The present invention relates generally to melter kettles that are designed and used to melt thermoplastic materials that are applied to pavements such as roadways, airport runways, parking lots, bicycle paths and other surfaces requiring pavement markings. More particularly the present invention is directed to systems and methods to improve the melting efficiency of melter kettles.
Thermoplastic materials are the product of choice for many types of pavement marking operations. However, unlike most other types of marking materials thermoplastic materials must be melted to very high temperatures that can reach up to about 420° F. in order to be fluid enough to be applied.
Early types of thermoplastic material application equipment applied the thermoplastic material at slow rates. Therefore, the long melting times it took to melt thermoplastic materials in melter kettles were not a problem. Melter kettles could keep up with the low output of application equipment.
Eventually improvements in the designs of melter kettles achieved reductions of melting times. However, over time application equipment was improved to the point at which thermoplastic material could be applied at much faster rates than the improved kettles could keep up with melting the thermoplastic material. The present invention increases the efficiency of melting thermoplastic in melter kettles that can be mounted on either thermoplastic trucks, nurse trucks, trailers or the like.
For some time heat domes, also called heat risers or heat tubes, have been installed in melter kettles. The dome structure is formed by a tube of variable diameter that is attached to a hole in the base of a kettle where the OD of the dome base matches the ID of the hole in the base of the kettle. The top of the dome is closed by a metal disc. The dome reduces the heating surface area of the base. However, the dome provides additional circumference surface area that compensates for the loss of the heating area in a kettle with no dome and compensates for the lost surface area of the base within a few inches of dome height. From this point the dome adds melting (heat transfer) surface area to the kettle with a dome as compared to a kettle without a dome thereby increasing the overall heating surface area in the kettle that acts on thermoplastic material in the kettle. This reduces the ratio of thermoplastic material to melting (heat transfer) surface area of the kettle which improves heating efficiency. Additionally, heating thermoplastic material in a melter kettle from the middle of the kettle in an outwardly direction is more efficient than heat transfer from the outside of the kettle in an inward direction. Heat domes have reduced melting times in kettles. However, heated air in the dome cools as heat transfers through the dome wall and into the thermoplastic kettle. Melting times are reduced with the use of domes but still needed to be improved.
A recent improvement in melter kettle efficiency has been developed by the present inventor and is disclosed in U.S. provisional application Ser. No. 62/291,316, entitled “HEAT DOME TEMPERATURE REGULATING SYSTEM,” filed Feb. 4, 2016. In this copending application a heat dome chimney stack tube is attached to the top center of a heat dome about which an agitator drive shaft tube rotates. Hot combustion gases travel from the heat dome up the center of the heat dome chimney tube stack and vent into a top tube drive shaft heat chamber that has driveshaft tube relief vents through which combustion gases vent into the atmosphere. The venting of the combustion gases can be regulated by providing a rotational vent relief collar about the top tube drive shaft heat chamber. This system exhausts combustion gases from the dome that has been heat depleted thereby allowing a continual flow of hot combustion gases to maximize/optimize efficient temperature in the dome such that the maximum amount of heat is transferred through the dome and chimney stack surface areas into the thermoplastic material in the kettle. In this system the heat dome chimney stack tube and rotational drive shaft become heating surfaces through the centerline of the melter kettle. This system improves the rate of thermoplastic melting.
Another recent improvement in melter kettle efficiency developed by the present inventor is disclosed in U.S. provisional application Ser. No. 62/322,640, entitled THERMOPLASTIC MELTING KETTLE MATERIAL CIRCULATION SYSTEM, filed Apr. 14, 2016. In this improvement a single vertical material transfer tube is affixed to the side of the thermoplastic melter kettle either directly to the kettle side wall or to the outer insulation skin. The tube is attached to ports at the bottom and top of the melter kettle and an auger rotated by a direct drive motor within the vertical material transfer tube moves molten material from the bottom of the kettle to the top. When the vertical material transfer tube is connected directly to the kettle outer wall the bottom interface is within the heat chamber's outer wall.
When the vertical material transfer tube is affixed to the outer insulation skin there is an extended heat chamber surrounding the vertical material transfer tube. A port larger in diameter than the lower material transfer tube allows heat from the combustion chamber to contact the vertical material transfer tube.
Another recent improvement in melter kettle efficiency developed by the present inventor is disclosed in U.S. provisional application Ser. No. 62/291,309, entitled THERMOPLASTIC KETTLE AUXILIARY HEAT EXCHANGER SYSTEM, filed Feb. 4, 2016. This invention combines an odd number of interconnected vertical tubes within an oil bath through which heated heat transfer oil flows. The function of the system is to increase the temperature of molten thermoplastic moving through the circuit of interconnected heat transfer tubes by action of an independent high BTU output furnace that heats circulated heat transfer oil that circulates around the interconnected tubes. Molten thermoplastic enters the base of the first tube through a kettle bottom material flow port and the tube bottom material flow port both of which are isolated from the oil bath. The molten thermoplastic reenters the kettle at the top center through the top flow tube that connects to the top of the discharge tube that is above the level of the kettle top and is isolated from the oil bath. Each tube contains an auger. The augers are interconnected by a gear train. A single hydraulic motor attached to any auger drives each gear and auger in a counter rotational direction. This circulates the molten thermoplastic material from the bottom of the kettle where it is hottest through the kettle bottom material flow port into the bottom of the first tube then up and down the plurality of tubes. The material flows up the last tube and through a tube top port which is isolated from the oil bath and through the top material flow tube located at a level above the top of the kettle. The molten thermoplastic is deposited near the top center of the kettle where it heats and displaces downward the thermoplastic at the surface of the kettle. The heat transfer oil enters the oil bath tub adjacent the thermoplastic discharge port where both the oil and thermoplastic are at their hottest temperature and is directed through and leaves the system adjacent the thermoplastic inlet port where it is heat depleted. When the system is disengaged and circulation ceases the hydraulic motors are run in a reverse direction to purge as much thermoplastic from all tubes except for the inlet tube. This will leave solid material in only the first tube so that when the system is restarted it will take less heat and hydraulic energy to engage the system and begin moving molten material.
There is a limit to the various available energy outputs of mobile equipment systems that can be incorporated in thermoplastic equipment such as heat, electrical, engine, hydraulic air and other systems. Some serious draw backs to thermoplastic oil bath auxiliary heat exchanger systems are that they require a separate high BTU boiler system, separate hot oil circuits as well as oil expansion chambers designed for use with exotic heat transfer oils some of which require inert gas blanket interfacing. The high BTU output boilers required need more space than is available on most thermoplastic application trucks. Where they can be used they require special designs and fabrication. Motors to run the hydraulics and oil circulation systems also are subject to space limitations. Weight is also a serious consideration. For each pound that the system weighs the carrying capacity of the thermoplastic application truck is reduced by a similar amount. Costs are high for all of the system components.
According to various features, characteristics and embodiments of the present invention which will become apparent as the description thereof proceeds, the present invention provides an improvement for a melter kettle used for melting thermoplastic pavement marking material wherein the melter kettle is provided with a combustion chamber the improvement comprising a tube assembly coupled to a side portion of the melter kettle and located within a heat chamber that surrounds the melter kettle through which heat chamber hot combustion gases from the combustion chamber can flow upward around the tube assembly, the tube assembly including an odd number of vertical tubes that are connected at the tops and bottom in a serpentine manner, the tube assembly is coupled at one end to a lower portion of the melter kettle and coupled at another end to the top of the melter kettle for receiving molten thermoplastic from the lower portion of the melter kettle and discharging molten thermoplastic material to the top of the melter kettle.
The present invention further provides a melter kettle for melting thermoplastic pavement marking material which comprises:
a melter kettle having a combustion chamber adjacent a bottom of the melter kettle and a heat chamber that surrounds the melter kettle; and
a tube assembly coupled to a side portion of the melter kettle and located within the heat chamber through which heat chamber hot combustion gases from the combustion chamber can flow upward around the tube assembly, the tube assembly including an odd number of vertical tubes that are connected at the tops and bottom in a serpentine manner, the tube assembly is coupled at one end to a lower portion of the melter kettle and coupled at another end to the top of the melter kettle for receiving molten thermoplastic from the lower portion of the melter kettle and discharging molten thermoplastic material to the top of the melter kettle.
The present invention also provides a method of melting a thermoplastic material in a melter kettle having a lower combustion chamber and a heat chamber surrounding the melter kettle, said method comprising:
charging thermoplastic material into the melter kettle;
combusting a fuel source in the combustion chamber to heat and melt the thermoplastic material in the melter kettle;
providing a tube assembly comprising an odd number of a plurality of tubes for heating and transferring thermoplastic material from a bottom of the melter kettle to a top of the melter kettle, the tube assembly being coupled to a side portion of the melter kettle and located within the heat chamber;
transporting molten thermoplastic material from the bottom of the melter kettle through the tube assembly and into the top of the melter kettle.
The present invention will be described with reference to the attached drawings which are given as non-limiting examples only, in which:
An object of the present invention is to reduce the melting time of thermoplastic pavement marking material that is melted in thermoplastic kettles that may be stationary, mounted on support trucks, support trailers or on truck mounted thermoplastic application vehicles where the vehicle is the applicator. It has long been recognized that the rate of melting thermoplastic in kettles has not been able to keep up with improvements in application equipment that have increased the rate at which the thermoplastic material can be applied. While methods of application and equipment development have increased the rate of application, production melting capacity has recently lagged far behind the ability to apply the material.
The present is based upon the recognition that material melts at a faster rate at the bottom of a melter kettle, that there is a temperature gradient between the base and sides of a melter kettle, and that there is a temperature gradient from the bottom of the sides to the top of the sides of a melter kettle. The present invention takes advantage of the fact that material in a melter kettle melts most efficiently at the bottom and more efficiently from the center of the kettle towards the sides than from the sides towards the center. Therefore, while a melter kettle without a heat dome can be used in conjunction with the present invention, using a kettle with a heat dome and heat dome temperature regulation system is preferred as the rate of melting and rate of application will be greatly improved.
The present invention first increases the rate of melting thermoplastic pavement marking material by increasing the heat differential between the application temperature of the thermoplastic and the temperature of the medium that transfers heat across the plurality of interconnected heat transfer tubes as compared to previous systems. Second the present invention provides a lower tube interface insulation chamber for the tube bottom interfaces of the plurality of interconnected tubes to make it possible for that greater heat differential. Third according to the present invention the lower tube interface insulation chamber provides access to the lower interfaces of the heat exchanger tubes for servicing. Fourth the present invention provides a full depth bottom insulation chamber that supports the lower tube interface insulation chamber and provides protection from outer kettle wall radiated heat radiating from the combustion chamber.
According to the invention the thermoplastic material in a melter kettle is heated to a viscosity where it will enter the heat chamber fired auxiliary heat exchanger intake at the base of the kettle where the material is hottest. Then the heated, molten material moves through the heat exchanger tubes of a tube assembly by action of counter rotating augers to the top of the last tube's outlet where it is deposited into the top of the melter kettle and mixed by action of agitators with the cooler material at the top of the kettle thereby increasing the overall rate of heating. Additionally, a heat dome and chimney stack tube can be incorporated to greatly increase the rate of heating in the base of the kettle such that the material being introduced at the top of the kettle transfers more heat to the material at the top of the kettle thereby reducing melting time as compared to melter kettle without a heat dome system.
Another aspect of this invention is based upon dynamic heat exchange. The action of heating material by moving material from the bottom of the kettle to the top of the kettle where material is added and therefore coolest is passive. The heat exchange system of the present invention is also a dynamic system whereby combustion chamber fired air is heated to a temperature well above that of the temperature required to apply thermoplastic and is circulated through, up and out of a chimney stack of the extended heat chamber surrounding the variable number of interconnected tubes through which the thermoplastic flows by action of counter rotating augers. Heat is transferred from the hot combustion gases through the tube walls and into the thermoplastic. The addition and use of this type of system to a thermoplastic kettle makes it now possible to keep up with the rate of application of thermoplastic from high output application equipment.
Kettle melting chamber 1 is defined between the kettle side wall 2, kettle bottom 3, and top of the kettle. Pavement marking thermoplastic material in either granular or solid form is added into the kettle melting chamber through material fill chute 4 that is provided with a safety splash back preventer (not shown) to protect the material handler from burns. A diesel-fired or other type of burner 5 is attached to the outside of the kettle 1 adjacent the combustion chamber 6 to provide the heat energy required to heat the material to a molten state and maintain it at the correct application temperature. External air is introduced at burner 5 to allow for combustion. The heated air within the combustion chamber acts upon the kettle bottom 3 first and then flows towards the outside of the kettle wall 2 where it enters and travels up the heat chamber 7 and exhausts the system through exhaust stacks 8. It is this action that defines the system in
A temperature gradient is created from the kettle bottom 3 where it is hottest and to the top most point on the kettle side wall 2 where the temperature is coolest. Heat transfer is most efficient at the hottest point of the kettle bottom and loses efficiency adjacent the upper portions of the kettle wall 2. The heat chamber is surrounded by an outer heat chamber/inner insulation chamber wall 9 and insulation chamber 10 in which there is insulation shielding the external surface from radiant heat. An outer insulation skin 11 surrounds the melter kettle and the kettle assembly base 12 also contains insulation and provides support for the structure. Molten thermoplastic material exits the kettle shown in
All tubes 18 of the tube assembly can be of equal diameters and lengths with each having an auger 19 with equal length and diameter shafts 20 and all flights 21 running in the same direction in each tube 18. Each tube 18 has an identical upper interface assembly (See
As shown in
At the top of the first tube 25 and the second tube 26 there is a top tube cross over connector 33 that allows material to flow between the tubes. At the bottom of the second tube 26 and the bottom of the third tube 27 there is a bottom tube cross over connector 34 that allows material to flow between the tubes. This pattern of cross over connectors is repeated between tubes 28-31 as shown in
A removable lower tube insulation compartment 53 that shields the tube assembly from the extreme heat of the combustion chamber 6 is shown in
Although the present invention has been described with reference to particular means, materials and embodiments, from the foregoing description, one skilled in the art can easily ascertain the essential characteristics of the present invention and various changes and modifications can be made to adapt the various uses and characteristics without departing from the spirit and scope of the present invention as described above and set forth in the attached claims.
The present application is based upon U.S. Provisional Application Ser. No. 62/368,468, filed Jul. 29, 2016 to which priority is claimed under 35 U.S.C. § 120 and of which the entire specification is hereby expressly incorporated by reference.
Number | Name | Date | Kind |
---|---|---|---|
1709016 | Hendricks | Apr 1929 | A |
2515136 | Pigott | Jul 1950 | A |
4416614 | Moody | Nov 1983 | A |
4418681 | Moody | Dec 1983 | A |
4623279 | Smith | Nov 1986 | A |
4905663 | Magee | Mar 1990 | A |
5252808 | Morgan | Oct 1993 | A |
8608370 | Fishman | Dec 2013 | B1 |
20050115558 | Farmer | Jun 2005 | A1 |
20140083638 | Waniuk | Mar 2014 | A1 |
20160138868 | Bosworth et al. | May 2016 | A1 |
20170227291 | Shea | Aug 2017 | A1 |
20170299265 | Shea | Oct 2017 | A1 |
20180066892 | Shea | Mar 2018 | A1 |
Number | Date | Country | |
---|---|---|---|
20180031320 A1 | Feb 2018 | US |
Number | Date | Country | |
---|---|---|---|
62368468 | Jul 2016 | US |