Abstract:
The present invention refers to a process and installation for cooling combustion air of gas turbines, in which the humidity contents of the air is first reduced in a dehumidifier (7, 7') by means of a first external fluid (4), or the discharge gases of the turbine, then the air is cooled in a cooler (11, 11') by means of a second external fluid (12), reaching approximately the same initial dry bulb temperature and followed by cooling, after at least one dehumidification stage, the air being then rehumidified. in a saturator (13).
Abstract:
A rotary heat regenerator wheel in which one or more performance characteristics, such as heat exchange efficiency and air flow rate, can be adjusted during manufacturing, during or after installation and/or after use of the regenerator. The wheel comprises removable segments having differing performance characteristics. One embodiment of the regenerator wheel includes segments containing both latent and sensible heat exchange material. Latent heat transfer efficiencies between those provided by heat regenerators having segments made only of sensible heat exchange material, and by regenerators having segments made only of latent heat exchange material, are achieved by adjusting the ratio of segments with exposed surface area of latent heat exchange material relative to segments having exposed surface area of the sensible heat exchange material. In another embodiment the air flow, pressure drop or surface area density of the wheel can be adjusted by using segments having different surface area densities.
Abstract:
An integrated air conditioning and hot water supply system for conditioning air and supplying hot water to a building is described. The system incorporates a hot water tank in the system which feeds a heat exchanger to heat air which is recirculated from the building when required during cool weather periods. A combined air dehumidification device and cooling device are also provided to dehumidify and cool return air from the building in a recirculation circuit when required by the building during warm weather periods. The cooling devices incorporate coils connected to the city water supply whereby to preheat a supply of water to the hot water tank. The combined circuit also cools fresh air and treats it to provide a source of heated air to regenerate a desiccant wheel which is used as the dehumidification device. A heat recovery ventilator is also incorporated in the integrated system to treat exhaust air from the building during cool weather periods and to admit warmed fresh air thereto.
Abstract:
In an adsorbing body for humidity and odorous gas exchange such as an adsorbing sheet for dehumidification, an adsorbing element for dehumidification or an adsorbing element for total heat energy exchange, a sheet or a honeycomb laminate is impregnated or coated with silica sol containing, as solid content, not more than 30% of the silica sol weight of minute silica particles not larger than 120 .ANG. in diameter which contain many stable silanol radicals on the surface and 0.01-1% of alkali metal ion Na.sub.2 O. It is then dried to rigidly fix silica gel. Other humidity adsorbing or absorbing agents such as zeolite, organic high-polymer electrolyte, etc. may be mixed in said silica sol. Silica gel with excellent humidity adsorbing ability can be strongly adhered to a sheet or a honeycomb laminate in an extremely simple method.
Abstract:
A method of conditioning a process stream of air in an air conditioning system wherein a process stream of air is dehumidified and cooled to provide a conditioned stream of air for introducing to a conditioned space. The method comprises the steps of providing an adsorption wheel having a multiplicity of passages through which process air can flow for adsorbing moisture therefrom, the wheel capable of adsorption of moisture from the process air and of regeneration on a continuous basis as the wheel rotates. An indirect evaporative cooler is provided having a dry side and a wet side separated by a moisture-impervious wall wherein heat is extracted from said dry side through the wall to the wet side. Cooling in the dry side is achieved by evaporation of water into air passing through the wet side. The process air is passed through the adsorption wheel to remove moisture therefrom to provide a moisture-depleted stream of process air exiting the adsorption wheel. The adsorption wheel is regenerated by passing hot gases therethrough to remove moisture from the adsorption wheel. The moisture-depleted stream of process air exiting said adsorption wheel is divided into a relatively hot stream and a relatively cool stream, and the relatively hot stream of process air is introduced into the wet side of the indirect evaporative cooler, and the relatively cool stream is introduced into the dry side, the relatively hot stream evaporating water thereinto thereby cooling the moisture-impervious wall and removing heat from the relatively cool stream to provide cooled air to be introduced to a conditioned space.
Abstract:
An active silica gel honeycomb adsorbing body capable of adsorbing humidity and odorous components in a process air having 100% relative humidity. A single-faced corrugated sheet having a wave length of approximately 2.5-6.5 mm and a wave height of approximately 1.3-4.0 mm, a quantity of active silica gel approximately 0.5-3.0 times the weight of inorganic fiber papers and a thickness of approximately 0.1-0.3 mm is laminated to form a honeycomb structure laminated body. The honeycomb structure laminated body is impregnated with an aqueous water glass solution, and is then impregnated with acid and dried to form active silica gel having micropores and mesopores. The micropores and the mesopores have a diameter distributed in the range of not more than 200 .ANG. and a surface area of approximately 300-600 m.sup.2 /g. The active silica gel is adhered in fiber gaps and on the surface of the inorganic fiber paper.
Abstract:
A resistor, such as a resistor wire, is contained in a sheet, preferably a low density sheet consisting mainly of inorganic fiber. Adsorbent or absorbent (hereinafter "sorbent" collectively) is fixed to the sheet to obtain sorbing characteristics, such that desorption and reactivation can be accomplished by applying an electric current to the resistor to heat the sheet. A sorbing laminate with many channels may be used by laminating the sorbing sheets. The sorbing sheet can therefore be heated directly from the inner side by the resistor contained in the sheet desorbing the sheets rapidly while the time for reactivating the sorbing sheet is reduced and the reactivation efficiency increased.
Abstract:
A method of conditioning a process stream of air in an air conditioning system wherein a process stream of air is dehumidified and cooled to provide a conditioned stream of air for introducing to a conditioned space, the method comprises the steps of providing an enthalpy wheel comprised of an adsorbent contained in a paper web, the enthalpy wheel having a multiplicity of passages through which the process air can flow, the enthalpy wheel capable of regeneration by passing an air stream therethrough having a temperature and humidity lower than the process air. In the method, process air is passed through the enthalpy wheel to remove heat and moisture therefrom, and the enthalpy wheel is regenerated by passing air therethrough to remove heat and moisture therefrom. Thereafter, the method includes providing an adsorption wheel having a multiplicity of passages through which the process air from the enthalpy wheel can flow for adsorbing moisture, the wheel capable of adsorption of moisture from the process air and of regeneration. Process air from the enthalpy wheel is passed through the adsorption wheel to remove moisture, and the adsorption wheel is regenerated by passing hot gases therethrough to remove moisture. After passing through the adsorption wheel, process air is introduced to an indirect evaporative cooler having a dry channel and a wet channel separated by a moisture-impervious wall wherein heat is extracted from the dry channel through the wall to the wet channel, the process air from the adsorption wheel being introduced to the dry channel to provide cooled process air exiting the indirect evaporative cooler to provide a cooled stream of air having a controlled level of humidity. Air is directed to the wet channel of the indirect evaporative cooler, the air directed to the wet channel being selected from at least one of outside air, air returned from the conditioned space, a portion of the air from the enthalpy wheel, and a portion of the cooled air exiting the dry side of the indirect evaporative cooler.
Abstract:
A hybrid air-conditioning system for controlling the condition of air in a building enclosed space. The hybrid air-conditioning system includes a rotatable moisture transfer wheel having first and second zones. The first zone is located in a process air flow and the second zone is located in a regenerative air flow. The second zone of the moisture transfer wheel has relatively wet and dry regions. A compressor having a suction side and a discharge side is provided. The suction side of the compressor is in fluid communication with a recovery evaporator coil, and the discharge side of the compressor is in fluid communication with a subcool condenser coil. The recovery evaporator coil is positioned such that the regenerative air flow through the dry region of the second zone of the moisture transfer wheel passes through the recovery evaporator coil. The subcool condenser coil is positioned such that the regenerative air flow through the wet region of the second zone of the moisture transfer wheel passes through the subcool condenser coil.
Abstract:
A vapor extraction apparatus includes a gel sorbent capable of absorbing vapor directly into the liquid state and capable of disgorging the absorbed liquid in a phase-transition. The apparatus includes a housing adapted for movement from a first position, where it is exposed to a vapor-containing gas stream and a first environmental condition, and capable of moving to a second position, where it is exposed to a second environmental condition. A gel sorbent is disposed on at least one surface of the housing. The gel sorbs vapor from the gas stream as liquid when the sorbent is in its first position. The sorbent disgorges the liquid during phase-transition collapse when it is in the second position. A method of extracting vapor from a process gas stream includes contacting a phase transition gel sorbent with vapor under conditions sufficient for the gel sorbent to undergo a phase transition and absorb vapor as liquid inside the gel sorbent. The gel sorbent is then exposed to conditions sufficient for it to undergo a phase transition and disgorge the liquid from inside the gel sorbent. The disgorged liquid is removed from the gel sorbent.