Abstract: A method of operating a laundry treating appliance with a treating chamber for treating a load of laundry the method comprising supplying a rinse to the treating chamber during a rinse cycle, rotating the treating chamber at a tumbling speed, spinning the treating chamber in an extraction cycle to remove excess moisture from the load of laundry, sensing a parameter indicative of a remaining moisture content value in the load of laundry, comparing the remaining moisture content value to a pre-determined remaining moisture content value.

Abstract: Methods are provided which include placing one or more objects into a cabinet, subsequently closing the cabinet and remotely starting a disinfection device disposed therein to disperse a germicide within the closed cabinet. Embodiments of cabinets include an interior void of at least 10 ft3, a door to enclose the cabinet and one or more support structures arranged within the cabinet adjacent the interior void. Portions of the support structures facing the interior void are transparent and/or have through-holes. Other embodiments of cabinets include a moveable germicidal blocking partition for separating portions of the cabinet, a door for accessing one of the portions and a sensor for detecting when the partition is in position to separate the portions. An embodiment of a support structure includes a base having transparent materials and/or one or more through-holes, sidewalls shaped to match a peripheral contour of a medical device, and a weight sensor.

Abstract: A method of operating a laundry appliance in a drying cycle includes motivating a flow of process air from a drum of the laundry appliance across an evaporator of a sealed system. Refrigerant in the evaporator of the sealed system absorbs heat from the flow of process air and the refrigerant circulates through the sealed system. The method also includes receiving, by a controller of the laundry appliance, an input indicative of a characteristic of the sealed system. The method further includes determining, by the controller, a dryness level of articles in the drum of the laundry appliance based on the received input indicative of the characteristic of the sealed system.

Abstract: A method of operating a laundry treating appliance with a treating chamber for treating a load of laundry the method comprising supplying a rinse to the treating chamber during a rinse cycle, rotating the treating chamber at a tumbling speed, spinning the treating chamber in an extraction cycle to remove excess moisture from the load of laundry, sensing a parameter indicative of a remaining moisture content value in the load of laundry, comparing the remaining moisture content value to a pre-determined remaining moisture content value.

Abstract: A laundry appliance includes a blower that directs process air along an airflow path. An evaporator dehumidifies the process air and removes condensate from the process air. A heat exchange plate is disposed within the airflow path and supports the evaporator from below and within the airflow path. The heat exchange plate receives the condensate from the process air. A sloped area of the heat exchange plate directs the condensate downward and along the heat exchange plate to a condensate drain, wherein the sloped area includes a directing surface that blocks the process air from pushing the condensate upward and away from the condensate drain.

Abstract: A continuous-flow dryer for drying a material by means of hot air is provided with a fresh air supply device for supplying fresh air as supply air, an exhaust air recirculation device for removing exhaust air and for recirculating exhaust air as supply air, and a heat exchanger, through which fresh air on the one hand and exhaust air on the other hand are led, for transferring waste heat of the exhaust air into the fresh air. According to the invention, the removed exhaust air is supplied at the bottom into the heat exchanger.

Abstract: Hot air containing water is discharged from a heating space to pass through a vertically bent fluid pipeline (1035) formed by an hot air section (1030) of a water condensing pipeline structure (1029) and a vertically bent flow guiding structure (1032). Meanwhile, external inlet air having relatively low temperature is pumped through an cold air section (1031) of the water condensing pipeline structure (1029) to enable the hot air to be cooled, thereby condensing the water contained in the hot air. The condensed water is collected or flows with a first part of the hot air to pass through an hot air shunt port (1026) for being guided to an external discharging port (109). A second part of the hot air is guided by the hot air shunt port (1026) to flow towards a hot air return inlet (1022), thereby reducing the thermal energy loss and saving electric energy.

Abstract: A method for efficient utilization of hot air flows in a dryer system for goods to be dried is provided, in particular for a vehicle painting plant. Waste air from the dryer is heated in a thermal post-combustion plant and, as clean gas is conducted through circulating air recuperators, the circulating air extracted from the dryer is heated up and returned into the dryer. A device for efficient utilization of the hot air flows in a dryer system for goods to be dried is also provided, in particular for a vehicle painting system. The device includes a dryer, the waste air of which is heated in a thermal post-combustion plant. Clean gas is fed to circulating air recuperators and at least one fresh air recuperator. At least one additional heat source for the clean gas is also provided.

Abstract: A laundry dryer has a casing (1) accommodating therein a drying air circuit and operational devices for carrying out a drying treatment on laundry. The dryer further includes a basement (8, 108) having a condensate draining path (21, 121) for conveying moisture condensed from drying air towards a reservoir (24, 124). At least one condensate retaining region (29A, 29B; 129A, 129B) is provided in the condensate draining path (21, 121) and/or on reservoir (24, 124) thereby forming a liquid trap for preventing drying air dispersing along path (21, 121) from entering reservoir (24, 124).

Abstract: A biomass drying system includes a rotary biomass dryer that includes a helically threaded auger shaft rotatably driven by a prime mover, such as an electric motor. No external source of heat is required to dry a wet biomass material that is supplied to an input of the biomass dryer. Instead, the helical threads on the shaft have a variable width, designed to gradually increase the compression applied as the biomass material is advanced through a generally cylindrical bore in the biomass dryer. A variable compression nozzle is disposed at a distal end of the bore and can be adjusted to achieve a desired level of a parameter such as the moisture content of the dried biomass material produced by the system. The variable compression nozzle, which can be automatically controlled, includes longitudinally extending segments that are forced radially inwardly to increase the compression force applied to the biomass material.

Abstract: Disclosed is an apparatus for drying and concentrating, using waste vapor, which includes: a vapor supplying unit that produces and supplies vapor, using a boiler; a vapor storing unit that temporarily stores the vapor from the vapor supplying unit; a drying/concentrating unit that receives the vapor from the vapor storing unit and dries/concentrates a high-moisture material, in an indirect heat transfer type; a waste vapor collecting unit that collects waste vapor produced from the high-moisture material in the drying/concentrating unit; a vapor compressing unit that compresses the waste vapor collected by the waste vapor collecting unit; a condensate water discharging unit that separates condensate water, which is discharged after used as heat source in the drying/concentrating unit, and stink gases and discharges them; and a stink gas supplying line through which the stink gases separated by the condensate water discharging unit is supplied to the boiler.

Abstract: The present invention relates to a laundry treating machine, including an air supply unit for supplying air, a tub for having the air supplied thereto from the air supply unit to treat the laundry, the tub having an air recovery opening formed in an outside circumferential surface thereof for recovery of the air to the air supply unit, a lint filter mounted to an inside of the air recovery opening for filtering the lint from the air, a filter cleaning unit for spraying cleaning water to separate the lint from the lint filter, and a flow passage member for guiding the cleaning water dropping from the lint filter to an inside of the tub to an inside surface of the tub.

Abstract: A clothes treating apparatus including a drum, an air suction duct forming a flow path of air introduced into the drum, an auxiliary fan introducing air into the air suction duct, an air exhaustion duct forming a flow path of air exhausted from the drum, a main fan exhausting air to the air exhaustion duct from the drum, a condenser heating air sucked into the drum through the air suction duct, an evaporator cooling air exhausted from the drum through the air exhaustion duct, and a compressor and an expander forming a heat pump together with the condenser and the evaporator. The method includes measuring a discharge side pressure of the compressor, and comparing the measured discharge side pressure with a maximum allowable pressure, and determining that the auxiliary fan does not operate when the discharge side pressure is more than the maximum allowable pressure.

Abstract: A fuel preprocess system for a coal combustion boiler is disclosed. The fuel preprocess system for a coal combustion boiler that dries biomass or refuse-derived fuel in accordance with the present invention can include: a dryer configured to dry the biomass or refuse-derived fuel by use of flue gas generated after combustion in the boiler; and a torrefier configured to devolatilize a fibrous component contained in the dried fuel from the fuel dried in the dryer by use of primary air that is heat-exchanged after the combustion in the boiler.

Abstract: A system for treating objects includes a device for tempering objects in which a tempering tunnel having at least one air outlet and at least one air inlet is arranged in a housing. At least one heating unit, in which a hot primary gas flow can be generated, is assigned to the tempering tunnel, wherein the hot primary gas can be guided into a circulating air heat exchanger, in which air from the tempering tunnel can be heated by hot primary gas as circulating air, which can be fed back to the tempering tunnel in a circuit via the at least one air inlet. The heating unit is coupled in the manner of a combined heating and power plant to an electric generator in such a way that electrical energy is produced during operation of the heating unit.

Abstract: Disclosed is a grain drying apparatus installed in a combine harvester. The grain drying apparatus using exhaust heat of a combine harvester according to the present invention comprises: an intake duct one end of which is connected to an exhaust port of the combine harvester and the other end of which outputs the hot air discharged from the exhaust port; a filter unit located at the other end of the intake duct for removing harmful components from the hot air; and an exhaust duct connected to the other end of the filter unit to supply the hot air from which the harmful components are removed to a grain selection pan of the combine harvester.

Abstract: In a method for reprocessing wet waste materials containing organic components, in particular sludges in a cement clinker production plant, in which raw meal is preheated in a preheater (3) in countercurrent flow to the hot exhaust gases of a clinker furnace (2), and calcined in a calciner (4) fired with alternative fuels, the wet waste materials are dried in a drying unit (18) using a hot gas produced from the preheater waste heat and the dried waste materials and the drier exhaust gases are discharged from the drying unit (18), wherein the drier exhaust gases are introduced into the calciner (4).

Abstract: To provide a cement production apparatus in which heat-exchanging efficiency can be improved by even pre-heating by supplying material equally to cyclones above a duct and which can perform an operation with low pressure loss and small energy consumption. A cement production apparatus includes: a duct 21 provided between upper cyclones 13A and a lower cyclone 13B being provided below the upper cyclones 13A, the duct 21 in which the exhaust gas drained from the lower cyclone 13B flows upward, distributing and introducing the exhaust gas to the upper cyclones 13A; a plurality of material-supplying pipes 22 for supplying cement raw material provided on the duct 21 below a distribution part 23 to the plurality of the upper cyclones 13A with a same number of distribution outlets 21a among the upper cyclones 13A; and connection ports 22a of the material-supplying pipes 22 to the duct 21 each provided at each of positions corresponding to swirl flows of the exhaust gas poured into the distribution outlets 21a.

Abstract: A dryer dries particles, wherein the dryer comprises two circular decks mounted substantially horizontally and rotating in opposite directions relative to one another about a same vertical axis, Z, the surface of said decks being perforated and permeable to air, steam and water, a means for blowing hot gas in a flow substantially parallel to the axis Z, passing through the second deck before passing through the first deck, means for distributing said particles to be dried on the first and second decks and means for recovering the particles after a rotation of each deck, and a means for transferring the particles collected from the first deck by the recovery means to a second distribution means suitable for distributing said particles along a radius of the second deck.

Abstract: The invention relates to a household appliance, more particularly a tumble dryer, comprising a working chamber and at least one latent heat store having a respective storage medium, wherein the respective storage medium is thermally coupled via a respective associated heat exchanger to a working medium circulating through the working chamber, wherein the working medium first moves from the working chamber to a heat sink, from said heat sink to the heat exchanger, from said heat exchanger to a heat source, and from said heat source back to the working chamber, and wherein the respective storage medium forms a substance mixture together with a respective carrier fluid, wherein said substance mixture can be conducted in a respective closed circuit through the associated heat exchanger for an exchange of heat with the working medium.

Abstract: A spray dryer exhaust gas treatment system and process recovers waste heat, removes odors from the exhaust gas, or both. The spray dryer may be used to dry digestate from an anaerobic digester. Spray dryer exhaust is at least partially recirculated to the spray dryer, or condensable vapors are removed from the spray dryer exhaust, or both. Optionally, a bleed from a recirculating exhaust stream may pass through a combustion chamber. Preferably, waste heat is added to the recirculating exhaust stream or used to evaporate water upstream of the spray dryer. In a case where the spray dryer is used to treat digestate, a biogas burner may provide the combustion chamber and a source of waste heat. The system and method reduce odors from spray dryer exhaust by condensing odorous compounds, by combustion, or both while using waste heat and spray dryer exhaust gas recirculation to reduce energy consumption.

Abstract: A dryer having a waste heat recovery device includes a cabinet, a drum rotatably mounted within the cabinet and having a front surface and a rear surface, an intake duct configured to provide an intake flow path through which air flows into the drum, an exhaust duct configured to exhaust air coming from the drum out of the cabinet, a heater configured to heat air flowing into the drum, and an ambient air duct configured to inhale air from outside the cabinet and supply the air from outside the cabinet into the drum. The waste heat recovery device includes an evaporation unit configured to absorb heat from air that is exhausted from the drum, a condenser unit configured to transfer heat absorbed from the evaporation unit to ambient air that flows into the ambient air duct, and a heat transfer medium configured to transfer heat between the evaporation unit and the condenser unit.

Abstract: A clothes dryer configured to cause air to flow through a drying chamber, an exhaust passage (an air passage) 103 and a filter by a blower to dry clothes includes a heat pump installed in the exhaust passage (103) and having a heat exchanger (122) including a refrigerant pipe (132) and a pin, and a flow velocity sensor (107) of airflow having a hot thermistor (a heat generating body) 107a and a temperature compensation thermistor (a temperature detecting body) 107b and installed downstream from the heat exchanger (122), wherein the thermistors (107a and 107b) are disposed at a refrigerant pipe (132) of the heat exchanger (122) in parallel.

Abstract: A lint catching system is provided for a clothes dryer. The lint catching system filters lint from exhaust air expelled from the clothes dryer.

Abstract: A clothes treating apparatus includes a cabinet and a drum rotatably installed within the cabinet. The clothes treating apparatus also includes a circulation flow path in which exhaust air discharged from the drum is re-supplied to the drum and a condenser configured to allow the exhaust air and cooling air introduced from an outside of the cabinet to be heat-exchanged. The clothes treating apparatus further includes a cooling flow path configured to guide the cooling air toward the condenser and a blowing fan configured to introduce air from outside of the cabinet to an interior of the cooling flow path. In addition, the clothes treating apparatus includes a discharge opening that discharges cooling air, which has passed through the condenser, to an interior of the cabinet. The rotational shaft of the drum is disposed between the discharge opening and the blowing fan.

Abstract: The present invention provides grain-drying facilities which can effectively use the heat energy of biomass combustion hot-air that has been generated in a biomass combustion furnace. The grain-drying facilities 1 include: a biomass combustion furnace 3 provided with a heat exchanger 24 for generating a hot air from a combustion heat of a biomass fuel and an outside air which has been taken in from the outside; and a circulation type grain-drying apparatus 2 provided with a grain-drying portion 7 to which the hot air that has been generated in the biomass combustion furnace 3 is supplied through a pipe 15 for supplying a hot air, wherein the circulation type grain-drying apparatus 2 has a plurality of warming pipes 6a in the grain-drying portion 7, and an exhaust hot-air is supplied to the warming pipes 6a from the biomass combustion furnace 3 through a pipe 11 for supplying the exhaust hot-air.

Abstract: The invention relates to a laundry treatment apparatus, in particular dryer (2a) or washing machine having drying function, comprising: a cabinet having a front wall, a rear wall, side walls and a base section, wherein the base section comprises an internal side facing the interior of the cabinet and an external side exposed to the outside of the cabinet, a laundry storing chamber for treating laundry using process air (A), a process air loop for circulating the process air through the laundry storing chamber, and a heat pump system for dehumidifying and heating the process air, the heat pump system having a refrigerant loop comprising: a first heat exchanger (10) for heating a refrigerant and cooling the process air (A), a second heat exchanger (12) for cooling the refrigerant and heating the process air, a refrigerant expansion device, a compressor, and an auxiliary heat exchanger (13). According to the invention the auxiliary heat exchanger (13) is arranged at the external side of the base section.

Abstract: The invention relates to a vented laundry dryer, comprising an air inlet duct, an air outlet duct, a heat recovery system for transferring heat from the air outlet duct to the air inlet duct, and an additional heater, wherein the heat recovery system is a heat pump comprising an evaporator, a liquefier, a condenser, and a relaxation unit, wherein the liquefier is thermally coupled to the air inlet duct, and the evaporator is thermally coupled to the air outlet duct, and a relaxation property of the relaxation unit can be adjusted depending on at least one parameter that is connected to an activity of the additional heater. A method is used to operate a vented heat dryer comprising an additional heater and a heat pump having a relaxation unit, wherein the method comprises the following steps: (a) monitoring at least one parameter that is connected to an activity of the additional heater; and (b) changing a relaxation property of the relaxation unit depending on the at least one parameter.

Abstract: A dryer including a housing, a drying chamber disposed within the housing, and a heating element coupled to the housing. The dryer further includes an intake configured to supply intake air to the drying chamber and an exhaust vent configured to vent exhaust air out of the drying chamber. The intake, the drying chamber, and the exhaust vent define an air flow path from the intake through the drying chamber and out the exhaust vent. The dryer includes a heat exchanger and a heat pump having a condenser. The heat exchanger and the heat pump are each configured to absorb thermal energy from the exhaust air and transfer the thermal energy to the intake air. The air flow path is configured such that the intake air is heated directly or indirectly by the heat exchanger prior to the intake air being further heated directly or indirectly by the condenser.

Abstract: A dryer with a heat pump that includes a cabinet, a drum installed within the cabinet, and an exhaust duct configured to exhaust air from the drum to outside of the cabinet. The dryer also includes a fan configured to inhale air from the drum and pump the air to the exhaust duct, an evaporator configured to exchange heat with air being exhausted through the exhaust duct, and a condenser disposed at a rear side of the drum. The dryer further includes an intake passage member configured to guide air that has passed through the condenser into the drum and a compressor and an expansion apparatus configured to define a heat pump along the evaporator and condenser.

Abstract: A heat pump type dryer is provided that enhances supercooling performance using condensation water. The circulation type heat pump dryer may include a cabinet, a drum, a drying duct that circulates dry air, an evaporator, a condenser, a compressor and an expansion apparatus. The condenser may include a first condenser that liquefies a high-temperature, high-pressure refrigerant circulated from the compressor, and a second condenser that condenses the refrigerant condensed by the first condenser again. The second condenser may be formed below a condensation water level, the condensation water being accumulated at a lower portion of the drying duct, below the first condenser, to cool the second condenser using condensation water chilled by the evaporator.

Abstract: A laundry treating apparatus may include a drum that receives laundry item therein, a heat pump that circulates a heating medium, a compressor that compresses the heating medium, a condenser that heats air to be transmitted to the drum, an expander that expands the heating medium, and an evaporator that cools air transmitted from the drum. A heater may re-heat air heated by the heat pump, and a sensing device may sense a state, such as temperature, of the heating medium. A controller may calculate energy efficiency based on the sensed state of the heating medium. Energy related information including the calculated energy efficiency may be displayed on a display so that energy efficiency may be monitored real time.

Abstract: A composite washing system is disclosed which is capable of continuously circulating laundry-drying air through dryers while obtaining a more efficient drying effect, so that the composite washing system has a suitable built-in structure having minimal influence on the indoor environment.

Abstract: A boiler system includes an arrangement for drying fuel material to be combusted in the boiler system. A combustion chamber combusts fuel material, and generates ash and flue gases. An ash removal conduit connected to the combustion chamber leads ash out of the combustion chamber. A flue gas conduit connected to the combustion chamber leads Hue gases out of the combustion chamber. A flue gas heat recovery system, arranged to the flue gas conduit, recovers heat from the flue gases. A fuel dryer, provided with a first heat transfer device, transfers heat into the fuel to be dried. A second heat transfer device is arranged in connection with the flue gas conduit downstream of the flue gas heat recovery system. A third heat transfer device is arranged in connection with the ash removal conduit and a fourth heat transfer device is arranged in heat transfer connection with the fuel dryer.

Abstract: A heat pump laundry dryer has a casing (1) accommodating therein a heat pump system having a refrigerant fluid evaporating unit and a refrigerant fluid condensing unit for carrying out a drying treatment on laundry. The dryer further includes a basement (8) having a condensate draining path (21) for conveying moisture condensed from a drying air flow towards a reservoir (24). The condensing unit lays over a basement surface (14) which is provided with a condensate guide (26) for driving water condensed onto the condensing unit to the condensate draining path (21).

Abstract: A laundry dryer (1) includes a closed-circuit, hot-air generator (5). The hot-air generator (5) is provided with a heat-pump assembly (11). The heat-pump assembly (11) in turn includes an evaporator (13) and a condenser (14). Refrigerant vapor-quality adjusting means (17) is structured for adjusting, at the refrigerant-outlet of the evaporator (13), the ratio between the amount of refrigerant in gaseous state and the whole amount of refrigerant. Detecting means are able to measure the current value of at least one physical quantity of the laundry dryer (1). An auxiliary refrigerant/refrigerant heat exchanger (18) is crossed, at the same time, by the high-pressure refrigerant directed towards the refrigerant expansion device (16), and by the low-pressure refrigerant coming out of the refrigerant-outlet of the evaporator (13), and is structured for transferring heat from the high-pressure refrigerant to the low-pressure refrigerant so to heat up the low pressure refrigerant.

Abstract: A drying system includes a desiccant wheel that dries incoming air. The dried air is heated using a heating element to promote drying of an article within the drying system. A portion of the heated air is diverted to a secondary air path that leads away from the drum holding the article. The diverted portion is used to regenerate an area of the desiccant wheel. A secondary heating element is used to promote regeneration and located in the secondary air path.

Abstract: An apparatus (1) and method for drying polymer powders is described. The apparatus has an inlet (2) and an outlet (3) for the polymer powder, heat registers (5) installed in the interior space (4) and lines (7) for a heated gas (6a) for drying the polymer powder. The lines open into the interior space (4) and are connected to heat exchangers (9) for heating gas (6). The heat exchangers (9) are connected to a plant for the preparation of 1,2-dichloroethane (15) and/or for the preparation of vinyl chloride from 1,2-dichloroethane so that thermal energy from the plant can be utilized for heating the gas (6). The method comprises treatment of a polymer powder with a heated gas (6a) in the drying apparatus (1).

Abstract: In accordance with one aspect of an exemplary embodiment, a dryer for removing hydrocarbons and/or moisture from metal chips is provided. The dryer has a chamber including a top portion and a base portion. The top portion is comprised of a material having a higher emissivity than the material forming the base portion. A burner is provided which introduces heated gas into the top portion. A device for transporting the metal chips is provided in the base portion. The device receives the metal chips at an inlet and transporting the metal chips to an outlet.

Abstract: A laundry dryer is provided with a heat pump system. The heat pump system comprises a closed refrigerant circuit (10) for a refrigerant and a drying air circuit (12) for drying air. The refrigerant circuit (10) includes a compressor (14) and lamination means (18). The air stream circuit (12) includes a laundry drum (52) and at least one fan (52). The refrigerant circuit (10) and the air stream circuit (12) are thermally coupled by a first heat exchanger (16) for heating up the air stream and cooling down the refrigerant and a second heat exchanger for cooling down the air stream and heating up the refrigerant (20). The refrigerant circuit (10) comprises a low pressure side (24) between the outlet of the lamination means (18) and the inlet of the compressor (14). The refrigerant circuit (10) comprises a high pressure side (26) between the outlet of the compressor (14) and the inlet of the lamination means (18).

Abstract: A sludge drying system using steam extracted from a boiler unit. The sludge drying system includes a boiler flue, boiler feedwater pipes, an extraction system, a sludge drier, and a waste heat utilization device. A deaerator and an economizer are disposed on the boiler feedwater pipes. The economizer functions as a heating surface and is arranged in the boiler flue. A water outlet pipe of the deaerator is connected to a water inlet pipe of the economizer. The sludge drier is connected to the extraction system. The waste heat utilization device includes a heat absorption member and a heat release member which communicate with one another through circulating pipes. The heat absorption member functions as a final heat surface and is disposed in the boiler flue. The heat release member is disposed on a water inlet pipe of the deaerator.

Abstract: Heat pump dryer (1) comprising a process air circuit and a heat pump unit (5) having a primary refrigerant evaporator (6) for cooling process air (4) and a primary refrigerant condenser (7) for heating process air (4), further comprising either—an auxiliary refrigerant evaporator (16) connected between the primary refrigerant evaporator (6) and a compressor (8) of the heat pump unit (5) and an auxiliary refrigerant condenser (17) connected between the primary refrigerant condenser (7) and refrigerant expansion means (14), both arranged outside the process air circuit or—an auxiliary heat exchanger (27) arranged outside the process air circuit wherein the auxiliary heat exchanger (27) is a dual mode heat exchanger operable in refrigerant evaporator mode or in refrigerant condenser mode.

Abstract: Provided is cement burning apparatus 1 comprising a dryer 6 for drying high-water-content organic waste of which water content is 40 mass percent or more, in which combustion gas extracted from outlet portions or ceiling, portions of preheater cyclones 3A to 3D of a cement kiln 2 is fed to the dryer 6. As the dryer 6, a grinding-type flash dryer, which directly contacts the combustion gas G with the high-water-content organic waste W while grinding it, can be used. In addition, the apparatus 1 further comprises a coarse powder separator 12 for separating coarse powder from the combustion gas extracted from the range described above, and the combustion gas G from which dust is separated by the coarse powder separator 12 can be fed to the dryer 6, and the dust concentration of the gas fed to the dryer 6 may be adjusted to 0.05kg/Nm3 or more and 0.35kg/Nm3 or less.

Abstract: A non-contact sludge drying system with flue gas heat according to the present invention includes a dryer, and further includes an economizer, a high-temperature flue gas heat recovery device, and an air preheater that are successively disposed in the flue along a flue gas flowing direction. A heater is disposed in the dryer, the high-temperature flue gas heat recovery device is connected to the heater by a circulation pipe, a heat transfer medium is disposed in the circulation pipe, a heat transfer medium driving device is disposed on the circulation pipe, and the dryer is connected to a sludge vapor recovery system. The non-contact sludge drying system with flue gas heat according to the present invention uses the flue gas heat from a thermal power plant boiler or another industrial boiler as a heat source to further dehydrate and dry the dehydrated sludge of the sewage treatment plant, so that the dried sludge can be used as a fuel with certain heat of combustion or composted for further treatment.

Abstract: A clothes dryer is provided. The clothes dryer may include a main body having a drum rotatably installed therein, a circulation channel formed in the main body, the circulation channel defining a path of air that flows through the drum to dry an object to be dried, and a heat pump system having an evaporator, a compressor, an expansion apparatus, and a condenser, the heat pump system cooling and heating air that flows through the circulation channel. The evaporator may be mounted in the circulation channel, and a ‘U’ trap may be positioned below the evaporator in the circulation channel.

Abstract: The recirculating dryer includes a housing having an operator control panel and a locking door mounted to a side of the housing. A rotating tumbler for holding the laundry to be dried is mounted inside the housing. Heated air is introduced through an inlet of the tumbler, and the outlet is kept closed by a flap. The heated air is recirculated and recycled through the tumbler. The air is reheated back to a predetermined temperature if the temperature falls below a level suitable for drying. A layer of moisture-absorbent material surrounds the tumbler to absorb the moisture gathered in the air from the drying process. At drying completion, the flap is opened to vent the used air. A control system controls various features with data from a thermostat and a moisture detector.

Abstract: A drying apparatus is disclosed that includes a drum and an open-loop airflow pathway originating at an ambient air inlet, passing through the drum, and terminating at an exhaust outlet. A passive heat exchanger is included for passively transferring heat from air flowing from the drum toward the exhaust outlet to air flowing from the ambient air inlet toward the drum. A heat pump is also included for actively transferring heat from air flowing from the passive heat exchanger toward the exhaust outlet to air flowing from the passive heat exchanger toward the drum. A heating element is also included for further heating air flowing from the heat pump toward the drum.

Abstract: A method for providing fresh air fed through a fan to a burner of a dryer, thereby charging the burner, when the dryer is operated with recirculating air. In commercial dryers in which the drying air is heated by a burner, it is customary to reuse the moist air leaving a drum containing the laundry to be dried as recirculating air. The recirculating air component is increased with increasing drying of the laundry. At the end of the drying operation, when the moist air no longer contains as much moisture as at the start, the moist air is used as recirculating air. The burner then no longer gets enough combustion air, which leads to an incomplete combustion. The dryer can be operated with a higher recirculating air component, an optimal combustion being guaranteed through the charging of the burner with fresh air. The invention permits more economical drying.

Abstract: The present invention relates to an improved method for using heat energy in a gypsum board plant. More specifically, the method contemplates taking heat from a gasifier, or other alternative heat source, and using it to dry gypsum boards. In order to control humidity levels, this heat is delivered to one or more board dryers via a heat exchanger.

Abstract: A condensing type dryer uses a heat exchanger in which condensed water can be smoothly discharged through a water-discharging slot formed in a rear end portion of a rear cover of the heat exchanger. The water-discharging slot prevents an air flowing resistance which can be caused by condensed water pooling at the rear end portion of the rear cover. Also, leakage-preventing walls enhance the heat exchanging function by ensuring a uniform flow of cold external air through the heat changer. The leakage-preventing walls prevent external air from leaking around the lateral edges of the heat exchanger.