Patent Application
20050005509
The present invention relates generally to the thermal control of vegetation, particularly weeds, and more specifically to a method and apparatus for the control of weeds using hot foam.
Thermal methods have been proposed for weed control wherein a variety of heated materials are applied to the weeds, including hot water, steam, hot air, flame and hot foam. These methods overcome some of the disadvantages of herbicides, such as spray drift and soil/groundwater pollution. They also avoid the physical effort required for manual weed removal.
New Zealand patent no. 240568 describes the use of hot water applied under a shroud. Compared to herbicides, the method is fast-acting, effective over a range of vegetation and weather conditions, and being non-toxic its use is less restricted e.g. personal protective clothing or certification is not required for applicators. However, the long shroud (to provide a thermal screen for temporary insulation from ambient temperature and wind) restricts the use and speed of coverage of hot water systems.
An alternative is described in U.S. Pat. No. 5,433,758 wherein a spray of hot water is applied to the weed, followed by a cold foam blanket to provide the temporary thermal screen. This method, however, requires separate apparatus for the production and distribution of the hot water and foam. Also, some cooling results from the application of a cold foam blanket which reduces the effectiveness of this method.
U.S. Pat. No. 5,575,111 describes a method where heated compressed air is mixed with a stream of hot water and surfactant to form a hot foam for application to the weeds. In this method heated air is used to melt the plants waxy cuticular coating while the foam acts to provide the temporary thermal screen. The foam used is relatively dry, being from 80 to 95% hot air by volume. It has been found however, that this method is not particularly effective at killing weeds. It appears that several factors may influence the lack of effectiveness of this method. Although the high temperature air disrupts the cuticle, it has been found that weeds treated in this manner grow back more quickly than those treated with hot water systems. Relatively dry foams have a low heat capacity and have a reduced ability to penetrate below the outermost surface of the plant to produce deeper more long lasting damage, particularly to the harder surfaces such as the stems of the target plants. Due to the stiffness of relatively dry foams they are unable to flow to obtain good intimate contact with the plants, thereby protecting, for example, the underside of foliage from contact with the foam. The size of bubbles formed in the foam is also an important factor, as large bubbles also reduce the heat flux through the foliage and stems with which they are in contact.
It is an object of the present invention to provide a system of thermal weed control which overcomes the drawbacks of hot water methods while retaining its advantages, but which also addresses the foregoing problems of foam methods.
Further aspects and advantages of the present invention will become apparent from the ensuing description which is given by way of example only.
According to one aspect of the present invention there is provided a method of controlling vegetation, including the steps:
Although the method is primarily intended for the control of vegetation, particularly weeds, this should not be seen as limiting as it is also applicable to soil, for example, and for killing or controlling fungus, bacteria, virus and insects etc.
Preferably the foam is prepared by heating the aqueous solution and mixing a stream of air with a stream of aqueous solution to produce the stream of foam which is discharged at low pressure.
The foam discharge pressure may range from 5 PSI to 15 PSI, but is preferably 10 PSI (0.7 bar).
Preferably the water and foaming agent are mixed in the correct proportions in a reservoir. Optionally, the foaming agent may be metered into a flow of water, before or after the flow is heated.
Preferably the aqueous solution is alkyl polygclycoside (APG) mixed with water at a dilution rate of approximately 0.4%. Optionally other biodegradable foaming agents maybe employed.
Preferably the solution is pumped through a boiler into a mixing device, where it is mixed with the air to produce foam which then passes through an elongate delivery passage before being discharged through a divergent shroud.
The solution delivery rate for commercial applications may be from 10 litres per minute to 500 litres/minute, or more. In the preferred embodiment, the foamable solution is supplied at a rate of approximately 10 litres per minute and at a pressure in the range of 5-15 PSI and most preferably 10 PSI.
The method produces a wet foam which consists volumetrically of 60% to 75% aqueous solution. Generally, this volumetric ratio should not normally exceed 85% with 60% being about optimum. Optionally, the stream of low pressure air may be heated prior to mixing with the solution.
According to another aspect of the present invention there is provided a method of controlling vegetation, including the steps:
Optionally, two or more channels may be provided, each drawing in a respective stream of ambient air to foam the solution. Preferably each channel provides a free jet of solution.
Preferably the solution is pumped through a boiler, the full stream flowing through one channel to facilitate low pressure that creates a venturi to draw in the stream of ambient air into a mixing chamber, where it is mixed with the solution to produce foam that then passes through an elongate delivery passage before being discharged through a divergent shroud.
According to another aspect of the present invention there is provided a provided an apparatus for performing the method of controlling vegetation substantially as described above, the apparatus including:
Preferably the solution is directed through a conduit to enter the mixing chamber in a jet-like flow substantially perpendicular to the air flow.
Preferably a foam control mesh is provided in the foam flow path. The mesh may be positioned in the shroud, near the outlet thereof. The mesh preferably has generally 4.76 mm holes at 6.35 mm triangular pitch, 51% open area.
Preferably the internal cross-sectional area of the delivery passage is approximately 60% greater than that of the air delivery conduit and approximately ten times that of the solution delivery conduit.
Preferably the foam is applied from a mobile means, most preferably a self-propelled vehicle e.g. a truck or tractor.
In the apparatus for performing the method of controlling vegetation substantially as described above, the means for supplying a stream of air includes channel means which facilitate low pressure that creates a venturi to draw in a stream of ambient air.
In an embodiment for controlling vegetation by the application of hot foam through a hand lance, the venturi created by flow through the channel is preferably mounted on the hand lance. Preferably the apparatus includes a hand-operated valve for controlling the flow of air into the mixing chamber.
As well as reducing equipment cost and energy usage, it has been found that using a venturi as described reduces the drop in temperature between the solution and the foam, producing a higher temperature foam for more effective treatment, whether using a hand lance, a vehicle mounted system or otherwise. It is possible when using a hand lance to considerably increase the length of hose that can be employed, thus providing the operator with additional versatility.
This apparatus and method is particularly useful to enable better application of heat in places where application is difficult, for example dense swards and vegetation substantially above 200 mm in height. The application is less confined by surface conditions and obstacles since the foam adheres to vertical surfaces and does not run off like liquids. The residence time of hot foam on target areas is greater than that of hot water. The evaporation rate of wet foams is less, resulting in longer contact with the target. Also, foams provide visual evidence of coverage of the application area. Faster and more long-lasting control of weeds is provided, compared to the known hot air foam method.
With the application of hot foam instead of pure hot water a thermal screen is superfluous because the foam performs this function. Unlike pure hot water the hot foam can be blown over a certain distance without considerable heat loss.
Compared with other thermal methods it is distinguished by considerably higher working speed and lower costs. An area may be covered more quickly with lower water consumption and energy input per square meter than is possible with hot water systems.
Besides weed control in horticulture and agriculture, other application areas include the control of vegetation around trees, at the edge of concrete or paving, on roadside berms, around buildings and other obstructions, along railway lines, and other areas where the overgrowth of vegetation and in particular weeds is to be controlled.
Further aspects of the present invention will become apparent from the following description which is given by way of example only and with reference to the accompanying drawings in which:
a and 3b are plan and side elevations respectively of the shroud of the hand lance of
a and 8b are plan and side elevations respectively of the liquid jet of the hand lance of
As illustrated in the drawings, the apparatus is mounted to a vehicle (not shown), preferably a truck and includes an aqueous foamable solution supply tank 1, a boiler 2 for heating the solution from the tank 1 and a blower 3 for supplying air to foam the solution. The boiler 2 is positioned adjacent to the tank 1, and solution is supplied to the boiler 2 by a pump 4 powered by electricity from a generator 5. In one presently preferred embodiment, the boiler 2 has a burner (not shown) which burns liquid fuel, and the pump 4 is a single-stage centrifugal pump. Alternatively, the pump may be driven directly by a small petrol engine.
Referring to
a and 3b illustrate in more detail the shroud 12, which diverges from a circular section at the delivery tube end to a generally rectangular outlet 15, having an included angle of approximately 60 degrees. Located in a medial section of the shroud 12, a foam control mesh 16 is provided which is arranged approximately perpendicular to the flow. The mesh 16 is preferably bent into a 90° V about an axis perpendicular to the flow direction.
Foam producing apparatus as known heretofore, are primarily intending to efficiently produce foam having a relatively low moisture content for applications such as fire fighting, herbicide application or for insulating purposes (e.g. U.S. Pat. No. 5,575,111). For high efficiency in these applications it is important to have a high expansion ratio—that is to produce a high volume of foam in relation to the quantity of liquid solution and compressed gas employed.
The system of the present invention, however, results in a relatively low expansion ratio producing wet foam with reduced cooling and a foam temperature of approximately 92° C. or higher in the preferred embodiment.
While the apparatus shown is illustrative of the requirements for performing the method of the present invention, it will be appreciated that many variations of the apparatus may be employed to perform the method. For example, if desired, instead of being mixed with water in the tank 1, the foaming agent can be introduced into hot water at the output of the boiler. The foaming agent may stored in a separate tank (not shown) and introduced into the hot water stream from the outlet of the boiler, with a flow control valve (not shown) for controlling the amount of agent which is introduced, alternatively a metering pump (not shown) may supply the foaming agent.
To utilize the apparatus above described for the purpose intended, the foamable solution preferably comprises alkyl polyglycoside (APG) mixed at a 0.4% dilution rate with water. APG is able to withstand temperatures in excess of 100° C. without adverse effects and produces a foam which is stable for between 5 to 20 minutes under most ambient conditions. Moreover, the foam produced breaks down without drifting off the target plant and APG is a naturally occurring product which biodegrades both aerobically and anaerobically.
The output of the boiler 2 consists of pressurised solution at a temperature of close to 100° C. Actuation of the trigger 9 directs the solution into the stream of air from the blower 3. As the air mixes with the liquid solution it creates bubbles forming foam which builds up and is forced from the chamber 10 toward the outlet by the air pressure. Air is supplied at a rate of approximately 0.7 m3 per minute, with solution supplied at approximately 10 litres per minute—the apparatus producing a foam which is approximately 60% solution by volume and at a temperature of 92° C., or more.
Factors which have been found to affect the correct foam production include the dimensions of the shroud 12 and the delivery tube 11. A 32 mm internal diameter delivery tube of approximately 400 mm length diverging to a shroud opening of approximately 200 mm×15 mm has been found to give good results. The internal cross-sectional area of the delivery tube is approximately ten times that of the tube supplying the solution.
It is thought that the relative lack of foam flow constriction resulting from this arrangement is important in producing the foam, which is pressurised only to approximately 10 PSI (0.7 bar). Higher pressures and air flows have been found to disperse the foam from the target and result in excessive cooling. The mesh 16 provided in the shroud 12 controls bubble size and foam formation and a mesh 16 having generally 4.76 mm holes at 6.35 mm triangular pitch, and 51% open area has been found satisfactory.
The cross-sectional area of the chamber 10 is approximately 60% larger than that of the air hose 6. This, accordingly, does not permit a large expansion and a volume of wet, high density foam is continuously produced in response to the continuous agitation of the foamable solution by the air flow.
In preferred embodiments the generator 5, tank 1, pump 4, boiler 2 and blower 3 are sized to provide foamable solution and air to two lances 8, which are operable separately or together. The system is capable of treating a nominal 1000 m2 per hour, at an approximate treatment width of 200 mm to 300 mm from each lance.
As used in
As illustrated in
a and 8b illustrate the construction of the chamber 100 in more detail. The chamber 100 comprises a tubular section 33 joined to a conical section 34 tapered out to the larger diameter of the delivery tube 11. An opening at the end of the tubular section 33 receives a nozzle 32 having a central outlet 35 which produces a single jet of solution directed longitudinally through the chamber 100.
As will be understood the flow through the nozzle 32 facilitates low pressure that creates a venturi to draw in a stream of ambient air through the openings 31. This system results in a relatively low expansion ratio producing wet foam with reduced cooling and a foam temperature of approximately 92° C. or higher in the preferred embodiment.
With the operating parameters described in application no. 514497, satisfactory results have been obtained employing a jet having a 4.5 mm diameter directing flow into a tubular section 33 having a 19 mm bore, with both the tubular section 33 and conical section 34 having substantially the same lengths. The apparatus produces a regular foam structure and more even temperature spread across the shroud 12.
It will be appreciated however, that this method of introducing the air for foaming the solution can be employed in a number of different applications, and is also not limited to applications employing a hand lance.
In an alternative embodiment (not shown) a sliding cover is provided for engagement with the tubular section 33 to form a valve that may be controlled for regulating the flow of air through the openings 31. This valve may be closed allowing the lance to be used for purposes other than foam production e.g. spraying. Varying the opening of the valve allows the composition and texture of the foam to be adjusted, as may be preferable for treating different types of vegetation, for example.
On the hand lance, the valve may be directly controlled by the operator. The valve also provides a method of protecting the operator. It can be closed when a sensor measures a temperature in excess of 100° C. to prevent the escape of steam which (because of the position of the air inlet on the lance) may blow back on the operator.
To achieve higher foam production rates, satisfactory results have been obtained by maintaining the ratio (1:70) between the solution and flow rates air e.g. 40 litres per minute solution flow rate requires 2.8 m3 per minute of air supply.
In preferred embodiments for large scale commercial applications, it is anticipated that spray booms of up to 10 metres in width could be used, with proportionate increases in the flow rates to provide the specified foam temperature and composition.
Trials have been conducted to examine the effect of a number of variables associated with the present apparatus and method of producing hot foam. These trials determined the following important features.
Aspects of the present invention have been described by way of example only and it should be appreciated that modifications and additions may be made thereto without departing from the scope thereof.
| Number | Date | Country | Kind |
|---|---|---|---|
| 514497 | Sep 2001 | NZ | national |
| 519805 | Jun 2002 | NZ | national |
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/NZ02/00194 | 9/27/2002 | WO |
