[0001] The invention relates to a hydraulically powered compressor, and hydraulic control
and power svstem therefor, for elevating the pressure of
qaseous substances, wherein infinitely variable ca
pacitv control is provided.
[0002] Prior art compressors for compressing qaseous substances (such as air, nitroaen or
methane) all suffer from one major disadvantage. Such prior art compressors do not
provide infinitely variable capacity control with a proportionately variable horsepower
requirement. Such prior art compressors have attempted to alleviate this disadvantage
by utilizing various means of capacitv control such as valve unloaders or variable
or fixed volume pockets. These types of capacity controls are limited in range. Valve
unloaders provide large capacity changes or capacity "spikes". Compressors driven
by reciprocating enaines or turbines provide smooth capacity control over a portion
of the speed range of the engine or turbine, but the engine or turbine cannot normally
be used to operate the compressor when the speed of the engine or turbine falls below
50% of its maximum speed. Below 50% speed these units must use a bypass valve which
bypasses the excess capacity not reauired. This process is extremely inefficient because
the horsepower required does not change. This inefficiency becomes more of a factor
on constant speed compressors with no unloaders or pockets installed.
[0003] In situations such as when a compressor is being utilized to compress and elevate
the pressure of natural gas flowing from a wellhead, the flow conditions of the gas
which is entering the compressor may vary widely. If small volumes of flowing gas
are entering the compressor, it is necessary for the compressor to operate very slowly
in order to act upon the natural gas to raise it to the desired pressure. Conversly,
if a large volume of natural qas is naturally flowing from the wellhead, the compressor
must operate more quickly to compress the larqer volume of natural gas to the desired
elevated pressure. Thus, it would be very desirable to have a compressor which is
operable at an infinitelv variable speed, so as to be able to be operable over a wide
range of incoming gas flow conditions.
[0004] Other disadvantages associated with prior art compressors are that they are extremely
complicated in their design and manufacture, thus increasing the cost associated with
manufacturing and servicing such compressors. Particularly in the case of compressors
which may be utilized at remote wellhead locations, it is important that the compressor
may be readily serviced and repaired. Further, many prior art compressors provide
coolina for the compressor assembly, which cooling is provided bv a water iacket.
Thus, such compressors reauire a source of water or a closed cooling system in order
to dissipate the heat caused by the compression of the
qaseous substance. Such a water source may be unavailable at many remote locations.
Additionally, such compressors require additional components, such as water pumps
which are readily susceptible to maintenance problems.
[0005] Accordingly, prior to the development of the present invention, there has been no
hvdraulicallv powered compressor or hydraulic control and power system therefor, which:
provides infinitely variable capacity control with a proportionately variable horsepower
requirement; is efficient and economical in its design; is readily serviced and repaired;
and does not require water cooling. Therefore, the art has sought a hydraulically
powered compressor, and hydraulic control and power system therefor, which: provides
infinitely variable capacity control; is efficiently and economically manufactured;
is easily readily repaired and serviced; and is air cooled.
[0006] In accordance with the invention the foregoing advantages have been achieved through
the present hvdraulicallv powered compressor and hvdraulic control and power system
therefor. The present invention includes: a first double-acting piston and compression
cylinder for initially compressinq the qaseous substance; second double- actinq piston
and compressor cylinder for additional compression of the gaseous substance; a hydraulic
power piston and cylinder disposed between the first and second double-acting pistons
and cylinders; the first and second double-acting pistons and the hydraulic powered
piston each being disposed on a common elongate piston rod; first piping for transferring
the compressed gaseous substance from the first piston and compression cylinder to
the second piston and compression cylinder; second nipin
q for transferring the compressed gaseous substance from the second piston and compression
cylinder to an exit orifice; first and second cooling coils respectively associated
with the first and second piping for cooling the compressed gaseous substance; means
for forcing air to flow over the first and second cooling coils; the first and second
pistons and compression cylinders, power piston and cylinder, first and second piping,
first and second colling coils, and air forcing means, all being disposed within an
air-cooling duct to provide coolina thereto; and means for providing infinitely variable
capacitv control for the first and second pistons and compression cvlinders, the capacity
control means including a variable displacement hydraulic pump for actuatinq the hydraulic
power piston and cylinder, whereby the first and second pistons and compression cylinders
may be operated over a range of 0 to 100% of their capacity, with a proportionately
variable power requirement.
[0007] Another feature of the present invention is that the means for forcing air includes
a fan and a hydraulic motor therefor, the motor having a pressure regulatinq valve,
and a pressure compensated flow control valve associated therewith, and the flow control
valve is associated and disposed between the variable displacement hydraulic pump
and the motor, whereby the fan operates at a constant speed to provide cooling to
the first and second coolina coils, first and second pistons and cylinders and hydraulic
power piston and cylinder and to blow out of the air cooling duct any accumulated
gaseous substances. An additional feature of the present invention is that a cooling
chamber is provided between the hydraulic power piston and cylinder and each of the
first and second pistons and cylinders, each cooling chamber surrounding a portion
of the piston rod and including means for directing air flow from the means from forcing
air over the piston rod.
[0008] A further feature of the present invention is that the first and second pistons and
compression cylinders and hydraulic power piston and cylinder are disposed on a mounting
plate by means of two mountinq bolts, whereby transmission of stress forces to the
compression cylinders and power cylinder from the mountina plate deflection is qreatlv
minimized. An additional feature of the present invention is that the first and second
pistons are threadedlv affixed in a first direction to the piston rod and are secured
to the piston rod by a locking member which is threaded into the piston rod in a second
opposite direction.
[0009] The present invention further includes a hydraulic control and power system for a
compressor for qaseous substances which compressor has first and second double-acting
pistons and compression cylinders and a reciprocating hydraulic power piston and cylinder
for actuating the first and second pistons, which includes: a variable displacement
hydraulic pump for providing hydraulic fluid to the power piston and cylinder to reciprocate
the power piston within its cvlinder; a shuttle valve for alternatinq the flow of
hydraulic fluid from the pump into and out of the ends of the hydraulic power piston
cylinder; a cam-operated, spring loaded check valve associated with each end of the
power piston cylinder, the check valves beina actuated by the reciprocating motion
of the power piston to discharge hydraulic fluid from the respective end of a pilot
valve; a pilot valve for actuating the shuttle valve in response to a pressure differential
caused bv the discharqe of hydraulic fluid through one of the cam-operated, spring
loaded check valves; a hydraulic fluid reservoir, and hydraulic fluid pi
pina operatively associating the pump, shuttle valve, check valves, pilot valve, and
resevoir with one another, whereby upon varving the displacement of the pump, the
speed of reciprocation of the power piston is varied.
[0010] A further feature of the present invention is that a flow control valve may be operatively
associated with each end of the shuttle valve to throttle the hydraulic fluid flowing
from the pilot valve to either end of the shuttle valve, whereby the reciprocatinq
speed of the shuttle valve is controlled and hydraulic shocks caused by the shuttle
valve reciprocating too quickly are controlled. An additional feature of the present
invention is that the ball check valves and fluid control valves may he each operatively
associated with needle valves for creatina a pressure differential to reciprocate
the pilot valve.
[0011] A pressure regulator is installed to reaulate pump discharge pressure down to a lower
level for the control system. This regulator also controls fan speed by reducing pressure
to the fan motor. Regulation of the control system pressure assures uniform response
times on all needle valves in the control system as the pressure differential across
these valves is maintained constant regardless of the pump pressure.
[0012] An additional feature of the present invention is that a pressure relief valve may
be operatively associated with the pump, whereby an excessive pressure build-up within
the piping or either compression cylinder is safely relieved. Another feature of the
present invention is that a pressure compensated flow control valve and distribution
block may be operatively associated with the pump and piping to provide lubricating
hydraulic fluid to the compression cylinders and piston rod for the double-acting
piston.
[0013] The hydraulically powered compressor, and hydraulic control and power system therefor,
of the present invention, when compared with previously prior art compressors has
the advantages: of providing infinitelv variable capacity control with directly associated
horsepower requirements; is efficientlv and economically manufactured; is readily
repaired and serviced; and provides air cooling of the various components of the compressor.
Brief Description of the Drawings
[0014] In the drawings:
FIG. 1 is a partial cross-sectional view along the longitudinal axis of a compressor
in accordance with the present invention;
FIG. 2 is an enlarged, partial cross-sectional view alona the axis of a compressor
in accordance with the present invention;
FIG. 3 is a schematic hydraulic flow diagram of an exemplarv hydraulic control and
power system in accordance with the present invention;
FIG. 4 is a schematic flow diagram of the gaseous substance to be compressed in accordance
with the present invention; and
FIG. 5 is a schematic like FIG. 3 only showinq an alternative embodiment of a hydraulic
control and power system according to the present invention.
[0015] While the invention will be described in connection with the preferred embodiment,
it will be understood that it is not intended to limit the invention to that embodiment.
On the contrary, it is intended to cover all alternatives, modifications, and equivalents
as may be included within the spirit and scope of the invention as defined by the
appended claims.
Detailed Description of the Invention
[0016] In FIG. 1, the hydraulically powered compressor 51 of the present invention for elevating
the pressure of gaseous substances, such as air, nitroqen, or methane is shown. Compressor
51 qeneraly includes a first double-acting piston 52 and compression cylinder 53 which
initially compress the qaseous substances (not shown), as will be hereinafter described;
a second double-acting piston 54 and compression cylinder 55 which provide the second
stage of compression, as will be hereinafter described; and a hydraulic power piston
56 and cylinder 57, which power piston 56 and cylinder 57 are disposed between the
first and second double-acting pistons 52, 54 and cylinders 53, 55. As seen in FIG.
I, the first and second double-acting pistons 52, 54 and the hydraulic power piston
56 are each mounted upon a common elongate piston rod 58, wherebv the longitudinal
axes of the cylinders 53, 55, 57, are aligned axially. The foregoing described components
of compressor 51 may be manufactured of any suitable material having the requisite
strength characteristics; however, for ease of assembly and economy in manufacture,
cylinders 53, 55, and 57 are preferably manufactured from commercially available drawn-over
mandrel steel tubing, which is readily and economically available. As is customary
in the design of two- staqe compressors, the diameter of the second compression cylinder
55 is smaller than that of the first compression cylinder 53, in order to provide
for the second stage of compression of the gaseous substance. Of course, if desired,
the diameter of the second compression cylinder 55 could be the same as the diameter
of the first compression cylinder 53, in order to provide a one-stage compressor.
Suitable piping connections would be provided whereby the inlet gaseous substance
enters both cylinders simultaneously via a common inlet manifold and the compressed
gas exits into a common discharge manifold into the coolinq means to be hereinafter
described. Likewise, by use of steeple design cylinders, up to four stages of compression
could be obtained.
[0017] Still with reference to FIG. 1, it is seen that compressor 51 of the present invention
also aenerallv includes first piping 59 (for ease of illustration, shown in dotted
lines) for transferring compressed
qas from the first piston and compression cylinder 52, 53 to the second piston and
compression cylinder 54, 55. Second piping 60 (also shown in dotted lines for ease
of illustration) is provided for transferring compressed gas from the second piston
and compression cylinder 54, 55 to an exit orifice, shown generally at 6]. It should
be understood that upon the
qaseous substance being compressed and elevated to an increased pressure, the gaseous
substance exiting compressor 51 at exit orifice 61 may be piped to whatever location
and/or use is desired, such as a storage tank, or pipe line, etc.
[0018] With reference to F
IG. 1, it is seen that there are first and second cooling coils 62, 63 associated with
the first and second piping 59, 60 for cooling the compressed gaseous substance. As
seen in FIG. 1, first cooling coil, or intercooler, 62 is disposed intermediate the
ends of first piping 59, and the second cooling coils, or aftercooler, 63 is disposed
intermediate the ends of second piping 60. Compressor 51 is further provided with
a means for forcina 64 air to flow over the first and second cooling coils 62, 63.
Preferablv the means for forcing air 64 includes a plurality of fan blades 65, which
are rotated by a hydraulic motor 66. Of course, additional cooling coils could be
provided, if necessary, as well as a thermostat to control the operation of the fan
dependent upon ambient temperatures. As seen in FIG. 1, the first and second pistons
and compression cylinders 52-55, power piston and cylinder 56, 57, first and second
piping 59, 60, first and second cooling coils 62, 63, and air forcing means 64 are
preferably disposed within an air-cooling duct 67, which extends the len
qth of compressor 51. Air-cooling duct.67 may be manufactured of any suitable material,
such as sheet metal, and may have any suitable cross-sectional configuration, such
as circular, U-shaped or square, etc., so long as it serves to confine the air flow
generated by air forcing means 64 to pass across coolinq coils 62 and 63 and the other
components of compressor 51. Should any leaks develop in compressor 51, the constant
air flow from fan blades 65 will exhaust any accumulation of gas.
[0019] Air-cooling duct 67 also serves the function of protecting the various components
of compressor 51 from the elements and adverse environmental conditions. Thus, upon
hydraulic fluid beina supplied to hydraulic motor 66 of air forcing means 64, fan
blades 65 will be caused to rotate and will suck air into air-cooling duct 67, which
air will pass over cooling coils 62 and 63, as well as pass from right to left as
shown in FIG. 1, down air-cooling duct 67 over all of the other components of compressor
51. Thus, as gas which has been compressed in the first staqe piston and compression
cylinder 52, 53 passes down piping 59 to intercooler 62, air flow from fan blades
65 will dissipate the heat in the gas caused by its compression thereof as the gas
flows through intercooler 62 and aftercooler 63. A coolinq coil for the hydraulic
oil may also be installed in air coolina duct 67 to reduce the hydraulic oil operatino
temperature if required.
[0020] With reference to FIGS. 1 and 2, it is seen that compressor 51 is provided with cooling
chambers 68, 69. Cooling chamber 68, with particular reference to FIG. 2, is disposed
between first-stage piston and cylinder 52, 53 and hydraulic power piston and cylinder
56, 57; and cooling chamber 69 is disposed between hydraulic power piston and cylinder
56, 57 and second stage piston and cylinder 54, 55. The coolinq chambers 68, 69 each
surround a portion of piston rod 58 and include means for directing to air flow, from
the means for forcing air 64, over piston rod 58. Preferably, the means for directing
air flow 70 comprises a pipe elbow, or duct, 71, which directs air from fan blades
65 to flow inwardly into cooling chambers 68 and 69. Cooling chambers 68, 69 each
have suitable openings (not shown) to allow the air from ducts 71 to be vented out
of the cooling chambers 68, 69. Thus, additional heat generated during operation of
compressor 51 may be dissipated via convection in coolinq chambers 68, 69.
[0021] Still with reference to FIGS. 1 and 2, it is seen that each cvlinder 53, 55 and 57,
is provided with first and second cylinder header members. First stage cylinder 53
is provided with first and second header members 72, 73; hydraulic cylinder 57 is
provided with first and second header members 74, 75; and second stage compression
cylinder 55 is provided with first and second header members 76, 77. Each set of header
members and compression cylinders 72, 73, 53; 74, 75, 57; and 76, 77, and 55, are
held together by a plurality of elongate tie rods (not shown for clarity of illustration
purposes) whereby the various components of compressor 51 may be readily assembled
and disassembled for servicing. As shown in detail in FIG. 2, each cylinder end is
sealed against its respective header members by an 0-ring seal 50 which contacts the
inner surface of each cylinder. Accordingly, the amount of surface area of each header
member upon which gas pressure acts upon is reduced, whereby the stresses on the connecting
tie rods for each set of header members is likewise reduced.
[0022] With reference to FIGS. 1 and 2, it is seen that coolinq chambers 68, 69 are formed
by an outer housinq member 78, 78' and header members 79, 79'. Fousinqs 7R, 78' may
have any cross-sectional configuration; however, housing members 78, 78' preferably
have a circular cross-sectional confiquration. Housing member 78 is received into
header member 73 as by groove 80, as seen in FIG. 2, and is received into header member
79 as shown at 81. The construction of housing member 78' and header member 79' is
the same as that previously described for housing member 78 and header member 79.
Further with reference to FIGS. 1 and 2, it is seen that header members 79, 79' are
attached to header members 74, 75 of power cylinder 57, as by a pluralitv of bolts,
or tie rods, 82.
[0023] Still with reference to FIGS. 1 and 2, it is seen that all the previously described
components of compressor 51 are disposed upon a mounting plate 83 which rests upon
the earth's surface 84 or any other suitable structure, such as a portable skid. Air
forcing means 64 is fixedly secured to mounting plate 83 as by a vertical brace 85,
and cooling coils 62, 63 are provided with any suitable base members 86 which are
secured to mountinq plate 83 in any conventional manner. The first stage piston and
cylinder 52, 53, second stage piston and cylinder 54, 55, and the hydraulic power
piston and cylinder 56, 57 are disposed on mounting plate 83 via two bolts 87, 88
which pass through depending flanges 89, 90 affixed to housing members 78, 78' of
cooling chambers 68, 69, which flanges 89, 90 are received in mounting lugs 91 and
92 secured to mounting plate 83. Accordingly, the foregoing compressor components
of compressor 51 have a two-point mounting system, whereby transmission of stress
forces to the compression cylinders 53, 55 and power cylinder 57 from the mounting
plate 83 is greatly minimized. This two-point mounting system allows a certain amount
of flexinq and movement between the various components of compressor 51, which is
not detrimental to the operation of compressor 51, and provides for a verv simple,
economical, and efficient system for mounting the various components of compressor
51 to mountinq plate 83.
[0024] As shown in FIG. 1, and particularly in FIG. 2, both the first stage cylinder 53
and second stage cvlinder 55 are sealed where piston rod 58 ; enters cylinders 53
and 55. A rod packing 93 is provided in header member 73, and an identical rod packing
94 is provided in header member 76. Header members 73 and 76 are each provided with
a lubrication connection passageway, or duct 95, 96 which are in fluid transmitting
relationship to rod packings 93 and 94 to lubricate the packings 93 and 94 and the
packinct housing which also support the piston rod 58. The transmission of the hydraulic,
lubrication fluid throuqh ducts 95, 96 will be hereinafter described with reference
to FIG. 3.
[0025] With reference to FIG. 1, the construction of the first and second stage pistons
52, and 54 will be described. Pistons 52 and 54 are sealed a
qainst the interior surface of cylinders 53, 55 by ) a plurality of polytetrafluoroethylene
(PTFE) piston rings 97 which are mounted in a plurality of groove 98 formed in the
outer surface of pistons 52, 54. The PTFE rings 97 support pistons 52 and 54 within
cylinders 53, 55, whereby the outer surface of pistons 52, 54 do not contact the interior
surface of cylinders 53, 55. Accordingly, pistons 52 and 54 may be reciprocated within
the cylinders 53, 55 without any lubrication being provided to cylinders 53, 55. If
compressor 51 is being utilized to compress and elevate the pressure of certain types
of wet gaseous substances, wherein lubrication is desired within the first and second
stage pistons and cylinder-52-55, hydraulic lubricating oil can be provided via lubrication
connections 99 for cylinder 53 and 100 for cylinder 55. Suitable piping (not shown)
is provided for transmitting the hydraulic fluid to the lubrication connections 99,
100, as will he hereinafter described with regard to FIG. 3.
[0026] An important safetv feature of the present invention is that pistons 52, 54 are fixedly
secured to piston rod 58 as by a threaded connection 101 (for ease of description,
the threaded connection for piston 52 is illustrated and it is identical to that utilized
for piston 54). Peferably, threaded connection 101 has a first thread direction, preferably
as by right-hand threads. A locking member, or socket head cap screw, 102 is threadedly
received into the outer surface of piston 52 until it enga
qes the end of piston rod 58. Locking member 102 is threaded through piston 52 into
piston rod 58 in a second opposite direction. Locking member 102 and its mating surface
in piston 52 is preferably provided with left-hand threads. Accordingly, the possibility
of the pistons 52, 54 becoming disengaged from piston rod 58 from vibrational forces
is areatlv reduced. Since severe damage to compressor 51 and/or personnel in the vicinity
of compressor 51 can result when a piston comes loose from piston rod 58, the safety
aspects of compressor 51 are greatly enhanced.
[0027] Hvdraulic power piston 56 is likewise provided with suitable seals 103 disposed in
grooves in the outer surface of piston 56, in a manner similar to pistons 52 and 54.
It should be noted that if no lubrication fluid is fed through lubrication connections
95 and 96 for piston rod packinq 93 and 94, adequate lubrication oil will be supplied
by hydraulic fluid left on piston rod 58 as piston rod 58 reciprocates past the seals
104 for power cylinder 57 disposed in header members 74 and 75.
[0028] With reference to FIGS. 1 and 2, the piping and valving connections for the hydraulic
fluid (not shown) of compressor 51 will be described.
Hvdraulic power piston and cylinder 56, 57 are provided with hydraulic fluid feed and
discharge ports 105 disposed in power cylinder header members 74, 75. Pall check valves
106 and 107 are alternately opened upon power piston 56 being reciprocated within
cylinder 57. With particular reference to FIG. 2, it is seen that power piston 56
includes tubular camminq members 108 and 108' disposed on either side of piston 56.
As piston 56 reciprocates within cylinder 57, camming member 108 will engage and open
cam-operated, spring loaded ball check valve 106, and camming member 108' will likewise
engage and open the other check valve 107, as will be hereinafter described in greater
detail. The opening of the cam-operated check. valves 106, 107 create a pressure differential
to reciprocate pilot valve 133 to be hereinafter described.
[0029] With reference to FIGS. 1 and 4, the flow diagram for the gaseous substance to be
compressed will be described in greater detail. The gaseous substance to be compressed,
which may come from a wellhead, storage tank, etc., may first pass throuqh a conventional,
optional scrubber unit 109, as seen in FIG. 4. From the scrubber unit 109, the gas
passes via pipinq (shown schematically as 110 in F
TG. 4) into the first compressor stage cylinder 53 via inlet manifold 111, which distributes
the gas throuah piping 112 to two inlet ball check valves 113, 114 disposed in header
members 72, 74. Reciprocation of hydraulic power piston 56, as will be hereinafter
described, causes piston 52 to reciprocate within first stage cylinder 53 which alternately
sucks gas throuah inlet check valves 113, 114 and compresses the gas within cylinder
53 on both sides of piston 52. The compressed gas is then discharqed from first cylinder
53 through discharqe check valves 115, 116 which are likewise mounted in header members
72, 73. Discharge check valves 115, 116 feed into piping 117 into discharge manifold
118 and into first piping 59 as previously described. The compressed gas then passes
through intercooler 62 throu
qh first pipino 59 into another optional scrubber unit 119 as shown in FIG. 4. It should
be noted that optional scrubber units 109 and 119 would be disposed outside of air-cooling
duct 67; and would be provided with suitable, conventional piping connections. After
the gas has been first compressed into the first stage, cooled, and then optionally
scrubbed, it passes through first pipina 59 into the second stage inlet manifold 120,
through piping 121, and past second inlet ball check valves 122, 123 and the gas is
compressed within the second sta
qe cylinder 55 in the same manner as occured in the first stage cylinder 53. The aas
is then discharoed through second stage discharge check valves 124, 125 into piping
126 and discharge manifold 127. The compressed gas then passes through second piping
60 into aftercooler 63 and to exit orifice 61, as previously described. It should
be noted that at least one of the compression cylinders 53, 55 may be provided with
a clearance bottle 129 which may be associated with a pipe-tapped opening as at 128
in header 77, whereby the clearance volume of second stage compressor cylinder 55
is variable to provide for balancing compression ratios between the first and second
compression cylinders 53, 55. It should be noted that header 72 of the first stage
compression cylinder 53 may likewise be provided with a similar pipe-tapped opening
such as 128, with a similar clearance bottle 129.
[0030] Turning now to FIG. 3, the hydraulic control and power svstem for compressor 51 will
be described. It should first be noted that the components to be hereinafter described,
with the exception of the hydraulic power piston and cylinder 56, 57, may be disposed
within air-cooling duct 67 if space permits, or may be disposed adjacent to compressor
51 on any suitable base member or skid. In general, the hydraulic control and power
system 103 includes the following components: a variable displacement hydraulic pump
131; a shuttle valve 132; cam-operated, spring loaded check valves 106, 107, as previously
described; hydraulic power piston and cylinder 56, 57, as previously described; pilot
valve 133; hvdraulic fluid reservoir 134; flow control valves 135, 136, operatively
associated with each end of shuttle valve 132; needle valves 137-140; ball check valve
141; manual bypass valve 142; relief valve 143; bladder accumulator 144; pressure
compensated control valves 145, 146; a hydraulic distribution block 147; hydraulic
feed ports 105, as previouslv described; hydraulic fluid filters 148, 149; bladder
accumulator 156; and back pressure control valve 157. Hvdraulic fluid piping as shown
throuahout FIG. 3 is further provided which operatively associates pump 131, shuttle
valve 132, check valves 106, 107, pilot valve 133, resevoir 134, and the other components
of hydraulic control and power system 130 to each others as will be hereinafter described
in greater detail.
[0031] Hydraulic oil 150 is stored in reservoir 134 and is drawn into the variable displacement
hydraulic pump 131 throuqh suction screen 148 and piping 151 upon the actuation or
starting of pump 131. Suction screen 148 serves to prevent any impurities from entering
the hydraulic control and power system 130. Pump 131 is controlled via a control signal
152 being applied to pump actuator head 153. Pump 131 is initially destroked to zero
flow bv venting the control signal 152 operating on actuator head 153. After a period
of warm-up time, the control signal 152 is restored to pump actuator head 153, and
pump 131 increases in stroke in response to the increasing control signal on actuator
head 153. Accordingly, flow of hydraulic fluid 150 through system 130 commences and
the pressure of the hydraulic fluid 150 throughout system 130 increases to the necessary
pressure to overcome the pressure loads on the first stage and second stage pistons
52, 54 due to the presence of a gaseous substance within compression cylinders 53,
55. It should be noted that by increasing the control, or pressure, signal 152 to
pump actuator head 153, presence the flow of hydraulic fluid throughout the hydraulic
control and power system 130 is increased, which in turn increases the cycling, or
reciprocation, speed of power piston 56. This increased speed in turn increases the
capacity, or ability, of compressor 51 to compress increased volumes of inlet gas
with an associated increase in required horsepower. Likewise, by decreasina the pressure,
or control signal, 152 upon pump actuator head 153 the speed of the hvdraulic control
and power svstem 130 is slowed down, which in turn allows compressor 51 to slow down
to accommodate decreased volumes, or a lower capacity, of incominq gas with an associated
increase in required horsepower. Accordingly, the hydraulic control and power system
130 of the present invention allows compressor 51 to operate over an infinitely variable
speed range to provide infinitely variable capacity control of compressor 51. If the
incoming flow and pressure conditions into the first staqe compressor cylinder 53
vary, it is merely necessary to change the control signal to the variable displacement
pump 131 in order to compensate for the changing incoming pressure and flow conditions
of the gaseous substance. The power source for variable displacement pump 131 may
be of anv conventional tvpe, including a constant speed electric motor, a reciprocating
engine, or any other suitable rotatin
q power source. It should be understood that with a variable displacement pump, the
power source speed can remain constant and its horsepower requirements to operate
the pump vary proportionately with the flow of the pump. Thus, when compressor 51
operates upon gas flowing under decreased flow conditions, e.g., a lower capacity,
eneray is conserved because the horsepower requirements from the power source are
likewise proportionately decreased.
[0032] Still with reference to FIG. 3, it is seen that hydraulic fluid 150 exits from variable
displacement pump 131 from its exit orifice as shown at 154 and passes throuqh ball
check valve 141, or other suitable valve. Ball check valve 141 prevents hydraulic
fluid pressure backing up upon pump 131 and from reversing the hydraulic fluid flow
and drainino the hydraulic fluid 150 in the pump 131 when pump 131 is turned off.
It should be noted that pressure relief valve 143, is of conventional manufacture
and protects all the hydraulic components of system 130 from an excessive pressure
build-up within the hydraulic piping or compression cylinders 53, 55, whereby such
excessive pressure build-ups may be safely relieved through relief valve 143. Additionally,
pressure relief valve 143 allows compression cylinders 53 and 55 to have liquid substances
pass therethrouqh without damage to the compression cylinders 53, 55. It is not unusual
for a compressor working upon well head natural gas to have liquids from the wellhead
flowing in the gas stream. This situation is commonly called "liquid slugging", and
such liquid "slugs" flowing in a gas stream into a compressor can cause serious damage
to the compressor cylinders due to the increased pressure build-un when such liquid
"sluqs" enter the compression cylinders.
[0033] As seen in FIG. 3, hydraulic system pressure acts upon the cam-operated, spring loaded
check valves 106, 107 across needle valves 137, 138, whereby check valves 106 and
107 are normally maintained in a closed position until opened by tubular cammina members
108, 108'. Hydraulic power piston 56 moves to the riqht toward ball check valve 107
until the camming member 108' opens ball check valve 107 to release the hydraulic
fluid pressure through hydraulic fluid feed port 105 and header member 75. The openinq
of ball check valve 107 thus vents the hydraulic fluid at the end of pilot valve 133
to the reservoir 134 via piping 155. The venting of hydraulic fluid previously described
creates a pressure differential across four-way pilot valve 133 and thus strokes it
to apply system pressure to the opposite end of the four-way shuttle valve 132. Simultaneously
therewith, the formerly pressurized end of the shuttle valve 132 is vented through
the pilot valve 133 to the reservoir 134, as shown in FIG. 3. The shifting of the
shuttle valve 132 causes hydraulic fluid 150 to be alternately applied to, and exhausted
from, the hydraulic fluid feed ports 105 in headers 74, 75, which cause power piston
56 to reciprocate within cylinder 57. Flow control valves 135 and 136 control the
speed at which the shuttle valve 132 moves by throttling the hydraulic fluid 150 flowing
from the pilot valve 133 to the ends of the shuttle valve 132, whereby hydraulic shocks,
caused by the switching of the shuttle valve 132 too quicly are dampened. It should
be noted that flow control valves similar to valves 135, 136 could also be operatively
associated with the ends of pilot valve 133 to further control the switchinq response
of the hydraulic components of system 130. It should be noted that pilot valve 133,
shuttle valve 132, and flow control valves 135, 136 are conventional, commercially
available valves. Oil exhausted from four-way shuttle valve 132 is discharged in a
pulsating manner. These pulsations which could be harmful to the hydraulic system
components are effectively dampened using accumulator 156 in association with back
pressure control valve 157 assuring lonq system component life. Four-way pilot valve
133 incorporates a mechanical latching mechanism or detent which locks the pilot "valve
spool" 133 in position when system flow is interrupted. Without this feature, the
pilot valve spool 133 could seek a neutral position in the valve body so that compressor
51 could not be started.
[0034] Still with reference to FIG. 3, it is seen that pressure compensated control valve
146 may also be operatively associated with pump 131 to meter hydraulic fluid 150
to distribution block 147. Distribution block 147 thus meters exact volumes of hydraulic
fluid 150, if desired, to the first and second staqe cylinder lubrication connections
99, 100, and to the rod packing lubrications 95, 96. Manual bvpass valve 142 may be
provided to manually unload the pressure in pump 131 if desired. Bladder accumulator
144 mav be also operatively associated with pump 131 and svstem 130 to reduce system
pulsations or pressure shocks when the shuttle valve 132 switches. Bladder accumulator
144 also serves the function of storing and conserving hydraulic energy within system
130 when switching of shuttle valve 132 occurs.
[0035] - As previously described, the motor 66 for fan blade 65 is hydraulically operated,
and its speed is controlled by a pressure compensated flow control valve 145. Once
valve 145 is set to the desired pressure rating, the speed of fan motor 66, and in
turn the rotation of the fan blades 65 will remain constant even though there are
hydraulic system pressure changes in the system 130. In this regard, it should be
noted that the fan speed can be varied by adjusting the pressure compensated control
valve 145 in order to control varyina temperature conditions caused by increased ambient
temperature conditions at the location of compressor 51, or from increased temperature
conditions caused by the imcoming gaseous substance into compressor 51.
[0036] Each of the ball check valves 106 and 107 and fluid control valves 135 and 136 may
be operatively associated with needle valves 137-140 for varving the flow to such
valves to vary the response time of such valves. It should be readily apparent to
one of ordinary skill in the art that two compressors 51 of the present invention
could be connected in series, one along side each other with suitable piping connections
there between, to porovide a four-stage compressor.
[0037] FIG. 5 shows an embodiment similar to that of
FIG. 3, with a somewhat fine design. In this embodiment, filter 149' is provided in
the suction Line in place of return filter 149 of the FIG. 3 embodiment. Filter 149'
filters minute particles before they enter the pumps 131, thereby increasing pump
life.
[0038] Also in FIG. 5, a pressure regulation valve 1559 is provided as part of the hydraulic
control and power system 130, and check valves 160, 161 are installed in the control
feed lines to the check valves 106, 107 to prevent counterflow and pressure surges
in the control system when the main shuttle valve 132 shuttles the main oil flow to
port 105 in the main power cylinder 156.
[0039] Pegulated hydraulic control system and pressure provided by the pressure regulator
159 acts upon the cam-operated spring loaded check valves 106, 107 plus needle valves
137, 138, whereby check valves 106, 107 are normally maintained in a closed position
until opened by tubular camming members 108, 108'. The motor 66 for fan blade 65 has
its speed control by pressure regulator 159, which also controls the control system
pilot pressure. Once that pressure regulating valve 159 is set to the desired pressure
rating, the speed of the fan motor 66 will remain constant even though there are hydraulic
system pressure chanqes in the system 330. By adjusting the pressure regulating valve
159, the fan speed can he varied.
[0040] It is to be understood that the invention is not limited to the exact details of
construction, operation, exact materials, or embodiment shown and described, as obvious
modifications and equivalents will be apparent to one skilled in the art; for example,
the intercooler and after cooler and air forcing means could be utilized as a separate,
skid- mounted unit, of a larger size should additional cooling of the compressed gas
be necessary. Accordingly, the invention is therefore to be limited only by the scope
of the appended claims.
1. A hydraulically powered compressor for elevating the pressure of gaseous substances,
comprising: a first double-acting piston and compression cylinder for initially compressing
the oaseous substance; a second double-acting piston and compression cylinder for
additional compression of the gaseous substance; a hydraulic power piston and cvlinder
disposed between the first and second double-actin
q pistons and cvlinders; the first and second double acting pistons and the hydraulic
power piston each being disposed on a common elongate piston rod; first piping for
transferring the compressed gaseous substance from the first piston and compression
cylinder to the second piston and compression cylinder; second piping for transferring
the compressed gaseous substance from the second piston and compression cylinder to
an exit orifice; first and second cooling coils respectively associated with the first
and second piping for cooling the compressed gaseous substance; and means for forcing
air to flow over the first and second coolina coils; characterized in that:
the first and second pistons and compression cylinders, power piston and cylinder,
first and second pipinq, first and second cooling coils, and air forcinq means are
all disposed within an air-cooling duct to provide cooling thereto; and further characterized
by means for providing infinitely variable capacity control with a proportionately
variable power requirement for the first and second pistons and compression cylinders,
such means including a variable displacement hydraulic Dump means for actuating the
hydraulic power piston and cylinder so that the first and second pistons and compression
cylinders may be operated over a range of from 0 to 100% of their capacity with a
proportionately variable power requirement.
2. A compressor of claim 1, further characterized in that the first and second pistons
and compression cylinders and hydraulic power piston and cylinder are disposed on
a mounting plate by means of two mounting bolts, whereby transmission of stress forces
to the compression cylinders and power cylinder from the mounting plate is greatly
minimized; and the first and second pistons are threadedly affixed in a first direction
to the piston rod and are secured to the piston rod by a lockinq member which is threaded
into the piston rod in a second opposite direction.
3. The compressor of claim 1, further characterized in that the means for forcing
air includes a fan and hydraulic motor therefor, and the motor has a pressure compensated
flow control valve associated therewith, and is associated with and disposed between
the variable displacement hydraulic pump and the motor, so that the fan operates at
a constant speed to provide cooling to the first and second cooling coils, a hydraulic
system cooler also mounted in the duct, the first and second pistons and cylinders,
and the hydraulic power piston and cvlinder, and to blow out of the air coolinq duct
any accumulated gaseous substance.
4. The compressor of claim 1, further characterized by a pressure relief valve means
associated with the hydraulic variable displacement pump and first and second compression
cylinders, for preventing excessive pressure build-up from occuring in the first or second compression cylinders due to liquid, rather
than a gaseous substance, entering either cvlinder, so that the liquid may pass therethrough
at a safe operating pressure level.
5. The compressor of claim 1, further characterized by a cooling chamber between the
hydraulic power piston and cylinder, and each of the first and second pistons and
cylinders, each cooling chamber surrounding a portion of the piston rod and including
means for directing air flow from the means for forcing air over the piston rod.
6. A hydraulic control and power system for a compressor for gaseous substances having
first and second double-acting pistons and compression cylinders and a reciprocating
hydraulic power piston and cvlinder for actuating the first and second pistons, characterized
bv: a variable displacement hydraulic pump for providinq hvdraulic fluid to the power piston and cvlinder to reciprocate the power
piston within its cylinder; a shuttle valve for alternatina the flow of hydraulic
fluid from the pump into and out of the ends of the hydraulic power piston cylinder;
a cam-operated, spring loaded check valve associated with each end of the power piston
cylinder, said check valves being actuated by the reciprocating motion of the power
piston to discharge hydraulic fluid from the respective end of a pilot valve; a pilot
valve for actuating the shuttle valve in response to a pressure differential caused
by the discharge of hydraulic fluid through one of the cam-operated, spring loaded
check valves; a hydraulic fluid reservoir; and hydraulic fluid piping operatively
associating the pump, shuttle valve, check valves, pilot valve and reservoir, with
one another, so that upon varying the displacement of the pump, the speed of reciprocation
of the power piston is varied.
7. The hvdraulic control and power system of claim 6, further characterized by a flow
control valve means operatively associated with each end of the shuttle valve for
throttling the hydraulic fluid flowing from the pilot valve to either end of the shuttle
valve, so that the reciprocating speed of the shuttle valve is controlled and hydraulic
shocks caused by the shuttle valve reciprocating too quickly are controlled.
8. The hydraulic control and power system of claim 6, further characterized by a bladder
accumulator operatively associated with the pump and piping, so that pressure shocks
caused by reciprocation of the shuttle valve are absorbed, and pump enerqy is stored
durinq the time required to switch the shuttle valve.
9. A hydraulically powered compressor for elevatina the pressure of gaseous substances,
comprising: a first double-acting piston and compression cylinder for compressing
the gaseous substance; a second double-acting piston and compression cylinder for
compression of the gaseous substance; a hydraulic power piston and cylinder disposed
between the first and second double-acting pistons and cylinders; the first and second
double acting pistons and the hydraulic power piston each being disposed on a common
elongated piston rod; piping for transferring the compressed gaseous substance from
the first and second pistons and compression cylinders to an exit orifice; cooling
coils respectively associated with the piping for cooling the compressed gaseous substance;
and means for forcing air to flow over the cooling coils; characterized in that:
the first and second pistons and compression cylinders, power piston and cylinder,
piping, cooling coils, and air forcing means all beinq disposed within an air-cooling
duct to provide cooling thereto; and further characertized by:
means for providinq infinitelv variable capacity control for the first and second
pistons and compression cylinders, the capacity control means including a variable
displacement hydraulic pump for actuating the hydraulic power piston and cylinder,
whereby the first and second pistons and compression cylinders may be operated over
a range of from 0 to 100% of their capacity with a proportional variation in power.
10. The compressor of claim 9, further characterized in that the means for forcing
air includes a fan and hydraulic motor therefor, and the motor has a pressure regulating
valve associated therewith, and is associated with and disposed between the variable
displacement hydraulic pump and the motor, so that the fan operates at a constant
speed to provide coolinq to the first and second cooling coils, first and second pistons and cylinders, and
hydraulic power piston and cylinder and to blow out of the air cooling duct any accumulated
qaseous substance.