Patent application number | Description | Published |
20100068792 | METHOD FOR THE VOLUME AND BULK REDUCTION OF DOMESTIC WASTE - A method for the volume and bulk reduction of domestic waste is disclosed, comprising comminution of the domestic waste, separation of the organic fraction of the domestic waste, generation of biogas from the separated organic fraction by anaerobic fermentation along the principal of dry fermentation in a biogas plant, relocation of the organic fraction from the biogas plant into an aerobization container, aerobization and composting of the organic fraction by supplying air, and drying of the composted organic fraction by injection of air. | 03-18-2010 |
20100159571 | BIOGAS PLANT FOR METHANIZING BIOMASS HAVING A HIGH SOLIDS FRACTION - A biogas plant for methanizing biomass having a high solids fraction includes a digestion tank system having a plurality of digestion tanks adapted to be closed in a gas- and liquid-tight manner, each of which includes a charging and withdrawing opening for charging with biomass and withdrawing the biomass, a biogas discharge means, a percolate reservoir, a percolate drainage means for discharging percolate from the plurality of digestion tanks and supplying the percolate to the percolate reservoir, a percolate distributing means for distributing the percolate from the percolate reservoir over the biomass in the plurality of digestion tanks, and a percolate regulating means for regulating the percolate level in the plurality of digestion tanks. The percolate reservoir includes a first and a second percolate container, and supplying and discharging of percolate to/from the first and/or the second percolate container takes place with the aid of the percolate regulating means. | 06-24-2010 |
20110236947 | Reducing methane slack when starting and stopping biogas fermenters - A novel method reduces methane slack when operating a biogas fermenter. When starting up a freshly charged fermenter, the methane portion of the produced biogas is initially so low and the portions of carbon dioxide and nitrogen are so high that the biogas cannot be directly used in a combined heat and power plant. Conventionally, the biogas generated during the startup phase has a small portion of methane that is discharged directly into the atmosphere or is flared off if the methane fraction is larger. The initially produced methane is consequently not used and becomes methane slack. To reduce methane slack, the biogas with the low methane fraction is fed to a gas treatment unit in which non-methane components of the gas mixture are partially separated, and the remaining gas mixture with a higher methane content is returned to the biogas fermenter until the methane fraction is sufficiently high. | 09-29-2011 |
20110287527 | Gas treatment appliance and gas treatment process - A gas treatment appliance and a gas treatment process are provided. The proportion of tar is decreased in a product gas formed on the gasification of carbonaceous feedstocks. The product gas or synthesis gas formed on the gasification of carbonaceous feedstocks is generally highly polluted with tar. This tar-polluted gas is exposed to a solid support substrate which is a support for bacteria which degrade tar. Suitable bacteria are, in particular, bacteria that occur in biogas-generating processes. The bacteria contained in the solid support substrate convert at least some of the tars and polycyclic aromatic hydrocarbons (PAHs) contained in the product gas into shorter-chain hydrocarbon compounds and methane which are not an industrial problem, and so their proportion is reduced in the product gas leaving the support substrate. In this manner the tar pollution in a synthesis gas or product gas can be reduced in a simple and inexpensive manner. | 11-24-2011 |
20120159848 | Method of Operating a Reactor Module for Endothermic Reactions and a Reactor Having a Plurality of Such Reactor Modules - A reactor has multiple reactor modules for endothermic reactions. Each reactor module comprises a reaction channel enclosed by a tubular boundary wall and having first and second ends. The reactor module has an inlet element for introducing reactants into the reaction channel. The inlet element is arranged at the first end of the reaction channel. The reactor module has an outlet element for discharging the reaction products from the reaction channel. The outlet element is arranged at the second end of the reaction channel. The reactor module has a heat supply device in the form of a porous burner arrangement that is arranged on the outside of the tubular boundary wall of the reaction channel. Because a porous burner arrangement is used instead of a heat source having catalytic combustion, high reactor performance is achieved at an economical price. The porous burner is substantially less expensive than a combustion catalyst. | 06-28-2012 |
20120329120 | Reducing Methane Slack When Starting and Stopping Biogas Fermenters - A novel method reduces methane slack when operating a biogas fermenter. When starting up a freshly charged fermenter, the methane portion of the produced biogas is initially so low and the portions of carbon dioxide and nitrogen are so high that the biogas cannot be directly used in a combined heat and power plant. Conventionally, the biogas generated during the startup phase has a small portion of methane that is discharged directly into the atmosphere or is flared off if the methane fraction is larger. The initially produced methane is consequently not used and becomes methane slack. To reduce methane slack, the biogas with the low methane fraction is fed to a gas treatment unit in which non-methane components of the gas mixture are partially separated, and the remaining gas mixture with a higher methane content is returned to the biogas fermenter until the methane fraction is sufficiently high. | 12-27-2012 |
20150068259 | Method for Operating a Bioreactor that Methanizes Biomass - The invention relates to a bioreactor for methanizing biomass, a biogas plant having a plurality of such bioreactors, and a method for operating such a bioreactor. Because the elongated reactor vessel includes both a loading gate and an unloading gate that are arranged at opposite ends of the elongated reactor vessel, it is possible to remove consumed biomass, which is harmless in terms of epidemiologic hygiene and plant hygiene due to thermophilic process control during the fermentation, from the reactor vessel through the unloading gate and to transfer this consumed biomass directly to the composting process. The bioreactor thus has a “clean” unloading gate and an “unclean” loading gate. | 03-12-2015 |
20150147745 | Method for Operating a Biogas System in a Batch Mode - A biogas system operates according to the principle of dry fermentation with multiple biogas fermenters that are run in batch mode. One of the biogas fermenters has just been loaded with fresh biomass and the other biogas fermenters are in the state of producing biogas with a higher concentration of methane. The biogas fermenter just loaded with fresh biomass is closed and connected to the other biogas fermenters that are already producing biogas. In addition, there is a return of the biogas mixture from the freshly loaded biogas fermenter to at least one of the other biogas fermenters producing biogas. After expiration of a defined time duration, the return of the biogas mixture from the freshly loaded biogas fermenter is stopped. The defined time duration is determined based on the concentration of methane in the mixture of biogas generated in all of the biogas fermenters. | 05-28-2015 |