TREATMENT OF A MASS OF MATERIAL BY PRESSING

Abstract

--A device and method for dewatering a mass of material and a method and system for recycling a biogenic material. A vertical press has a press space formed between a tool provided with openings and a press plunger movable relative thereto. Conveying means convey the mass of material from a feed side toward an opposite discharge side. The press space is laterally confined by opposite side walls but is not confined in the direction of the feed side and the discharge side. A biogenic material is converted microbially and/or enzymatically into gas and fermentation residues in a fermentation plant and the latter are dewatered by means of a vertical press to such an extent that thermal utilization is made possible.--

Claims

1. Device for dewatering a mass of material, comprising a vertical press with a press space formed between a tool provided with openings and a press plunger movable relative to the tool, conveying means for conveying the mass of material from a feed side into the press space and for conveying the pressed mass of material in the direction of a discharge side out of the press space opposite the feed side, wherein the press space is laterally confined by opposite side walls extending between the feed side and the discharge side, and wherein the press space is not laterally confined in the direction of the feed side and the discharge side.

2. Device of claim 1, wherein the conveying means comprise a liquid-permeable conveyor belt which extends from the feed side to the discharge side and rests on the tool in the press space.

3. Device of claim 2, wherein the conveyor belt is closed by a return outside the press space (24).

4. Device according to claim 1, wherein the side walls have a surface with openings and/or grooves in the direction of the press space.

5. Device according to claim 1, wherein the press plunger has a surface with openings and/or grooves in the direction of the press space.

6. Device according to claim 1, wherein the tool comprises a perforated plate with the openings, a base plate and a support frame arranged therebetween, so that a flow space for discharging liquid through the openings and the interior of the support frame is formed.

7. Device according to claim 1, wherein collection means and at least one conduit are provided for collecting and directing liquid forced through the openings.

8. Device according to claim 1, wherein a scraper is arranged on the feed side to limit a filling level in the press space.

9. Device according to claim 1, wherein an arrangement for pre-compacting the mass of material is arranged on the feed side.

10. Method of dewatering a mass of material, in which the mass of material is conveyed from a feed side into the press space of a vertical press and the mass of material in the press space is pressed by movement of a press plunger relative to a tool provided with openings, so that at least a part of a contained liquid drains off through the openings, and the pressed mass of material is conveyed to a discharge side opposite the feed side out of the press space, wherein the press space is laterally confined by opposite side walls extending between the feed side and the discharge side, and wherein the press space is not laterally confined in the direction of the feed side and the discharge side.

11. Method of utilization a biogenic material in which the biogenic material is converted microbially and/or enzymatically into gas and fermentation residues in a fermentation plant, and the fermentation residues are dewatered by a vertical press to such an extent that thermal utilization of the dewatered fermentation residues is made possible.

12. Method according to claim 11, wherein the fermentation residues are dewatered by the vertical press to a dry substance value of 50 to 90%.

13. Method according to claim 11, wherein the press water pressed out by the vertical press is fed to the fermentation plant and/or to a treatment plant.

14. Method of claim 11, wherein the dewatered fermentation residues are thermally utilized, and the resulting heat is used to operate the fermentation plant.

15. Method of claim 11,wherein the fermentation residues are dewatered by a device according to claim 1.

16. System for recycling a biogenic material (62), with a fermentation plant for microbial and/or enzymatic conversion of the biogenic material into gas and fermentation residues, and a vertical press for dewatering the fermentation residues in such a way that thermal utilization is possible.

17. Method according to claim 11, wherein the fermentation residues are dewatered by the vertical press to a dry substance value of 55 to 80.

18. Method according to claim 11, wherein the fermentation residues are dewatered by the vertical press to a dry substance value of 60 to 75%.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0027] In the following, embodiments are described in more detail with reference to drawings. Thereby show:

[0028] FIG. 1 in schematic side view an embodiment of a dewatering device with a vertical press;

[0029] FIG. 2 in side view, partially in elevation, a tool of the vertical press of FIG. 1;

[0030] FIG. 3a a schematic front view of the device from FIG. 1;

[0031] FIG. 4a a schematic side view of a plant with a dewatering device according to FIGS. 1-3;

[0032] FIG. 5 schematically an embodiment of a system and method for the utilization of a biogenic material

[0033] FIGS. 6, 7 in schematic representation a first and a second alternative embodiment of a dewatering device with a vertical press.

DETAILED DESCRIPTION OF EMBODIMENTS

[0034] FIG. 1 shows a side view of an embodiment of a dewatering device 10 with a vertical press 12 and a conveyor 14.

[0035] The vertical press 12 comprises a press table 16, opposite which a press ram 18 is vertically guided and movable by a press drive (not shown). The press drive and the conveyor 14 are controlled by a process control system (not shown).

[0036] A tool 20 rests on the press table 16. The press ram 18 is provided with a punch 22. A press space 24 is formed between the punch 22 and the tool 20, which has a different height relative to the tool 20 depending on the stroke position of the press ram 18 and punch 22. The tool 20 is larger in length and width than the punch 22, thus protruding in all lateral directions beyond the press space 24.

[0037] The conveyor device 14 comprises an endless conveyor belt 26 which runs in a conveying direction indicated by an arrow in FIG. 1 from a feed side 28 of the press space 24 on the left in FIG. 1 to a discharge side 30 of the press space 24 arranged on the right in FIG. 1 and is returned outside the press space 24. The conveyor belt 26 is designed to be permeable to liquid and is guided over guide rollers, a drive roller and a tension roller.

[0038] FIG. 2 shows the structure of the tool 20, which comprises a closed base plate 32 and a perforated plate 34 arranged parallel to and at a distance from it and having openings, in this case round bores 36. Between the base plate 32 and the perforated plate 34, exemplary plate-shaped support elements 38 are arranged, between which a tool space 40 remains free. The tool space 40 is closed to the sides (and shown open in the drawings for illustrative reasons only). A downpipe 42 is attached to the base plate 32 and connected to the tool space 40.

[0039] FIG. 3 shows the dewatering device 10 in front view, i.e. from the feed side 28. As shown there, the press space 24 is confined laterally of the conveyor belt 26 by side walls 44. The plunger 22 is in a lower position between the side walls 44. However, towards the feed side 28 and discharge side 30 the press space 24 is open over its entire height and width. The side walls 44 extend between the feed side and discharge side and, in the embodiment shown, are longer than the press space 24 so that they project beyond the press space 24 on both sides.

[0040] FIG. 4 shows the dewatering device 10 as part of a system for dewatering a mass of material with a liquid component, in this case in particular fermentation residues 52 from a fermentation plant or biogas plant 70 (see FIG. 5).

[0041] A bulk material feeder 46 serves to receive and meter the fermentation residue mass 52 onto the conveyor belt 26. By means of the conveyor belt 26, the fermentation residue mass 52 is conveyed from the feed side 28 into the press space 24 of the vertical press 12. A scraper 48 serves to limit a filling height within the press space 24.

[0042] After the fermentation residue mass 52 is introduced into the press space 24, it is pressed between the punch 22 and the tool 20 and thus dewatered. The liquid contained in the mass drains off through the liquid-permeable conveyor belt 26 and the openings 36 on the upper side of the tool 20 (see FIG. 2). During pressing, the side walls 44 (see FIGS. 1, 3; not shown in FIG. 4 for clarity) act as boundaries preventing lateral escape of the fermentation residue mass 52. In the direction of the feed and discharge sides 28, 30, the press space 24 is open, but escape of the fermentation residue mass is limited by the portions thereof resting in front of and behind it on the conveyor belt 26.

[0043] In the embodiment shown, the punch 22 and the sidewalls 44 each have planar, closed surfaces so that the pressed out liquid 56 drains only through the perforated plate 34 and from there passes through the tool space 40 into the downpipe 42. In alternative embodiments, grooves or through openings may be formed in the surfaces of the punch 22 and/or the side walls 44 to assist in draining the liquid.

[0044] Due to the lateral projection of the tool 22 over the press space 24, liquid components that may occur laterally from the press space 24 are also collected and pass through the tool space 40 into the downpipe 42.

[0045] After the pressing process, the pressed, dewatered fermentation residue mass 54 is conveyed by the conveyor belt 26 to the discharge side 30, where a scraper 50 assists in separation from the conveyor belt 26.

[0046] In this case, the operation of the plant and the dewatering device 10 is clocked by a control system (not shown), i.e. the advance through the conveyor belt 26 is not continuous. Instead, in each cycle step, the unpressed fermentation residue mass 52 is fed in at a predetermined maximum filling level, followed by a pressing operation by lowering the ram 22 and, after the ram 22 has been raised, the pressed fermentation residue mass 54 is conveyed on to the discharge side 30. The stroke of the press ram 18 and the ram 22 follows a movement profile predetermined by the control system with set parameters for the course of the press speed and the applied pressure.

[0047] FIGS. 6, 7 illustrate further embodiments of vertical presses 112, 212 for use in a dewatering device 10. Here, the vertical presses 112, 212 largely correspond to the vertical press 12 according to the embodiment described above. Identical elements are indicated by identical reference signs. In the following, only the differences will be discussed in more detail.

[0048] In the vertical press 112 in FIG. 6, a pre-compaction plate 58 is arranged on the press plunger 22, which projects in the direction of the feed side 28. The pre-compaction plate 58 has the same length and width as the press ram 22, but its lower surface facing the fermentation residue mass 52 is displaced relative to the lower surface of the press ram 22, namely arranged higher by a distance.

[0049] This arrangement serves to pre-compact the fermentation residue mass 52 and thus to further reduce the filling height of the fermentation residue mass 52 on the conveyor belt 26. When the press plunger 22 moves downwards during the pressing process and the fermentation residue mass 52 is pressed in the press space, the pre-compacting plate 58 compresses the fermentation residue mass 52, which has already been applied to the conveyor belt 22 for feeding, by a certain amount. In this way, the necessary stroke of the press plunger 22 can be limited and particularly well utilized. Due to the vertical distance between the lower surface of the press plunger 22 and the lower surface of the pre-com-paction plate 58, the pressing pressure during pre-compaction is lower than during the subsequent pressing process.

[0050] In the vertical press 212 in FIG. 7, a pre-compaction plate 58 is also provided, but in this example it is driven by a pre-compaction press 59 independently of the press plunger 22. Thus, the entire press power is available for the pressing process.

[0051] FIG. 5 shows an embodiment of a system 60 for the utilization of biomass 62, for example agricultural waste such as liquid manure with portions of energy crops. The system 60 comprises, in addition to the dewatering device 10, for example according to the embodiment described above, a fermentation plant (biogas plant) 70, a solid-liquid separation 64, a combustion chamber 66 and a fertilizer processing 68.

[0052] In the schematic representation in FIG. 5, the transfer of solids is shown with solid lines, of liquids with dotted lines, and of heat with dash-dotted lines.

[0053] In the biogas plant 70, methane-containing biogas is produced from the biomass 62 with the addition of heat and, if necessary, additional liquid. Liquid and solid fermentation residues remain from the biomass 62, from which a liquid phase 72 is separated in the solid-liquid separation 64. The liquid phase 72 can be processed in the fertilizer processing unit 68, for example, to produce mineral fertilizer.

[0054] In addition to the liquid phase 72, a solid phase 52 is separated in the solid-liquid separation 64, namely the fermentation residues 52. These further have a high liquid content or low dry substance content of, for example, 15 to 35%. By means of a vertical press, in particular preferably as described above with regard to FIG. 4, the dry substance content is substantially increased in a very short time to, for example, 60 to 70% by pressing. Depending on the embodiment, the press liquid 56 obtained and discharged during the pressing process can either be partially or completely returned to the fermentation plant 70, fed to the fertilizer processing 68 or otherwise utilized.

[0055] Pressing enables thermal utilization of the pressed fermentation residues 54. These are thermally utilized in the combustion chamber 66, in particular by combustion. Depending on the embodiment, the resulting heat can be returned in whole or in part to the fermentation plant 70 to operate the biogas process and/or used in whole or in part elsewhere, for example as district heating.

[0056] The system 60 according to FIG. 5 and the method carried out therein exhibit particularly high efficiency in the utilization of the biomass 62, in particular by the pressing process in the dewatering device 10. Although this does not achieve complete drying of the fermentation residue mass 52, it does achieve such a targeted increase in the dry substance content that the subsequent thermal utilization in the combustion chamber 66 is made possible. By the feedback, namely on the one hand use of the heat of the thermal utilization and on the other hand return of the press liquid 56 to the biogas plant 70, an advantageous cycle process is implemented.