U.S. patent number 3,890,797 [Application Number 05/418,527] was granted by the patent office on 1975-06-24 for air conditioning process.
Invention is credited to Ted R. Brown.
United States Patent |
3,890,797 |
Brown |
June 24, 1975 |
Air conditioning process
Abstract
A process for efficiently conditioning air for beneficial use by
sequentially cooling dry air in three distinct steps, e.g.
pre-cooling the air out of the presence of moisture, refrigerating
the air to cool the air and coincidentally condense excess
moisture, and adiabatically cooling the air in the presence of
moisture.
Inventors: |
Brown; Ted R. (Salt Lake City,
UT) |
Family
ID: |
27000451 |
Appl.
No.: |
05/418,527 |
Filed: |
November 23, 1973 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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359368 |
May 11, 1973 |
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172968 |
Aug 19, 1971 |
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Current U.S.
Class: |
62/91; 62/92;
62/311; 62/93 |
Current CPC
Class: |
F24F
5/0035 (20130101); Y02B 30/54 (20130101) |
Current International
Class: |
F24F
5/00 (20060101); F25D 017/06 () |
Field of
Search: |
;62/91,93,311,92 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Wye; William J.
Attorney, Agent or Firm: Workman; H. Ross Young; J.
Winslow
Claims
What is claimed and desired to be secured by United States Letters
Patent is:
1. A process for controlling the temperature and moisture content
of air having a dew point of not more than 57.degree.F
corresponding to at least 90.degree.F dry bulb temperature,
sequentially
preparing an air flow path accommodating 400-600 CFM/ton net
sensible cooling;
drawing fresh dry air exclusively from a fresh air source and
through the flow path in the amounts of 400 to 600 CFM/ton net
sensible cooling;
pre-cooling the fresh air with a heat exchanger without altering
its moisture content;
refrigerating the pre-cooled air to further cool the air and
coincidentally condense excess moisture; and
scrubbing the cooled air with recirculating water to adiabatically
cool the air to within a range of 53.degree. to 60.degree.F.
2. A process for conditioning air sequentially comprising (a) first
cooling 100 percent fresh air having a dew point of not more than
57.degree.F corresponding to at least 90.degree.F dry bulb
temperature without altering its moisture content; (b) second
cooling the air by refrigeration to reduce the wet bulb and dry
bulb temperature and to control the amount of moisture which can be
added; (c) third cooling the air adiabatically to within the range
of 53.degree. to 60.degree.F by scrubbing the air with
recirculating water; all three cooling steps being applied
sequentially to air quantities exclusively within the range of 400
to 600 CFM/ton net sensible cooling.
Description
BACKGROUND
1. Field of the Invention
This invention is a division of my copending application Ser. No.
359,368, filed May 11, 1973, which is in turn a
continuation-in-part of my copending application Ser. No. 172,968,
filed Aug. 19, 1971 (now abandoned). The present invention relates
to the production of low temperature gases such as air for
beneficial use in air conditioning.
2. The Prior Art
It is well-known that the efficiency of air conditioning systems is
highly dependent upon the temperature of ambient air. In summer
months, where the ambient air temperature is high, usually
refrigerated air conditioning systems are employed to produce
consistently cold air. This is particularly true where high
temperatures are accompanied by relatively high humidity levels.
So-called "swamp cooler" type air conditioning systems become of
almost negligible value when both the temperature and humidity of
ambient air are high.
Because of the great difficulty with which air is reduced to a very
low temperature in hot summer months, most air conditioning systems
have been engineered so as to recirculate and recool the
conditioned air instead of continuously cooling fresh air. This
procedure has been found necessary to keep the size and attendant
costs of air conditioning systems from becoming prohibitive. Until
this present invention, an economical and efficient way of
substantially reducing the temperature of air or other gas for
cooling purposes year-round without refrigeration has not been
known.
It is also well-known to condition air by successive cooling,
humidifying, drying and recooling steps which are inefficient,
complicated and expensive. See, for example, U.S. Pat. No.
1,863,578.
BRIEF SUMMARY AND OBJECTS OF THE INVENTION
The present invention relates to conditioning fresh air by
sequentially (1) pre-cooling dry air out of the presence of
moisture, (2) refrigerating to cool the air and coincidentally
condense excess moisture and (3) adiabatically cooling the air.
Surprising efficiency and cooling results from this process using a
total fresh air system and treatment of the air in quantities
between 400 and 600 cubic feet per minute per ton of net sensible
in-space cooling.
It is, therefore, a primary object to efficiently provide air
having controlled temperature and humidity for air
conditioning.
It is another important object to provide a process for effecting
sensible cooling using a total fresh air system.
These and other objects and features of the present invention will
become more fully apparent from the following description and
appended claims taken in conjunction with the accompanying
drawing.
BRIEF DESCRIPTION OF THE DRAWING
The FIGURE is a schematic flow diagram illustrating a fluid circuit
and apparatus for reducing air temperature according to the present
invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENT
GENERAL
Heat exchange processes such as used in air conditioning systems
have always been required to have increased capacity in order to
adequately cool air when the temperature and/or the humidity of
external air climbs as in summer months and on hot days.
While it is relatively easy and comparatively inexpensive to remove
heat from gases when the temperature of the gas is high, the
difficulty with which heat is removed increases at an astonishing
rate when the temperature of the gas is already low. Thus,
generally speaking, it is much easier and less expensive to make
hot air cool than to make cool air cold using prior art techniques.
Historically, the approach used to make cool air cold was to
increase the size and capacity of cooling systems.
The present invention includes treating dry warm air out of the
presence of moisture to reduce its wet bulb temperature. Air most
efficiently used with the illustrated embodiment has a dew point of
not more than 57.degree. which is low compared to the dry bulb
temperature of the warm air. This treatment can be performed by
pre-cooling in a conventional heat exchanger.
According to the present invention, the temperature of the
pre-cooled gas is first reduced by refrigeration which serves to
further remove moisture and finally is adiabatically reduced so
that the gas is cold. Adiabatic processes are defined as those
processes carried out in such a manner that heat is not exchanged
between the system and its surroundings. Thus, the adiabatic
cooling step does not require an energy input to reduce the
temperature. When the gas is adiabatically cooled according to the
present invention, heat is not actually removed from the cooling
system but is reduced psychrometrically.
If a stream of gas is intimately mixed with a quantity of
recirculating liquid at a given temperature in an adiabatic system,
the temperature of the gas will drop and its humidity will
increase. Furthermore, the temperature of the recirculating liquid
will approach the web bulb temperature of the gas.
When 100 percent fresh (unrecirculated) air is used for cooling,
air quantities treated according to the preferred embodiment of the
invention must necessarily be limited to a rather narrow range in
order to efficiently produce desired cooling to within a range of
53.degree. to 60.degree.F without imposing larger than necessary
pre-cooling and refrigeration loads on the air cooling process.
It has been found according to the present invention that
approximately 400 to 600 cubic feet of fresh air per minute per ton
(CFM/ton) of net sensible in-space cooling is an adequate amount to
develop conditioned air at a desirable temperature of between
53.degree. and 60.degree.F. The surprising efficiency of this
system can be recognized by observing that conventional fresh air
swamp coolers require about 1000 CFM/ton even with very dry fresh
air. The efficiency of the system using this air volume range
presumes 100 percent fresh (unrecirculated) air having a dew point
of not more than 57.degree.F coincident with dry bulb temperatures
of not less than 90.degree.F. Under these climatic conditions, the
presently preferred embodiment of the invention produces 53.degree.
to 60.degree.F moisture conditioned air with surprising efficiency
and without requiring intermediate drying steps. In this
specification, refrigeration is defined to include cooling with
mechanically or chemically refrigerated fluids.
Referring more particularly to the FIGURE, warm dry air is first
obtained from a fresh air source, e.g. ambient. To maximize the
efficiency of the system, the dew point of the air should be at
least as low as 57.degree.F when air having a dry bulb temperature
of not less than 90.degree.F is used.
The warm air is first pre-cooled in a heat exchanger 62. The heat
exchanger 62 may be any one of a variety of heat exchangers which
will not add moisture to the air, one suitable type being the
fin-coil heat exchanger often called an extended surface heat
exchanger. This type of heat exchanger is very inexpensive to
acquire and operate and is very efficient at high temperatures.
Therefore, according to the illustrated embodiment of the
invention, the pre-cooled dry air emerging from the heat exchanger
62 is conducted to a refrigeration coil 76 which acts upon the
pre-cooled air as it traverses from the heat exchanger 62 to the
air washer 64 (i.e. from the pre-cooling to the adiabatically
cooling steps). When the pre-cooled air is further cooled, its wet
bulb temperature is lowered. Accordingly, upon adiabatic cooling in
the air washer 64, its dry bulb temperature is further reduced to
about 53.degree. to 60.degree.F.
The moisture content of the effluent from the air washer 64 will be
controlled in proportion to the amount of cooling to which the air
is subjected in advance of the adiabatic cooling in air washer 64.
The dry bulb and wet bulb temperatures imposed upon the air in
advance of the adiabatic cooling step will determine the amount of
moisture that can be added in the adiabatic cooling step.
The air is then directed through air washer 64 which scrubs the air
with water or, if desired, other cooling liquid. The water used to
scrub the pre-cooled dry air is recirculated through an external
circuit 66 continuously. The temperature of the recirculating water
in the circuit 66 approaches the wet bulb temperature of the air
which enters the air washer 64. Thus, the entering cold air has its
temperature further adiabatically reduced from the dry bulb to near
the web bulb temperature in the air washer.
The refrigeration circuit 70 conventionally comprises a condenser
72 and a compressor 74 with an evaporating coil 76 interposed
therebetween. A conventional expansion valve 78 admits refrigerant
fluid into the evaporating coil 76.
It should be observed that unless the temperature of the air were
adiabatically reduced in the air washer 64, a far larger and more
expensive coil 76 and larger refrigeration system 70 would be
necessary to obtain the same very cold air temperature developed
according to the embodiment of the FIGURE.
The system of the FIGURE is designed to transport and condition
about 400 to 600 CFM/ton net sensible cooling. Using the air having
a 57.degree. dew point, temperatures as low as 53.degree. to
60.degree.F may be economically and efficiently achieved.
Accordingly, the effluent conditioned air has a surprisingly low
temperature and controlled humidity without requiring expensive
dehumidifying (warming) and recooling steps.
Using the embodiment of the FIGURE, cold air in the range of
53.degree. to 60.degree.F for air conditioning or any other desired
beneficial use can be obtained with surprising efficiency using a
100 percent fresh air system at maximum outdoor temperatures. Thus,
the need for recirculating the same air in order to reduce the
costs of cooling is unnecessary. Furthermore, cold air can be
obtained without using large and expensive refrigeration systems.
The refrigeration system 70 required for this combination of
cooling steps has been found to be approximately one-third the size
required if conventional recirculating air refrigeration systems
are employed. Accordingly, the advantages of a complete fresh air
system can be substituted for the lower quality, more expensive
recirculating air systems.
The invention may be embodied in other specific forms without
departing from its spirit or essential characteristics. The
described embodiment is to be considered in all respects only as
illustrative and not restrictive and the scope of the invention is,
therefore, indicated by the appended claims rather than by the
foregoing description. All changes which come within the meaning
and range of equivalency of the claims are to be embraced within
their scope.
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