised by features given in the characterising clause of claim 1. Further advantageous embodiments are defined in the dependent claims.
In a stove with an after-installed afterburner according to the invention, uncombusted components will burn out and the emissions will be reduced proportionately. The amount of air and the degree of pre-heating are adapted to the individual stove construction by size and location of holes for air supply, as well as the surface area (height and width) of the afterburner.
A detailed description of the present invention is given in the following, with references to the drawings where:
The plate 1 is preferably rectangular and has a size that is adapted to the size of the wall of the stove in question. In a preferred embodiment, the folded plate can have a folded depth of about 12 mm (the depth of the afterburner) where the air flows through. The height of the afterburner according to the present invention is about 200 mm, and the width can vary between about 150 mm and 250 mm if the plate is adapted for this. This can be arranged by having the plate 1 be made of two parts 15a and 15b which lie on top of each other and can be mutually displaced horizontally, see
In order to get air into the afterburner 1, holes or slits 2 are drilled through the side or rear plate of the stove, preferably far down in order to allow the air to enter at the bottom of the chamber defined by the folded plate 1. In this manner, air is drawn from outside the stove, in through the drilled hole(s) 2. When the air enters the afterburner 1, it will rise up to the upper part of the afterburner and out through the holes 4 in the plate and out into the upper part of the stove 14 just below the vault 7. As the air runs its course through the afterburner, it will be preheated by heat from the flame in the combustion chamber 13 in the stove.
As mentioned above, the hole 6 arranged at the bottom end of the plate 1 establishes and maintains a pilot flame, that is to say that when the combustibles 12 are burning, some air will be sucked in already at the bottom through this hole and ensure an increased combustion near the hole itself. A separate flame will be near the hole and ensure increased heating of the remaining air which is drawn through the chamber behind the plate 1 up towards and through the holes 4, and ensure that the pilot flame ignites the uncombusted inflammable gases at the bottom of the combustion chamber 13.
In the above, it has been mentioned that hole 5 is for fastening plate 1 with screws. The idea is to screw auto-grooving screws into the side/rear wall of the stove. But alternative adhesives could be used, for instance magnetic fastening organs comprising for example four permanent magnets arranged at the plate's corners instead of screw holes. The magnets must be resistant to high temperatures, in the sense that the magnetism does not disappear or is weakened to the extent that they do not adhere. Magnets suitable for use in high temperatures are currently being developed. Another possibility is to use a glue or plastic adhesive of a type which can take the high temperatures that occur in a stove.
The plate 1 does not necessarily have to be rectangular, in the case of some stoves, a trapezoid shape may for instance be more suitable. However, there must be folds along all the ends in order to create the necessary canal/chamber for the air that is to be pre-heated before afterburning in zone 14 to rise up.
A series of experiments have been conducted to document that the after-burner works according to plan. Traditional stoves have particle emissions that vary a great deal depending on the loading on the stove, low loading cause higher emissions. There are also great variations between stoves. Typical particle emission values for traditional stoves are on average 12 g per kilo of combustibles (a variation of between 5 and 17 g per kilo of combustibles) with a load of 2 kg combustibles per hour and 50 g per kilo of combustibles (variation of between 40 g per kilo of combustibles and 60 g per kilo of combustibles) with a loading of 1 kg combustibles per hour.
In laboratory tests, experiments were first conducted with a traditional stove without an afterburner. The results showed emissions of 9 g per kilo of combustibles with a load of 2 kg combustibles per hour and emissions of 35 g per kilo of combustibles with a load of 1 kg/hour. This is somewhat lower than the average values for typical traditional stoves. An afterburner was then installed in the stove, which brought the emissions down to 1 g per kilo of combustibles with a load of 1 kg/hour. In total, this gives a reduction in particle emissions of between 70 and 90 percent, depending on the loading. Compared to the average for traditional stoves, this corresponds to a reduction of between 80 and 92 percent. With an even lower loading down to 0.5 kg combustibles per hour, the emissions increase to 35 g per kilo of combustibles. Traditional stoves have emissions of up to 80 g per kilo of combustibles in this loading range. For comparison purposes, experiments were also conducted with a stove which has been approved as clean-burning. The results show that a traditional stove wherein an afterburner has been installed, gives just as low emissions as a so called clean-burning stove at loading ranges above 1 kg combustibles per hour.
Number | Date | Country | Kind |
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2003 3457 | Aug 2003 | NO | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/NO04/00235 | 8/4/2004 | WO | 7/2/2007 |