A typical asphalt mix plant is comprised of a cold aggregate storage system. This can be a series of storage piles, or bins that hold the structural elements of asphalt, such as sand, crushed rock, mineral fillers, and the like, collectively referred to as aggregate. Additionally, Reclaimed Asphalt Pavement (RAP) or Reclaimed Asphalt Shingles (RAS) can be a component of an aggregate blend.
A liquid asphalt binder which is added to the aggregate or blend aggregate and RAP is stored in heated tanks. The liquid asphalt binder may be a PG graded binders identified by well-known ASTM D6373 or AASHTO M320 or M332 standards or an asphalt emulsion which meets grades identified by well-known ASTM D977 or D 2397 or AASHTO M140 or M208 standards. The asphalt emulsion may include any of a variety of softening or rejuvenating oils obtained from petroleum refining or derived from biological sources such as soybean, corn, flax seed, rape seed and other sources of seed oil. Additionally, bio-derived oils may be obtained from tree sources where tall oil (obtained as a by-product of the Kraft paper pulping process) may be used in crude, distilled, or in modified forms.
The aggregate is then fed into a drum dryer heater, to which is added RAP (if used) and the asphalt binder. The drum dryer heater heats, dries and mixes the components to produce the finished asphalt mix. This drum mix process is well known in the bituminous paving industry. Bituminous mix plants known as batch plants may accomplish the same finished asphalt mix and although the process is not used as widely today the batch plant mixing procedure is also well known in the paving industry.
The drum mixer is typically heated with an open flame burner using a fuel source, such as natural gas, LP gas, or fuel oils ranging from #2 through #6 or slurry oil.
The finished asphalt mix is then normally conveyed to a storage silo, and then dispensed as needed into trucks that take the finished asphalt to an application site.
Such plants may also include dust collectors, a bag house to remove harmful or volatile particulates, screens, scales, bitumen storage system, heaters for maintaining asphalt binder at usable temperatures, or an onsite generator for power unless power is commercially available for the plant.
Thus, asphalt mix plants require a great deal of infrastructure and special air pollution permitting. They need to be able to produce large volumes of asphalt to justify the expense; however, the demand for asphalt in most of the country is seasonal and/or sporadic. In the winter, in colder climates, it may not be possible to produce and supply asphalt; and as a result plants may shut down for a large portion of the year. These economics place constraints on when and where asphalt can be produced.
Another type of plant comprises a portable asphalt mix plant. Portable asphalt mix plants are similar to the plant described above, but typically would include one or two silos for storage and the asphalt mix produced is for a specific project. In some circumstances, the portable plant can be operated at a remote site and provides asphalt mix to customers on an as needed basis. Other plants may use some form of a silo at the end of the process to store a “batch” of finished asphalt mix of predetermined size that can be loaded, for example, into a truck.
As noted above, because of the cost of fixed site plants, the long hauling distances from permanent plants to the job site, and the sometimes infrequent demand for asphalt, portable plants may be set up to meet a specific short term need. For example, smaller municipalities, or counties, may have a small demand for asphalt at any given time, that would not justify a permanent plant, and instead they save up the demand and then use a portable plant every few years or as needed to make the asphalt or bituminous mix.
This is not an optimal situation, as the plants are still expensive to move, setup, and take down, and the need to wait until sufficient capacity has built up means that needs may be unmet for years before the demand justifies setting up a portable asphalt mix plant.
In some situations, the raw materials may not need to be stored on site, and especially with the portable asphalt mix plants, the raw materials must be brought on site in bulk quantity or in what are known as super sacks. Super sacks are large bags of aggregate, treated aggregate, reclaimed asphalt pavement (RAP), and other raw materials typically used in an asphalt mix in the range of 2,000 to 5,000 pounds. These super sacks may be brought to the mix site as needed.
In any event, substantial infrastructure is still needed, which is expensive and time consuming to set up, move, and/or maintain. This is especially the case when even under the best of conditions the asphalt mix plant may be idle a great deal of the year due to weather or demand issues. Thus, a need exists for a batch asphalt mix plant that eliminates the drawbacks of the prior art.
The present disclosure relates to a plant for manufacturing finished asphalt mix (in Europe, asphalt mix or finished asphalt mix are typically referred to as bituminous mix or finished bituminous mix; those skilled in the art readily understand this distinction). In particular, the disclosure relates to a batch asphalt mix plant for using a microwave heating vessel located in close proximity to a heated storage silo to maintain temperature of the finished asphalt mix at the point of production
One embodiment is a mobile batch asphalt mix plant comprising a flatbed trailer, an electric generator mounted the trailer, a microwave energy system powered by the generator, wave guides directing microwave energy into one or more heating vessels, a conveyor and dragline to move unheated asphalt from a hopper to the heating vessel, and a silo for storing asphalt heated in the heating vessel with microwave energy.
In some embodiments the microwave energy system comprises a single microwave transmitter; in other embodiments the microwave energy system comprises a plurality of microwave transmitters.
In other embodiments the heating vessel contains agitation mechanisms to mix the asphalt during heating. One embodiment of an agitation mechanism a plurality of paddles that move the asphalt from one side of the heating vessel to the other side during heating. Another embodiment of an agitation mechanism is a pug mill to mix the heated asphalt before being moved the silo for storage.
Another embodiment is a stationary batch asphalt mix plant comprising a source of electricity, a microwave energy system powered by the source of electricity, wave guides directing microwave energy into one or more heating vessels, a conveyor and dragline to move unheated asphalt from a hopper to the heating vessel, and a silo for storing asphalt heated in the heating vessel with microwave energy.
Still another embodiment is a modular batch asphalt mix plant with a low energy heating system comprising two T-shaped wings, wherein a first wing houses various facility components comprising a microwave energy system and a microwave heating vessel; and a second other wing comprises three or more modular silos for storage of heated asphalt.
An embodiment of a process for using a batch asphalt mix plant described in this disclosure to produce a finished asphalt mix comprises the steps to moving an asphalt mix from a hopper to a microwave heated batcher, heating the asphalt mix in the microwave heated batcher to a predetermined temperature using only microwave energy to provide a finished asphalt mix, and moving the finished asphalt mix to a silo for storage. In some embodiment the asphalt mix comprises aggregate, treated aggregate, RAP, RAS or combinations thereof.
In all disclosed embodiments, heated, liquefied asphalt binder (bitumen) or asphalt emulsion (generally referred to as a binder component) may added to the aggregate, treated aggregate, RAP, RAS or combinations thereof (generally referred to as an aggregate component) prior to introducing the combined aggregate component and binder component into the microwave heated batcher and mixing systems described below. The binder component may be added to the aggregate component well in advance of or just prior to the microwave heating and mixing procedure or at the time of actual production. A heated, liquefied asphalt binder could be added directly to the aggregate or in the form of foamed bitumen. A pug mill mixer could be used to incorporate the binder component into the aggregate component, although it is understood that intimate mixing of binder and aggregate is not accomplished as this stage.
An electrical generator 14 is located on the trailer 12 to provide electricity to power the plant, or a connection for house power is provided (which is especially useful with the stationary plant configuration). The generator 14 can run on a variety of fuels such as diesel, fuel oil, gasoline, natural gas, and the like. Also, provided is a microwave energy system 16, and in particular a Low Energy Heating System (“LEHS”), wherein a LEHS power unit powers a plurality of microwave transmitters. The LEHS power unit typically includes a plurality of microwave transmitter units (not shown) with a splitter/wave guides that direct microwave energy from each transmitter into one or more rotary head heating chambers, stationary corporate wave guides can also be used, using either 2.4 GHz or 915 MHz. The microwave process is referred to in this disclosure as LEHS or as a mobile low energy heating system (“MLEHS”). Using a single or multiple microwaves transmitters in a series gives the ability to cycle the power and intensity to achieve the best heating results over a controlled surface. The microwave energy in
A hopper is provided where unheated aggregate or a mixture of unheated aggregate and RAP (or alternatively RAS) is loaded. This aggregate material may be loaded from stockpiles using a front end loader or in some instances may be brought to a mixing site in super sacks 22. In some embodiments, the aggregate is combined or treated with an emulsified asphalt binder when it is used in the disclosed batched asphalt mix plant.
The aggregate material is carried along the top of drag line (slat conveyor) 20, where it then falls into a drop chute 24, and then into the LEHS batcher 26. The batcher 26 receives the microwave energy from the wave guide 18. The asphalt mix is heated in the batcher 26 and the entire batch is then delivered to a silo 28. The finished asphalt mix can be stored in the silo until it is loaded into a truck. In another embodiment, the heating vessel is designed without any agitation mechanism and instead uses additional wave guide splits (not shown) that can be mounted either on the top of the silo or on the ground where heating can occur, and then conveyance of the heated material to the silo for storage. Ramps 29 are provided (or gravel can be used) to allow the truck to move under the silo for material loading. The silo 28 is on a tilt-able mount and can be moved to a flat position on the trailer for transportation.
In order to more effectively heat the material a mixer 58 is provided, having a plurality of paddles 58a (preferably stainless steel) that move the material from one side of the cavity to the other and back again. In another embodiment, this mixing can occur outside the LEHS cavity, with a detached mixer (not shown). The mixer 58 is powered by motor 59 attached to the side of the LEHS cavity. Microwave energy enters the LEHS cavity through a wave guide 51. After the bituminous mixture is heated by the microwave energy, the mixture is dropped through doors 57a and 57b at the bottom of the LEHS cavity into the silo for storage and eventual distribution.
In one embodiment, the asphalt mix plant is mobile; however, the disclosed microwave batcher/cavity can be adapted to a stationary asphalt mix plant as well. The asphalt mix plant can be used with super sacks of aggregate, treated aggregate, with some percentage RAP (including up to 100% RAP), RAS or combinations thereof. Depending on the anticipated amount of finished asphalt mix needed, the time of year, and geographical location the aggregate, treated aggregate, RAS and/or RAP can be stockpiled outside or inside a building. The microwave batcher cavity or vessel is adapted for heating batch sizes in the range of 1 to 4 tons of bituminous mixture, which is typically heated to a temperature in a range of about 280° F. to 325° F. The target heating temperature will vary depending on the type of bituminous mixture or asphalt used, the time of year, and hauling distance and in some instances could be outside the typical target temperature range stated above. The silo can hold in the range of 50-75 tons of finished asphalt mix.
As shown above the disclosed asphalt mix plant may include a microwave heating vessel that is attached to the end of the conveyor, that sits between the slat conveyor and silo but is attached to the silo, or alternatively the heating vessel can be located in the silo itself. In particular, the heating vessels illustrated in
In particular, this figure illustrates 3 modular silos (labeled 94A, 94B, 94C and shown transparently in
Finished asphalt mix is moved to the silos by a combiner 96, which uses a series of paddles (not shown) to move and mix the finished asphalt mix from the microwave rotary heating vessel 98 to the silos 94A, 94B and 94C. Drop chutes (not shown) located on the underside of the combiner allow the finished asphalt mix to drop from the combiner into the chosen silo. The drop chutes can be mechanically operated to allow for selection between the silos, such that the silos can be filled on demand. For example, diverters can be used to channel the flow of the finished asphalt mix to the appropriate drop chute and silo. The silos, as well as the combiner are wrapped in insulated jackets, and an oil boiler (or similar system) can be used to circulate hot oil thereto to ensure that the finished asphalt mix is kept at a stable elevated temperature after leaving the microwave vessel in a target temperature range of about 280° F. to 325° F.
The second level 102 can include space for offices, as well as facility equipment such as the HVAC unit for heating and cooling any of the various areas of the plant including the vessel area as well as the office space.
At the second highest level 106 LEHS power units are located. The power units are electrically power and included a magnetron for generating microwave energy. Wave guides channel the microwave energy waves to the heating vessel. The microwaves can be introduced into to the vessel directly or using rotary joints.
The finished asphalt mix is introduced into the combiner 120 through a hatch 121 that can be open and closed as needed. A set of paddles 122 move the finished asphalt mix along the length of the combiner under the power of an electric motor 123. Exit gates 124 are located along the bottom of the combiner over the silos (not shown), which can be selectively opened and closed to fill the silos. The combiner 120 is preferably insulated to avoid heat loss, and lined with a material that is not susceptible to microwave heat such as stainless steel. Heated oil can be circulated through the lining of the combiner to heat the combiner to a temperature consistent with that of the finished asphalt mix.
The advantage of the present invention is that it greatly simplifies the components of an asphalt mix plant and in particular a mobile plant. By eliminating the need for a large costly heater the present invention greatly reduces the required infrastructure and cost associated with prior art plants. Further, the heating step is moved to the point of storage which also reduces the amount of infrastructure. For example, since heated asphalt mix is no longer moved on a conveyor, the conveyor experiences far less wear and tear which occurs when the belts move heated asphalt mix. The present invention allows for small cost effective mobile plants to be used in environments where it was not cost effective in the past. Still further, the present invention makes it possible for retail providers of cold mix asphalt to easily provide hot mix asphalt by reducing the cost of such a plant, and the space needed for a plant. The asphalt mix plant of the present invention can be used at a retail home center and the like to provide hot mix asphalt. Municipalities which lack the demand for a dedicated prior art asphalt mix plant, can now afford to have a plant or more easily set up a temporary mobile plant at any time instead of waiting until long periods of time until the demand justified the investment.
These and other advantages will be apparent to those of ordinary skill in the art.
While the various embodiments of the invention have been described, the invention is not so limited. Also, the method and apparatus of the present invention is not necessarily limited to any particular field, but can be applied to any field where an interface between a user and a computing device is applicable. There are two earlier filed and related U.S. patent applications, U.S. Ser. Nos. 13/887,828 and 13/887,859; the disclosures of which are hereby incorporated by reference.
Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention belongs. Although methods and materials similar to or equivalent to those described herein can be used in the practice or testing of the present invention, suitable methods, and materials are described below. All publications, patent applications, patents, and other references mentioned herein are incorporated by reference in their entirety to the extent allowed by applicable law and regulations. In case of conflict, the present specification, including definitions, will control.
The present invention may be embodied in other specific forms without departing from the spirit or essential attributes thereof, and it is therefore desired that the present embodiment be considered in all respects as illustrative and not restrictive, reference being made to the appended claims rather than to the foregoing description to indicate the scope of the invention. Those of ordinary skill in the art that have the disclosure before them will be able to make modifications and variations therein without departing from the scope of the invention.
This application claims priority to International Application No. PCT/US2017/023840, filed on Mar. 23, 2017, which claims the benefit of U.S. Provisional Patent Application No. 62/312,168, filed on Mar. 23, 2016, entitled “BATCH ASPHALT PLANT”, the entire disclosures of which are incorporated by reference for all purposes.
Filing Document | Filing Date | Country | Kind |
---|---|---|---|
PCT/US2017/023840 | 3/23/2017 | WO | 00 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2017/165664 | 9/28/2017 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
3239643 | Kluck | Mar 1966 | A |
3665141 | Schiffmann et al. | May 1972 | A |
3774003 | Kaufman | Nov 1973 | A |
3856275 | Dydzyk | Dec 1974 | A |
4176267 | Rueggeberg | Nov 1979 | A |
4180718 | Hanson | Dec 1979 | A |
4252459 | Jeppson | Feb 1981 | A |
4253005 | Gordon et al. | Feb 1981 | A |
4276093 | Pickermann | Jun 1981 | A |
4319856 | Jeppson | Mar 1982 | A |
4338869 | Hoskinson | Jul 1982 | A |
4488027 | Dudley et al. | Dec 1984 | A |
4619550 | Jeppson | Oct 1986 | A |
4861955 | Shen | Aug 1989 | A |
5083870 | Sindelar et al. | Jan 1992 | A |
5092706 | Bowen et al. | Mar 1992 | A |
5242493 | Glynn et al. | Sep 1993 | A |
5303999 | Nath et al. | Apr 1994 | A |
5447388 | Rouse | Sep 1995 | A |
5902510 | Balbaa et al. | May 1999 | A |
6186700 | Omann | Feb 2001 | B1 |
6207462 | Barclay et al. | Mar 2001 | B1 |
6455826 | Araya et al. | Sep 2002 | B1 |
6618957 | Novak et al. | Sep 2003 | B2 |
6768089 | Minobe et al. | Jul 2004 | B2 |
7432483 | Wilson | Oct 2008 | B2 |
7758235 | Collette | Jul 2010 | B1 |
7927465 | Novak | Apr 2011 | B2 |
7931806 | Logan et al. | Apr 2011 | B2 |
8101893 | Bogdan | Jan 2012 | B2 |
8586898 | Novak | Nov 2013 | B2 |
9624625 | Coe | Apr 2017 | B2 |
9642194 | Wilber et al. | May 2017 | B2 |
10081920 | Coe | Sep 2018 | B2 |
10214786 | Logan et al. | Feb 2019 | B2 |
10239331 | Gervais et al. | Mar 2019 | B1 |
10294616 | Crupi et al. | May 2019 | B2 |
20020191481 | Cox et al. | Dec 2002 | A1 |
20070122235 | Kasahara et al. | May 2007 | A1 |
20100020630 | Musil | Jan 2010 | A1 |
20130343145 | Villalobos Davila | Dec 2013 | A1 |
20140119829 | Eliot | May 2014 | A1 |
20140146632 | Eliot | May 2014 | A1 |
20150164108 | Logan et al. | Jun 2015 | A1 |
20150237684 | Huber | Aug 2015 | A1 |
20180187385 | Reinke et al. | Jul 2018 | A1 |
20190017233 | Coe | Jan 2019 | A1 |
Number | Date | Country |
---|---|---|
2051445 | Oct 1990 | CA |
2660700 | Feb 2008 | CA |
108547199 | Sep 2018 | CN |
2627588 | Dec 1977 | DE |
0529285 | Jul 1992 | EP |
1611788 | Jan 2006 | EP |
2689833 | Jan 2014 | EP |
2522798 | Sep 1983 | FR |
2755450 | May 1998 | FR |
2008518930 | Jun 2008 | JP |
101251102 | Apr 2013 | KR |
1993009647 | May 1993 | WO |
1996034241 | Oct 1996 | WO |
2006050122 | May 2006 | WO |
2006057563 | Jun 2006 | WO |
2011036773 | Mar 2011 | WO |
2013166489 | Nov 2013 | WO |
2013166490 | Nov 2013 | WO |
2017165664 | Sep 2017 | WO |
2018154094 | Aug 2018 | WO |
Entry |
---|
International Search Report for Application No. PCT/US2017/023840, dated Jul. 6, 2017, 6 pages. |
Written Opinion for Application No. PCT/US2017/023840, dated Jul. 6, 2017, 7 pages. |
Extended European Search Report for European Application No. 17771164.5, dated Dec. 10, 2019, 12 pages. |
Extended European Search Report for 13785234.9 dated Jun. 28, 2016. |
Number | Date | Country | |
---|---|---|---|
20190100886 A1 | Apr 2019 | US |
Number | Date | Country | |
---|---|---|---|
62312168 | Mar 2016 | US |