Patent Application
20240133595
The present invention is directed to a structure for heat ventilation and air conditioning, and more particularly a heat ventilation and air conditioning system utilizing recycled water to act as a heat sink to cool condenser coils within the system.
As known in the art, heat ventilation and air conditioning systems (HVAC) are the most commonly used technology to cool large buildings, commercial and industrial facilities and data centers. Chillers, the heart of the HVAC system, facilitate the transfer of heat from an internal environment to an external environment. The heat transfer device relies on the physical state of a refrigerant as it circulates through the chiller system. Chillers provide a continuous flow of coolant to the cold side of a process water system at a desired temperature of generally about 50° F. (10° C.).
In the prior art, there are three commonly used cooling approaches for cooling condenser coils in chillers: air cooling, evaporation cooling and adiabatic cooling.
Generally, as seen in
Generally, as seen in
While condenser water 214 cools the condenser coils 212, it subsequently generates a warm water stream also known as condenser water return 222 which is pumped to a cooling tower 216 to cool the content. As water is cooled in cooling tower 216, the warm air 224 is concurrently released into atmosphere. A dosing station 226 provides corrosion inhibitors and biocide for corrosion control and Legionella control in cooling tower 216. Cooling tower 216 is designed to operate a few cycles to reduce water consumption. As more cycles is achieved dissolved solids concentrate in the condenser water 214 which requires periodic blowdown 228 to discharge the blowdown, generally to a sewer, to avoid excessive dissolved solids accumulation in cooling tower 216. To compensate evaporative losses 224 and blowdown losses 228, in cooling tower 216, a makeup water in the form of potable water or recycled water 230 is provided. A makeup water storage tank 232 stores and conveys the makeup water 230 to cooling tower 216 water storage basin. A blend of make up water 230 and cooled water 214 from the cooling tower 216 are input to condenser 212 to remove heat returning from compressor 210.
The prior art air cooling systems have been satisfactory however they suffer from the disadvantage that they are energy inefficient. During peak use seasonal periods, chillers consume more than fifty percent of a building's electrical energy. It is estimated that more than 120,000 chillers in the United States are expending a further thirty percent of building energy due to operational inefficiencies.
Evaporative cooling chiller systems are more efficient as a result of their advantageous heat absorption capacity. However, they suffer from the disadvantages that they require high water consumption because of evaporative losses. Additionally, they are relatively more complex to operate and maintain; requiring continuous use of cooling tower chemicals such as corrosion inhibitor and biocides, as well as requiring structure for disposal of blowdown steam. Therefore, they require a higher initial investment as compared to air cooling systems.
An adiabatic cooling system (not shown) is an air cooled system assisted by evaporative cooling. Wetting installed cooling pads, via water, pre-cools the ambient air, allowing a more efficient air cooling system. While the adiabatic cooling system is more energy and water efficient than air cooling and evaporative cooling it suffers from the disadvantage that it is more complex in operation and requires biocides, increasing the maintenance requirements.
Accordingly, a structure and methodology to overcome the shortcomings of the prior art, is desired.
A system for using recycled water to cool a condenser includes a water reclamation source. A water cooled condenser receives the recycled water. The received water has a first temperature. A refrigerant at a second temperature, greater than the first temperature, is input to the water cooled condenser. The condenser heats the recycled water with the refrigerant to a third temperature greater than the first temperature and less than the second temperature, and inputs recycled water at the third temperature to the water reclamation source and lowers the temperature of the refrigerant to a fourth temperature less than the second temperature.
In a further embodiment of the invention the second water is water returned from HVAC systems for commercial building, data center and other large cooling operations. The first water may be returned to the water reclamation source after passing through the cooled condenser.
The present disclosure will be better understood by reading the written description with reference to the accompanying drawing figures in which like reference numerals denote similar structure and refer to like elements throughout in which:
Reference is now made to
In the invention presented in
A chilled water return 308 from the air handling units of HVAC of a building, commercial facility, data center, etc., fluidly connected to evaporator 302 returns chilled water to evaporator 302 to initiate heat transfer between the water and refrigerant to produce chilled water again. Evaporator 302 boils the refrigerant such as R 717 (ammonia based) and R 747 (carbon dioxide based) used in closed loop chiller systems and converts the refrigerant from a low-pressure liquid to a low-pressure gas. A compressor 310 receives the low-pressure gas and compresses the low-pressure gas into high pressure gas.
A condenser 312, in fluid communication with the compressor 310, and a flow distribution and recycled water pump station 506, receives the high pressure high temperature gas from the compressor 310. The flow Distribution and recycled water pump station 506 pumps recycled water as the condenser water supply 508 to the cooling coils 312a of condenser 312. The condensed liquid from coils 312b of condenser 312 passes through a dry filter 320 to remove excessive moisture prior to being input to an expansion valve 322, upstream of evaporator 302, which controls how much liquid refrigerant enters the evaporator 302, beginning the refrigeration cycle again
In a second closed loop 500, recycled water as condenser water supply source (cold) 508, as discussed above, is input to condenser coils 312a of condenser 312 to cool the condenser coils 312b of loop 300. As a result heat is concurrently transferred from hot refrigerant to recycled water and it exists condenser as condenser water return (warm) 514, generally 10° F. warmer than the recycled water used as the condenser water supply source 508. As known in the art refrigerant may be water, fluorocarbons, hydrocarbons, even ammonia, or any combination thereof.
Depending upon season and relative contributions of condenser water return 514 and recycled water 504 generated at water reclamation plant 502, the condenser water return 514 either passes through a heat exchanger 516 or bypass 518 around heat exchanger 516 before entering the blending and reclaimed water pump station 512. Heat exchanger 516, if used, can reduce the temperature of condenser water return 514 by typically 3° F. and produces a cooled condenser water return stream 520.
The flow distribution and recycled water pump station 506 has two functions: (1) It pumps the needed amount of condenser water supply source (recycled water) 508 to the condenser coils 312 and (2) conveys the remaining recycled water 510 to the blending and water reclamation pump station 512. Once the amount of condenser water supply for cooling is determined, the remaining recycled water 510 is calculated by taking flow difference between stream 504 and stream 508.
The blending and water reclamation pump station 512 receives flow streams from streams 510 and 520 and pumps the blended stream of 510 and 520 to other reclaimed water customers for non-potable reuse purposes 522. The recycled water temperature in blending and water reclamation pump station 512 may increase to a value that is dependent upon flow and temperature of the two streams (510 and 520) and it falls within the temperatures of the streams 510 and 520.
By constructing an HVAC system in accordance with the invention a simplified, more efficient cooling system is provided as there is no longer a need for a cooling tower of the evaporative system or energy intensive compressor condenser systems of the air cooled chiller systems. Furthermore because of its single loop and closed nature the above system lends itself to the use of recycled water only once without cycling it several times and without spraying the water and does not need to make us of complex biocide, corrosion inhibitor or other treatment systems significantly reducing operation and maintenance needs and associated costs for condenser cooling.
A system for using recycled water as condenser water supply source, in accordance with the invention, provides a condenser in a closed loop chiller system in HVAC systems for commercial building, data center and other large cooling operations; recovering and utilizing recycled water from cooling operation that eliminates potable water use for cooling, eliminates need for cooling tower, reduces cost and complexity of the evaporative cooling, eliminates evaporative water losses and maximizes recycled water available for community; offering highly innovative and sustainable solution for commercial building, data center and large industrial scale cooling.
It will thus be seen that the objects set forth above, among those made apparent from the preceding description, are efficiently attained and, since certain changes may be made in carrying out the above method and in the construction set forth without departing from the spirit and scope of the invention, it is intended that all matter contained in the above description and shown in the accompanying drawings shall be interpreted as illustrative and not in a limiting sense.
It is also to be understood that the following claims are intended to cover all of the generic and specific features of the invention herein described, and all statements of the scope of the invention which, as a matter of language, might be said to fall therebetween.
This application claims the benefit of U.S. Provisional Application No. 63/417,415 filed on Oct. 19, 2022. The entire contents of this application is incorporated herein by reference in its entirety.
| Number | Date | Country | |
|---|---|---|---|
| 63417415 | Oct 2022 | US |
