Large-scale plants are often unable to find sufficient disposal possibilities in acceptable distances. Therefore it is sensible to treat fermentation residue substrates by suitable screening processes in such a way that they can be discharged and re-used in the form of free flowing solids and nutrient-poor process service water. The main steps in the treatment of fermentation residue substrates from biogas plants areas follows: liquid-solid-matter separation, ultrafiltration using ceramic membranes and reverse osmosis. For the filtration of liquids with highly abrasive components – such as undissolved macromolecules in fermentation residue substrates – a highly abrasion-resistant membrane named Duratech has been developed.
During fermentation only easily degradable organic matter is decomposed to methane and carbon dioxide, leaving fermentation residue substrates. These mainly consist of relatively stable organic substances that are more difficult to decompose. The nutrients contained in these residues, such as organic nitrogen, potassium and phosphorus, are mineralised by the fermentation process. This means that fermentation residue substrates from biogas plants are an equivalent substitute for inorganic fertilisers, in particular because they can be spread on crop areas without the need for a lot of technical equipment, penetrate the ground quickly and because their nutrients are available to the plants.
The nitrogen contained in the fermentation residue substrates is easily available which means that the substrate should be applied as close as possible to the time when nitrogen is needed. If fermentation residue substrates are spread outside these times they show a poor nitrogen effect and may cause nitrate pollution in seepage water. Therefore, fermentation residue substrates need to be stored. As a result, biogas plant operators are faced with expenses for plant engineering, personnel and logistics which ultimately lead to high operating costs.
Fermentation residues undergo a complete treatment process involving the following treatment stages:
- • Decanter, combined with metered adding of precipitants as needed to eliminate solids and to reduce organic components, followed by screening.
- • Ultrafiltration using ceramic membranes to reduce undissolved macromolecules.
• Reverse osmosis to remove dissolved low-molecular substances such as hardness constituents and salts.
During the first treatment stage the fermentation residue substrates from the storage tank undergo a liquid-solid-matter separation in a decanter centrifuge. If the fermentation residue substrates contain coarse-fibred substances they are first treated in a pressure worm separator before entering the decanter. If needed to better separate solid particles, colloidal turbid matter and organic matter contained in the feed line to the decanter an inorganic flocculator is added which dramatically reduces the fouling potential of the fermentation residue substrates.
The solids discharged from the separator and the decanter are fed onto a screw conveyor and transported to an outdoor storage area. The separated liquid phase (“centrate”) still has a dry substance content of up to 2% and is led to a subsequent screening process. Any fibrous substances and fine particles that can not be removed by the decanter are separated by means of a screen. This is mainly required in order to prevent particles from blocking the downstream ultrafiltration modules. The separated solids are removed from the screen through a discharge opening and are also fed to the screw conveyor to be transported to the outdoor storage area. The discharge water is collected in a pump tank and led into the receiving container of the downstream ultrafiltration plant.
High abrasion resistance
In the ultrafiltration stage a selective pore membrane with pore diameters between 0.2 and 0.05 μm is used to remove macromolecular particles from the centrate. The preferred membranes are ceramic multi-channel membranes which due to their special material properties have proved their worth in the treatment of fermentation residues. In this respect, high flux rates combined with a very high chemical, thermal, and mechanical resistance and the resulting operational reliability are of particular importance. For applications involving highly abrasive media such as those encountered during the treatment of fermentation residues atech innovations gmbh has developed Duratech®, a ceramic membrane made of titanium oxide. Thanks to an innovative coating process which is essentially based on controlled crystal growth Duratech has an abrasion resistance that is even higher than that of standard membranes, which are also very rugged. This has been proven by standardised scratch test measurements that were performed under defined conditions and by several applications.
In the treatment of fermentation residues ultrafiltration using ceramic membranes is used to:
- • separate solids and dissolved macromolecules;
- • eliminate germs and bacteria;
• retain the fermenter biomass;
• remove the particulate COD.
To incorporate the membranes in filtration plants they are arranged in so-called modules, where several supports are combined in stainless steel vessels. These pressure vessels as well are offered by atech in various steel qualities and designs. During cross-flow filtration by means of ceramic membranes the medium to be filtered flows through the channels of the membrane support. All particles/molecules whose size exceeds the pore diameter of the membrane are retained. The particles/molecules build up in the concentrate. The filtrate permeates through the pores and – in the application described here – is fed into the reverse osmosis process.
The difference between reverse osmosis and other membrane filtration processes is that reverse osmosis not only retains low-molecular macromolecules but also separates low-molecular substances such as salts, hardness constituents and other dissolved, ionogenic substances from a liquid medium. The particle sizes that can be retained are between 0.1 and 1 nm. A3-Water Solutions GmbH has designed a process for the treatment of fermentation residues which uses a reverse osmosis system of a multi-permeate stage configuration. This means that several reverse osmosis plants of different pressure levels are connected in series and where permeate from the first reverse osmosis stage is further purified in a second and a third reverse osmosis stage. The permeate produced in the first reverse osmosis stage is already substantially free of salts dissolved in water, nitrogen and other nutrients but, due to the shift in the carbonate balance, still has a high carbonic acid content that needs to be removed. Therefore, a forced-draft degasifier is installed between the first and the second reverse osmosis stage. In this way it is possible to reduce the content of free carbonic acid to < 10 mg/l.
During the planning phase of the first reference plant built by A3-Water Solutions GmbH – which has a capacity of 64,000 litre per year and has been in operation for approximately 18 months – it was assumed that the costs for the treatment of fermentation residues including debt services would be EUR 5.10 per 1,000 kg. Already during the first year of operation optimisations in process engineering and an efficient operations management made it possible to remain under this amount. Treating fermentation residues produces a permeate with a high pure water quality and a solid and a liquid residue with the qualities of a valuable substance.
Added value potential
The liquid fermentation residue obtained as concentrate in the reverse osmosis plant complies with the legal stipulations of the German Regulation on the Principles of Good Manuring and Fertilising Practice (Duengeverordnung), the German Ordinance on Biowastes (Bioabfallverordnung) and the German Soil Protection and Contaminated Sites Ordinance (Bodenschutz- und Altlastenverordnung). The mass concentrations of nutrient salts contained in the concentrates exceed those in the original, untreated fermentation residue substrates by approximately 10 to 15 mass percent. Meanwhile, the liquid fermentation product has been awarded the RAL quality mark “Fermentation Product” (RAL-GZ 256/1).
Similar to the liquid fermentation product, the solid fermentation product obtained from the pressure worm, or the decanter, or the screen complies with all applicable requirements and has also been awarded the RAL-GZ 256/1 quality mark. This quality mark is evidence that the fermentation products obtained by decantation or screening and membrane filtration are certified valuable substances that can be used for sustainable soil improvement and for manuring and fertilising. This considerably increases the added value potential of a treatment plant for fermentation residues.
The treatment of fermentation residues from biogas plants is gaining in importance due to the growing number of biogas plants, especially of large scale plants.
Several new treatment plants, composed of the described unit operations decanter/centrifuge, ultrafiltration and reverse osmosis are proof for successful complete treatment of fermentation residues.
The treatment process creates high pure water quality for internal use (permeate RO) and a liquid and solid fertiliser with high amount of nutrients, turning residues into a valuable product.