U.S. patent number 3,591,946 [Application Number 04/779,074] was granted by the patent office on 1971-07-13 for fluid-degassing system.
This patent grant is currently assigned to Loe Industries. Invention is credited to Wallace Dawson Loe.
United States Patent |
3,591,946 |
Loe |
July 13, 1971 |
FLUID-DEGASSING SYSTEM
Abstract
The system removes gases and moisture from dielectric fluids
such as, for example, insulating oils normally used to provide
electrical insulation between electrical components in a tank
filled with such dielectric fluid. Degassing occurs in a treatment
reservoir into which the fluid is initially introduced and such
degassing is accomplished using a combination of vacuum and
ultrasonic vibration and also, in some instances, the fluid may be
heated in the reservoir to a sufficiently high temperature to
assure efficient liberation of moisture from the fluids. Special
valving and connections between the treatment reservoir, the
aforementioned tank and a supply container provides versatility and
transfer of fluids under optimum conditions. For example, the fluid
may be first introduced into the treatment reservoir from a supply
container and then after treatment in the reservoir be transferred
to the tank wherein the same serves as an insulating medium for
electronic equipment; alternatively the fluid already in the tank
may be treated by causing the same to enter the treatment reservoir
for treatment after which the fluid is returned to such tank.
Inventors: |
Loe; Wallace Dawson (Lakeside,
CA) |
Assignee: |
Loe Industries (N/A)
|
Family
ID: |
25115241 |
Appl.
No.: |
04/779,074 |
Filed: |
November 26, 1968 |
Current U.S.
Class: |
96/175; 96/193;
96/201 |
Current CPC
Class: |
B01D
19/0078 (20130101); B01D 19/0068 (20130101); B08B
3/12 (20130101); B08B 2203/002 (20130101) |
Current International
Class: |
B01D
19/00 (20060101); B08B 3/12 (20060101); B01d
019/00 () |
Field of
Search: |
;55/15,33,55,40,43,159,178,189,190,195,277 ;174/14 ;208/184
;336/58 |
References Cited
[Referenced By]
U.S. Patent Documents
Foreign Patent Documents
Primary Examiner: Zaharna; Samih N.
Assistant Examiner: Burks; R. W.
Claims
I claim:
1. Apparatus for treatment of fluids including a fluid treatment
chamber, said chamber having a vacuum port located near the top of
said chamber; said chamber having a fluid port located near the
bottom of said chamber; an air line; first conduit-connecting
means; means for communicating said air line with said first
conduit-connecting means; second conduit-connecting means; means
for communicating said fluid port with said second
conduit-connecting means; said first conduit-connecting means and
said second conduit-connecting means being connectable to a fluid
tank; vacuum-producing means; means communicating said
vacuum-producing means with said vacuum port; first valve means in
said means communicating said vacuum-producing means with said
vacuum port; second valve means connected between said air line and
said vacuum-producing means and operable to intercommunicate said
air line with said vacuum-producing means; third valve means in
said means for communicating said fluid port with said second
conduit connecting means; additional means for communicating the
bottom of said chamber with said second conduit-connecting means;
check valve means in said additional means for preventing fluid
flow from said second conduit-connecting means to the bottom of
said chamber but allowing fluid flow from the bottom of said
chamber to said second conduit-connecting means; and means
associated with said chamber for degassing fluids contained
therein, an enlarged transparent conduit in said means
communicating said air line with said first conduit-connecting
means for serving as an overflow; said transparent conduit having
one of its ends connected to said first conduit-connecting means
and the other one of its ends connected to said air line; said
vacuum-producing means including a vacuum pump having a vacuum port
and a discharge port, said pump vacuum port being connectable with
said chamber vacuum port; valve means connected between said pump
discharge pump and said transparent conduit for communicating said
pump discharge port either to the atmosphere or to that side of the
transparent conduit which is connected to said air line; and
additional valve means for intercommunicating the top of said
chamber with said airline.
2. Apparatus as set forth in claim 1 including a third
conduit-connecting means for connection to a supply container,
additional valve means the last mentioned valve means having one of
its sides connected to said third conduit-connecting means and the
other of its sides in communication with said means communicating
said second conduit-connecting means with the bottom of said
chamber.
3. Apparatus for treatment of fluids including: a fluid treatment
chamber; first conduit-connecting means; second conduit-connecting
means; said first and second conduit-connecting means being
connectable respectively to the top and bottom of a fluid tank;
third conduit-connecting means for connection to a fluid supply
container; valve means for communicating said third conduit
connecting means with the bottom of said chamber; an air line;
means communicating said air line with said first
conduit-connecting means, means communicating the bottom of said
chamber with said second conduit-connecting means; vacuum-producing
means; valve means for communicating said vacuum-producing means
with the top of said chamber; valve means for intercommunicating
said vacuum-producing means with said first conduit-connecting
means; and valve means for communicating the top of said chamber
with said air line; and valve means in said means communicating
said air line with said first conduit-connecting means, an enlarged
transparent conduit in said means communicating said air line with
said first conduit-connecting means; said vacuum-producing means
comprising a pump having a vacuum port and a discharge port; valve
means connected between said vacuum port and the top of said
chamber for communicating said vacuum port with said top of said
chamber; valve means connected between said vacuum port and said
air line for communicating said port with said air line; said
transparent conduit having a first end thereof connected to said
first conduit-connecting means; and valve means connected between
said discharge port and said transparent conduit for connecting
said discharge port to either the atmosphere or to the other side
of said transparent conduit.
4. Apparatus as set forth in claim 3 in which said means
communicating said second conduit-connecting means with the port of
said chamber includes a check valve for preventing flow in a
direction from the second conduit-connecting means to said chamber;
and additional valve means for communicating said second
conduit-connecting means with the bottom of said chamber.
5. Apparatus as set forth in claim 2 in which said fluid treatment
chamber includes a pair of spaced transparent sidewalls and a
bottom and a top; a light source adjacent one of said walls; liquid
level indicating means on the other of said walls; and means
coupled to said bottom for transmitting ultrasonic vibrations to
the fluid in said chamber for the formation of gas bubbles.
6. Apparatus as set forth in claim 2 including fluid filter means
through which fluid flows into said chamber either when fluid is
transferred from said tank or from said supply container.
Description
The present invention relates to the improved means and techniques
for degassing dielectric fluids.
Briefly, dielectric fluids initially supplied in a supply container
42 may be transferred to a tank 40 in which they are ultimately
used as an insulating medium after being treated in a treatment
reservoir 10 under vacuum and ultrasonic vibration. Special valving
and conduits interconnected with a vacuum pump 62 provide optimum
fluid transfer under ideal conditions such as, for example, the
fluid is not contaminated by atmosphere during its transfer from
the treatment reservoir 10 to the tank 40 in which it is ultimately
used.
The term "degassing" has reference also to the removal of moisture
under those conditions wherein, for example, the fluid is heated to
condition the moisture for removal by vacuum.
An object of the present invention is to provide improved means and
techniques whereby dielectric fluids are degassed and transferred
under optimum conditions.
A specific object of the present invention is to provide a system
of this character in which a tank for dielectric fluids may be
filled with such fluids either from an original supply container or
by the dielectric fluid which was once in the tank and which
required degassing.
The features of the present invention which are believed to be
novel are set forth with particularity in the appended claims. This
invention itself, both as to its organization and manner of
operation, together with further objects and advantages thereof,
may be best understood by reference to the following description
taken in connection with the accompanying drawings in which:
The single FIGURE of the drawing illustrates in schematic form the
hydraulic and electrical equipment embodied in the present
system.
The dielectric fluid is treated in a reservoir 10 referred to
herein as a fluid treatment chamber, to which a vacuum may be
applied via line 12 simultaneously with the application of
ultrasonic vibrations produced by three ultrasonic transducers 14,
16, and 18 acoustically coupled to the bottom tank wall 20.
The tank 10 may be of rectangular construction with windows 21 and
22 in opposite end walls of the same such that the light from a
long light bulb 24 may pass, in turn, through the window 21,
through the fluid F in tank 10, through the opposite window 22 and
glass sight gauge 26. The general purpose of this optical
arrangement is to allow a person to observe the fluid level in tank
10 and also to observe the gas bubbles being formed at or near the
bottom of the tank 10 and rising upwardly for removal by vacuum
applied to the vacuum line 12.
The transducers 14, 16 and 18 are supplied with ultrasonic current
from the source 30 which is effective when the on-off switch 32 is
closed to apply the energizing voltage 34 to source 30. The
energizing source 34 has been shown as a DC source but, of course,
this showing is diagrammatic and the source may be an AC or a DC
rectified source.
The tank 10 is connectable in a special manner to a fluid tank 40
or to a supply container 42 through corresponding fittings or
conduit-connecting means 44, 46 and 47. Actually, in practice, the
apparatus located between the fittings 44, 46 on the one hand and
47 on the other hand, is mounted as a separate unit so as to be
mobile and be connectable to the tank 40 and/or supply container
42. For purposes of the present description, it will be assumed
that the tank 40 has its inlet and outlet 40A, 40B respectively
connected to fittings 44 and 46 herein referred to as
conduit-connecting means and that the supply container 42 has its
outlet 42A connected to the fitting 47. The tank 40 is
representative of any container or housing of electronic equipment
in which there is also present a dielectric fluid within which the
electronic equipment is immersed for insulation purposes. The fluid
in container 42 may either be new fluid as originally supplied by a
manufacturer or fluid reconditioned as described herein.
Fitting 47 is connected to the inlet 10A referred to herein as a
fluid port, of tank 10 via valve 50 and a filter 52 such that fluid
may enter the tank 10 through the fill line 54, valve 50, line 56,
line 58, filter 52 and line 60. During such filling operation the
tank 10 may be evacuated using an electrically driven vacuum pump
or vacuum-producing means, 62 which has its suction line 64
extending from vacuum port 62A, connectable to the tank opening 10B
referred to herein as a vacuum port, via line 66, valve 68 and line
70. The pump 62 may have its pressure line 72 extending from
discharge port 62B vented to the vent line 76 via check valve 78,
line 80 and the two-position, three-way valve 82 which is
illustrated in its vent position. As illustrated, line 80
terminates at a stationary port 80A and vent line 76 terminates at
a stationary point 76A and the two ports 76A and 80A are
communicated by the L-shaped channel 84A in the movable or
rotatable valve member 84. The valve member 84 is rotatable from
its position shown in the drawings to a position 180.degree. with
respect to the same where the port 80A may then be placed in
communication with a stationary port 88A leading to a line 88 whose
function is later described.
The previously mentioned vacuum pump 62 may be operated by closing
the on-off switch 90 to thereby apply current from the energizing
source 92 to the electrically driven pump 62.
Using the arrangement previously described, it will be seen that
the reservoir 10 may be filled with fluid from container 42 by (1)
connecting the supply container 42 to the reservoir fill line 54,
(2) operating the valve 82 to its vent position shown in the
drawings, (3) opening valves 50 and 68, (4) operating the vacuum
pump 62 by closing switch 90. During this filling operation the
readings on the vacuum gauges 93 and 95 may be observed and checked
to reassure that, for example, a vacuum pressure of 21 inches of
mercury pressure exists in lines 66 and 70, the gauge 93 being
connected to line 66 and the gauge 95 being connected to line 70.
Also during this filling operation the liquid level in the tank may
be continuously observed through the glass sight gauge 26 and when
the fluid level reaches a desired amount, which may, for example,
be somewhat less than 5 gallons valves 50 and 68 are then closed
and the vacuum pump 62 may be deenergized by opening switch 90.
Thus in this condition the treatment reservoir 10 is filled and in
condition for degassing.
The fluid degassing process involves the following steps,
namely:
1. energization of the sonic energy generator 30 by closing switch
32,
2. operating the vacuum pump 62 by closing switch 90,
3. opening valve 68, the valve 82 being still in its vent position
illustrated in the drawings,
4. the vacuum and sonic energy is thus supplied for a duration of
approximately 30 minutes after which,
5. the valve 68 is closed and the switches 90 and 32 are then
opened in that order.
The next operation involves the transferring of the treated fluid
from the reservoir 10 to the module or tank 40. This involves
apparatus in addition to that previously described and in general
valves 100, 102, 104, gauge 106 and overflow tube 108, and a vent
line or air line 110 which is in communication with the atmosphere
through an air filter 112. One side of valve 100 is connected to
tank opening 10C via line 111 and the other side of valve 100 is
connected to the vent line 110. Valve 102 has one side thereof
connected to vacuum line 66 and the other side of valve 102 is
connected to line 114. A fixed orifice or restrictor 120 is
interposed between vent line 110 and line 114. The pressure in line
114 may be monitored by the vacuum gauge 106 which is connected to
line 114. Valve 104 has one side thereof connected to line 114 and
the other side connected to the overflow tube 108 via line 124. The
other end of overflow tube 108 is connected to fitting 46.
Thus with the equipment described above flow is transferred from
the treatment reservoir 10 to the module or tank 40 in accordance
with the following procedure:
1. The fluid inlet tank opening 40A is connected to the fitting 44
and the tank outlet 40B is connected to the other fitting 46,
2. the valve 100 is slowly opened until the reading on vacuum gauge
95 begins to drop in which case air enters solely through the
filter 112, the valve 100 being opened slowly to prevent breaking
of surface tension of the fluid in reservoir 10 and when the gauge
95 reads substantially zero the valve 100 is fully opened, and
then
3. valves 102 and 104 are opened to thereby communicate the vacuum
line 66 with the upper end of tank 40, valve 100 still remaining
open, and then
4. switch 90 is close to operate the vacuum pump 62, then
5. the readings on gauges 95 and 106 are compared in which case the
reading on gauge 95 may be in the range of 0 to 1 inch of mercury
pressure whereas the reading on gauge 106 may be in the order of 8
inch of mercury pressure, this difference in pressure being caused
by the pressure drop across the fixed orifice 120, and this
pressure drop is an indication that fluid is being drawn through
the tank opening 10D and check valve 130 and fitting 44 to the
fluid tank inlet 40A, and
6. the overflow tube 108 which is of clear glass is observed and
when such tube 108 begins to fill the module or tank 40 is
completely full and thus the overflow tube condition serves as an
indication that the valves 102, 100 and 104 should be quickly
closed in that order followed by a deenergization of the vacuum
pump by opening switch 90.
It will be noted from the foregoing operation in which fluid is
transferred to the module 40 that fluid enters the tube 108 and the
next step described below involves the evacuation of the vacuum
line and overflow tube 108 which is essentially a transparent
conduit. This is accomplished in the following sequence,
namely:
1. the flexible fluid line 140 and flexible vacuum line 142 are
disconnected from the tank 40 and the flexible vacuum line 142 is
extended into a waste container, and then
2. valves 68 and 100 are opened, and then
3. valve 82 is operated to its other position to the so-called
"pressure" position wherein ports 80A and 88A are interconnected by
the L-shaped channel 84A thereby placing the line 124 in
communication with the vacuum pump pressure line 72 via check valve
78, and then
4. the vacuum pump switch 90 is closed in which case this causes
air to flow through filter 112, valve 100 and through opening 10C
to the top side of the reservoir 10, i.e. the vacuum side of the
pump, through line 72 and through the check valve 78 and through
line 82 to force all residual fluid out of the overflow tube 108
and into the waste container, and then
5. after all fluid has thus been blown out of the overflow tube 108
and vacuum hose 142, the valve 82 is moved to its "vent" position
illustrated in the drawings, and then the vacuum pump switch 90 is
opened and then valves 68 and 100 are closed.
The apparatus described also allows transfer of fluid from the
module or tank 40 to the degassing unit or reservoir 10 and this is
accomplished in the following sequence, namely:
1. The vacuum lines 142 and inlet line 140 are connected to the
tank 40 and then
2. valves 68, 104 and valve 200 are opened, the valve 200 having
one of its sides connected to the fluid line fitting 44 and the
other one of its sides connected to the previously mentioned line
56 and 58. At this stage it will be observed that the opening of
valve 68 places the top side of reservoir 10 in communication with
the vacuum line 66, but the opening of valve 104 allows the topside
of the module or tank 40 to be vented to the atmosphere through the
orifice 120 and vent line 110 and filter 112, and that the opening
of valve 200 places the tank inlet 40A in communication with the
inlet side of the filter 52 through which fluid may then flow into
the bottom of tank 10 through opening 10A, and then
3. the vacuum pump switch 90 is closed, and then
4. the differential reading between gauges 106 and 95 is observed
in which case the gauge 106 may read 7 inches to 8 inches of
mercury pressure, whereas the gauge 95 may read 20 inches to 21
inches of mercury pressure, and then
5. the interior of reservoir 10 is observed for the appearance of
large bubbles which do appear when the module 40 is completely
empty. Of course, the capacity of the reservoir 10 is greater than
the capacity of the tank 40, and then
6. valves 68, 104 and 200 are closed in that order after which the
vacuum pump switch 90 is opened.
It is noted that in the foregoing description of the five
operations it was assumed, as is the case, that all valves are
originally closed and that all valves, with the exception of valve
82, are on-off valves and that valve 82 as previously described
either communicates line 80 to the atmosphere or to line 88.
Further, valve 82 is operated only during the operation in which
fluid is removed from overflow tube 108, and even in that case
valve 82 is initially in the vent position and after that operation
is restored to its vent position.
Thus, it will be seen from the foregoing that fluid introduced from
supply container 42 may be treated in reservoir 10 and then
discharged into the module or tank 40. Alternatively, fluid in the
module or tank 40 may be introduced into the reservoir 10 where it
is treated and then returned to the tank 40. In each case the fluid
is transferred under vacuum conditions and without opportunity for
the oil to be contaminated by ambient atmosphere.
While the particular embodiments of the present invention have been
shown and described, it will be obvious to those skilled in the art
that changes and modifications may be made without departing from
the invention in its broader aspects and, therefore, the aim in the
appended claims is to cover all such changes and modifications as
fall within the true spirit and scope of this invention.
* * * * *