The present invention relates to patching devices, and more particularly, to vehicle mounted patching systems for patching potholes and the like and incorporating method and apparatus for removing and flushing asphalt emulsion from the feed lines of the patcher which eliminates any external discharge.
Asphalt patching systems are well known in the art. For example, U.S. Pat. No. 5,263,790 issued Nov. 23, 1993 and U.S. Pat. No. 5,419,654 issued May 30, 1995, teach a patcher comprising a motor driven, wheeled vehicle having a gravel hopper and a storage tank for liquid asphalt, as well as pressurized conduits for respectively advancing gravel and asphalt to a mixing head. The asphalt emulsion is delivered from the storage tank to the mixing head by feed lines. The mixing head is arranged to extend from a free end of a swingably mounted, telescoping boom, which is moveable in both horizontal and vertical planes as well as being selectively extendable and retractable to expedite desired positioning of the mixing head above a roadway surface to be patched. The pressurized conduits may also be initially employed to blow debris from the pothole or crevice being patched whereupon asphalt, with or without aggregate, is delivered to the mixing head. The need for rolling or tamping is eliminated by the use of high-pressure air.
The feed lines carrying the asphalt emulsion must be cleaned on a regular basis, typically at least once per day.
Present day cleaning operations have the disadvantage of expelling a significant amount of asphalt emulsion and solvent during the cleaning process which constitutes an environmental hazard as far as safe disposal of the emulsion and solvent is concerned, as well as requiring means for collecting and storing the hazardous material and further requiring labor intensive activity in the performance of the cleaning operation. It is therefore desirable to provide method and apparatus for performing a cleaning operation which significantly reduces the labor intensive activity and, in one embodiment, substantially eliminates such labor intensive activity by performing the cleaning steps substantially automatically, as well as retaining the emulsion and solvent in the patcher and avoiding need for discharge of these materials during the cleaning operation and providing for continued reuse.
The present invention is characterized by comprising method and apparatus embodiments for cleaning the asphalt emulsion feed lines of a patching system while eliminating any external discharge throughout the cleaning operation.
Feed lines providing asphalt emulsion to a mixing head, which is utilized to mix aggregate and the asphalt emulsion, are selectively fed emulsion and cleaned under control of a pair of four-position valves arranged adjacent to and preferably on opposite sides of the mixing head. When moved to a “patching” position, normal patching operations are performed i.e., asphalt is fed to the mixing head to perform patching.
By moving both valves to a “clearing” or “blowback” position, and opening a valve at the tank holding the asphalt emulsion, the ports of the pair of four-position valves enable high pressure air, preferably derived from the air brake system of the patcher, to enter the asphalt emulsion feed lines that are connected between the tank holding the asphalt emulsion and the mixing head. The pressure in the asphalt emulsion tank is lower than the entering pressure from the air brake system, whereby the asphalt emulsion in the feed lines is forced back to the asphalt storage tank, leaving only a small residue in the asphalt emulsion feed lines. If desired, the patching and clearing operations may be reversed in their order of performance.
The next step performed in the procedure is to close the conduit between the emulsion storage tank and the feed lines and place the pair of four-position valves adjacent to the mixing head in a third (“flushing”) position which opens the ports to a conduit connected to a flush tank containing a solvent maintained under pressure. The valve at the asphalt emulsion tank is turned to the flush position, coupling the asphalt emulsion feed lines to the pressurized flush tank, which causes the cleaning agent to move through and flush the feed lines and valves, which feed lines include at least one section of clear hose coupled to a given port of one of the pair of control valves to facilitate observation of the progress of the flushing operation. The solvent flushes the feed lines as well as the pair of valves adjacent to the mixing head and the valve coupling the flush tank to the pair of valves. The solvent then flows out through given ports of the pair of valves into a recovery tank and is maintained in the recovery tank. The solvent is returned from the recovery tank to the flush tank by closing the line between the flush tank and the source of air pressure, and venting the flush tank to the atmosphere and opening the valve in the line between the flush tank and the recovery tank when the flush tank is depressurized, causing the solvent to return by the force of gravity to the flush tank. The flush tank is then sealed from the atmosphere and air supply valve is then opened to pressurize the flush tank in readiness for a subsequent flushing operation.
Pressurized air is drained out of the flush tank by opening an air bleed valve. When the pressure gauge of the flush tank reads “0” psi, the valve in the line coupling the recovery tank to the flush tank is opened to enable the cleaning agent to flow by gravity back into the flush tank. This valve remains open for approximately 2 to 3 minutes and is then closed. The flush valve adjacent to the flush tank is closed and the valve between the flush tank and the air pressure source is opened to re-pressurize the asphalt storage tank in readiness to perform a subsequent flushing operation, at which time the cleaning process is completed without removal of either asphalt or solvent from the patching system and thereby providing for recycling of both the asphalt and the solvent.
The embodiments of the present invention will be understood from a consideration of the detailed description and drawings, wherein like elements are designated by like numerals, and wherein:
Chassis 12 supports a gravel hopper 16 and an enclosure 18 of substantially hexagonal shape which contains an asphalt supply tank 20. The asphalt is normally heated to maintain a temperature of the order of 135 to 160 Degrees F.
A front boom assembly 21 is pivotally mounted to the front end of the cab 14 to enable the boom assembly to swing in a horizontal plane by means of pneumatic cylinder 24, shown in
A flexible hose 35 communicates between gravel hopper 16 and a mixing head 34 arranged at the free end of boom assembly 21. Flexible hose 35 couples gravel hopper 16 to mixing head 34 through a telescoping delivery assembly 36.
The details of the movement of the boom assembly and its various components are set forth in U.S. Pat. No. 5,419,654 which is incorporated herein by reference and further details of the boom assembly and its operation are omitted herein for purposes of simplicity.
It is sufficient to understand, however, that a heated asphalt emulsion and aggregate are respectively fed to the mixing head under suitable air pressure as will be described in detail below.
The hollow, insulated non-collapsible hose 44 typically contains five (5) different fluid carrying lines as well as electrical wires as will be described below in greater detail. Non-collapsible hose 44 is maintained substantially taut regardless of the expansion or retraction of the telescoping delivery tube assembly 36, under control of piston cylinder 16, as is described in detail in the aforementioned issued U.S. Pat. No. 5,419,654.
As was described above, the aggregate hopper 16 is coupled to the mixing head 34 by means of the telescoping assembly 36 also shown, for example, in
Coolant from the engine cooling system of the patcher 10, which is typically heated to a temperature in the range of 135-160 of 150 degrees F., enters into a hot water inlet coupling 34b and circulates through the hollow interior of the mixing head defined by the inner and outer cylinder walls 34c and 34d, shown in
The emulsion storage tank 18 is coupled to an inlet port 102a of a multi-port valve 102 having a common outlet port 102b which is selectively coupled to one of the ports respectively arranged at 3 o'clock, 6 o'clock, 9 o'clock and 12 o'clock positions about the sidewalls of valve 102. Valve 102 is preferably enclosed within an insulating jacket 104 having inlet and outlet ports 104a and 104b for respectively introducing hot water from the engine cooling system into jacket 104 and for returning the hot water to the engine cooling system. The hot water flowing through jacket 104 maintains asphalt emulsion passing through valve 102 in a heated, flowable condition to prevent clogging of the valve.
When valve 102 is moved to the position coupling 12 o'clock port 102a to common port 102b, heated asphalt from tank 18 passes through valve 102 and enters asphalt line 106, which is one of the lines that is enclosed within the hollow, insulated non-collapsible hose 44, shown in
A valve assembly, preferably a one-half inch (0.50″) ball valve assembly 108 is connected in line 106 and is operated under the control of a custom linear actuator 109 operated under control of an actuator switch 111 located in the patcher cab 14 to provide an adjustable flow rate of the asphalt emulsion through line 106. Line 106 is split by a T-coupler 110, providing a first branch 112a which is coupled to the common port 114a of control valve 114 and a second branch 112b coupled to common port 116a of control valve 116.
Multi-position control valves 114 and 116, as well as valve 102, are substantially identical in design and function, as will be more fully described in connection with
The control valve 116 shown in
The valve assembly 116 comprises a hollow housing and is further provided with a pair of openings 116g and 116h along respective diagonal side surfaces for receiving coolant from the patcher engine cooling system to heat the valve and thereby maintain asphalt passing through the control valve 116 during a patching operation to be in a heated, flowable state and thereby prevent the control valve 116 (as well as control valves 114 and 102) from becoming clogged with cooled emulsion.
An air supply line 118 derives air under pressure directly from the air brake supply of the patcher air brake system (i.e., without any reduction in pressure), not shown for purposes of simplicity. Air pressure of the order of 120 psi is supplied to the air line 118. A T-coupler 120 feeds the pressurized air to branch lines 122a and 122b, each of which are respectively coupled to inlet ports 114b and 116b of multi-position valves 114 and 116.
Ports 114c and 116c of multi-position valves 114 and 116 are respectively coupled through one-way valves 122 and 124 to one of the inlets 34f and 34g which extend through outer and inner jacket walls 34c and 34d of mixing head 34 (see
As was previously mentioned, the aggregate passes through curved member 40 and into the hollow interior of mixing head 34 where the aggregate is admixed with and coated by the liquid emulsion and then passed through the outlet end 34h of the mixing head 34 for deposit into a pothole or other crevice or recess being and/or repaired. As was mentioned above, air under pressure may be introduced into mixing head 34 while the emulsion feed lines and aggregate line are closed, to clean debris from a pothole. Also, air under pressure enters the flexible hose 35 and telescoping assembly 36 to advance the aggregate into the mixing head 34.
Check valves 122 and 124 are preferably respectively coupled between outlet ports 114c and 116c and couplings 34f and 34g, allowing emulsion to pass in only one direction and enter into the mixing chamber of mixing head 34 while preventing any reverse flow of the asphalt emulsion from the mixing head back into the control valves 114 and 116 through ports 114c, 116c.
The one-way check valves 122 and 124 are preferably provided with jackets having inlet and outlet ports similar to the ports 116g and 116h of valve 116, as shown in
Control valves 114 and 116 are further provided with outlet ports 114d and 116d. Back flush conduits 126 and 128 are coupled between ports 114d, 116d and recovery tank 130. Flush tank 132 contains solvent under pressure, employed for flushing the feed lines 106, 112a and 112b. Recovery tank 130 is located above flush tank 132 to provide for the flow of fluid by gravity from recovery tank 130 to flush tank 132, when normally-closed valve 134 is open. The solvent is typically diesel fuel but may be any other suitable cleaning agent having like cleansing and/or flushing capabilities.
Patcher 10 operation is initialized by assuring that air pressure provided to the asphalt storage tank 18 and the flush tank 132 are within the range of 50-70 psi and that the air brake system is developing air pressure in the range of 100-120 psi. Valve 136, coupled near the outlet of the air brake pressure source, is a regulator valve which, when open, regulates the output pressure introduced into the flush tank 132 and the asphalt storage tank 18, through valve 102., to obtain the desired pressure levels mentioned above. Valves 114 and 116 are then placed in the 12 o'clock position, causing air entering 122a and 122b to pass through valves 114 and 116 and enter into the feed lines 112a and 112b. The air brake pressure source fed to the line 118 bypasses the valve 136 and thus provides maximum pressure (i.e., 100-120 psi) to the 12 o'clock ports of valves 114 and 116 to clear line 106. Valve 102 is then placed in the 12 o'clock position. The actuator switch 111 in the patcher cab 14 (see
During a typical patching operation, a pothole in the roadway surface is cleaned by blowing high-volume air into the pothole. Air under pressure is introduced into feed line 106 by placing valve 102 in the 3 o'clock position and placing valves 114 and 116 in the 6 o'clock position. Thereafter, a tack coat of emulsion may be applied to the area to be treated. Thereafter, a mixture of aggregate coated with heated emulsion is emitted from the mixing head 34 to fill the pothole. The valve 102 is then placed in the 12 o'clock position and valves 114 and 116 are placed in the 6 o'clock position to cause emulsion to flow (under pressure) from the supply tank 18 to mixing head 34 through 106, 112a, 112b and 124. A finished coat of dry aggregate may then be applied, if desired. The 3 o'clock port of valve 102 can also receive air to blow out the feed line 106, if desired. It has been found that sprayed injection patching is the most economical and longest lasting method for pothole repair.
In order to clean the internal lines of asphalt emulsion while at the same time eliminating any external discharge of fluid from the system and completely recycling the asphalt and solvent, control valves 102, 114 and 116 are operated in the following manner:
A shut-down storage operation is initiated by introducing air into the feed lines by operating switch 111 in cab 14 to fully close the ball valve 108. The operating handles of control valves 102, 114 and 116 are respectively moved to the 3 o'clock, 12 o'clock and 12 o'clock positions. Ball valve 108 is then opened and maintained open for approximately 1 to 2 minutes until the air pressure in the feed lines drops (monitored by the aforementioned air gauge in cab 14) whereupon the ball valve 108 is fully closed.
Valves 114 and 116 are then respectively moved to the 9 o'clock and 3 o'clock positions. Control valve 102 is then moved to 6 o'clock position, coupling flush tank 132 to feed line 106 through valve 102 in readiness to perform a flushing operation. Actuator 109 is operated to open ball valve 108, causing solvent in pressurized flush tank 132 to enter the 6 o'clock port of valve 102 and pass through valve 102, feed lines 106, 112a and 112b and valves 114 and 116 and then to recovery tank 130 through back flush lines 126 and 128. One of these hoses, such as hose 128, is preferably formed of a clear transparent material, enabling an operator to view the cleaning agent as it moves from flush tank 132, through valve 102, feed lines 106, 112a, 112b, valves 114 and 116 and back flush lines 126, 128 and enter into recovery tank 130, shown in
The cleaning agent is returned to flush tank 132 from recovery tank 130 by respectively moving valves 114 and 116 to the 3 o'clock and 9 o'clock positions and closing valve 102 (by moving valve 102 to the 9 o'clock position). The air supply line to flush tank 132 and to the emulsion tank 18 is closed by closing valve 136. The air under pressure in flush tank 132 is vented to the atmosphere by opening valve 138 as shown in
Closed valve 134 is then opened for 2-3 minutes to drain the recycled cleaning agent, delivered to recovery tank 130 by lines 126 and 128, back into flush tank 132 and valve 34 is then closed.
The air pressure release valve 138 which bleeds air from tank 132 to the atmosphere is closed and valve 136 is opened to repressurize tank 132 and emulsion supply tank 18 from pressure source 118, completing the back flush operation and retaining all of the solvent and emulsion in the closed system. The connections for the flush operation may be reversed by coupling the flush tank 132 to valves 114 and 116 and coupling the recovery tank 130 to valve 102.
When the pressure in the lower half FC of tank 150 is greater that in the upper half RC of the tank, poppet valve 152 is urged in an upward direction by the force of the pressure in compartment FC, to firmly seal the lower compartment and thereby maintain the cleaning agent in the lower half of tank 150 under pressure. During the flushing operation, the cleaning agent under pressure flows from the lower half of tank 150 to valve 102 when it is in the flush position.
When the flush operation is completed, the valve 136 is closed and the valve 138 is opened to bleed air from the lower half of tank 150. The force of the solvent collected in upper compartment RC is greater than the spring force of spring 159, urging sealing disk downwardly, enabling the cleaning agent to automatically return to the lower compartment of tank 150. When the cleaning agent has been drained from the upper compartment, the spring force of spring lightly urges sealing disk 158 to the sealed position. Valve 138 is closed and valve 136 is opened thereby repressurizing the flush compartment FC of tank 150 (containing the cleaning agent) in readiness for a subsequent flushing operation. In order to retain the air-tight integrity of tank 150, a threaded opening 150e is provided along the bottom end 150b of tank 150 to facilitate insertion and maintenance of poppet valve assembly 152. The threaded opening 150e is sealed by threaded plug 161, having a flange 161a which engages a marginal portion of bottom end 150b surrounding opening 150e. A gasket 162 is preferably arranged between flange 161a and the bottom end 150b of tank 150.
This application which claims the benefit of U.S. provisional application No. 60/832,171 and filing date of Jul. 20, 2006, which is incorporated by reference as if fully set forth.
Number | Date | Country | |
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60832171 | Jul 2006 | US |