U.S. patent number 3,721,109 [Application Number 05/149,552] was granted by the patent office on 1973-03-20 for high pressure multiple pump for absorption refrigeration machine.
This patent grant is currently assigned to The Trane Company. Invention is credited to James M. Porter.
United States Patent |
3,721,109 |
Porter |
March 20, 1973 |
HIGH PRESSURE MULTIPLE PUMP FOR ABSORPTION REFRIGERATION
MACHINE
Abstract
A pump for circulating a plurality of fluids in an absorption
refrigeration machine, the pump having a plurality of fluid
impellers, at least two of which are arranged in series.
Inventors: |
Porter; James M. (La Crosse,
WI) |
Assignee: |
The Trane Company (La Crosse,
WI)
|
Family
ID: |
22530806 |
Appl.
No.: |
05/149,552 |
Filed: |
June 3, 1971 |
Current U.S.
Class: |
62/476;
415/199.1; 62/483 |
Current CPC
Class: |
F25B
15/025 (20130101); Y02B 30/62 (20130101); Y02A
30/277 (20180101); Y02A 30/27 (20180101) |
Current International
Class: |
F25B
15/02 (20060101); F25b 015/06 () |
Field of
Search: |
;62/476,483,487,488
;415/199R |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: O'Dea; William F.
Assistant Examiner: Ferguson; Peter D.
Claims
I claim:
1. An absorption refrigeration system comprising a first stage high
pressure generator, a second stage low pressure generator, an
absorber, an evaporator, a condenser, an absorbent solution, a
refrigerant, and pump means for moving said absorbent solution and
said refrigerant within said system; said pump means including a
shaft having a motor drivingly connected thereto, a first impeller
mounted at one end of said shaft to receive refrigerant from a
first portion of said evaporator and transfer said refrigerant to a
second portion of said evaporator; a second impeller mounted on
said shaft at the end opposite said first impeller to receive
absorbent solution from a first portion of said absorber and
transfer said solution to a second portion of said absorber; a
third impeller mounted on a central portion of said shaft to
receive absorbent solution from said absorber and transfer said
solution to a fourth impeller, said fourth impeller mounted on a
central portion of said shaft to receive said solution form said
third impeller and transfer said solution to said first stage high
pressure generator, all of said impellers being mounted in a common
housing whereby all of said impellers are driven by said motor.
Description
BACKGROUND OF THE INVENTION
Pumps are commonly associated with absorption refrigeration
machines in order to convey the various fluids used in the machine
from one point in the system to another. Thus it is not uncommon
for an absorption machine to employ three distinct pumps. One such
pump normally circulates absorbent solution between the absorber
and the generator or concentrator. A second pump normally
circulates absorbent solution within the absorber section, such as
from a drain pan to a spray header or drip pipe located above the
absorber tube bundle. Yet another pump may circulate refrigerant
within the evaporator section of the machine in a similar
manner.
Certain unique advantages can be gained by consolidating the
aforementioned three pumps into a single, multi-stage pump driven
by a single source of motive power. Such a multi-stage pump is
described in U.S. Pat. No. 3,296,823, issued Jan. 10, 1967.
However, the pump disclosed in that patent may not be satisfactory
for use in an absorption machine having a high pressure generator,
such as a multi-stage absorption machine, because the size of the
impeller required may vary considerably from one pump stage to
another.
SUMMARY OF THE INVENTION
It is an object of the present invention, therefore, to provide a
pump that may be used on a high pressure type of absorption
machine.
It is a further object to provide a pump having a plurality of
impellers driven by a single power source.
Other objects and advantages will become obvious as the
specification proceeds.
The present invention provides a pump for an absorption
refrigeration system, the system including an absorption
refrigeration machine having a generator, a condenser, an
evaporator, an absorber, a refrigerant and a solution capable of
absorbing the refrigerant. A multiple pump is provided for
circulating refrigerant and absorbent solution as required for the
operation of the machine. The pump has a plurality of impellers
wherein separate impellers may circulate different fluids between
diverse portions of the machine. At least two of the impellers are
serially arranged and adapted to transfer absorbent solution
between the absorber and the generator.
DESCRIPTION OF PREFERRED EMBODIMENTS
Certain preferred embodiments of the present invention will be
described in greater illustrative detail and with particular
reference to the accompanying drawings, in which:
FIG. 1 is a diagrammatic sectional view of an absorption
refrigeration system including the fluid circulating system,
FIG. 2 is a front elevation view in vertical cross-section of the
pump used in the present system.
Referring now to FIG. 1, the absorption system shown is of the type
having a single shell 10, a partition 11 separating a first
generator stage from a second generator stage 12 and a condenser
14. Partition 16 further separates the second stage generator and
condenser section from a low pressure chamber containing an
evaporator 18 and an absorber 20. It should be understood that
other arrangements might be used; for instance, the first stage
generator 13 might be contained in a single shell with the
remaining components in a second shell. Alternatively the
generators of 13 and 12 and the condenser 14 might be in one shell
and the absorber 20 and evaporator 18 might be in a second shell
with conduits therebetween for conducting fluids.
Various combinations of refrigerant and absorbent may be used. A
solution of lithium bromide and water has been found to be highly
satisfactory.
The absorber 20 has a coil 22 supplied with cooling fluid from a
source 24 to remove the heat from the absorber. The cooling fluid
is conducted by conduit 26 to a cooling coil 28 in the condenser 14
and the cooling fluid leaves the machine through a conduit 30. The
cooling coil 28 in the condenser 14 removes the heat from and
condenses the refrigerant vapor in the condenser.
The first stage or high pressure generator 13 has a heating coil 31
supplied with heating fluid from a source 33. The heating fluid is
discharged from the coil through conduit 35. The coil 31 heats the
absorbent solution in the generator 13 causing it to boil whereby
refrigerant vapor is released therefrom. The refrigerant vapor
passes through conduit 32 and through the coil 34 of the second
stage or low pressure generator 12. The refrigerant vapor condenses
and releases heat to further concentrate intermediate strength
solution present in the second stage generator 12. The refrigerant
then passes to the condenser 14 via conduit 36, flow of refrigerant
being controlled by restrictor 38.
The condensed refrigerant in the condenser 14 flows through an
opening 40 into the evaporator 18. The absorbent solution in the
absorber 20 reduces the pressure in the absorber 20 and in the
evaporator 18 by the absorption of refrigerant vapor, thus causing
the refrigerant in evaporator 18 to boil. A low temperature is thus
maintained in the evaporator 18.
Evaporator 18 has a coil 42. Fluid from a refrigerating load such
as an air conditioning system enters coil 42 through conduit 44.
This fluid is reduced in temperature in the coil 42 and returns to
the refrigerating load through conduit 46.
The liquid refrigerant in the evaporator 18 collects in a pan 50,
and flows from the pan via conduit 52 to a pump indicated generally
at 60, and specifically to an impeller portion 62 of the pump 60.
Pump 60 may be driven by any suitable motor means 130. The liquid
refrigerant is discharged by pump 60 through conduit 54 from which
it flows through nozzles 56 into an evaporator 18.
Dilute solution flows from the absorber 20 through conduit 58 to
pump 60, and specifically to impeller portion 64. The solution is
discharged from impeller portion 64 through conduit 66 and to a
second impeller portion 68. It can be seen, therefore, that
impeller sections 64 and 68 are thereby arranged in series. The
dilute solution is discharged from pump 60 through conduit 70 which
conducts the fluid to heat exchanger 71 from which it flows through
conduit 72 to heat exchanger 73 and from there through conduit 74
to the high pressure generator 13.
The dilute solution is partially concentrated in generator 13 by
the boiling off of refrigerant as herein before described in
detail. The intermediate strength solution is withdrawn from
generator 13 via conduit 76 and passes through heat exchanger 73
from which it is conducted through conduit 78 to the second stage
generator 12.
The intermediate solution is further concentrated in generator 12
and is withdrawn therefrom via conduit 80 and passes through heat
exchanger 71, conduit 82, and into conduit 84. Dilute solution from
the absorber 20 passes into conduit 84 wherein it is mixed with the
concentrated solution passing from conduit 82 and the resulting
mixture enters pump 60 and specifically impeller portion 65,
exiting from pump 60 via conduit 86. From conduit 86 the
intermediate strength solution is sprayed from nozzles 90 over the
tube bundle in absorber 20.
Pump 60 has a pump body 91 and end walls 92 and 93. Attached to end
plate 92 is a bearing housing 94, and at the opposite end of pump
60, bearing housing 95 is mounted to transverse portion 96 of pump
body 91. Bearing 97 is carried by bearing housing 94 and bearing 98
is carried by bearing housing 95. Shaft 99 is rotatably mounted in
bearings 97 and 98.
A refrigerant impeller 62 is mounted on shaft 99 to rotate
therewith. Pump 60 has an inlet passage 100 in fluid communication
with conduit 52 and impeller 62. A discharge passageway 101 is in
fluid communication with impeller 62 and conduit 54. A labyrinth
seal 102 provides the seal between the discharge passage 101 and
the inlet passage 100, thus creating the differential pressure for
flow through passage 103 to chamber 105 and bearing 98 and through
passage 104 back to the suction side of impeller 62. Chamber 105
also provides cooling for seal 106.
Threaded into discharge chamber 101 is conduit 107 shown
terminating in valve 108. Valve 108 may be used to open discharge
passageway 101 to the air during servicing of pump 60 if desired.
However, it is preferred to extend conduit 107 around to the pump
motor 130 in order to provide refrigerant to the motor for
cooling.
An absorption solution impeller 65 is mounted on shaft 99 to rotate
therewith, on the end of pump 60 opposite impeller 62. Pump 60 has
an inlet passage 108 in fluid communication with conduit 84 and
impeller 65. A discharge passageway 109 is in fluid communication
with impeller 65, conduit 86, and conduit 110 which terminates in
valve 112. Valve 112 is normally closed but may be opened to admit
air to pump 60 during servicing.
In the approximate center portion of pump 60 impellers 64 and 68
are mounted in back-to-back relationship on shaft 99 for rotation
therewith. Pump 60 has an inlet portion 114 in fluid communication
with conduit 58 and impeller 64. A discharge passageway 16 is in
fluid communication with impeller 64 and conduit 66. Conduit 118 is
in fluid communication with narrower upper portion of discharge
passageway 116, and said conduit is shown terminating in valve 119,
which is normally closed and may be opened during servicing and the
like as hereinbefore described in connection with similar vent
valves.
Conduit 66 communicates with discharge passageway 116 and with
inlet portion 120, which inlet portion is also in fluid
communication with impeller 68. Accordingly, the discharge from
impeller 64 is introduced to the suction side of impeller 68,
thereby arranging these impellers in series. Impeller 68 is also in
fluid communication with discharge passageway 122 which in turn is
in fluid communication with conduit 70. In this manner, the dilute
solution from absorber 20 is conveyed to the high pressure
generator 13 via impellers 64 and 68 of pump 60, whereby the
discharge pressure from impeller 68 is greater than the discharge
pressure from impeller 64, thereby enabling pump 60 to satisfy the
pressure requirements of a high pressure generator as may be found
in a two-stage absorption machine. At the same time, the size of
the impellers 64 and 68 remains compatable with impellers 62 and 65
so that the entire pump assembly can be driven by a single motor.
Conduit 115 is in fluid communication with the narrower upper
portion of discharge passageway 122, and terminates in valve 117
which functions in the same manner as the other vent valves such as
valves 112 and 119 previously described.
An electric motor 130 may be mounted at end of shaft 99 which
protrudes beyond the pump housing. It is desired to route lubricant
from the motor lubrication system through chamber 125 to bearing 97
for lubrication thereof. Seal 127 is provided between bearing 97
and inlet portion 108.
While the invention has been described in considerable detail, it
will be understood that such detail is for the purpose of
illustration and not by way of limitation, and that the scope of
the invention is delineated in the appended claims.
* * * * *