Abstract:
A purge system for removing contamination from a chiller system includes a purge chamber including a degassing membrane, the degassing membrane dividing the purge chamber into an inlet portion and an outlet portion, the inlet portion for fluid communication with the chiller system, the degassing membrane to pass contamination from the inlet portion to the outlet portion; a valve coupled to the outlet portion of the purge chamber, the valve providing an exit for contamination from the outlet portion of the purge chamber; and a controller to open or close the valve in response to pressure in the outlet portion of the purge chamber.
Abstract:
An evaporator or a condenser includes a surface on which the operating liquid is arranged. Further, turbulence generators are provided to generate turbulences in the operating liquid located on the operating surface. In the condenser, alternatively or additionally, a laminarizer is present to make the vapor stream laminar provided by the compressor. On the evaporator side, the evaporation efficiency is increased and, on the condenser side, the condenser efficiency is increased, which may be used for a substantial reduction in size without loss of power of these components, in particular for a heat pump for heating a building.
Abstract:
Disclosed is a purging apparatus for conducting an air purge required when an equipment such as a split type air conditioner is installed or repaired, and to a to-be purged apparatus and a purging method: a to-be purged apparatus having a to-be purged room with two or more valve openings capable of connecting to a main circuit or to a circuit other than said main circuit; and a purging apparatus having a replacing gas container into which a replacing gas to be exchanged for a to-be purged gas is previously charged and a gas collecting container for collecting gas including said to-be purged gas, one of said valve openings of said to-be purged room and said exchanger gas container can be connected with each other, and the other valve opening of said to-be purged room and said gas collecting container can be connected with each other; said method comprising the steps of: sending said exchanger gas in said exchanger gas container, thereby pushing out said to-be purged gas in said to-be purged apparatus; and collecting said to-be purged gas into said gas collecting container.
Abstract:
The improved refrigeration system of the present invention includes an accumulator with a diffuser pipe extending downwardly into the upper end of a vapor refrigerant tank, the diffuser pipe extending from an evaporator and discharging vapor refrigerant therefrom into the tank. The diffuser pipe includes a lower end located within the interior of the tank which is expanded in diameter relative to the upper end, thereby reducing the velocity of fluid flowing through the pipe and entering the accumulator tank. A diffusion plate is mounted in the lower end of the diffuser pipe, to further diffuse fluid flowing therethrough. The improved refrigeration system also includes a tee having a stem portion extending horizontally from the condenser of the system, and a pair of upper and lower arms connected in a vertical orientation to the stem. The tee lower arm is connected to the receiver and the upper arm is connected to a purge connection. The improved refrigeration system further includes a two stage refrigeration system with the condenser of the high stage having a second section with a desuperheating coil therein to cool vapor refrigerant from the low stage compressor and supplying it to the high stage accumulator.
Abstract:
An apparatus and method are described for refrigeration employing a condenser, an evaporator, and a compressor, wherein a condenser vent is provided for exhausting accumulated mixtures of non-condensable gas, such as air, and refrigerant gas, wherein accumulated non-condensable gas mixed with refrigerant gas from the condenser vent is provided to a membrane separator comprising at least two chambers separated by a selective membrane, said chambers being a high pressure chamber to which the non-condensable gas mixed with refrigerant gas is supplied, and a low pressure chamber into which the refrigerant gas is selectively permeated through said selective membrane for reintroduction and reuse in the refrigeration cycle, and on said high pressure chamber of said membrane separator, a vent is provided to exhaust non-condensable gas-rich raffinate gas.
Abstract:
A portable apparatus for recovering refrigerant from a refrigeration system and delivering the refrigerant to a refrigerant storage tank. The recovery is automatically terminated when the liquid refrigerant occupies 80% of the volume of the recovery tank. The apparatus includes a liquid sensing thermistor that is in contact with the entering refrigerant to the recovery machine. When liquid is detected, it is routed directly to the recovery tank. Gaseous refrigerant and any non-condensable gases from the top of the recovery tank are directed to the suction of a compressor then to a condenser and to a purge vessel that functions as a receiver. When the entering refrigerant is in a gaseous phase, it is routed to the suction of the compressor. A second liquid sensing thermistor is in contact with the gaseous refrigerant from the top of the recovery tank and if liquid is detected the recovery process is terminated. A liquid sensing device near the bottom of the purge vessel actuates a solenoid valve to return the condensed liquid to the liquid inlet of the recovery tank. A cooling coil at the interior top of the purge vessel also condenses refrigerant. When non-condensable gases accumulate around the coil, there is less latent heat input to the coil and the suction line temperature drops. A temperature control with the sensing bulb at the suction line at a preset point actuates a solenoid valve in a line from the top of the purge vessel to purge the non-condensable gas through a small orifice to the atmosphere.
Abstract:
A purge supplement includes a vessel that attaches to a gas discharge line of a purge system. Adsorbent material is disposed within the vessel. In a Vent Mode the purge system vents into the vessel and the vessel vents to the atmosphere, whereby the purge system effectively vents through the vessel and the adsorbent material in the vessel adsorbs refrigerant. The purge supplement senses, by employing a weight scale or a refrigerant detection monitor, when the adsorbent material has adsorbed a certain amount of refrigerant, and at that time operation of the purge supplement switches from the Vent Mode to a Recycle Mode. When the transition is made to the Recycle Mode the vessel is isolated from the purge system and, after a slight delay, the atmosphere. After the slight time delay, the vessel is placed in fluid communication with an evaporator of a refrigeration system that the purge supplement is associated with. Refrigerant is drawn out of the adsorbent material and into the evaporator. Then, operation of the purge supplement switches back to the Vent Mode until such time as the purge supplement senses that the adsorbent material has adsorbed the certain amount of refrigerant, at which time operation switches again to the Recycle Mode.
Abstract:
The presence of an undesirable quantity of noncondensible gases in a refrigeration unit is inferred as a function of both the vapor pressure and temperature at a selected point in the refrigeration unit where the noncondensible gases tend to gather. Purging of these noncondensible gases, which contaminate the refrigerant, is responsive to a comparison in a programmable controller of the actual vapor pressure measured at the selected point, and the known pressure of uncontaminated refrigerant at the temperature existing at the selected point. On detecting a difference between these pressures that is greater than a desired value, the controller calculates a control output signal needed to purge a volume of contaminated vapor from the unit that is effective for reducing the difference between the measured pressure of contaminated refrigerant and the known pressure of uncontaminated refrigerant to a desired value.
Abstract:
The invention is directed to a process and apparatus for recovering refrigerant from a refrigeration purge stream wherein a gaseous purge stream containing a refrigerant and non-condensible gasses is countercurrently contacted with a high boiling point liquid which absorbs the refrigerant from the purge stream. Preferably a scrubbing column is used to effect countercurrent contact between the purge stream and the liquid stream.
Abstract:
Thermal purge apparatus for a chiller removes air, moisture and other non-condensibles from the chiller system refrigerant by causing chiller system refrigerant vapor to condense in a purge tank as a result of its undergoing a heat exchange relationship with a second and different refrigerant employed in a discrete purge refrigeration circuit. Chiller refrigerant circulates from the chiller condenser to, through and out of the purge tank in a free-flowing circulatory manner as a result of temperature and pressure gradients which develop between the interiors of the chiller condenser and the purge tank when the purge apparatus is in operation.