METHOD FOR EXPANSION OF SAND GRAIN-SHAPED RAW MATERIAL

Abstract

The invention relates to a method for the expansion of sand grain-shaped raw material (1) in which the raw material drops downwards through a substantially vertical heated shaft (3) provided with means (2) for heating, in which a shaft flow (4) prevails and to a dosing element (6) which can be connected to a substantially vertical shaft (3) and a conveying line (7).

In order to prevent the pressure fluctuations coming from the conveying line (7) in the area of the shaft (3), a dosing element (6) is attached between the shaft and the conveying (7) line, in which the quantity of granulate which goes over from the shaft (3) into the conveying line (7) is regulated via means for regulating so that a defined material collection of the granulate is formed as a buffer is the dosing element (6), which decouples the shaft flow (4) from the conveying flow.

Claims

1. Method for the expansion of sand grain-shaped raw material (1) in which the raw material (1) drops downwards through a substantially vertical heated shaft (4) provided with means (2) for forming a temperature profile (3), in which a shaft flow (5) prevails wherein as a result of the heat transfer in the shaft (4) the raw material (1) expands to expanded granulate (6) and the granulate (6) produced enters into a pneumatic conveying line (7) with a conveying flow (8) for further transport, characterized in that the bulk density of the expanded granulate (6) is measured continuously, wherein upon detection of a deviation from at least one defined bulk density the temperature profile (3) in the shaft (4) is adapted automatically or manually and/or the feeding of raw material (1) into the shaft (4) is reduced automatically or manually, wherein the expanded granulate (6) is separated by a separating device, preferably a gas cyclone (10), from the conveying flow (8) in the conveying line (7), wherein the bulk density of the granulate (6) separated by the separating device, in particular the gas cyclone (10), is measured, wherein the separated expanded granulate (6) is concentrated to form a granulate flow (11) and said granulate flow (11) is guided into a measuring container (12), wherein the measuring container (12) is connected to a measuring device (13) configured as a weighing device to determine the bulk density and wherein the measuring container (12) has openings (21) in a base surface (17), through which at least one part of the granulate flow (11) drains continuously.

2. The method according to claim 1, characterized in that the conveying flow (8) is produced by means of an extraction device (9).

3. The method according to claim 1, characterized in that a dosing element (14) is disposed between shaft (4) and conveying line (7).

4. The method according to claim 1, characterized in that process air (16) is extracted from the head region (15) of the shaft (4) in order to stabilize the part of the shaft flow (5) directed to the head region (15).

5. The method according to claim 1, characterized in that process air (16) is blown into the head region (15) of the shaft (4) in order to stabilize the part of the shaft flow (5) directed to the head region (15).

6. Device for measuring the bulk density of expanded granulate (6) according to the method of claim 1, the device comprising a separating device configured as a gas cyclone (10), which can be connected to a pneumatic conveying line (7), wherein at least one measuring container (12) which has a base surface (17) is disposed underneath the gas cyclone (10) in the operating state for receiving at least a part of the granulate flow (11) from the separating device configured as a gas cyclone (10), wherein the measuring container (12) is connected to a measuring device (13) for determining the bulk density, characterized in that the measuring device is configured as a weighing device, preferably as scales, and that the measuring container (12) has openings (21) in the base surface (17), in order to allow at least a part of the granulate flow (11) to drain continuously.

7. The device according to claim 6, characterized in that a means for concentrating the granulate flow (11), preferably a funnel (18), is disposed between the separating device configured as a gas cyclone (10) and the measuring container (12).

8. The device according to claim 6, characterized in that the measuring container (12) is connected via a side arm (19) to the measuring device (13).

9. The device according to claim 6, characterized in that an overflow (20) for at least one part of the granulate flow (11) is provided on the measuring container (12).

10. System for performing a method according to claim 1 with a device for measuring the bulk density according to claim 6, wherein the substantially vertically heated shaft (4) is connected to the separating device configured as a gas cyclone (10) via the pneumatic conveying line (7).

Description

BRIEF DESCRIPTION OF THE FIGURES

[0029] A detailed description of a method according to the invention and a device according to the invention now follows. In the figures:

[0030] FIG. 1 shows a schematic image of a system according to the invention,

[0031] FIG. 2 shows a detailed view of a dosing element according to the invention,

[0032] FIG. 3 shows a sectional view of a dosing element according to the invention along line AA in FIG. 2.

WAYS FOR IMPLEMENTING THE INVENTION

[0033] FIG. 1 shows a system for expansion of sand grain-shaped raw material 1. In this case, the raw material 1 falls through a vertical shaft 3 which can be heated by means 2 for heating, in the present embodiment a plurality of electrical resistance heaters 2 are used. The raw material is fed in the head region 16 of the shaft 3. Since the resistance heaters 2 can be controlled individually, a specific temperature profile can be established along the shaft 3. As a result of the thermal radiation which acts on the raw material 1 from the shaft 3, the raw material 1 expands to form expanded granulate 5. Due to the heated walls of the shaft 3 and the ensuing process air 18, a shaft flow 4 is established in the shaft 3, which consists of a near-wall boundary layer flow in the direction of the head region 16 and a central core flow in the direction of the shaft connection 20.

[0034] An additional extraction device 17 is provided in the head region 16 of the shaft 3, which extracts process air 18 from the head region 16 and thus improves the shaft flow 4. In addition, a control loop 30 is coupled to the additional extraction device 17 which regulates the fraction of extracted process air 18 and sucked-in ambient air. Likewise, process air 18 can be blown into the head region 16 to stabilize the shaft flow 4 either by this additional extraction device 17 or by another device not shown here.

[0035] Located at the lower end of the shaft 3 is a dosing element 6 which regulates the quantity of granulate 5 conveyed from the shaft 3 into the pneumatic conveying line 7. The dosing element 6 has a shaft connection 20 at the connecting point to the shaft 3 and a conveying connection 23 at the connection point to the conveying line 7. Likewise a measuring device 15 is mounted in the part of the dosing element 6 adjoining the shaft 3, the measurement data of which is used to regulate the conveyed quantity.

[0036] An extraction device 12, which is preferably designed as a fan, is mounted at one end of the pneumatic conveying line 7 which sucks ambient air from the other end of the conveying line 7, which is designed to be open to the atmosphere and this conveys expanded granulate 5. A gas cyclone 13 is located inside this conveying line 7 via which granulate 5 is separated from the conveying line. Located in the conveying line 7 is a filter system 28 which is preferably disposed between gas cyclone 13 and extraction device 12 which separates small particles from the conveying line 7. By measuring the differential pressure by means of an additional measuring device 29, the conveyed quantity of the extraction device 12 is controlled so that the flow velocity in the conveying line 7 remains constant even when the filter system 28 is contaminated.

[0037] FIG. 1 shows that in this embodiment a weighing device 14 is additionally provided, this being arranged downstream of the gas cyclone 13 in relation to the flow of granulate 5 and can be used to determine the weight and therefore the bulk density of the separated expanded granulate 5. By means of this measurement, the quality of the expansion process can be assessed and accordingly the feeding of raw material 1 is either reduced, preferably stopped entirely or the output of the resistance heaters 2 is increased in a specific region of the shaft 3. Alternative embodiments of the invention do not provide a weighing device 14 so that the expanded granulate 5 is introduced directly from the gas cyclone 13 into a container, preferably a silo.

[0038] FIGS. 2 and 3 now show a detailed view of the dosing element 6. FIG. 3 shows one or the main functions of the dosing element 6: the formation of a material accumulation 10. Expanded granulate 5 falls from the shaft 3 via the shaft connection 20 (FIG. 1) into a first part of the dosing element, the material container 19 which has a longitudinal axis 21. Since the quantity of granulate 5 from the shaft in a first process step is higher than the quantity of granulate 5 which enters into the conveying line through the dosing element 6, the material container 19 is filled with expanded granulate 5 so that a material accumulation 10 is formed which fills at least a first cross-section 11 of the material container 19. By this means the space located above the material accumulation 10 in the operating state, in particular the shaft 3, can be decoupled in terms of pressure technology from the space located downstream of the material container 19 in the operating state, in particular the conveying line 7, so that the pressure fluctuations in the conveying line 7 do not affect the shaft flow 4. The material container 19 is designed so that it has at least the same cross-section as the shaft 3 in the area of the shaft connection 20, preferably the entire upper area of the material container 19 has the same cross-section as the shaft 3, which in particular is rectangular.

[0039] FIG. 2 shows that a conveying section 22, which preferably has a circular cross-section is guided through the lower region of the material container 19, which preferably has a larger cross-section than the shaft 3, wherein the largest diameter of the conveying section 22 is configured to be smaller than the smallest dimension of the interior of the material container 19. The distance between the outer side of the conveying section 22 and the inner sides of the material container 19 is a multiple of the largest diameter to be expected of a granule of the expanded granulate 5 known from process-related empirical values. Usually the multiplication factor lies in a range between 10 times and 100 times, preferably between 20 times and 40 times. Typical granule diameters of the expanded granulate 5 lie in the range of 0.5 to 5 mm. For example, for a granule diameter of 2 mm and a factor of 30, a distance of 2 mm30, i.e. 60 mm is obtained.

[0040] The material container 19 therefore encloses at least a part of the conveying section 22, preferably the entire conveying section 22. The conveying section 22 therefore preferably touches the base surface of the material container 19 and rests on this. The conveying section is guided transversely to the longitudinal axis 21 of the material container through this wherein in this variant of the inventions the longitudinal axis 21 intersects the axis of the conveying section 22 at a point and the angle between the axes is 90. Alternative embodiments of the invention can also have different angles and offset axes. In order to ensure the transition of expanded granulate 5 from the material container 19 into the conveying section, at least one opening 24 (FIG. 3) is provided in the conveying section 22. This at least one opening 24 is located in this variant of the invention on the side of the conveying section 22 opposite the shaft connection 20 (and specifically on both sides of the conveying section 22, here symmetrically to the longitudinal axis 21), i.e. in the operating state on the lower side wherein the at least one opening 24 is preferably designed as a multiplicity of slits. Alternative embodiments provide that the at least one opening 24 has the shape of a rectangle, square or circle. In any case, the at least one opening 24 must be dimensioned so that the granules having the largest diameter which are known from process-related empirical values can still pass through the at least one opening 24 without a blockage forming. Preferably the ratio between the granules and the diameter of the opening 24 lies between 1:3 and 1:100, particularly preferably between 1:5 and 1:50, in particular between 1:5 and 1:25. For example, for a granule diameter of 2 mm and a ratio of 1:5, the diameter of the opening 24 with 2 mm5 is obtained as 10 mm.

[0041] Located in the inside of the conveying section 22 is a means 9 for regulating the conveyed quantity which in this variant is designed as an inner tube 25 with a butterfly valve 26. In this case, the largest diameter of the inner tube 25 which like the conveying section 22 is preferably circular, is smaller than the smallest diameter of the conveying section 22 and these two elements are arranged concentrically. By varying the cross-section and the position of the inner tube 25, many alternative designs are feasible. The inner tube 25 is also, like the conveying section 22 and therefore the conveying line 7, connected to the atmosphere on the side opposite the conveying connection 23 whereby ambient air can be sucked through all the aforesaid elements.

[0042] The butterfly valve 26 is disposed inside the inner tube 25 and is preferably configured as a circular plate having a diameter which allows the closure of the inner tube 25. This butterfly valve 26 is rotatably mounted so that it is pivotable about an axis normal to the axis of the inner tube 25. This pivoting can take place in a region between a first position in which the butterfly valve 26 is parallel to the longitudinal axis of the conveying section 22 and a second position in which the butterfly valve 26 is normal to the longitudinal axis of the conveying section 22.

[0043] The same conveying flow 8 as in the conveying line 7 which is produced by the extraction device 12 (FIG. 1) prevails in the conveying section 22. By means of this conveying flow 8 granulate 5 is conveyed from the material container 19 via the at least one opening 24 into the conveying section 22 and further into the conveying line 7.

[0044] If the measuring device 15 (FIG. 1), which monitors the height of the material accumulation 10 in the upper part of the material container 19 in the operating state, detects that the height of the material accumulation 10 is too low, the butterfly valve 26 is opened, i.e. pivoted in the direction of the first position of the butterfly valve 26. As a result, the cross-section 27 through which flow takes place when the second position is reached is the same size as the diameter of the inner tube 25 and the same flow velocity of the conveying flow 8 prevails in the entire cross-section of the conveying section 22. As a result little granulate 5 is transferred from the material container 19 into the conveying section 22 and the height of the material accumulation 10 increases.

[0045] If the measuring device 15 (FIG. 1) now detects that the height of the material accumulation 10 is too high, the butterfly valve 26 is closed, i.e. pivoted in the direction of the second position of the butterfly valve 26. As a result, the cross-section 27 through which flow takes place when the first position is reached is minimal, preferably completely closed so that the flow velocity in the annular region between the inner tube 25 and the inside of the conveying section 22 becomes higher, with the result that a strong suction is produced and a large quantity of granulate 5 is transferred from the material container 19 into the conveying section and the height of the material accumulation 10 sinks.

[0046] This ensures that the height of the material accumulation 10 can always be held within a defined range in order to maintain the effect of decoupling of the shaft flow 4 from the conveying flow 5.

[0047] In this case, the minimum height of the material accumulation 10 is determined by the at least one opening 24 which must be covered with said minimum height. The actual height of the material accumulation 10 which is established during operation is determined by means of the distance of the measuring device 15 from the conveying section 22 which is preferably 1 cm to 15 cm. The measuring device 15 (or its detector) should therefore at best be attached only slightly higher than the outside diameter of the annular gap through which air flows (between the inner tube 25 and the inside of the conveying section 22) for sucking in the expanded granulate 5.

REFERENCE LIST

[0048] 1 Sand grain-shaped raw material [0049] 2 Means for heating (electrical resistance heaters) [0050] 3 Shaft [0051] 4 Shaft flow [0052] 5 Expanded granulate [0053] 6 Dosing element [0054] 7 Pneumatic conveying line [0055] 8 Conveying flow [0056] 9 Means for regulating [0057] 10 Material accumulation [0058] 11 First cross-section [0059] 13 Gas cyclone (separating device) [0060] 14 Weighing device [0061] 15 Measuring device [0062] 16 Head region [0063] 17 Additional extraction device [0064] 18 Process air [0065] 19 Material container [0066] 20 Shaft connection [0067] 21 Longitudinal axis [0068] 22 Conveying section [0069] 23 Conveying connection [0070] 24 Opening [0071] 25 Inner tube [0072] 26 Butterfly valve [0073] 27 Cross-section through which flow takes place [0074] 28 Filter system [0075] 29 Additional measuring device [0076] 30 Control loop