A PROCESS OF PREPARING A FUEL

Abstract: Fuel especially for use in cyclone burners is prepared in such a way that wood is ground in a first step to a powder with a particle size of up to 15 mm, that the resulting powder is dried to a moisture content of maximum 15%, preferably maximum 10%, and that this dried powder is ground in a second step to an average particle size of 100-900 //cm, preferably maximum 700 //cm. This fuel with an average particle size of below 900 //cm and with a moisture content of maximum 8% is used as fuel in boilers, hot water boilers, hot air boilers, internal combustion engines and the like.

Description: A PROCESS OF PREPARING A FUEL This invention relates to a process of preparing a fuel, especially for use in cyclone burners (turbulence burners) . Wood and firewood have been used for a long time as fuel both in industry and households. The firewood has been used as cut to various sizes, such as logs (split billets) and chips, and attempts have also been made to utilize- such waste products as sawdust for fuel. ' Investigations have shown that there will be a great excess of hardwood in the form of low-grade timber from thinned and cleared areas and such as is called thicket. Firing of this wood in the form of chips, so-called green chips, has beeh started but does not appear to lead to any market for the green chips (chips of new wood material!) • Now it has surprisingly been found that wood powder having an average particle size of approx. 100-900 μm, preferably 300-700 μm, can be combusted with a very good effect in cyclone burners similar to those now used in oil combustion. This invention relates consequently to a process of preparing fuel, which is characterized in that the wood is ground in a first step to a powder having a particle size of up to 15 mm, preferably 12 mm, as e.g. 5 mm, that the resulting powder is dried to a moisture content of maximum 15 , preferably maximum 10 % , and that this dried powder is ground in a second step to an average particle size of 100-900 μm, preferably 300-700 μm, and a moisture content of up to 8 % , as e.g. 3-5 % . The wood is preferably in the form -of chip ' s as starting material for the grinding process. The process is preferably carried out in such a way that chips conveyed to a plant for carrying out the process or produced on the spot in a way known per se are ground after storage or directly e.g. in a rotary cutter or hammer mill. The chips which , can be of any type o ' f wood, e.g. hardwood, such as birch, aspen, or softwood, such as spruce, pine, or mixtures thereof, have usual chip size, e.g. a thickness of about 5 mm and a length of about 30 m The moisture content of the chips is e.g. in the range of 30-65 % . It is suitable if the moisture content of the chips is about 30 % , which can be . achieved by stacking in the forest before transport to the milling plant or by pr drying in an automatic stack, where the chips are stored before grinding. Drying energy is saved by this lower moisture content. The mill for this first grinding is preferably provi ed with magnetic separator and separators for heavier material than chips, such as coarse sand, glass, nonmag¬ netic metals, etc. At this first grinding operation chips are ground to a powder having a particle size of up to 15 mm, material having a larger particle size being returned to the mill and with a particle size of below 15 mm being transferred to a drying plant, optionally wit an intermediate storage container for balancing the produ tion in the mill ' and the drying plant. The powder from the first grinding process has about the same moisture content as incoming chips, i.e. about 30-65 % . Drying can e.g. take place in a drum with e.g. hot air, flue gases and optionally supplied secondary air, and the flue gases can derive from a boiler fired with wood powder. The boiler need only consist of a burner and a combustion chamber but should be so well insulated that the heat, losses will be as small as possible. If * the grou powder has a minimum moisture content of 30 it is so we that . no problems will arise with explosion or ignition, even if the flue gases contain glowing or burning particl at the inlet of the drying drum. It is suitable to adjust the temperature of the flue gases (the drying air) to 550-850°C depending i.a. on the moisture content and the particle size of the starting material. For obtaining as good an efficiency as possible the temperature of the out going gases should be as low as possible, ' e.g. down to about 55 C. It is possible to control the whole drying process by means of a thermostat. The flue gas after the drying apparatus can be purified and rid of i.a. from dust and other solid partic- les, e.g. by means of cyclones and/or by cleaning with water (scrubber), automatic heat recovery taking place. In view of the explosion risk of this dust and its flamma- bility blow out panels and automatic fire extinguishing equipment should be arranged in connection with these cyclones, and in addition, at all exposed places in the whole process. The dried powder from the drying plant can be stored in containers so that a buffer is obtained for the follow-' ing grinding step. The .mills ' used in this second grinding step can be analogous to those used in the first grinding step but the sieve apertures " are smaller. Suitable sieve apertures are such that particles having a size of up to 0.700 mm are obtained; if the powder is intended for internal combustion engines the sieve apertures should be chosen ' smaller, say up to 0.300 mm. The powder is dried more by the friction heat generated in the mills and a "dry" powder (wood powder) with a moisture content of about 2-5 % is obtained. The powder is transported to a container for finished powder from this second grinding step. The finished powder can of course be used directly in a plant lying close to the place of the powder preparation for firing e.g. of steam boilers and hot water boilers. However, it is easily transportable e.g. in tank trucks. ' In this way it is possible to place the plant for the preparation of wood powder on a spot suitable for this production while the place of consumption is arranged more suitably for the use, i.e. e.g. for the production of electric power and heat for heating purposes. Mills, driers and transport means known per se can be used. The transport means can e.g. be belt, conveyors and chain conveyors, but it must be considered that explosive mixtures of wood powder and air should be avoided. Pneumat systems can be used considering this and screw conceyors can supplement other systems. Heat recovery is of course arranged in so far as this is economical. The combustion of the wood powder i.a. takes place i such a way that air and powder are' mixed by the aid of turbulence and form a dust-cloud which can be completely combusted, the combustion taking place substantially similarly to that in an oil burner. It is suitable to . ignite the dust-cloud by means of a pilot burner for oil or gas or a special incandescent filament. It is possible to use such wood powder burners in boilers now fired by oil. You can check and control the combustion in the same way as with oil. There will be no glowing mass and small amounts of ashes are obtained. The problems associated with firing -in boilers with stoker or grate are avoided. " '" The product, prepared according to this invention has a good storage ability; thus it will not absorb moisture, is not biologically degraded and will provide a good efficiency at combustion. Such high flame temperatures as 1200-1600 C can be obtained in combustion. Only negligibl quantities of toxic substances, such as polycyclic aromati "hydrocarbons, will arise in the flue gases as distinguishe from usual wood or chips firing. Thanks to the good possibilities of transporting the powder this can replace oil, if the transport ways from the place of the preparation to the place of consumption will not be too long. Moreover, it has the advantage over oil and carbon that the flue gases are not acidifying and that acid precipitation does not occur. As the size of a burner substantially decides the maximum particle size used therein the average particle size of powders to be delivered to a certain plant should be adjusted according to the capacity of this plant. Now it appears as if average particle sizes of up to 700 μm are suitable. In the lower average -particle size range of 100-300 μm there are uses in small burners and above all in internal combustion engines-. It is also evident that the resulting powder contains very small particles as well as bigger ones as only too big particles are separated. It is also clear that the wood can consist of other things than chips. Thus, the starting material can be sawdust, cutter shavings and waste material from wood working plants

Claims: PATENT CLAIMS 1. A process of preparing a fuel, especially for use in cyclone burners, characterized in that wood is ground in first step to a powder with a particle size of up to 15 that the resulting powder is dried to a moisture content maximum 15 , and that this dried.powder is ground in a second step to an average particle size of 100-900 μm.and a moisture content of less than 8 % . 2. The process of claim 1, characterized in that the moisture content is maximum 10 after drying. 3. The process of claim 1 or 2, characterized in that the moisture content after the second grinding operation is 2-5 4. The process of any one of claims 1-3, characterized that the average particle size of the resulting fuel is 300-700 μ . 5. The process of any one of claims 1-3, characterized that the average particle size of the resulting fuel is 200-400 μm. 6. The use of wood pow'der with an average particle size of below 900 μm, preferably below 700 μm, and with a moisture content of maximum 8 % as fuel in boilers, hot water boilers, hot air boilers, internal combustion engin and the like. 7. The use according to claim 6, characterized in that 3 the powder -has a bulk density of maximum 350 kg/m and consequently a high effective thermal value relative to th volume as compared with a usual wood fuel.

Inventors: GABRIELII S, HULTEN G
Applicants: EBE ENERGIBRAENSLE AB, GABRIELII S, HULTEN G
Application year: 1981
Main classification: C10L5
IPC codes: C10L5, F23K1