Disclosed is a flash closed heat exchanger, comprising a closed housing. A negative pressure fan is provided on the closed housing. A negative pressure environment is formed inside the closed housing by means of the negative pressure fan. A water atomization device is provided inside the closed housing. The water atomization device sprays atomized water into the inside of the closed housing, so that the atomized water evaporates into steam in the negative pressure environment. In the flash closed heat exchanger of the present invention, the evaporation of atomized water is promoted in a closed negative pressure environment, so that the overall temperature in the closed environment is reduced to achieve a refrigeration effect, without being affected by the temperature and humidity of the natural wind outside; the installed capacity of the equipment is small, and the space occupied is small; no heat is discharged into the atmosphere during a refrigeration process, no heat island effect is achieved, the refrigeration efficiency is high, and the effect is stable and reliable.

A multiple mode hybrid heat exchanger apparatus includes a frame assembly, an indirect heat exchange section, a spray system, an intermediate distribution basin, a direct heat exchange section, a vertical passage, a lower air inlet, a cold water collection basin, and a fan. The frame assembly includes a first end wall, a second end wall that opposes the first end wall, a first side wall that extends between the first and second end walls, and a second side wall that opposes the first side wall that extends between the first and second end walls. The direct heat exchange section is disposed below the indirect heat exchange section. The vertical passage is defined by the frame and the direct heat exchange section. The lower air inlet is defined by a plurality of openings n the direct heat exchange section. The lower air inlet is configured to provide an inlet for air into the vertical passage, The cold water collection basin is disposed below the direct heat exchange section. The fan is to induce a flow of air through the lower air inlet. The multiple mode hybrid heat exchanger is selectably configured to operate in an evaporative mode, a dry mode, and an adiabatic mode. The evaporative mode of operation includes activation of the spray system over the indirect heat exchange section, air enters the vertical passage through the direct heat exchange section, and the airflow also passes through the indirect heat exchange section. The dry mode of operation includes deactivation of the spray system, air enters the vertical passage through the direct heat exchange section, and the airflow then passes through the indirect heat exchange section. The adiabatic mode of operation includes the spray system is bypassed on the indirect heat exchange section, the direct heat exchange section is configured to facilitate a passage of water therethrough. The air enters the vertical passage through the direct heat exchange section, the air passing horizontally across a flow of water to directly cool the water. The water is collected in the cold water collection basin. The airflow then passes through the indirect heat exchange section.

A multiple mode hybrid heat exchanger apparatus includes a frame assembly, an indirect heat exchange section, a spray system, an intermediate distribution basin, a direct heat exchange section, a vertical passage, a lower air inlet, a cold water collection basin, and a fan. The frame assembly includes a first end wall, a second end wall that opposes the first end wall, a first side wall that extends between the first and second end walls, and a second side wall that opposes the first side wall that extends between the first and second end walls. The direct heat exchange section is disposed below the indirect heat exchange section. The vertical passage is defined by the frame and the direct heat exchange section. The lower air inlet is defined by a plurality of openings n the direct heat exchange section. The lower air inlet is configured to provide an inlet for air into the vertical passage, The cold water collection basin is disposed below the direct heat exchange section. The fan is to induce a flow of air through the lower air inlet. The multiple mode hybrid heat exchanger is selectably configured to operate in an evaporative mode, a dry mode, and an adiabatic mode. The evaporative mode of operation includes activation of the spray system over the indirect heat exchange section, air enters the vertical passage through the direct heat exchange section, and the airflow also passes through the indirect heat exchange section. The dry mode of operation includes deactivation of the spray system, air enters the vertical passage through the direct heat exchange section, and the airflow then passes through the indirect heat exchange section. The adiabatic mode of operation includes the spray system is bypassed on the indirect heat exchange section, the direct heat exchange section is configured to facilitate a passage of water therethrough. The air enters the vertical passage through the direct heat exchange section, the air passing horizontally across a flow of water to directly cool the water. The water is collected in the cold water collection basin. The airflow then passes through the indirect heat exchange section.

A process and a device are described for producing high purity and high temperature steam from non-pure water which may be used in a variety of industrial processes that involve high temperature heat applications. The process and device may be used with technologies that generate steam using a variety of heat sources, such as, for example industrial furnaces, petrochemical plants, and emissions from incinerators. Of particular interest is the application in a thermochemical hydrogen production cycle such as the Cu—Cl Cycle. Non-pure water is used as the feedstock in the thermochemical hydrogen production cycle, with no need to adopt additional and conventional water pre-treatment and purification processes. The non-pure water may be selected from brackish water, saline water, seawater, used water, effluent treated water, tailings water, and other forms of water that is generally believed to be unusable as a direct feedstock of industrial processes. The direct usage of this water can significantly reduce water supply costs.

A process and a device are described for producing high purity and high temperature steam from non-pure water which may be used in a variety of industrial processes that involve high temperature heat applications. The process and device may be used with technologies that generate steam using a variety of heat sources, such as, for example industrial furnaces, petrochemical plants, and emissions from incinerators. Of particular interest is the application in a thermochemical hydrogen production cycle such as the Cu—Cl Cycle. Non-pure water is used as the feedstock in the thermochemical hydrogen production cycle, with no need to adopt additional and conventional water pre-treatment and purification processes. The non-pure water may be selected from brackish water, saline water, seawater, used water, effluent treated water, tailings water, and other forms of water that is generally believed to be unusable as a direct feedstock of industrial processes. The direct usage of this water can significantly reduce water supply costs.

A liquid cooled thermal heat sink is provided. A plurality of jet orifices provide an exit for pressurised liquid to exit a plenum chamber and impinge on a thermal surface whereby they effect a cooling of the thermal surface, the heated liquid being transferred through an exit channel to dissipate heat away from the thermal surface.

A liquid cooled thermal heat sink is provided. A plurality of jet orifices provide an exit for pressurised liquid to exit a plenum chamber and impinge on a thermal surface whereby they effect a cooling of the thermal surface, the heated liquid being transferred through an exit channel to dissipate heat away from the thermal surface.

A hybrid heat exchanger apparatus having a heat exchanger device with a hot fluid flowing therethrough includes a cooling water distribution system and an air flow mechanism for causing ambient air to flow across the heat exchanger device. The cooling water distribution system distributes evaporative cooling water onto the heat exchanger device to wet only a portion of the heat exchanger device while allowing a remaining portion of the heat exchanger device to be dry. The air flow mechanism causes ambient air to flow across the heat exchanger device to generate hot humid air from the ambient air flowing across the wet portion of the heat exchanger device and hot dry air from the ambient air flowing across the remaining dry portion of the heat exchanger device. Methods are also described.

A hybrid heat exchanger apparatus having a heat exchanger device with a hot fluid flowing therethrough includes a cooling water distribution system and an air flow mechanism for causing ambient air to flow across the heat exchanger device. The cooling water distribution system distributes evaporative cooling water onto the heat exchanger device to wet only a portion of the heat exchanger device while allowing a remaining portion of the heat exchanger device to be dry. The air flow mechanism causes ambient air to flow across the heat exchanger device to generate hot humid air from the ambient air flowing across the wet portion of the heat exchanger device and hot dry air from the ambient air flowing across the remaining dry portion of the heat exchanger device. Methods are also described.

Embodiments are disclosed to help create longitudinal refrigerant streams, for example, in a shell and tube type evaporator, so as to manage refrigerant and/or lubricant in the evaporator. In some embodiments, the shell side of the evaporator may include a plurality of longitudinally extended pans stacked in a vertical direction. In some embodiments, refrigerant can be directed onto a top pan. The refrigerant can form a longitudinal refrigerant stream along the pan and flow down to the next pan in the vertical direction and form another longitudinal refrigerant stream. Each of the pans may form a refrigerant pool to help exchange heat with a process fluid carried in heat exchanger tubes. By forming longitudinal refrigerant streams in the pans, heat exchange efficiency may be improved and a lubricant content in refrigerant streams may be concentrated toward a bottom of the evaporator.