EP3523586A1

EP3523586A1 - Device and method for drying or heating and cooling pourable substances

Info

Publication number: EP3523586A1
Application number: EP17771333.6A
Authority: EP
Inventors: Mathias Trojosky; Gerd Stölzner; Christoph Fill
Original assignee: Allgaier Werke GmbH and Co KG
Current assignee: Allgaier Werke GmbH and Co KG
Priority date: 2016-10-04
Filing date: 2017-09-12
Publication date: 2019-08-14
Anticipated expiration: 2037-09-12
Also published as: US20200141648A1; PL3523586T3; EP3523586B1; MA46444B1; CA3039078C; DE102016011907A1; WO2018065082A1; ES2842449T3; CA3039078A1

Abstract

The device according to the invention for drying or heating and cooling pourable substances consists of a rotatable drum having means for receiving the pourable substance into a first region and means for discharging the pourable substance from a second region, wherein a central region is arranged between the first and second region, which central region consists of an annular structure having a first and a second diaphragm each having central diaphragm openings which substantially form two mutually parallel diaphragm planes, and have a plurality of transporting ducts which are closed to the central region and are intended for transporting the pourable substance from the first into the second region of the rotatable drum through the central region, wherein the transporting ducts extend from the first to the second diaphragm at an angle unequal to 90° with respect to the two diaphragm planes.

Description

Apparatus and method for drying or heating and cooling

of pourable substances

The present invention is an apparatus and a method for drying or heating and cooling of pourable substances.

In various industrial sectors, in particular the metallurgy, the chemical industry, the building materials and cement industry and the recycling industry, systems for drying a wide variety of products such as sands, slags, clays, bentonite, limestone granules, etc. are required.

The various products typically take after drying temperatures between, for example, at 70 C and 1 ^E 60 ° C. Without cooling the products that are hot after drying, further process control is often not possible. Depending on the specific process requirements and in particular the subsequent aggregates and processing steps, different high solids temperatures of the dried and cooled solid can be accepted. These desired temperatures move, for example, in sands in the range of 55 ° C to max. 65 ° C or from 30 ° C to max. 45 ° C for particularly demanding applications, eg approx. 1 0 K to max. 1 5 K above the respective ambient temperature.

There are various technologies for cooling or combined drying and cooling of such bulk materials, for the above tasks mainly drum dryers (also called "rotary tube dryer") and fluidized bed dryers (also called "fluidized bed dryer") are used. Known is a combined drying and cooling drum with the name System MOZER TK and TK + the company Allgaier. In these systems, via a so-called two-part (ie double-shell) construction consisting of two telescoped tubes, it is achieved that the dried material, which has reached an elevated temperature of, for example, 70.degree. C. to 1.degree Drying is cooled immediately and in the same apparatus.

While in the system TK the cooling is achieved by the contact of the dried, hot or warm solid with sucked cool ambient air, the cooling in the system TK + is achieved by mixing a certain amount of moist solid in the dried, hot solid and thereby causing evaporative cooling.

While the TK + system is characterized by a particular energy efficiency, both systems, due to their bivalve construction, can only have limited low solid-state temperatures of e.g. Reach 50 ° C to about 70 ° C depending on the ambient temperature and the temperature of the solid immediately after drying.

The reason for the limited cooling capacity is that the dried solid is led for cooling in the outer shell of the two-drum dryer. While in this case the cooling of the dried, warm solid is achieved by the contact with the ambient air, is for the cooling process of opposite importance, that used to dry the wet solid and therefore hot inner tube of the dryer-cooler in contact with the solid to be cooled stands and therefore the cooling to particularly low temperatures (eg only about 10 K above ambient temperature) counteracts.

A certain disadvantage of the described two-shell construction is that the internals for solids transport in the outer drum (ie the between see the outer and inner drum located internals) are quite difficult to access and replacement by eg the treatment of highly abrasive solids worn fittings or maintenance of the same is more difficult. In addition, the length ratio between the inner and outer drum is largely predetermined by the two-shell construction, whereby the flexibility of the process control between drying and cooling is limited.

If the described technology of double-shell drum dryers / coolers is also widely used in industrial practice and the achieved solid temperatures are also very often sufficient for further process control, there is nevertheless an increasing need to achieve particularly low temperatures of the products after drying and cooling ,

This has e.g. In the field of drying of sands for the production of Ready Mix building materials such as ready-mixed mortars, plasters and tile adhesives, its cause is the increased use of temperature-sensitive additives ("additives"), which are mixed into the respective recipes immediately after the sand has dried A similar requirement for particularly low sand temperatures (eg 30 ° C to 40 ° C) exists in the field of production or preparation of foundry sand.

In addition, it may be necessary to achieve particularly low solids temperatures if the dried solids are to be packaged immediately after drying and cooling in packages of eg temperature-sensitive plastics such as plastic bags. In order to meet the described requirement for particularly low solids temperatures after drying has taken place, combined fluidized bed dryers / coolers are used in various sectors of the industry, for example. Such fluidized-bed dryers consist of two successively arranged areas which, after drying, have the required cooling capacity. effect. For cooling, ambient air is usually used as well.

It is well-known that fluidized bed dryers / coolers, despite their principally good function, can not prevail without restriction especially in the areas of mineral industry, mining, recycling. Users in these areas prefer the drum dryers known as particularly robust and fault-tolerant in many cases.

In fact, drum dryers are capable of dealing with the problems that are particularly common in the mineral mineral, mining and recycling sectors. fluctuating production volumes, fluctuating product entry dampness, varying particle sizes of the products, particularly harsh environmental conditions, possibly low qualification of the operating personnel, simplest plant controls, etc.

Another possibility for cooling the hot solids obtained after drying is the use of heat exchangers operated with cooling water (so-called "bulk flow heat exchangers") .These heat exchangers have the disadvantage that the provision of cooling water is necessary for operation It also happens that, when the solids are not completely dried, the residual moisture in the solid material condenses on the heat exchanger surfaces cooled by the cooling water, as a result of which it may stick to the heat exchanger surfaces moistened by the condensation and subsequently come to blockages of the heat exchanger used.

In order to achieve the frequently desired low temperatures of the dried solids after cooling by means of drum dryers, various technical solutions and modifications of simple drum dryers are known. Thus, for example, two separate apparatuses are used, namely a first drying drum and a downstream, separate second cooling drum, wherein the dried solid flows either directly from the drying drum into the cooling drum, characterized in that the drying drum is placed higher than the cooling drum and a simple Connection between the dryer outlet and the cooler inlet, eg in the form of a chute, is realized.

Alternatively, conveyors (e.g., a bucket elevator or belt conveyor) may be used to transport the hot, dried solids out of the dryer outlet and into the cooling drum.

For a good cooling efficiency, a so-called counterflow of solid and cooling air is often used. The cooling air is guided against the conveying direction of the solid through the cooling drum. As a result, the necessary amount of cooling air is minimized and usually reaches a temperature of the cooled solid just above the temperature of the incoming cooling air (ie often the ambient temperature).

From US Patent 3,599,346 a technical solution of a combined dry-cooling drum is also known, in which the drying drum is designed with a smaller diameter than the cooling drum, whereby it is achieved that the outlet end of the drying drum with a certain necessary length of itself in the cooling drum protrudes. This ensures that the dried and hot solid is transferred directly into the cooling drum.

In this embodiment, the above-described, energetically efficient countercurrent between solid and cooling air can be advantageously realized in the cooling. However, a rather complex connection of the two separate drums for drying on the one hand and for cooling on the other hand is required, which it allows both the spent drying air and the spent cooling air at the Stel le the connection of the two drums can be sucked.

While on the one hand the aim is that the diameter of the drying drum to achieve optimum performance is as large as possible, on the other hand the aim is that the remaining between the drying drum smaller diameter and the cooling drum of larger diameter annular gap is sufficiently large to the sucked at this point Trocknerabuft and Kühlerabl So aspirate that as little as possible of the solid to be treated enters the exhaust air flow, so is entrained by the sum of the two exhaust air streams from the dryer and from the radiator. Since this entrained amount of solids depends on the velocity of the air in the space between the inner drying drum and the outer cooling drum, both objectives contradict each other. From US Patent 2,309,810 a device for a combined drying and cooling in a likewise clam shell drying and cooling drum is known in which the drying drum of smaller diameter similar to the system MOZER TK + is mounted in a cooling drum of larger diameter.

The inner drum used for drying is shorter than the outer drum and ends at about half the length of the outer drum. The solution described therein uses an admixture of the dried hot solid in a stream of not yet dried solid, after which both amounts of solid are dried together in the outer drum to the end.

Another technical solution of a combined drying and cooling drum is described in US Pat. No. 9,322,595 B 1, in which the drying and cooling of sands is carried out in a single drum, ie in a continuous tube of the same diameter. This solution also comes close to the basic idea of the system MOZER TK + by cooling the dried sand in a first Drum section given a certain amount of still wet sand and mixed into the dried, hot solids stream. This results in an evaporative cooling already dried hot sand with simultaneous drying of the added portion of still wet sand. This technical solution requires a rather complicated and described in the patent component or mechanism 'for introducing the proportion of wet sand after the drying zone without solid falls out in the range of Feuchtgutzugabe from the drum. In addition, the proposed solution has the disadvantage that the cooling does not take place in countercurrent with fresh, cool ambient air, but the entire solid from already dried material and moist material added contacted with the spent dryer exhaust air and is conducted in cocurrent to the outlet end of the dryer / cooler , As a result, the entire solid to be dried and cooled is in direct current with the drying air carrying the evaporated amount of water in contact. Despite the use of the principle of evaporative cooling, consequently, a low efficiency of the overall drying and cooling system is to be expected.

DE 3134084 A1 describes a method, albeit modified, but frequently used in the sugar industry, in which the solid is passed through a drum-dryer-cooler in countercurrent to the drying and cooling air. In the drying zone is dried with a mixture of about a separate centric arranged in the dryer tube and up to about the middle of the dryer guided hot air and coming out of the cooling zone preheated cooling air. The cooling takes place in the area of the dryer / cooler in which the hot drying air has not yet been mixed into the cooling air stream.

The invention is therefore based on the technical object to remedy the deficiencies of the known technical solutions by a suitable structural design and the function and efficiency ability of the dryer / cooler by better flow control of the solid and the drying and cooling air to ver improve and also reduce the manufacturing costs for the cooler by reducing the amount of work in the production (especially l for the welding and assembly work).

This object is achieved by the device according to the invention and the method according to the invention having the features according to claim 1 or claim 11. Advantageous developments of the present invention are characterized in the dependent claims.

The device according to the invention for drying or heating and cooling pourable substances consists of a rotatable drum with means for receiving the pourable substance in a first region and means for discharging the pourable substance from a second region, wherein arranged between the first and second region, a central region is, which consists of an annular structure having a first and a second aperture, each with central apertures, which form substantially two parallel ßlendenebenen, and a plurality of central region closed transport channels for transporting the pourable material from the first to the second region of the rotatable Drum through the central region, wherein the transport channels extend from the first to the second aperture at an angle not equal to 90 ° relative to the two diaphragm planes.

Advantageously, the transport channels are arranged distributed uniformly over the ring-like structure.

Advantageously, flow openings for the gaseous media in the rotatable drum are respectively provided in the central area next to the transport channels closed to the central area. In a further embodiment of the present invention, advantageously, the central region for separately guiding the dryer air and the cooler air is subdivided by a partition wall parallel to the diaphragm planes, and only the transport channels are excluded from the partition wall.

Advantageously, the first region of the drum for drying or heating or reaction control and the second region of the drum for cooling or further reaction of the pourable material is determined.

Advantageously, the first and second regions of the drum are each provided with conveying means which cause a transport of the pourable substance into the transport channels and, after its exit from the transport channels, a transport of the pourable substance in the second region until the pourable substance is dispensed.

Advantageously, the central region is surrounded by a housing for discharging or for supplying the gaseous media.

Advantageously, the housing has upwards one or two exhaust air ducts and on its underside one or two fine material outlets.

Advantageously, the entire device can be inclined relative to the horizontal in the transport direction.

Advantageously, the angle of inclination is between 0.5 ° and 7 °, preferably between 1 ° and 3 °.

The process according to the invention for drying or heating and cooling pourable substances consists of the following steps, which, however, do not have to be carried out in the stated sequence: • introducing a moist or at least cold, pourable substance into a dryer area;

• Rotate the drum with dryer area, central area and cooling area

• introducing hot gases into the dryer area;

Drying and transport of the pourable material within the dryer area to a central area;

• Transport of the dried, hot, pourable material in transport channels closed to the central area through the central area with exhaust air openings;

• discharge of the hot gas via the flow openings in the central area and over the housing and the connected exhaust air duct;

• transport of dry, hot, pourable material into the cooling area;

• introducing cooling air and cooling the dry, hot, pourable substance in a cocurrent or countercurrent process;

• outflow of the heated cooling air;

• Discharge of the dry, cooled, pourable substance.

Expediently, the method further consists of the step: deposition of fine material in the central region, preferably by gravity-induced falling down.

Advantageously, the inventive method further consists of the step: returning the exiting, heated cooling air flow in the dryer area as preheated drying air for drying the cold and at least wet, pourable material and associated heat recovery or waste heat recovery from the cooler exhaust air.

Advantageously, the method according to the invention for drying or heating and cooling a moist or at least cold, pourable substance uses the device according to the invention as described above. Alternatively, the drying or heating or reaction is carried out in the first region instead of in cocurrent in countercurrent between gas and pourable material according to the invention.

Alternatively, the cooling or reaction is carried out in the second region instead of in countercurrent in the direct current between gas and pourable material according to the invention.

Expediently, the first area is referred to below as the drying zone and the second area below as the cooling zone.

At one end of the drum, so on the side of the drying zone, a hot gas generator is installed via a housing and a nozzle for the supply of hot gas necessary for drying. Also located at the other end of the drum, the cooling zone, a housing, where the dried and cooled solid can escape. The solid to be dried is fed at one end of the dry-cooling drum and dried in the drying zone of the dryer-cooler, moving in the direction of the center of the dry-cooling drum.

At the end of the drying zone, i. In the central area, there is the suction housing for the used drying air as well as for the used exhaust air. The cooling air (ie, for example, ambient air) is introduced into the cooling zone at the other end of the dryer / cooler and, in countercurrent to the solid, also moves in the direction of the exhausted exhaust air extraction housing located approximately in the middle of the entire drum.

For extracting the dryer exhaust air as well as the exhaust air from the cooler via the suction housing, the central area is provided with flow openings which allow the outlet of the dryer and the exhaust air of the cooler to escape into the extraction housing. In order to prevent precipitation of the dried and subsequently to be cooled solid through the flow openings of the central region and instead to transfer the solid from the drying zone into the cooling zone, the central region is designed in the manner according to the invention.

The drying zone receives at its end a designed as a diaphragm annular weir. Centrally located in the aperture is a preferably circular opening through which the spent dryer exhaust air can enter the central region, where the suction is located and through the through-flow of the exhaust air can enter the suction and sucked.

The dried solid accumulated in the annular dam weir is guided via tunnel-like transport channels from the drying zone through the area of the air suction of the central area to the area of the cooling zone. The tunnel-like transport channels are closed at the top, bottom and sides and thus have no connection to the area of the air extraction and are located between the cut-outs in the drum wall for extracting the dryer and cooler exhaust air. In order to achieve a transport of the solid through the tunnel-like transport channels, the transport channels can be arranged at an angle to the axis of the device according to the invention, so that by the rotation of the device according to the invention a conveying effect is exerted on the solid, similar to that by the guide vanes in the drying zone and in the cooling zone of the dryer / cooler takes place.

The entry of the dried solid into the tunnel-like transport channels can be supported by suitable conveyor bars in front of the aperture. Conveniently, the angle of inclination is between 0.5 ° and 7 °, preferably between 1 ° and 3 °. In an inclined embodiment of the entire dry-cooling drum, in which the transport of the solid takes place by the combination of the rotation and the inclination of the drum, can be dispensed with in certain circumstances inclined to the axis of the drum arrangement of the tunnel-like transport channels.

The cutouts in the drum wall are preferably designed at the same angle to the axis of the dryer / cooler as the tunnel-like transport channels and are thus each between the tunnel-like transport channels. Another configuration of the cutouts in the drum wall, e.g. in the form of circular tubes, to achieve sufficient stability of the drum wall in this area is conceivable.

At the beginning of the cooling zone, or at the end of the extraction zone, a shutter similar to the weir after the drying zone can be installed, which prevents the solid transported through the tunnel-like transport channels into the cooling zone from flowing back into the region of the suction and through the throughflow openings in the extraction zone Drum wall in the suction housing falls into the suction housing.

In order to enable the passage of the used cooling air into the region of the suction, the diaphragm also has a central opening, preferably arranged centrally, e.g. in the form of a circular section. The spent and warmed radiator exhaust air flows through the aperture and is sucked together with the exhaust air from the drying zone via the flow opening in the drum wall and via the arranged in this region of the drum suction.

After passing through the dried, hot solid through the tunnel-like transport channels in the region of the suction housing, the solid is taken up by lifting and guide vanes and cooled in the cooling zone of the dryer / cooler. By the described preferred design, a countercurrent flow between the solid and the cooling air is achieved in the cooling zone, whereby a special efficiency of the cooling is achieved.

The solution described does not have the disadvantage that the solid to be cooled comes into contact with hot walls of an internal drying drum. The cooling effect is thereby maximized.

In a further embodiment of the present invention, a partition between the two panels for the suction of the drying air and the suction of the cooling air is inserted in the central region, which prevents the two exhaust air streams mix.

In addition, separate cutouts for the separate suction on the one hand the drying air and on the other hand the cooling air are introduced into the drum wall and also installed a separate suction housing for the exhaust air.

This embodiment of the central area in conjunction with the divided suction housing allows the separate discharge of the two exhaust air streams and thus a variable further use of the two exhaust air streams, e.g. for a return of the warmed up, still dry cooling air in the drying process or as preheated combustion air for the hot gas generator. Such continued use of the exhaust air streams has the advantage of significantly improving the energy balance of the device according to the invention.

Since the warmed-up cooling air contains a substantial part of the heat previously contained in the dried hot solid, the heat recovered from the solid can be used for particularly efficient operation of the dryer / cooler by the embodiment of the invention. In a further embodiment of the divided central region and the divided suction housing, the arrangement according to the invention can also be used, on the one hand, for the extraction of the drying air and in distinction to the previously described variant for the introduction of the cooling air. The cooling air then flows through the cooling zone in cocurrent with the dried and to be cooled solid and exits at the end of the drum, which also emerges from the solid.

In another embodiment of the present invention, instead of at the front end of the drum where the wet solid is input, the hot drying air may also be supplied via the split housing and the split central area. The drying air then flows through the drying zone in countercurrent to the moist and to be dried solid, which len in some practical cases can lead to a particularly efficient drying of the solid. In order to avoid heat losses in the area of the drying zone, this can be provided with a thermal insulation.

It may happen that fine-grained solid is entrained by the speed of the air flow of both the drying air and the cooling air through the apertures of the weirs. If this solid is subsequently not with the exhaust air over the cutouts in the drum wall and the suction z. B. transported to the downstream Staubabscheideeinrichtung, so there is a risk that this usually fine-grained solid falls down through the suction and accumulates in the lower part of the suction and leads to problems over the duration of the plant operation.

This solid can be discharged downwards via an opening in the lower area of the suction housing of the central area and a solids sluice (eg a rotary valve or a flap). Two preferred embodiments of the present invention are illustrated in the figures. Show it:

Figure 1 is a schematic sectional view through an inventive

Device with a "one-piece" central area;

Figure 2 is a schematic sectional view through an inventive

Device with a "two-part" central area;

FIG. 3 shows a schematic perspective view of the central region according to FIG. 1;

Figure 4 is a schematic side view of a central region according to the invention;

FIG. 5 shows a schematic front view of a central region according to the invention according to FIG. 4

Figure 1 shows an embodiment of the device according to the invention with an inlet housing 1 on the left side. In the vicinity there is a device for the solids inlet 2, through which the bulk material to be dried and cooled is introduced into the device according to the invention. Also located on the left end side of the device according to the invention is a burner 3, which has the function of a conventional heating burner, and ensures that sufficiently hot air is introduced into the device according to the invention. The burner 3 may also comprise a combustion chamber to achieve a uniform air inlet temperature and to prevent the flame of the burner from burning open in the dryer. According to Figure 1, the inlet housing 1 is fixedly installed and the drum of the device according to the invention rotatably supports with the race 1 1 on the rollers 12. As a drive mechanism, for example, a direct motor, a pinion with gear, a sprocket or a chain drive can be used. These technical solutions are from the state of the art Techn ic known and essentially gleichwirkend and interchangeable. They are not shown in FIG. 1 and FIG. 2.

When entering a certain amount of the pourable substance in the inlet housing 2, this amount has a certain temperature with a certain degree of humidity A ₀ . In the drying zone, this amount passes through different drying states from A to A _n , where Α denotes a rather moist state and A _n already an almost dry but heated state. Likewise, the temperature T changes in the drying zone 6 of T, which indicates a rather high temperature to T _{n /} which denotes a lower temperature.

The transport of the pourable substance within the drying zone 6 of the drum can be done by different technical measures. On the one hand, it is possible to accomplish the transport within the drying zone 6 of the drum by conveying means located on the drum wall, for example in the form of guide blade n (not shown). Such funding has long been known. It is also possible to tilt the drum and allow the inclination angle promotion. In principle, however, the use of guide vanes is to be preferred, since mixing the dry matter to be dried is advantageous and favors drying.

As soon as the pourable substance according to FIG. 1 is at the right edge of the drying zone 6, it leaves the region A and enters the central region B according to the invention. The central area B is bounded on both sides by a shutter 8A, 8B.

Through the central region B pass through tunnel-like transport channels 9 through which the pourable material to be dried is conveyed from the drying zone 6 into the cooling zone 7. A preferred embodiment of the central region B is described in more detail in FIGS. 3 to 5. After leaving the drying zone 6 or area A and the central area B of the pourable material should be substantially dry. As already shown schematically in Figure 1, the drying zone 6 wesentl I longer than the cooling zone 7 may be formed. In the cooling zone 7, or region C, the pourable material is cooled to a predetermined temperature and can leave the device according to the invention as a dried, cooled substance.

According to Figure 1, the drying is carried out in cocurrent, ie the drying gas stream at temperature until T _n runs in the same direction as the material flow Α to A _n . In the cooling zone 7, however, the cooling takes place in countercurrent, ie, the material flow C, after C _n takes place counter to the flow direction of the cooling air (KL) K-, to K _n . This promotes cooling. According to the invention, both the heated radiator exhaust air K _n and the wet dryer exhaust air T _n pass through the central region as exhaust air AL. For this purpose, the central area B between the two panels 8A and 8B, two central apertures 1 3A and 1 3B (see Figure 4), which allow the dryer exhaust T _n and the radiator exhaust air K _n first through these central apertures 1 3A and Ί 3 Β flow thereafter to leave through the flow openings 14A to 14F (see Figure 5), the device of the invention.

Dusts and particles entrained in the central area with the drying or cooling air are either carried along with the exhaust air AL and can be separated from the air in downstream separators (exhaust filters or cyclones) or fall down as fine material FG in the central area the respective bottom flow openings 14 in the housing 4. The dried and cooled solid FS is output as the final product on the right side of the device according to the invention shown in FIG. Figure 2 shows the same inventive device as Figure 1 except for the difference that the central region B is formed in two parts, ie the drying zone 6 is separated by a partition wall 1 0 of the cooling zone 7. Due to the spatial separation of the two areas, it is also necessary that the exhaust air discharge and the fines discharge also run separately and thus in the housing 4 also two deposition areas vorl project. The dryer exhaust air is designated according to Figure 2 with TAL and the radiator exhaust air with KAL. The two fines are called FG1 and FG2. The dried and cooled solid FS is output as end product on the right side of the device according to the invention according to FIG.

FIG. 3 shows a schematic representation of a central region B according to the invention with a multiplicity of baffles 1 5A to 15F. The function of the baffles 1 5A to 15F is to introduce the pourable substances from the dry zone 6 or A in FIG to favor and support the central area B. The baffles are preferably slightly inclined to allow trickling into the tunnel-like channels 9A to 9F.

Figure 4 and Figure 5 show a preferred embodiment of the central region B, but without baffles. Figure 4 shows a schematic side view, but with the drum wall covering the transport channels 9D, 9E and 9F not shown. According to FIG. 5, six tunnel-like transport channels 9A to 9F and six throughflow openings 14A to 14F are provided. The tunnel-like transport channels 9A to 9F extend from one aperture 8A to the other aperture 8B, but the tunnel-like transport channels 9A to 9F extend at an angle α not equal to 90 °, preferably between 2 ° and 30 °. By the angle α not equal to 90 °, the technical effect is achieved that upon rotation of the central region B in the clockwise direction of the pourable material is conveyed into the tunnel-like transport channels 9A to 9F in the direction of arrow AC and there, comparable to egg nem För- derrad in the position 9D to 9F is received in the dryer zone 6 and in the position 9A and 9B again, but in the region of the cooling zone 7 is discharged.

LIST OF REFERENCE NUMBERS

1 inlet housing

2 solids entry

3 burners

4 suction housing

5 outlet housing

6 drying zone

7 cooling zone

8 aperture

9 tunnel-like transport channels

10 partition wall

1 1 race ring

12 rollers

1 3 apertures

14 flow openings

1 5 baffles

Claims

claims

1 . Apparatus for drying or heating and cooling pourable substances consisting of a rotatable drum with means (2) for receiving the pourable substance in a first area (A) and means (5) for discharging the pourable substance from a second area (C) , characterized in that between the first region (A) and the second region (C), a central region (B) is arranged, consisting of an annular structure with a first aperture (8A) and a second aperture (8B), each with central apertures (13A, 13 B) which essentially form two mutually parallel diaphragm planes, and a plurality of transport channels (9A-9F) closed to the central region (B) for transporting the fluid from the first to the second region (A, C). the rotatable drum, wherein the transport channels (9A-9F) from the first to the second aperture (8A, 8B) at an angle α not equal to 90 ° with respect to the two diaphragm planes extend n.

2. Device for drying or heating and cooling of pourable substances according to claim 1, characterized in that the transport channels (9A-9F) are distributed uniformly over the ring-like structure.

3. Device for drying or heating and cooling of pourable substances according to claim 1 or 2, characterized in that in the central region (B) throughflow openings (14A-14F) for the gaseous media in the rotatable drum in each case next to the transport channels (9A-9F) are provided.

4. Device for drying or heating and cooling of pourable substances according to one of claims 1 to 3, characterized in that the central region (B) for separately guiding the dryer air and the cooler air from one to the Sliding planes parallel partition is divided and only the transport channels (9A-9F) are excluded from the partition.

5. Device for drying or heating and cooling of pourable substances according to one of the preceding claims, characterized in that the first region (A) of the drum for drying or heating or reaction and the second region (C) of the drum for cooling or further reaction of the pourable substance is determined.

6. Apparatus for drying or heating and cooling pourable materials according to one of the preceding claims, characterized in that the first region (A) and second region (C) of the drum are each provided with conveying means, which transport the pourable substance in the Transport channels (9A-9F) into it and after its exit from the transport channels (9A-9F) effect a transport of the pourable substance in the second region (C) to the delivery of the pourable substance.

7. Device for drying or heating and cooling pourable substances according to one of the preceding claims, characterized in that the central region (B) by a housing (4) for discharging or for supplying the gaseous media is surrounded.

8. An apparatus for drying or heating and cooling of pourable materials according to claim 7, characterized in that the housing (4) has upwardly one or two exhaust ducts and on its underside one or two fine material outlets.

9. Device for drying or heating and cooling of pourable substances according to one of the preceding claims, characterized in that the entire device is inclined relative to the horizontal in the transport direction.

10. An apparatus for drying or heating and cooling of pourable substances according to claim 9, characterized in that the angle of inclination between 0.5 ° and 7 °, preferably between 1 ° and 3 °.

1 1. Method for drying or heating and cooling pourable substances consisting of the steps:

Introducing a moist or at least cold, pourable substance into a dryer area (A);

Rotating the dryer section (A);

Introducing hot gases into the dryer area (A);

Drying and transporting the pourable material within the dryer area (A) to a central area (B);

Transport of the dried, hot, pourable material in the central region (B) closed transport channels (9) through the central region (B) with openings (14) for gas supply or discharge; Entry or exit of the hot gas via the flow openings (14) in the central area (B) and via the housing (4) and the connected exhaust air duct;

Transport of dry, hot, pourable material into the cooling area (C);

Introducing cooling air (KL) and cooling the dry, hot, pourable substance in a DC or countercurrent process;

Outflow of the heated cooling air;

Discharge of the dry, cooled, pourable substance (FS).

12. A method for drying or heating and cooling pourable substances according to claim 1 1, further comprising the step:

Separation of fines (FC) in the central region (B), preferably by gravity-induced dropping.

1 3. A method for drying or heating and cooling of pourable materials according to claim 1 1 or 1 2, further comprising the step:

Returning the exiting, heated cooling air flow in the dryer area (C) as preheated drying air for drying the cold and at least wet, pourable material and associated heat recovery or waste heat recovery from the cooler exhaust air.

14. A method for drying or heating and cooling a moist or at least cold, pourable substance, wherein the device is used according to one of claims 1 to 1 0.

1 5. The method according to one or more of the preceding claims, characterized in that the drying or erh itzung or reaction is carried out in the first region instead of in cocurrent in countercurrent between gas and pourable material.

1 6. The method according to one or more of the preceding claims, characterized in that the cooling or reaction is carried out in the second region instead of in countercurrent in the direct current between gas and pourable material.