Facility and Process for the Recycling of Biomaterial
20170267598 · 2017-09-21
Inventors
Cpc classification
C12M23/58
CHEMISTRY; METALLURGY
Y02P20/145
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C12M29/00
CHEMISTRY; METALLURGY
C05F17/80
CHEMISTRY; METALLURGY
Y02E50/30
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
Y02W30/40
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
C12M27/06
CHEMISTRY; METALLURGY
International classification
C05F17/00
CHEMISTRY; METALLURGY
Abstract
A facility for the recycling of biomaterial with a fermentation stage, whereby the fermentation stage has a fermentation chamber for the production of biogas through anaerobic fermentation of the biomaterial, and with a hygiene stage that is positioned downstream from the fermentation stage, whereby the hygiene stage has a hygienization chamber for the reception and the thermal hygienization of biomaterial discharged from the fermentation stage. A process for the recycling of biomaterial by zymosis is also provided, whereby biogas is produced in a fermentation stage through anaerobic fermentation of the biomaterial, whereby the biomaterial is, after flowing through the fermentation stage, conveyed to a hygiene stage in which the biomaterial thermal is hygienized, and whereby the biomaterial is, after flowing through the hygiene stage, made available as recyclable agricultural, hygienized fermentation residue.
Claims
1. A facility for the recycling of biomaterial, with a fermentation stage, comprising: (a) a fermentation stage having a fermentation chamber for the production of biogas by anaerobic fermentation of the biomaterial, (b) a hygiene stage, which is positioned downstream from the fermentation stage, wherein (c) the hygiene stage has a hygienization chamber for the reception and the thermal hygienization of biomaterial discharged from the fermentation stage.
2. The facility of claim 1, wherein the fermentation chamber is configured as a reactor with plug flow.
3. The facility of claim 1, wherein the hygienization chamber is configured as a reactor with plug flow.
4. The facility of claim 1, wherein a volume of the hygienization chamber is smaller than a volume of the fermentation chamber.
5. The facility of claim 1, wherein the fermentation chamber has a discharge device which is connected with a feeding device of the hygienization chamber.
6. The facility of claim 5, wherein a pumping device is provided for conveying biomaterial from the discharge device of the fermentation chamber to the feeding device of the hygienization chamber.
7. The facility of claim 1, wherein the hygiene stage has at least two hygienization chambers.
8. The facility of claim 7, wherein the hygiene stage is designed in such a way that the at least two hygienization chambers can be operated in parallel.
9. The facility of claim 1, wherein the fermentation stage and the hygiene stage are positioned in a common structure.
10. A Process for the recycling of biomaterial through zymosis, comprising: (a) producing biogas in a fermentation stage by anaerobic fermentation of the biomaterial, (b) conveying the biomaterial to a hygiene stage after flowing through the fermentation stage, wherein in the hygiene stage the biomaterial is thermally hygienized, and (c) making the biomaterial available as recyclable agricultural fermentation residue after flowing through the hygiene stage.
11. The process of claim 10, wherein the fermentation of the biomaterial in the fermentation stage takes place in a mesophilic temperature range.
12. The process of claim 10, wherein the biomaterial resides for a longer time in the fermentation stage than in the hygiene stage or for the same time in the fermentation stage as in the hygiene stage.
13. The process of claim 10, wherein the biomaterial passes through the fermentation stage in a plug flow.
14. The process of claim 10, wherein the biomaterial passes through the hygiene stage in a plug flow.
15. The process of claim 10, wherein the biomaterial is conveyed in the form of biological waste.
16. The process of claim 10, wherein the biomaterial is, after flowing through the fermentation stage, divided into at least two partial currents which are conveyed to the hygiene stage.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0025] Additional advantageous configurations of the invention are evident from the following description. Exemplary embodiments of the invention are thereby illustrated in further detail by means of the diagrams without being restricted to these. The following are depicted in simplified, schematic depiction:
[0026]
[0027]
[0028]
DETAILED DESCRIPTION OF THE PRESENT INVENTION
[0029] While this invention is susceptible to embodiments in many different forms, there is described in detail herein, preferred embodiments of the invention with the understanding that the present disclosures are to be considered as exemplifications of the principles of the invention and are not intended to limit the broad aspects of the invention to the embodiments illustrated.
[0030]
[0031] The fermentation stage 4 is equipped with a container 8, which is also termed a fermentation container, and which has a fermentation chamber 10 for the production of biogas through anaerobic fermentation of the biomaterial. The container 8 of the fermentation stage 4 has a feeding device 12, which is configured to bring biomaterial into the fermentation chamber 10. Biomaterial, which is conveyed to the fermentation with the help of the feeding device 12, can, in particular, be biological waste, such as from the biological waste disposal of household and/or residual materials from the food industry or from agribusiness and/or market wastes, as the case may be.
[0032] Biogas recyclable as energy is recovered in the fermentation container, whereby the container 8 depicted as an example is positioned horizontally. In principle, fermentation containers of different geometrical configurations, which can be positioned horizontally or vertically, for example, can be used. Concrete and/or steel, particularly stainless steel, for example, can be used as materials for the production of a fermentation container. Vertical fermentation containers can, for example, be provided with a circular cross-section. Horizontal fermentation containers, for example, can have a rectangular or square cross-section. Horizontal fermentation containers, for example, can even be configured essentially cylindrically.
[0033] The container 8 of the fermentation stage 4 depicted schematically in
[0034] An agitator 14 is provided in the fermentation chamber 10. The agitator 14 has an agitator shaft 18 on which stirring devices 16, which are only sometimes provided with reference figures, are positioned. A mixing of the fermenter contents by means of the stirring device 14 takes place, whereby the formation of floating and sinking layers is reduced and the microbiological activity in the fermenter is positively influenced. In the example depicted, the agitator 14 is configured as a reel stirring device, whereby the stirring devices 16 are placed along the agitator shaft 18 as agitator arms. In the example depicted, the stirring devices 16 project radially outwardly from the agitator shaft 18. It may be advantageous if the stirring devices 16 is positioned helically in at least one partial area of the container 8 and—as indicated in the diagram—are equipped on their ends with paddles. In the present exemplary embodiment, these paddles proceed in parallel to the agitator shaft 18.
[0035] The biogas that arises through the fermentation of the biomaterial in the container 8 of the fermentation stage 4 accumulates in a gas reservoir 22 underneath a cover 24. As indicated schematically in the example, the gas reservoir 22 is bounded at the top by the cover 24 and at the bottom by the level of the material located in the fermentation chamber 10. The cover 24 can, for example, be configured as a foil cover of flexible, gas-tight material. Another embodiment of the cover 24 is, for example, a so-called “membrane roof”. In a membrane roof, an external membrane, below which a gas reservoir membrane is positioned and by which the gas reservoir is bounded at the top, is generally provided. Alternately or in addition to the positioning of the gas reservoir 22 depicted, it is also possible to provide a separate storage unit for gas storage. A separate storage unit can, for example, be an external foil gas storage unit.
[0036] By means of a gas sampling device 26 that is only indicated in the diagram, the biogas recovered in the fermentation container can be removed from the gas reservoir 22 and conveyed for use and/or additional processing and/or storage.
[0037] In the example depicted, a discharge device 28 for the fermented biomaterial is provided on the side of the casing 20 of the fermentation container positioned opposite the feeding device 12.
[0038] The facility for recycling biomaterial depicted in
[0039] In principle, the container 38 of the hygiene stage 6 can, in regard to its design, such as in regard to its structures, the materials used, and its positioning, for example, resemble the fermentation container described above. The container 38 of the hygiene stage 6 has a hygienization chamber 40, which is equipped with a feeding device 42 for biomaterial. In the example depicted, a discharge device 58 for the hygienized biomaterial is provided on the side of the casing 50 of this container 38 positioned opposite the feeding device 42.
[0040] The hygienization chamber 40 depicted schematically in
[0041] In the example depicted, the hygienization chamber 40 is, similarly to the fermentation chamber 10 described above, equipped with an agitator 44, which has an agitator shaft 48 on which stirring devices 46, which are only sometimes provided with reference figures, are positioned.
[0042] Biogas can also arise in the hygienization chamber 50. The biogas arising in the hygienization chamber 50 accumulates in a gas reservoir 52 underneath a cover 54, whereby the gas reservoir 52 and the cover 54 of the hygiene stage can, in principle, be constructed similarly to the gas reservoir 22 and the cover 24 of the fermentation stage 4. A gas sampling device 56 can also be provided in the hygiene stage, as indicated in the diagram. By means of a gas sampling device 56, biogas can be removed from the gas reservoir 52 of the hygiene stage 6 and conveyed to use and/or storage.
[0043] In accordance with the exemplary embodiment depicted, the discharge device 28 of the container 8 of the fermentation stage 4 is connected with the feeding device 42 of the container 38 of the hygiene stage 6 in order to convey biomaterial from the fermentation chamber 10 to the hygienization chamber 40. The biomaterial is thereby preferably pumped from the discharge device 28 of the fermentation stage 4 to the feeding device 42 of the hygiene stage 6 by means of a pumping device 30.
[0044] If both the fermentation chamber 10 and the hygienization chamber 40 operate in accordance with the principle of the plug flow, then it may be suitable, in particular, if the volume of the hygienization chamber 40 is smaller than the volume of the fermentation chamber 10.
[0045] Both the fermentation stage 4 and the hygiene stage 6 are designed for the recycling of biomaterial, such as biological waste, for example, with a high content of impurities and dry material.
[0046] The fermentation of the biomaterial, such as biological waste, for example, occurs in the fermentation stage 4 in the mesophilic temperature range, that is to say, at a comparatively low temperature, such as approx. 40° C., for example, or in a temperature range of approx. 37° C. to approx. 40° C., as the case may be.
[0047] In the hygiene stage 6, which is downstream from the fermentation stage 4, microorganisms are killed thermally, and the greatest possible degassing of the biomaterial takes place. Methane bacteria are killed at a hygienization temperature of approx. 60° and above. The methane emissions emanating from biomaterial that has flowed through the hygiene stage 6 can thereby be clearly reduced. A particularly secure interim storage is consequently made possible.
[0048] The hygiene stage 6 is, preferably, designed for operation at up to approx. 70° C. By that means, hygienically unobjectionable biomaterial is present on the discharge device 58 of the hygiene stage 6, which can be used in agriculture as a high-value fertilizer, for example. Regulation (EG) no. 1069/2009 and Regulation (EU) no. 142/2011 can thereby be complied with.
[0049] The fermentation container of the fermentation stage 4 is designed for the necessary residence time of the biomaterial or of the corresponding substrate, as the case may be, whereby the real minimum residence time in the fermentation stage 4, for example, can amount to approx. 14 hours. The container 38 of the hygiene stage 6 is designed for the residence time of the biomaterial that is necessary for the hygienization, whereby the real minimum residence time in the hygiene stage 6, for example, can amount to approx. 7 hours. It may be advantageous if the residence time of the biomaterial in the hygiene stage 6 is lower than the residence time in the fermentation stage 4. The process temperature in the hygiene stage 6 is clearly higher than the process temperature in the fermentation phase 4.
[0050]
[0051] The hygiene stage 6 in accordance with
[0052] The first hygienization chamber 40-a and the second hygienization chamber 40-b of the hygiene stage 6 are positioned, in terms of process technology and in regard to the material flow of the biomaterial, next to one another. The two hygienization chambers 40-a and 40-b of the hygiene stage 6 are positioned downstream from the fermentation chamber 10 and downstream from the fermentation stage 4.
[0053] The discharge device 28 of the container 8 of the fermentation stage 4 is, in accordance with the example depicted in
[0054] The conveying device additionally has a separating device 64, which divides the current of the biomaterial coming from the fermentation chamber 10 into several partial currents. In the example depicted, a first partial current leads from the separating device 64 to the feeding device 42-a of the first container 38-a of the hygiene stage 6. A second partial current leads from the separating device 64 to the feeding device 42-b of the second container 38-b of the hygiene stage 6. Both hygienization chambers 40-a, 40-b are, in accordance with the exemplary embodiment depicted here, operated in parallel. The division of the biomaterial discharged from the fermentation chamber 10 to several hygienization chambers 40-a, 40-b can, for example, be advantageous precisely then if the facility 2 is preferably designed in such a way that the residence time of the biomaterial in the hygiene stage 6 ensures a reliable hygienization of the fermentation product. The configuration of the facility 2 depicted in
[0055]
[0056] While the fermentation stage 4 and the hygiene stage 6 are, in accordance with
[0057] One concept that forms the basis for the invention can be summarized as follows: The present invention relates to a facility 2 for the recycling of biomaterial, with a fermentation stage 4, whereby the fermentation stage 4 has a fermentation chamber 10 for the production of biogas through anaerobic fermentation of the biomaterial, and with a hygiene stage 6 that is positioned downstream from the fermentation stage 4, whereby the hygiene stage 6 has a hygienization chamber 40, 40-a, 40-b for the reception and the thermal hygienization of the biomaterial discharged from the fermentation stage 4. The invention also relates to a process for the recycling of biomaterial by means of zymosis, whereby biogas is produced, in a fermentation stage 4, through the anaerobic fermentation of the biomaterial, whereby the biomaterial is, after flowing through the fermentation stage 4, conveyed to a hygiene stage 6 in which the biomaterial thermal is hygienized, and whereby the biomaterial is, after flowing through the hygiene stage 6, made available as recyclable hygienized agricultural fermentation residue. By that means, biological wastes that are characterized by high impurities and inhomogeneity can also be fermented mesophilically and, after hygienization, be conveyed to an additional use, such as fertilizer, for example.
[0058] While in the foregoing there has been set forth various embodiments of the invention, it is to be understood that the present invention may be embodied in other specific forms without departing from the spirit or central characteristics thereof. The present embodiments, therefore, are to be considered in all respects as illustrative and not restrictive, and the invention is not to be limited to the details given herein. While specific embodiments have been illustrated and described, numerous modifications come to mind without significantly departing from the characteristics of the invention and the scope of protection is only limited by the scope of the accompanying claims.