An apparatus for controlling the temperature of workpieces, in particular of vehicle bodies, has a temperature-control tunnel, a traction chamber and an intermediate floor which is arranged between the temperature-control tunnel and the traction chamber and which has a connection passage. The apparatus includes a conveying device for conveying the workpieces in the temperature-control tunnel, wherein the conveying device has at least one conveying carriage with a running gear and has a workpiece carrier for holding the workpieces of which the temperature is to be controlled. The running gear is arranged in the traction chamber and is connected by a connecting device, which projects through the connection passage of the intermediate floor, to the workpiece carrier arranged in the temperature-control tunnel. To control the temperature of the traction chamber and thus adequately protect the running gear against heat or cold, the intermediate floor is equipped at least in regions with an active cooling and/or heating means.

A seed flow chamber for handling seed and grain commodity, especially for use with a seed treatment applicator. Seed flow is received through an upper inlet opening configured to receive a flow of seed and discharged through a lower discharge opening. A diverging guide member splits the seed flow. A converging guide member disposed below the diverging guide member reunites the seed flow prior to discharge. The converging member has a downward sloping surface and an air vent, such as a plurality of airflow apertures connected to a plenum. The air vent is configured to communicate with an air supply. A vacuum ventdisposed below the diverging guide memberis configured to communicate with a vacuum source. A fan system recirculates air between the air vent and the vacuum vent. Dehumidifier may condition the air supply to assist with drying.

A seed flow chamber for handling seed and grain commodity, especially for use with a seed treatment applicator. Seed flow is received through an upper inlet opening configured to receive a flow of seed and discharged through a lower discharge opening. A diverging guide member splits the seed flow. A converging guide member disposed below the diverging guide member reunites the seed flow prior to discharge. The converging member has a downward sloping surface and an air vent, such as a plurality of airflow apertures connected to a plenum. The air vent is configured to communicate with an air supply. A vacuum ventdisposed below the diverging guide memberis configured to communicate with a vacuum source. A fan system recirculates air between the air vent and the vacuum vent. Dehumidifier may condition the air supply to assist with drying.

A locker cabinet is positioned over and supported by a plenum which contains a blower for forcing air upwards through apertures in the floor of the locker for rapidly drying wetted apparel stored in the locker. Tubes disposed over the apertures serve to support apparel items such as boots, gloves, and helmets. Louvered vents provided in the locker door near the top enable moistened air to discharge outside the locker. A well is provided in the floor to facilitate storage of items such as skis.

The present invention discloses low cost, on-site, efficient, and compact (stationary or mobile) system for continuous (non-batch operation) conversion of waste to usable products such as sources of energy, fertilizer, etc.

My desiccator comprises a plurality of chambers in series communication with each other so a desiccating gas flows from one chamber into an adjacent chamber. A desiccating purge gas is introduced through an inlet into the desiccator's chambers at a predetermined flow rate, and a one-way bleed valve allows gas within the chambers to constantly flow from the desiccator while maintaining a positive pressure within the desiccator. A fan that constantly mixes and circulates the gas between the chambers as the desiccating purge gas is introduced into the desiccator, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. My method employs my desiccator to store items, wherein a dry, pressurized desiccating gas is introduced into the desiccator's chambers in a manner that constantly circulates the gas between the chambers as gas is slowly bled from the chambers, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. In my method the dew point of the desiccating gas is from 20 to 90 F. , the pressure of the desiccating gas is from 30 to 120 psi, and the average flow rate of the desiccating gas into the desiccator is from 0.25 to 4.0 cubic feet per minute.

My desiccator comprises a plurality of chambers in series communication with each other so a desiccating gas flows from one chamber into an adjacent chamber. A desiccating purge gas is introduced through an inlet into the desiccator's chambers at a predetermined flow rate, and a one-way bleed valve allows gas within the chambers to constantly flow from the desiccator while maintaining a positive pressure within the desiccator. A fan that constantly mixes and circulates the gas between the chambers as the desiccating purge gas is introduced into the desiccator, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. My method employs my desiccator to store items, wherein a dry, pressurized desiccating gas is introduced into the desiccator's chambers in a manner that constantly circulates the gas between the chambers as gas is slowly bled from the chambers, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. In my method the dew point of the desiccating gas is from 20 to 90 F. , the pressure of the desiccating gas is from 30 to 120 psi, and the average flow rate of the desiccating gas into the desiccator is from 0.25 to 4.0 cubic feet per minute.

My desiccator comprises a plurality of chambers in series communication with each other so a desiccating gas flows from one chamber into an adjacent chamber. A desiccating purge gas is introduced through an inlet into the desiccator's chambers at a predetermined flow rate, and a one-way bleed valve allows gas within the chambers to constantly flow from the desiccator while maintaining a positive pressure within the desiccator. A fan that constantly mixes and circulates the gas between the chambers as the desiccating purge gas is introduced into the desiccator, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. My method employs my desiccator to store items, wherein a dry, pressurized desiccating gas is introduced into the desiccator's chambers in a manner that constantly circulates the gas between the chambers as gas is slowly bled from the chambers, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. In my method the dew point of the desiccating gas is from 20 to 90 F, the pressure of the desiccating gas is from 30 to 120 psi, and the average flow rate of the desiccating gas into the desiccator is from 0.25 to 4.0 cubic feet per minute.

My desiccator comprises a plurality of chambers in series communication with each other so a desiccating gas flows from one chamber into an adjacent chamber. A desiccating purge gas is introduced through an inlet into the desiccator's chambers at a predetermined flow rate, and a one-way bleed valve allows gas within the chambers to constantly flow from the desiccator while maintaining a positive pressure within the desiccator. A fan that constantly mixes and circulates the gas between the chambers as the desiccating purge gas is introduced into the desiccator, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. My method employs my desiccator to store items, wherein a dry, pressurized desiccating gas is introduced into the desiccator's chambers in a manner that constantly circulates the gas between the chambers as gas is slowly bled from the chambers, constantly diluting the gas within the chambers with a fresh supply of the desiccating gas. In my method the dew point of the desiccating gas is from 20 to 90 F, the pressure of the desiccating gas is from 30 to 120 psi, and the average flow rate of the desiccating gas into the desiccator is from 0.25 to 4.0 cubic feet per minute.

A dual path kiln is provided that includes a kiln having at least three chambers including first and second end chambers separated by a central heating chamber. At least two lumber conveyors convey lumber through the kiln in opposite directions. External unidirectional fans are utilized to provide circular directional flows through the lumber. Also provided is a method utilizing the kiln to continuously dry green lumber.