A multi-pass contact tray for use in a mass transfer column has a mixture of fixed valves to movable valves, with the numbers of the respective valves being selected to balance the volumetric flow of vapor through deck segments when the vapor is ascending at volumetric flow rates insufficient to maintain the movable valves in an open position.

The present disclosure discloses a multi-bubbling region column tray and a corresponding plate column. The multi-bubbling region column tray includes: at least two bubbling regions, provided with first openings for liquid and gas to be mixed and in contact with each other; and at least one non-side downcomer, including at least one hanging downcomer, where the hanging downcomer has a bottom part which includes one or more second openings allowing the liquid to flow toward a lower left side, and one or more third openings allowing the liquid to flow toward a lower right side; and the bottom part of the hanging downcomer is designed to separate the liquid flowing out from the one or more second openings and the liquid flowing out from the one or more third openings.

The present disclosure discloses a multi-bubbling region column tray and a corresponding plate column. The multi-bubbling region column tray includes: at least two bubbling regions, provided with first openings for liquid and gas to be mixed and in contact with each other; and at least one non-side downcomer, including at least one hanging downcomer, where the hanging downcomer has a bottom part which includes one or more second openings allowing the liquid to flow toward a lower left side, and one or more third openings allowing the liquid to flow toward a lower right side; and the bottom part of the hanging downcomer is designed to separate the liquid flowing out from the one or more second openings and the liquid flowing out from the one or more third openings.

A method for condensing a vapor uses a multi-stage bubble-column vapor mixture condenser that includes at least a first stage, a second stage, and a third stage, each with a carrier-gas inlet and outlet as well as a condensing bath and a volume of carrier gas above the condensing bath. The carrier-gas inlet of the second and third stages is in the form of a sieve plate. The first-stage condensing bath is at a temperature of 60 C. to 90 C. Carrier gas flows at a temperature above 60 C. and up to 93 C. into and through the carrier-gas inlet of the first stage, then into and through the condensing bath in the first stage, and then into and through the volume of carrier gas above the condensing bath in the first stage. The carrier gas then similarly flows through the second- and third-stage condensing baths, each of which is at least 5 C. cooler than the temperature of the condensing bath in the preceding stage. Additional carrier gas is injected through an intermediate-exchange inlet into the volume of carrier gas above the condensing bath in at least one of the first and second stages to control the heat and mass profile of the carrier gas flowing through the stages of the multi-stage bubble-column vapor mixture condenser and to thereby maintain the temperature differentials between the condensing baths in the first, second, and third stages.

A method for condensing a vapor uses a multi-stage bubble-column vapor mixture condenser that includes at least a first stage, a second stage, and a third stage, each with a carrier-gas inlet and outlet as well as a condensing bath and a volume of carrier gas above the condensing bath. The carrier-gas inlet of the second and third stages is in the form of a sieve plate. The first-stage condensing bath is at a temperature of 60 C. to 90 C. Carrier gas flows at a temperature above 60 C. and up to 93 C. into and through the carrier-gas inlet of the first stage, then into and through the condensing bath in the first stage, and then into and through the volume of carrier gas above the condensing bath in the first stage. The carrier gas then similarly flows through the second- and third-stage condensing baths, each of which is at least 5 C. cooler than the temperature of the condensing bath in the preceding stage. Additional carrier gas is injected through an intermediate-exchange inlet into the volume of carrier gas above the condensing bath in at least one of the first and second stages to control the heat and mass profile of the carrier gas flowing through the stages of the multi-stage bubble-column vapor mixture condenser and to thereby maintain the temperature differentials between the condensing baths in the first, second, and third stages.

The present disclosure relates to a humidification-dehumidification desalination system. A humidification subsystem of the humidification-dehumidification desalination system includes a thermal element and a bubble column, in series. The thermal element further comprises a thermal energy storage unit including a phase change material and a thermal conductor. The thermal element can be supplemented by a Fresnel lens canopy. The thermal element and the bubble column of the humidification design are arranged in staircase design such that gravity drives the system.

The present disclosure relates to a humidification-dehumidification desalination system. A humidification subsystem of the humidification-dehumidification desalination system includes a thermal element and a bubble column, in series. The thermal element further comprises a thermal energy storage unit including a phase change material and a thermal conductor. The thermal element can be supplemented by a Fresnel lens canopy. The thermal element and the bubble column of the humidification design are arranged in staircase design such that gravity drives the system.

The present disclosure relates to a humidification-dehumidification desalination system. A humidification subsystem of the humidification-dehumidification desalination system includes a thermal element and a bubble column, in series. The thermal element further comprises a thermal energy storage unit including a phase change material and a thermal conductor. The thermal element can be supplemented by a Fresnel lens canopy. The thermal element and the bubble column of the humidification design are arranged in staircase design such that gravity drives the system.

The present disclosure relates to a humidification-dehumidification desalination system. A humidification subsystem of the humidification-dehumidification desalination system includes a thermal element and a bubble column, in series. The thermal element further comprises a thermal energy storage unit including a phase change material and a thermal conductor. The thermal element can be supplemented by a Fresnel lens canopy. The thermal element and the bubble column of the humidification design are arranged in staircase design such that gravity drives the system.

The present disclosure relates to a humidification-dehumidification desalination system. A humidification subsystem of the humidification-dehumidification desalination system includes a thermal element and a bubble column, in series. The thermal element further comprises a thermal energy storage unit including a phase change material and a thermal conductor. The thermal element can be supplemented by a Fresnel lens canopy. The thermal element and the bubble column of the humidification design are arranged in staircase design such that gravity drives the system.