Prior Art The present invention is based on the concept of em- ploying thermal radiation.

Thermal radiation has the characteristic property that it requires no medium for transferring energy between two bodies. This may be likened to the energy of the sun, which is conveyed to the earth.

Radiation having relatively short wavelengths will penetrate into openings of the surface layer of the mate- rial to be dehumidified, dried or the like. The radiation going through these openings will be reflected multiple times from moisture molecule to moisture molecule. If the moisture is absorbent enough, the likelihood is low that any part of the radiation will go out through the openings formed in the molecular structure of the material. Thus, the material will form a black surface.

The above process may be named"radiation of void", thus applying for radiation having wavelengths shorter than the openings of the surface structure. Due to the small openings in the molecular structure of the material to be dehumidified the radiation will be isotropic, i. e. the in- tensity is the same in all directions.

In the inner part of the material to be dehumidified and having its voids the radiation will have the spectral distribution described by Kirchhoff's law: <BR> <BR> elf, T) = ez (T) =.... es (g, T)<BR> r) r) and Stefan-Boltzmann's law regarding the total inten- sity:

The present invention is mainly developed for treat- ment, i. e. dehumidification, sanitation or drying, of sew- age sludge, but a person skilled in the art realises that it may be used for many different materials.

The present invention is also appropriate for dehu- midification or drying of some foodstuffs. Suitable food- stuffs may be crispbread, pasta etc.

In order to simplify the description the invention will be described mainly with sewage sludge as an example.

If at all treated sewage sludge at the present is often heated to rather high temperatures in the region of 800-900 °C. Such high temperatures make demands on the apparatus used, especially the vessel holding the sludge during heat- ing. However, sewage sludge is normally just used for land- filling or deposition.

Summary of the Invention The present invention is based on the concept of only employing radiation energy (thermal radiation) for heating the sludge or other material and that the radiation em- ployed encompasses a wave length range within which water has a high absorption coefficient. The radiation at other wavelengths is reduced.

A heat source is used to emit heat radiation. Vapor- ised moisture will be taken away by circulating air from the surface of the material to be dehumidified. The vapori-

sation of moisture of the material is done by means of ab- sorption and reflection. The heat source will emit heat ra- diation at wavelengths at which water has high capacity of absorption, with absorption coefficients larger than 1000 cm With radiation energy in a narrow wavelength band where the water has a high absorption capability, the ra- diation energy is transmitted direct to the water molecules in the material to be dehumidified. This result in rela- tively short drying times, relatively low energy consump- tion and normally no negative influence on the material to be dehumidified. Dehumidifying using"the void principal" as indicated above will give a low consumption of energy.

For sewage sludge the moisture ratio after drying should be 20% or less. By using the method of the present invention the moisture ratio may be decreased well below 20%. In the drying process the sludge will also be sani- tised to a certain degree. As the sludge is heated to 70- 120 °C in the process most bacteria of the sludge will be killed. The sanitised sludge may be recycled, i. e. it may be placed on e. g. fields for standing crops.

The method of the present invention can be used as a part of an ecological system of recycling. By such a system a number of advantages may be reached. The dried and sani- tised material, such as sewage sludge may be deposit or burned. The amount of refuse is reduced, decreasing the use of resources. If the dehumidified sludge is burned differ- ent materials may be recovered, saving resources and energy compared to using fresh raw material. It is possible to re- cover heavy metals, chromium, nickel, copper etc. from the ash after burning. It is possible to recover plant nutri- ents, such as phosphorous being a limited resource, for use in the cultivation of plants. The dehumidified and sani- tised sludge normally has a high energy value, e. g. 2.5-3. 5 MWh/ton. Thus, it may be used as fuel.

Brief Description of the Drawings Fig. 1 is a perspective view of a drying chamber ac- cording to the present invention.

Fig. 2 is a sectional side view of a modified chamber according to the present invention.

Fig. 3 is an"open"end view in sketch form of a chamber according to the present invention.

Fig. 4 is a sectional view of one example of a heat source to be used in the chamber of the present invention.

Detailed Description of Preferred Embodiments Figs. 1-3 show one embodiment of a drying apparatus including a drying chamber 1 in which the drying of the sludge or other material takes place.

The expression"element"2 will be employed below to refer to a radiation source. The element is designed as a device emitting radiation comprising a selected wavelength region. In one embodiment the elements 2 are made of a cen- tral electric resistor 15 surrounded by a tube 14. In other embodiments the electric resistor is replaced by hot water as the radiation source of the element 2. Also other energy media is possible to use as the radiation source. Independ- ent of which energy media that is used, it should be sur- rounded by a tube 14. Furthermore, the energy medium may be made more effective by the use of a plasma or a dielectric.

The elements 2 may be placed in racks or frames 120 Reflectors are normally placed in connection with the ele- ments. In order to realise good reflection of the radia- tion, the reflectors are generally made of aluminium, stainless steel or other high-reflective material. In the frequencies employed, these materials display reflection coefficients exceeding 95%. Radiation which impinges on the reflectors is guided by them back to the sludge. It is not a requirement that reflectors are employed, but they do

contribute to a reduction in energy consumption. Normally, the elements 2 are disposed in any optional direction what- ever in relation to the longitudinal direction of the dry- ing chamber 1.

As a rule, the walls of the chamber are clad on the inside with stainless and/or acid proof steel, aluminium or similar high-reflective material for radiation within the above-indicated selected wavelength region. In other words, the interior of the drying chamber is designed as a large reflector. The walls are generally thermally insulating. As shown in Fig. 1 a door 21 is arranged at each end of the chamber 1. In other embodiments there is a door 21 only at one end of the chamber 1, in which case the sludge 7 or other material is taken in and out of the chamber 1 at the same end.

The sludge 7 is normally received on a conveyor belt 13. In some embodiments a conveyor belt 13 of stainless steel is used to support the material to be dehumidified, reflecting some radiation back to the sludge 7. In some em- bodiments the conveyor belt 13 is made of a net of wires of stainless steel or the like. If the conveyor belt has a mesh form some elements 2 are placed in the centre of the conveyor, i. e. between the upper and lower horizontal parts of the conveyor. In other embodiments the sludge 7 is re- ceived on one or more carriages, that may be rolled into and out of the drying chamber 1. Also the carriages may have sludge receiving surfaces of a high reflective mate- rial, such as stainless steel. If a conveyor belt 13 is ar- ranged in the chamber 1, the sludge 7 is normally feed in at one end of the conveyor and feed out at the other end.

During the dehumidification process the conveyor belt is normally at a standstill.

The drying chamber 1 is normally placed on legs 19.

The drying chamber 1 is, in the illustrated embodiment, provided with a circulation fan 4 and a ventilation damper

11. An air inlet 16 and an air outlet 17 are placed at op- posite ends of the chamber 1. Both the air inlet 16 and the air outlet 17 are normally furnished with dampers, to open and close the inlet 16 and outlet 17, respectively. Nor- mally, the areas of the air inlet and outlet, respectively, are separated from the proper drying chamber 1 by parti- tions 20. The partitions 20 normally have openings for the conveyor belt 13. Furthermore, a conduit 3 for recircula- tion of air is provided, giving recovery of energy. A heat exchanger 18 is placed in the conduit 3 for recirculation.

The conduit 3 including the heat exchanger 18 makes it pos- sible to dehumidify and recirculate the air of the drying chamber. Furthermore dampers 11 are placed at each end of the conduit 3.

In one embodiment, as indicated in Fig. 2 the active part of the circulation fan 4 is placed in the conduit 3.

In other embodiments, as indicated in Fig. 1, the active part of the circulation fan 4 is placed inside the chamber 1. The circulation fan 4, irrespective of the exact plac- ing, circulates the air in the drying chamber 1 and thereby conveys off moisture, which departs from the surface of the sludge 7. The task of the fan system is to circulate the air around the sludge and thereby entrain moisture from the surface of the sludge. In the present invention, use is normally made of a flow rate of 1-5 m/s.

The ventilation damper 11 is employed for regulating the air velocity and the speed of dehumidification in the drying chamber 1. In some embodiments there are more then one damper 11.

In the drying apparatus, there is disposed an indica- tor 5 for measuring the temperature in the drying chamber 1 and/or of the air which departs from and/or is fed to the drying chamber 1. Also the temperature of the sludge 7 may be controlled. Different indicators for different tempera- tures may be used, measuring both the"wet"and"dry"tem-

peratures. For a"wet"thermometer water is cooled by evaporation until equilibrium, i. e. the heats of evapora- tion and volatilisation are the same. The dampers 11 of the chamber 1 may be controlled by the wet temperature. Nor- mally an indicator 9 measuring the temperature of the sludge 7 is used. Said indicator 9 is placed in the sludge 7. In certain embodiments, there are also indicators 6, which measure the moisture ratio of the drying chamber 1.

For accurate monitoring of the air humidity in the chamber, use is made of indicators 6 that measure the relative air humidity. As indicator for the relative air humidity a psy- chrometer is used in some embodiments. In order to measure the decrease of the moisture in the sludge 7, use is made, in certain embodiments, of a weighing machine. The weighing may be performed in that the chamber is placed on scales or load sensing elements 10. Said scales or load sensing ele- ments 10 are in some embodiments integrated in the legs 19 on which the chamber 1 is placed.

In some embodiments of the present invention a con- denser 8 placed below the conveyer belt 13 is used. By means of the condenser 8 some energy is recovered.

As stated above drying of the sludge 3 takes place with the aid of the elements 2. These elements 2 emit a ra- diation in a limited wavelength interval adapted to the ab- sorption of water.

In the embodiment according to Fig. 4, the element 2 consists of an electric resistor 15 disposed centrally in the tube 14 and heated when current from a voltage source passes through the resistor via conductors (not shown).

The wavelength band has been selected at the range of approx. 2-20um and as a rule approx. 5-20um, a range that encompasses wavelengths at which the absorption of radia- tion by water is great. In such instance, use is made of the fact that, within these ranges, water has peaks with absorption coefficients higher than 1,000 cm~1.

The water has peaks at approx. 3pm, 6-7pm and 10-20pm regarding the absorption. Between approx. 7pm and 10, um the absorption coefficient of water is lower, sinking under 1,000 cm~1. Thus, to maximise the effect of the radiation of the elements 2, they should have maximal intensity at the frequencies where water has maximal absorption, while the radiation at other wavelengths should be reduced.

Thus, one object of the present invention is to have a radiation with maximal intensity at the wavelengths where water has a high absorption coefficient, while the inten- sity is reduced at other wavelengths. The peak at 3pm is rather thin and demands a very high temperature making it less suitable to use. Furthermore, it is very hard and even virtually impossible, to reduce the radiation at the wave- length range approx. 4-6pm. In view of this the intensity of the radiation of the elements is directed to the inter- vals approx. 6-7pm and 10-20pm and the intensity is reduced in the intermediate area, i. e. approx. 7-10pm. Thus, the energy of the radiation is used in a way to give maximal effect.

The intensity is dependent on the material of the elements according to the following formula: I=IOe where I is the intensity, e is the natural logarithm and a is a constant depending on the material of the tube 14 or the like surrounding the resistor 15. By varying the material it is possible to control both the spectrum and the position of the radiation of the elements 2. This is used according to the present invention in such a way that the radiation of the elements 2 are adapted to the absorp- tion of water as indicated above. Thus, according to the present invention the material surrounding the electrical resistor 15 is chosen to give the desired radiation spec- trum of the element 2. Said material may be any material giving the desired properties. According to known technol-

ogy, there is a plurality of examples of how, by suitable material selection and suitable current force, to obtain the working temperature of the radiation source which en- tails that the radiation is maximised within the wavelength interval at which water best absorbs radiation.

Normally the conveyor belt 13, and thus, the sludge 7, is at standstill during the treatment phase. The treat- ment phase is normally an automated process, controlled by use of one or more of the different indicators referred to above. The process may be controlled using either the mois- ture ratio of the chamber 1 or sludge 7, or time as inde- pendent variable. By using a thermometer in the circulating air or the sludge 7 dehumidification may be conducted at a certain temperature level of the chamber 1 or sludge 7, re- spectively. A combination of these temperatures may be used as depending variables.

Usually a control system (PLC system) is provided for controlling the elements 2, the fan 4 and the damper 11 in response to signals received from the indicators 5,6, 9, 10. The control system may also be referred to as a regis- tration and calculation unit. Normally the process is run automatically, but a person skilled in the art realises that the process may also be run manually by continuous monitoring of the values of the indicators 5,6, 9.

The temperature in the drying chamber 1 is governed with the aid of the elements 2. In the process often the temperature of the sludge 7 is kept at a fixed level (e. g.

1 °C). It is also possible to keep the temperature of the chamber 1 at a fixed level. To keep any of said fixed tem- perature levels the elements 2 are turned on and off based on the temperature of the sludge 7 or chamber 1, respec- tively. For treatment of sewage sludge the air temperature in the chamber 1 is kept at about 150 °C and the tempera- ture of the sewage sludge is held at about 50-120 °C. The process goes on until the moisture ratio of the sludge 7

has decreased into a predetermined level. As an alternative to the moisture level the process may be run for a prede- termined time. To kill of bacteria the temperature of the sludge 7 may be raised for a short period, usually in the end of the process.

After the dehumidification process the sludge 7 is treated whether any material are to be recovered before or after a possible burning, whether it should be spread on the ground, whether it should be used as a fuel etc.

A drying process for foodstuffs, such as crispbread, pasta etc. , is run after the same principals as described above. The type and number of indicators used will be adapted to the material to be dried.