A method and apparatus for the continuous sublimation of a substance includes cascading a material containing a substance capable of sublimation, such as water, between a plurality of trays vertically stacked within a processing zone provided within a processing chamber. A substantially atmospheric environment is maintained within the processing zone at a temperature whereby the substance sublimes forming a sublimate within the environment. The environment containing the sublimate is contacted with a drying agent such as a desiccant to maintain the environment whereby the substance sublimes at substantially atmospheric pressure and at the controlled temperature.

A method and apparatus for the continuous sublimation of a substance includes cascading a material containing a substance capable of sublimation, such as water, between a plurality of trays vertically stacked within a processing zone provided within a processing chamber. A substantially atmospheric environment is maintained within the processing zone at a temperature whereby the substance sublimes forming a sublimate within the environment. The environment containing the sublimate is contacted with a drying agent such as a desiccant to maintain the environment whereby the substance sublimes at substantially atmospheric pressure and at the controlled temperature.

An upper surface of a substrate is supplied with a pre-drying processing liquid which is a solution of a sublimable substance and a solvent. Thereafter, the solvent is evaporated from the pre-drying processing liquid on the substrate and a solid of the sublimable substance is precipitated in the pre-drying processing liquid on the substrate. Thereafter, at least a portion of the solid of the sublimable substance is dissolved in the pre-drying processing liquid on the substrate. Thereafter, the solvent is evaporated from the pre-drying processing liquid in which the solid of the sublimable substance has been dissolved and the solid of the sublimable substance is precipitated onto the substrate. Thereafter, the solid of the sublimable substance is sublimated and removed from the upper surface of the substrate.

A solid-liquid separation device performs dehydration or deoiling from a treated object using a substance A that is a gas at normal temperature and pressure and is capable of dissolving water and oil when liquefied. The separation device includes a substance B that circulates while generating phase change in a closed system, a compressor that compresses the substance B, a first heat exchanger that condenses substance B and evaporates of the substance A, an expansion valve that decompresses the condensed substance B, a second heat exchanger that evaporates substance B and condenses substance A, and a treatment tank wherein substance A is mixed with the treated object, substance A is evaporated while separated from the liquid in the first heat exchanger, and condensed in the second heat exchanger. The center of gravity of the first heat exchanger is lower than the second heat exchanger in a vertical direction.

A solid-liquid separation device performs dehydration or deoiling from a treated object using a substance A that is a gas at normal temperature and pressure and is capable of dissolving water and oil when liquefied. The separation device includes a substance B that circulates while generating phase change in a closed system, a compressor that compresses the substance B, a first heat exchanger that condenses substance B and evaporates of the substance A, an expansion valve that decompresses the condensed substance B, a second heat exchanger that evaporates substance B and condenses substance A, and a treatment tank wherein substance A is mixed with the treated object, substance A is evaporated while separated from the liquid in the first heat exchanger, and condensed in the second heat exchanger. The center of gravity of the first heat exchanger is lower than the second heat exchanger in a vertical direction.

A drying apparatus promotes drying of a wet item while protecting a surrounding environment from moisture escaping the wet item as it dries. The apparatus includes a waterproof casing comprising one or more waterproof materials and constructed (a) to receive a wet item and (b) prevent the moisture in the wet item from contacting items in the surrounding environment. The waterproof casing also includes a drain structure at one end having an opening through which moisture from the wet item escapes the drying apparatus and one or more rigid structures extending from within the waterproof casing through the opening to create a pathway for the escaping moisture. The drying apparatus also has an intake vent positioned to draw air into the drying apparatus and direct the air over the wet item within the apparatus and through the opening in the drain structure.

A drying apparatus promotes drying of a wet item while protecting a surrounding environment from moisture escaping the wet item as it dries. The apparatus includes a waterproof casing comprising one or more waterproof materials and constructed (a) to receive a wet item and (b) prevent the moisture in the wet item from contacting items in the surrounding environment. The waterproof casing also includes a drain structure at one end having an opening through which moisture from the wet item escapes the drying apparatus and one or more rigid structures extending from within the waterproof casing through the opening to create a pathway for the escaping moisture. The drying apparatus also has an intake vent positioned to draw air into the drying apparatus and direct the air over the wet item within the apparatus and through the opening in the drain structure.

A drainage system for drying frac sand without heat comprises multiple layers through which liquid passes to dewater sand resting on the drainage system. At the bottom of the drainage system, perforated collection pipes, at least partially surrounded by rocks, collect the liquid and carry it to a collection pond for reuse. A cellular confinement layer comprises sections of panels which, upon expansion, have cells filled with rocks. A woven monofilament geotextile fabric layer comprising woven monofilament geotextile fabric sheets sewn together has sized openings which allow fluid, but prevent sand from passing through the openings. The top layer comprises perforated sheets of high density polyethylene welded together. A watertight liner sits below the perforated collection pipes and below the cellular confinement layer. Protective layers above and below the watertight liner prevent rocks from damaging the watertight liner.

A drainage system for drying frac sand without heat comprises multiple layers through which liquid passes to dewater sand resting on the drainage system. At the bottom of the drainage system, perforated collection pipes, at least partially surrounded by rocks, collect the liquid and carry it to a collection pond for reuse. A cellular confinement layer comprises sections of panels which, upon expansion, have cells filled with rocks. A woven monofilament geotextile fabric layer comprising woven monofilament geotextile fabric sheets sewn together has sized openings which allow fluid, but prevent sand from passing through the openings. The top layer comprises perforated sheets of high density polyethylene welded together. A watertight liner sits below the perforated collection pipes and below the cellular confinement layer. Protective layers above and below the watertight liner prevent rocks from damaging the watertight liner.

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.