In a method for physical and thermochemical treatment of biomass, the biomass moisture content is reduced in a dryer and ammonia (NH.sub.3) is also released from the biomass during drying. The dried biomass is then either pyrolyzed in a pyrolysis reactor and the pyrolysis gas is forwarded to and combusted in a combustion device to form flue gas, or is combusted in a combustion facility unit to form flue gas. In either case the flue gas is fed to a mixer. Oxygen (O.sub.2) is metered to the flue gas in the mixer and is fed directly to the dryer as drying gas. As the drying gas passes through the dryer, the sulfur dioxide (SO.sub.2) contained in the drying gas and/or the sulfur trioxide (SO.sub.3) chemically reacts with the ammonia (NH.sub.3) to form ammonium sulfite ((NH.sub.4).sub.2SO.sub.3) and/or ammonium sulfate ((NH.sub.4).sub.2SO.sub.4). Also a treatment facility physically and thermochemically treats the biomass.

A novel solar chimney-based liquid desiccation system includes a solar collector, an embedded desiccator with a novel structure, and a heated chimney. The solar collector heats up an incoming external airflow with solar radiation, and mobilizes the heated air to pass through the embedded desiccator. The embedded desiccator contains a liquid solution or another content that can undergo a thermal transfer process upon contacting the heated air from the solar collector. Typically, this thermal transfer process involves desiccation of the liquid solution and vaporization of some liquid or other elements. This desiccation process may be utilized to separate liquid from remaining contents, or as a purification process. The embedded desiccator is further connected to the heated chimney with a heated inner surface to minimize undesirable reflux and condensation within the chimney structure. A liquid recovery unit may also be added to the system to collect condensed liquid after desiccation.

A pellet made of dried, unfermented livestock manure has N, P and K values in the range of N: 3 to 7 g/kg, as ammoniac and organic nitrogen, P: 2 to 6 g/kg as phosphorus pentoxide and K: 2 to 6 g/kg as potassium oxide (g/kg). The pellet has a hardness exceeding 10 kg and has a shell composed of manure-base lignin. A press roll, including a hollow rotatable drum with a perforated screen, may be used in combination with an endless belt and a scraper to produce the pellet.

The invention relates to a drying system (T) according to FIG. 1 for drying goods to be dried (LTG), comprising—a drying tunnel (TT), —a line (LAG) for exhaust gas (AG) containing (VOC) out of the drying tunnel (TT), —a controlled fan (GBL) for further transporting the exhaust gas (AG) to a heat exchanger (WT), —a heat exchanger (WT) for heating the exhaust gas (AG) using the clean gas (RG), —an exhaust gas line (LAG) downstream of the heat exchanger (WT) for further transporting the exhaust gas (AGWT) to a burner (BR) in a combustion chamber (BK) of a thermal post-combustion system (TNV), —a cold bypass (BP) which bypasses the heat exchanger (WT) and which can be regulated using an electronically controlled controller (R), —a fuel line (LEG) for a fuel (EG) to the burner (BER), —a clean gas line (LRG) for transporting the clean gas (RG) out of the combustion chamber (BK) to the heat exchanger (WT) in order to cool the exhaust gas (AG), —a clean gas line (LRG) for conducting the clean gas (RG) from the heat exchanger (WT) to the heat consumers (WA), —a heater (HZTT) for heating the drying zone (TT) by means of the heat consumers (WA), and—a clean gas line (LRG) for conducting the clean gas (RGD) to a stack (K). The invention also relates to a drying method and a method for a thermodynamic regulation (TDR).

An apparatus and a method are provided for continuously drying bulk goods, in particular wood fibers and/or wood chips, in a dryer, wherein the drying vapors are led to a dryer circuit, in which the drying vapors are indirectly heated via a heat-exchanger and are conducted to the dryer again.

An apparatus and method for the temperature control of objects, in particular for drying coated vehicle bodies, with a temperature control chamber with at least one lock region, a fresh air device for producing fresh air which can be supplied to the temperature control chamber, a circulating air device which extracts exhaust air from the temperature control chamber and produces circulating air which can be supplied to the temperature control chamber, an air intake device for supplying air to the temperature control chamber, and a control device. A fresh air volume flow and a circulating air volume flow can be supplied to the air intake device, and the control device is configured to control the fresh air volume flow and the circulating air volume flow in such a manner that the overall volume flow which is supplied to the temperature control chamber does not fall below a lower limit.

A plant for drying objects which release volatile substances may include: a drying tunnel; a conveying system configured to convey the objects through the drying tunnel; a plurality of sensors arranged along the drying tunnel; and/or a plurality of air exchange units. The sensors may be configured to measure a concentration of the volatile substances along the drying tunnel. The air exchange units may be controlled by the sensors to keep the concentration of the volatile substances in the drying tunnel below a pre-established value. A method for keeping volatile substances below a pre-established value within a plant for drying objects may include: measuring with sensors concentration of the volatile substances at points along the drying tunnel; and/or operating air exchange units, according to the concentration of the volatile substances measured by the sensors, to keep the concentration of the volatile substances in the drying tunnel below the pre-established value.

Flue gases are produced in a combustion chamber of a burner unit, in particular for the combustion of exhaust air. Combustion gas can be supplied to a gas burner via a combustion gas line and feed air, in particular exhaust air that can be used as feed air, is supplied to said burner via a feed air line. The feed air is divided into primary air and secondary air by a device. The primary air is mixed with the combustion gas, in a mixing zone, to form a primary air/combustion gas mixture, said primary air/combustion gas mixture being supplied to the combustion chamber. A flue gas re-circulation system comprises a through-flow chamber which is connected to the combustion chamber and in which the secondary air is mixed with the flue gases occurring in the combustion chamber to form a secondary air/flue-gas mixture. The secondary air/flue-gas mixture is supplied to the primary air/combustion gas mixture in the combustion chamber by means of a device. At least one internal cylindrical surface of the through-flow chamber forms a Coanda profile in the direction of flow. A device for the temperature control of objects, in particular for drying painted vehicle bodies, comprises a temperature-control tunnel that is accommodated in a housing and that defines at least one tunnel section comprising at least one air outlet and at least one air inlet. A heating assembly, in which a hot primary gas can be generated by means of a burner unit of this type, is associated with the tunnel section.

A system for heating, drying or curing an object, the system comprising a housing having a first wall and at least one second wall adjacent the first wall. The first wall and at least one second wall define an interior for holding an object to be heated, dried or cured. The system also includes an air plenum adjacent to, covering and disposed inward from the first wall, and at least one air plenum opening in the air plenum to supply air into the interior. A fan is disposed in the one air plenum opening. The system also includes a ductwork assembly adjacent to, covering and disposed inward from the second wall. The ductwork assembly is in air-communication with the air plenum, and has a ductwork opening so that substantially all air circulation in the interior is between the air plenum opening and the ductwork opening.

A novel solar chimney-based liquid desiccation system includes a solar collector, an embedded desiccator with a novel structure, and a heated chimney. The solar collector heats up an incoming external airflow with solar radiation, and mobilizes the heated air to pass through the embedded desiccator. The embedded desiccator contains a liquid solution or another content that can undergo a thermal transfer process upon contacting the heated air from the solar collector. Typically, this thermal transfer process involves desiccation of the liquid solution and vaporization of some liquid or other elements. This desiccation process may be utilized to separate liquid from remaining contents, or as a purification process. The embedded desiccator is further connected to the heated chimney with a heated inner surface to minimize undesirable reflux and condensation within the chimney structure. A liquid recovery unit may also be added to the system to collect condensed liquid after desiccation.