US3842901A

US3842901A - Air conditioning system and method

Info

Publication number: US3842901A
Application number: US00264544A
Authority: US
Inventors: A Mcfarlan
Original assignee: Individual
Current assignee: Individual
Priority date: 1970-06-29
Filing date: 1972-06-20
Publication date: 1974-10-22
Anticipated expiration: 1991-10-22
Also published as: SE7108317L; DE2131793A1; GB1354742A; CH539247A; ZA714145B; US3670806A; FR2098078A5

Abstract

Air conditioning systems having a plurality of refrigeration units with a hot water stream flowing through the condensers in series, and with a chilled water stream flowing through the evaporator-chillers in series. The system balances the heating and cooling loads so that the internally produced heat is used to heat the periphery when such heat is required. Excess heat is dissipated, and additional heat is provided when needed. The temperature of the hot water is higher than with the normal practice, and special advantages are obtained from the standpoint of providing efficient and dependable operations with wider ranges of the load and ambient conditions.

Description

[ AIR CONDITIONING SYSTEM AND METHOD [76] lnventor: Alden I. McFarlan, 691 Dorian Rd,

Westfield, NJ. 07090 22 Filed: June 20,1972

211 Appl.No.:264,544'

Related US. Application Data [62] Division of Ser. No. 50,874, June 29, 1970,-Pat. No.

[52] US. Cl. 165/2, 165/22 [51] Int. Cl F24! 3/00 [58] Field 01' Search 62/159, 325; 165/22, 2

[56] References Cited UNITED STATES PATENTS 2,796,740 -6/1957 McFarlan 62/159 2,797,068 6/1957 Mcl-arlan.... 62/159 2,935,857 5/1960 McFarlan., t 62/159 2,984,458 5/1961 McFarlan 62/305 3,067,587 12/1962 McFarlan.... 3,354,943 11/1967 62/159 McFarlan 165/22 Primary Examiner-Charles Sukalo Attorney, Agent, or Firm-Curtis, Morris & Safford 5 7 ABSTRACT Air conditioning systems having a plurality of refrigeration units with a hot water stream flowing through the condensers in series, and with a chilled water stream flowing through the evaporator-chillers in series. The system balances the heating and cooling loads so that the internally produced heat is used to heat the periphery when such heat is required. Excess heat is dissipated, and additional heat is provided when needed. The temperature of the hot water is higher than with the normal practice, and special advantages are obtained from the standpoint of provid ing efficient and dependable operations with wider ranges of the load and ambient conditions.

2 Claims, 2 Drawing Figures AIR CONDITIONING SYSTEM AND METHOD This is a divisional application of Application Ser. No. 050,874, filed June 29, 1970, now US. Pat. No. 3,670,806.

This invention relates to air conditioning systems and methods, and particularly to such systems which heat and cool the various zones or rooms of an overall project, e.g., a buidling or buildings. lllustratively, the system provides separate streams of chilled water and hot water which are carried through lines to various units which heat or cool the various zones, as required.

An object of this invention is to provide improved air conditioning systems and methods. A further object is to provide air conditioning systems which operate in an efficient and dependable manner throughout wide ranges of conditions of use. These and other objects will be in part obvious and in part pointed out below.

In air conditioning systems which heat and cool the various zones of an overall project by transferring heat from one zone to another, it is necessary to provide for critical heating loads and extreme cooling loads, even though these extreme conditions occur only rarely. It is also necessary to insure efficient and dependable operation throughout the entire range of intermediate heating and cooling load conditions which exist the vast majority of the time. It is important to insure satisfactory operation from all standpoints with minimum first cost and minimum operating costs.

In accordance with the present invention, the internally generated heat is used to heat the exterior zones when such heating is required. Excess in heat is delivered to a heat sink, and additional heat is added when there is a deficiency. The breakeven temperature is the outside air temperature at which the total loss of heat from the overall project to the outside air exactly equals the total heat gain, which is principally the internally created heat. The internally created heat includes the heat produced by the lights, the electrical equipment, the occupants and the components of the refrigeration system.

An increase in the internally created heat causesa drop in the breakeven temperature, because the breakeven temperature will not be reached until that increase in heat is represented by an increase in the heat loss. Conversely, a decrease in the internally created heat causes an increase in the breakeven temperature. Assuming a balanced heat condition for the overall project at a particular breakeven temperature, an increase in the cooling load or a reduction in the heating load will cause an excess of the internally generated heat beyond the heating requirements; and that reduces the breakeven temperature and additional heat must be added. However, the temperature of the heating water must also be increased to provide the required heating, because the air-heating coils must receive hot water at the increased temperature so as to deliver more heat to the air.

Adhering to the basic principle of not adding heat from an external source above thebreakeven temperature and relying upon the refrigeration system as the sole heat source, at outside temperatures within the range just above the breakeven temperature, there would normally be a reduced cooling load and relatively low temperature hot water from the refrigeration system. Hence, when the low outside temperature produces a need for an increase in the temperature of the hot water from the refrigeration system, normally there is actually a decrease in that hot water temperature. In that way and others, the various types of refrigeration systems are limited in normal operation with respect to the ability to provide the desired increase in the hot water temperature at low outside temperatures. This is particularly evident when there is an extreme drop in the breakeven temperature.

A constant speed centrifugal compressor necessarily displaces enough refrigerant to satisfy its full capacity, and at reduced loads there must be means to provide a corresponding reduction in the capacity. Generally, this reduced capacity is obtained by means of inlet vanes which impose a reduction in the quantity of gas compressed. However, centrifugal compressors tend to surge at partial loads and high compression ratios. In order to avoid surging it is important to utilize the highest temperature for the water being cooled and the lowest possible temperature for the water which is cooling the condenser. As indicated above, that is a serious normal mode of the operation when it is desirable to have high temperature hot water with low outside temperatures.

With variable speed centrifugal compressors, such as is common with steam turbine driven units, the surging problem can be reudced, but there are still problems with respect to compression ratios and there are limitations on the normal maximum hot water temperature. With absorbtion systems there is a constant or fixed temperature of the hot water relative to any specific cold water temperature. Hence, with a drop in outside temperature, as discussed above, it is possible to increase the temperature of the cold water and thereby provide hot water of increased temperature. However, that produces serious control problems. Refrigeration systems having positive displacement compressors are also deficient from the standpoint of providing hot water at an increased temperature when there is a drop in the outside air temperature. The efficiency falls off as the compression ratio increases, and to some extent there is a reduction of the capacity.

The present invention overcomes the difficulties referred to above with respect to providing hot water at increased temperatures when there is a drop in the outside temperature at the breakeven temperature. How ever, the invention also provides important benefits even in systems which do not involve heat recovery for heating the outside zones. In accordance with the present invention, the temperature of the hot water from the refrigeration system is raised substantially above the normally accepted range at low breakeven temperatures, so that the hot water temperature is sufficient to maintain satisfactory heating. Also, at high outside temperatures, when heat is dissipated to a cooling tower or to another heat sink, the high temperature hot water carries away the required amount of excess heat and dissipates it with a smaller amount of water than would be required with lower temperature hot water. Hence, the system requires smaller pumps, control valves, and water lines, and less insulation, as well as smaller heat transfer coils if it is necessary to have more coil surface at the breakeven temperature than is required at the full cooling load. Also, the cooling tower will handle a smaller stream of hot water so that it can be of lesser horizontal area, thus occupying less roof space.

The present invention also contemplates that the temperatures of the water flowing to the chillers and to the cold water line can be higher than would be expected with the usual type of prior system. That permits the operation of the refrigeration units at higher temperature levels, so as to increase further the temperature of the hot water when that is desirable. Also, the invention contemplates wider ranges in the temperatures of the chilled water and hot water so as to give freedom of design and greater leeway in the mode of operation.

It has been recognized that the air conditioning of extremely tall buildings with chilled water and hot water from a central station in the basement creates serious problems. If the water lines were to extend directly from the basement to the tower of the building, the head pressures could not be tolerated. Hence, chilled water and hot water can be supplied to heat exchangers at an intermediate level in the building and the air conditioning from the spaces above that level can be carried on by streams of water which are chilled and heated by those exchangers and the return lines from above that level extend to those heat exchangers. In that way, the pressure head conditions are kept within acceptable limits. The staged heating and cooling of the streams of chilled water and hot water delivers to the heat exchangers the streams at higher temperature hot water and lower temperature chilled water more efficiently than is normally used for air conditioning purposes. Streams of chilled water and hot water are then taken off at intermediate stages in the refrigeration system so as to provide streams of water at the desired temperatures for the air conditioning in the lower portion in the building.

In the illustrative embodiment of the present invention, three staged refrigeration units are used which have constant-speed, centrifugal compressors. The stream of chilled water flows through staged evaporator-chillers of the three refrigeration units in series, and the stream of hot water flows through the condensers of the refrigeration units in the opposite direction. The two streams of water flow to air-treating unitsfor heating and cooling the air, and there is a common return line through which all the water from the various air treating units is returned to the refrigeration units where it divides to form the chilled water stream and the hot water stream. The system is so arranged that it provides relatively high temperature hot water and adequately cold-chilled water. However, the system also has the very important characteristic that it will operate efficiently and dependably throughout the entire range between the maximum heating load and the maximum cooling load.

IN THE DRAWINGS FIG. 1 is a schematic representation of one embodiment of the invention; and,

FIG. 2 is a somewhat schematic, exploded perspective view of one of the condensers of the system of FIG. 1.

In the drawings, the air conditioning system 2 includes three refrigeration units 4, 6 and 8 at a central station, a cooling tower l and a large number of air treating units which are represented by units 12 and 14. A chilled water line 16 and a hot water line 18 extends from the central station to each of the air treating units and water from all of the air treating units flows back to the central station through a common return line 19. Each of the refrigeration units has a constant speed, centrifugal compressor 20 driven by an electric motor (not shown), an evaporator-chiller 22 and a double condenser 24 of the water tube and shell type. The components of the respective refrigeration units are identified in the drawings by numbers with suffixes 4, 6 and 8, respectively. The water returning from the air treating units through line 19 flows to two

pumps

30 and 32.

Pump 32 directs a stream of water in series through the evaporator-chillers 22-4, 22-6 and 22-8, and thence through the chilled water line 16. Pump 30 directs a stream of water in series through the condensers 24-8, 24-6 and 24-4, and thence through the hot water line 18. Hence, there is staged heating of the water by the condensers and staged cooling of the water by the evaporator-chillers. However, the staging of the heating in the series of refrigeration units is opposite to the staging of the cooling in the series, i.e., through the condensers of the series is opposite to the flow through the evaporators of the series. Therefore, the evaporator-chiller 22-4 of unit 4 receives the stream of water to be cooled at its highest temperature, and its associated condenser 24-4 receives its stream of water to be heated after it has been heated by condensers 24-8 and 24-6 and produces the highest temperature water and delivers the stream of hot water to line 18. Condenser 24-8 and evaporator 22-8 receive their streams of water at the respective lowest temperatures; and, the respective temperatures of the two streams of water flowing through condenser 24-6 and evaporator-chiller 22-6 are intermediate the respective highest and lowest temperatures of those streams. As will be explained more fully below, that reverse staging of the heating and cooling gives special advantages and insures efficient and dependable operation with systems of the type of the illustrative embodiment.

A balancing water line 34 interconnects the outlets of

pumps

30 and 32 so that water may flow from pump 32 to condenser 24-4 and the hot water line, and water can flow from pump 30 to evaporator-chiller 22-4 and the chilled water line. A steam converter 38 in line 18 supplies additional heat to the stream of hot water when the operating conditions cause the temperature of the stream of hot water to drop below a predetermined level. Cooling water for the condensers flows by the action of pump 41 to and from the cooling tower through

lines

37 and 39, respectively, the circuit being through the double-condenser circuit of condensers 24-8, 24-6 and 24-4 in that order, and then to the cooling tower. A bypass line 43 and valve 45 provide a flow path around the condensers for all or part of the water from the cooling tower. Units 12 and 14 have mixing

valves

40 and 42, respectively, each of, which has an inlet port from each of

lines

16 and 18, and its outlet port to the coil of its unit. Each of these valves is operable to supply chilled water or hot water or a mixture of the two to the coil of its unit. However, as indicated above, all of the water which flows through all of these units is combined into a single stream in the return line 19.

The double condensers 24 are of the type shown in FIG. 2 with a shell 47,

end plates

49 and 44, and water tubes mounted between a pair of tube plates 46 at the opposite end of the shell. The space between each of the end plates and its tube plate is baffled along quadrant lines to form two separate water-flow paths. One path is from the inlet connection 50 in end plate 42 through one quadrant of the tubes to an outlet connection 52 in plate 44. The other path is through the other three quadrants of tubes from inlet connection 54 in plate 49 through one quadrant of the tubes to end plate 44, then back to end plate 49 through another quadrant to the tubes, and thence through the other quadrant of tubes to the outlet 56 in end plate 44. The single quadrant circuit between

connection

52 and 54 is the hot water circuit, and the three-pass or three-quadrant circuit is the circuit for the water which flows to the cooling tower. Hence, during operation when there is a substantial cooling load and the cooling tower is operating, the refrigerant is condensed by the cooling action of three quadrants of each of the condensers. However, when there is a substantial heating load and the cooling tower is operating, valve 45 is turned to by-pass some or all of the water from the cooling tower through line 43 around the condensers. The refrigerant in each of the condensers then delivers most or all of its heat to the water in the hot water circuit, and in that way heat is delivered to the hot water at an increased rate up to the maximum rate.

With the system of the illustrative embodiment, a very wide range of load conditions is handled automatically and in an efficient and dependable manner. Unit 12 is illustrative of the units which cool and heat the air for the interior spaces. During normal occupancy, the interior space requires only cooling. However, in this embodiment, it is considered that the heat load in the interior space may be relatively small and a variable amount of hot water may be mixed with chilled water to provide the optimum temperature conditions. Also, when the building has been unoccupied for a long weekend during the heating season, the interior space requires some heating in preparation for occupancy. Unit 14 is illustrative of the units which supply heating and cooling for the perepheral space. That space requires chilled water or hot water or a mixture of the two, depending upon the outside temperature, the sun effect and the other normally understood variable conditions.

It has been indicated above that this invention has special advantages in extremely tall buildings. Accordingly, the chilled water line 16, the hot water line 18, and return line 19 extend to two

heat exchangers

70 and 72. A three-pipe heating and cooling circuit extends from the heat exchangers to units 75 in the tower portion of the building, there being a chilled water line 74 and a hot water line 76 and a return line 78. A single pump circulates the water, and the water temperatures in

lines

74 and 76 are regulated by

controllers

81 and 82 which operate valves to control the flow water from

lines

16 and 18, respectively.

A chilled water line 84 extends from line 86 between evaporator-chillers 22-6 and 22-8 to a three-way valve 88. Valve 88 is shown in its position to direct chilled water from evaporator-chiller 22-8 to units 12 and 14. When in this position the entire stream of chilled water flows through evaporator-chiller-22-8. However, valve 88 may be turned to cause the chilled water flowing to units 12 and 14 to bypass evaporator-chiller 22-8. In that way the chilled water for units 12 and 14 is at a higher temperature than that which flows to heat exchanger 70,-as discussed above.

In this embodiment, the temperature of the heated water is within the range of 90 F. to F. In general that temperature is increased within that range when there is an increase in the heating load.

What is claimed is:

1. The method for maintaining comfort conditions within a plurality of zones or spaces wherein one or more of the zones orspaces requires cooling when another requires heating, the steps of, producing separate streams of chilled liquid and heated liquid by staged heating and cooling steps with refrigeration units having the flow path therethrough for the heated liquid by which the heat is discharged from the refrigeration units in series relationship opposite to the series relationship of the flow path therethrough for the chilled liquid, supplying said streams of chilled liquid and heated liquid as is required to handle the respective heating and cooling loads in the various zones or spaces and returning the liquid to the refrigeration units as return liquid, whereby heat is removed from one of said zones or spaces and is delivered by the return liquid to the refrigeration units and through said refrigeration units to the stream of heated liquid and is utilized to heat an exterior zone or space, discharging heat from the system when there is an excess, and controlling the discharge of heat from the system to maintain the stream of heated liquid at a temperature within the range of 90F to 135F when one of said zones or spaces requires heating with a progressively increasing temperature within said range as the heating load increases.

2. The method as described in claim 1 which includes the step of adding heat to the system to satisfy a heat

Claims

1. The method for maintaining comfort conditions within a plurality of zones or spaces wherein one or more of the zones or spaces requires cooling when another requires heating, the steps of, producing separate streams of chilled liquid and heated liquid by staged heating and cooling steps with refrigeration units having the flow path therethrough for the heated liquid by which the heat is discharged from the refrigeration units in series relationship opposite to the series relationship of the flow path therethrough for the chilled liquid, supplying said streams of chilled liquid and heated liquid as is required to handle the respective heating and cooling loads in the various zones or spaces and returning the liquid to the refrigeration units as return liquid, whereby heat is removed from one of said zones or spaces and is delivered by the return liquid to the refrigeration units and through said refrigeration units to the stream of heated liquid and is utilized to heat an exterior zone or space, discharging heat from the system when there is an excess, and controlling the discharge of heat from the system to maintain the stream of heated liquid at a temperature within the range of 90*F to 135*F when one of said Zones or spaces requires heating with a progressively increasing temperature within said range as the heating load increases.

2. The method as described in claim 1 which includes the step of adding heat to the system to satisfy a heat deficiency.