|Publication number||US3741532 A|
|Publication date||Jun 26, 1973|
|Filing date||Mar 26, 1971|
|Priority date||Sep 8, 1969|
|Publication number||US 3741532 A, US 3741532A, US-A-3741532, US3741532 A, US3741532A|
|Inventors||Farnham R, Plociennik J, Prill F, Smith D|
|Original Assignee||Barber Greene Co|
|Export Citation||BiBTeX, EndNote, RefMan|
|Patent Citations (4), Referenced by (18), Classifications (7), Legal Events (9)|
|External Links: USPTO, USPTO Assignment, Espacenet|
[ June 26, 1973 United States, Patent 1 Farnham et al.
 PROPORTIONING CONTROL SYSTEM FOR 2,877,524 3/1959 259/154 4/1968 Adams......
AN ASPHALT PLANT  Inventors: Robert E. Farnllam, Naperville;
Fredric w u; Donald w Smith, FOREIGN. PATENTS OR APPLICATIONS both of Aurora; Jam
es L. Plociennik, North Aurora, all of I11.
 Assignee: Barber-Greene Company, Aurora,
Primary Examiner-Robert W1 Jenkins Attorney-Clarence J. Fleming ABSTRACT Related US. Application Data  Division of Ser. No. 856,007, Sept. 8, 1969, Pat. No.
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i t nhe P m h W U 0 l S C Pe h mm uke a ob hn nu w P nn Sd ..l nu elm n n??? A.m:mCC hru wm m.
2 Pas 0 5 u d a sum 3 UIF  References Cited found in conventional asphalt plants.
UNITED STATES PATENTS 8/1966 F mham.............;..............
259/154 7 Claims, 4 Drawing Figures PAIENIEDJUI 26 I975 SHEH'HIF I In I J TF Li 1% IIIIII IL In Q"! IV- w m lm r.
PROPORTIONING CONTROL SYSTEM FOR AN ASPHALT PLANT This application is a division of application Ser. No. 856,007, filed Sept. 8, 1969, now US. Pat. No. 3,625,488.
BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to asphalt plants and more particularly to methods and apparatus for controlling the production of asphaltic mixes.
2. Description of the Prior Art Generally, a conventional asphalt plant utilizes certain basic components in order to produce high type asphaltic mixes for use in, for example, heavy-duty roadways. These components include a multiple aggregate cold feed wherein several sizes of stone and sand are required for a suitable mix; a cold conveyor or elevator to gather and transport material from the cold feeders and elevated to a dryer; a dryer for removing moisture from the aggregate and heating the aggregate to mixing temperature, most commonly about 300F.; a dust collector which provides one or more stages of dust collection from the exhaust gases of the dryer to return valuable dust to the system and for providing a draft to support combustion in the dryer; a hot elevator or conveyor for transporting the heated aggregate from the dryer to the screen; a screen for separating the output of the dryer into two or more sizes of stone and sand, which sizes mayor may not match the cold feed sizes; hot bins to receive and store surges of hot aggregates, which aggregates are divided into compartments to match the size segregation afforded by the screen separations; a hot aggregate proportioning mechanism which is usually a hopper on a scale in a batch plant,
and continuous feeders in a continuous plant, for each aggregate; an elevator or conveyor, except in tower plants where the hot bins are mounted over the mixer, for transporting the hot aggregate to the mix; an asphalt proportioning mechanism, usuallya bucket on a scale in batch plants, and a calibrated positive displacement pump in continuousplants, for providing the proper amount of asphalt to the mixture in accordance with the amount of hot aggregate; and a mixer, either batchtype or continuous, to convert the segregated aggregate and asphalt inputs into a homogeneous mix.
Each of the foregoing equipments are expensive, and of course, require a'certain amount of installation area. The screen, for example, is ordinarily a huge machine for present day capacities and would necessarily be increased in size, with an attendant increase in cost, to handle the capacities now being requested for future plants. This alone appears to be impractical. In addition, the hot aggregate proportioning mechanism merely recombines the materials separated by the screen and, inasmuch as material is not manufactured,
the cold feed must be correct in order to continue the 2-. runs continuously and includes supervision and control of the various operating components thereof resulting in a more compact and economical facility which may be operated at a high rate of production.
SUMMARY OF THE INVENTION According to the invention, the above-described screen, hot bins, aggregate proportioning mechanism and hot elevator of present production techniques may be eliminated and asphalt production may be realized by the utilization of a system employing the other mentioned equipments under the control of a supervisory and control system which employs sensing apparatus located at certain flow stations within the plant for signalling a monitoring system which, in turn, controls the amount of material inputs to the mixer. This control is effected by sampling the hot aggregates flowing into the mixer and controlling material flow in accordance with the samples. The amounts of cold and hot feeds to the dryer and mixer, respectively, and dust from the dust collector, are determined by weighing mechanism which provides signals as a function of weight to the control system. The control system causes samples to be made of the hot aggregate for adjusting the flow of aggregate and controls the output of asphalt pumping equipment in accordance with the hot aggregate input into the mixer.
It is therefore a primary object of the invention to ,provide a new asphalt plant which will operate at ahigher rate of production and at a lower rateof cost than present asphalt plants.
Another object of theinvention is to provide an asphalt plant in which material flow is continuously monitored and controlled by a supervisory and control system.
BRIEF DESCRIPTION OF THE DRAWINGS Other objects, features and advantages of the invention, its organization, construction and operation will be readily apparent from the following description of a preferred embodiment thereof, taken in conjunction with the accompanying drawings, although variations and modifications may be effected without departing from the spirit and scope of the novel concepts of the disclosure, and in which:
FIG. 1 is a schematic diagram of an asphalt plant according to the present invention which employs a supervisory and control system;
FIGS. 2A andZB together form an elevational view of an asphalt plant constructed and operable in accordance with the techniques of the present invention; and
FIG. 3 is an elevational view of a sampling .bin which may be advantageously employed in practicing the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENT to a second elevator or conveyor 19 which is moving in a direction indicated by the arrow 20.
Conveyor l9 delivers the cold aggregate to input 22 of a dryer 21. In the dryer the aggregate is heated for drying and for elevating its temperature to that suitable for mixing, preferably about 300F at which temperature it is delivered from the output 23 of dryer 21 to a conveyor 24 for movement to a mixer. In addition to outlet 23, dryer 21 has a second output 25 connected to a duct 26 through which air is drawn to support combustion for the dryer and for collecting dust given off from the aggregate during the drying process. This dust is valuable and should be returned to the aggregate flow.
Conveyor 24 operates in a direction indicated by arrow 31 to carry the hot dried aggregate to input 33 of a mixer pug mill 32.
Asphalt tank 40 supply a flow of liquid bitumen by way of pump 41, meter 42 and conduit 43 to an asphalt spray bar 43' in input 33 of the mixer 32, whereupon the asphalt and the aggregate are mixed as is well known in the art and delivered by way of mixer output 34 to a conveyor 35 operating as indicated by arrow 36 Conveyor 35 transports the asphalt composition to a mix storage hopper 37 having an input 38 for receiving the mix and an output 39 for servicing haulage vehicles.
The asphalt material stored in hopper 37 includes the aforementioned valuable dust which is drawn by way of duct 26 into a dust storage apparatus 27 having a dust collector 27a which separates the dust from the exhaust gases, a dust storage bin 27b and an output 28 which meters the dust onto conveyor 24 by way of conveyor 29 operating as indicated by arrow 30.
Conveyor 19, conveyor 24 and conveyor 29 each include a continuous weighing device operably associated therewith as referenced at 56, 61, and 59, respectively. Each of these weighing devices continually monitor the amount of aggregate flowing thereover and provides indications to a supervisory and control apparatus 54 over the respective signalling channels 55, 60 and 58. In this manner the amount of material traversing the cold conveyor, the hot conveyor and the dust conveyor may be continuously monitored by weight. In addition to the monitoring of total aggregate weight for delivery to the mixer, the present invention utilizes apparatus for monitoring the quality of the aggregate being supplied. In this connection, attention is invited to conveyor or chute 44 of FIG. 1 which receives samples of hot aggregate from the input to the mixer 32 and provides the sample to a separating screen 46 as a part of the sampling apparatus 73 and the weighing apparatus 45 for the samples. Screen 46 separates and sizes the aggregate into separate bins 47, 48, 49, and 50 for individual weighing thereof. The total weight of the individual aggregates are detected by scale 63 and signals to the supervisory and control circuit 54 over buss or channel 62 for monitoring. Individual weights, obtained by a subtraction process upon dumping, are recorded. Referring specifically to FIG. 3, the weighing apparatus 45 is illustrated in greater detail as comprising a plurality of bins 47-50 each of which includes an aggregate release apparatus, such as 75, 76 and 77, for releasing individual aggregate components to a chute 51 for delivery from the scale to a conveyor 52, upon receipt or release signals over channel 74. The weighing apparatus 45 is ofthe type well known in the art and no further description thereof is deemed necessary except that the scale is adapted to record, and deliver indications of such recordings to the supervisory and control system of the individual aggregate components by way of the scale mechanism 63 and information channel 62.
In order to provide the sampling as just described in general, apparatus such as a Type C cutting sampler is employed at reference 73 as is well known in the crushed stone art. More specifically, such a cutting sampler moves a receptacle through the aggregate flow and delivers the diverted sample of a true cross-section of material flow through a conveyor or chute 44 for delivery to screen 46. In this type of an arrangement screen 46 is much smaller than that required previously in the main flow of material and is therefore not pushed to capacity and accordingly can provide a much more accurate gradation analysis. It can make separations much finer than are practical over a screen which is required to handle the full plant capacity. Advantageously, it can be very small and inexpensive.
In addition to monitoring the weights of aggregate at various points of the plant the present invention includes the control of aggregate flow in accordance with the weights sensed. To realize this capability, the plant is provided with a supervisory control system 54 for receiving the weight indications from the sensing devices 42, 56, 59, 61 and 63 by way of their respective signalling channels 42a, 55, 58, and 62. Further, the control section of apparatus 54 includes outgoing control channel 57 for controlling the individual aggregate feeds and outputs 14-16 of the cold storage feeder containers 11-13 respectively. Also, the system includes a control channel 64 for controlling the flow from pump 41 by way of a pump flow adjuster 6S and a control channel 28a for controlling the output of the dust storage apparatus 27.
The supervisory and control system 54 receives weight signals from the various stations in the asphalt plant and responds accordingly .to vary the aggregate feed and pump operation to meet the requirements of the desired mix. The supervisory and control system 54 detects the aggregate flow rate at sensor 61 and employs the signals therefrom to control the proportioning of other additives, the dust and the asphalt, by way of their respective control channels. The sensors and corresponding signalling channels are employed to signal the control system 54 that the correct amounts are being added and corrections are automatically made if the correct proportions are not being added. Total capacity is sensed by sensor 56, and the apparatus 54 adjusts feeders 14-16 so as to maintain the preset desired flow rate over sensor 56. In addition, the proportional relationship between the feed rates of these aggregates is adjusted occasionally in response to the data received in the gradation analysis at elements 44 and 45. This may be done either manually or automatically.
A reject mechanism 67 is provided for diverting an unwanted aggregate mix which may occasion the input to the mixer. The reject mechanism includes a flop gate 69 and an actuator 68 which are operated manually to divert the aggregate into chute 70. This condition most normally will occur when proportions are not yet stabilized upon startup of the process.
All high-type asphalt paving mixes use dried and heated aggregates. However, there are some mixes which have asphalt emulsions for the bitumen and do not require heating and drying of the aggregate, nor
dust collection. The present invention also applies to such mixes and may be advantageously employed in the production of these cold mixes.
Generally then there has been described a novel asphalt plant having several advantages. Plant cost is reduced, particularly for larger plant sizes in that the components added to the plant of the present invention are less expensive than those eliminated from conventional asphalt plants. Segregation of material in the hot bins is eliminated with the elimination of such bins. There is no material waste such as occurs when the cold feed is out of balance with the gradation unit of a conventional plant. The sampling screen, because it is not in the main flow of material and is therefore not being pushed to capacity, can provide a much more accurate gradation analysis and make separations much finer than are practical over a screen which is required to handle the full plant capacity. In addition, the sampling screen is very much smaller and less expensive than those of conventional plants. The improved cold 7 feed control eliminates surges in the dryer resulting in better dryer operation and the valuable dust is collected and accurately controlled and metered back into the aggregate flow. The asphalt plant becomes more compact and portable with the elimination of the large gradation unit and screen of conventional plants which require a large crane to stack one upon the other.
The present invention makes a recordation practical with respect to continuous plants, such recordation being required by increasing numbers of highway departments and including a printed record of the weight of each ingredient of every batch for quality control of the mix. ln practicing the present invention, as each aggregate sample is removed, screened and weighed, a quality control record is produced.
1. A method of producing asphalt material from a supply of bitumen and a supply of aggregate having a plurality of aggregate components, comprising the steps of feeding the aggregate along a path from the aggregate supply to a first station,
continuously weighing the aggregate being fed,
drying the aggregate at the first station,
exacting dust from the aggregate during drying,
continuously weighing the dried aggregate at a second station along the path, metering the extracted dust back to the path of aggregate travel in accordance with the weight sensed at the second station, varying the aggregate feed in accordance with the weight sensed of aggregate being fed and the weight sensed of aggregate passing the second station,
delivering a flow of bitumen into the path of travel of the aggregate at a third station,
metering the flow of bitumen in accordance with the weight of aggregate sensed at the second station, and
mixing the bitumen and aggregate delivered to the third station.
2. The method defined in claim 1, wherein the step of drying includes heating the aggregate.
3. The method defined in claim 1, comprising the further steps of delivering a portion of aggregate flow from the path upstream of the third station,
separating the portion into the aggregate components,
weighing each of the components and automatically recording the weights thereof, and
delivering the portion back to the path upstream of the second station.
4. The method defined in claim 3, further comprising the steps of controlling individual aggregate component feed in accordance with the weight detected in a diverted portion.
5. A method of producing asphalt material from a supply of bitumen and a supply of aggregate having a plurality of aggregate components, comprising the steps of heating the aggregate,
transporting the heated aggregate along a path,
continuously weighing the aggregate passing a first point along said path,
delivering a flow of bitumen to a second point along said path,
diverting a portion of the aggregate from said path at a third point intermediate said first and second points for sampling,
separating said diverted portion of the aggregate into its constituent components and weighing each of said components,
returning said diverted portion to said path in advance of said second point,
metering the flow of bitumen in accordance with the weight of the aggregate passing said first point and in accordance with the weight of said components, and
thereafter mixing the heated aggregate and the bitumen.
6. A method of producing asphalt material from a supply of bitumen and a supply of aggregate having a plurality of aggregate components, comprising the steps of feeding aggregate from the supply for heating,
continuously weighing the aggregate fed from the pp y. transporting the heated aggregate along a path, continuously weighing the heated aggregate passing a first point along said path, varying the feed of aggregate in accordance with the weight of aggregate being fed from the supply and the weight of aggregate passing said first point, delivering a flow of bitumen to a second point along said path, metering the flow of bitumen in accordance with the weight of aggregate, and thereafter mixing the heated aggregate and the bitumen.
7. A method of producing asphalt material from supply of bitumen and a supply of aggregate having a plurality of aggregate components, comprising the steps of heating the aggregate,
extracting dust from the aggregate during heating of the aggregate,
transporting the heated aggregate along a path,
continuously weighing the aggregate passing a first point along said path, transporting the dust to said path and metering the dust into the heated aggregate in accordance with the weight of aggregate passing said first point,
delivering a flow of bitumen to a second point along said path,
metering the flow of bitumen in accordance with the weight of aggregate, and
thereafter mixing the heated aggregate and the bitumen.
t 4 t i
|Cited Patent||Filing date||Publication date||Applicant||Title|
|US2877524 *||Jul 1, 1954||Mar 17, 1959||Mechanical Handling Sys Inc||Apparatus for mixing and feeding shell molding material|
|US3263971 *||Mar 21, 1962||Aug 2, 1966||Barber Greene Co||Automatic sampling means for asphalt plants|
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|FR1541717A *||Title not available|
|Citing Patent||Filing date||Publication date||Applicant||Title|
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|US5251976 *||Apr 6, 1992||Oct 12, 1993||Astec Industries, Inc.||Asphalt plant adapted for the batch production of asphalt mix containing recycle asphalt paving|
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|US9146554 *||Oct 16, 2012||Sep 29, 2015||Adam Hoban||Aggregate processing control system|
|US20020075753 *||Jul 3, 2001||Jun 20, 2002||Kevin Taylor||Asphalt additive mixing apparatus and methods|
|US20050018530 *||Jul 21, 2003||Jan 27, 2005||Alain Romier||Method of manufacturing a bituminous coated aggregate mix|
|US20120051982 *||Aug 25, 2010||Mar 1, 2012||Kois Brother Equipment Co.||Brine maker|
|US20140108182 *||Oct 16, 2012||Apr 17, 2014||Okanagan Quality Control Ltd.||Aggregate processing control system|
|EP2354879A1 *||Jan 19, 2011||Aug 10, 2011||Famaro||Method to estimate the target flow of bitumen or bituminous binders to be introduced in an installation producing bituminous conglomerate in continuous|
|U.S. Classification||366/7, 366/8, 366/18|
|International Classification||E01C19/10, E01C19/02|
|Jul 10, 1995||AS||Assignment|
Owner name: ASTEC INDUSTRIES, INC., TENNESSEE
Free format text: TERMINATION & RELEASE OF SECURITY INTEREST IN PATENTS;ASSIGNOR:NATIONSBANK OF GEORGIA, N.A. (F/K/A CITIZENS AND SOUTHERN TRUST COMPANY, N.A.);REEL/FRAME:007603/0227
Effective date: 19940720
Owner name: FIRST NATIONAL BANK OF CHICAGO, N.A., THE, ILLINOI
|Dec 9, 1991||AS||Assignment|
Owner name: CITIZENS AND SOUTHERN TRUST COMPANY (GEORGIA), GEO
Owner name: FIRST NATIONAL BANK OF CHICAGO, THE, ILLINOIS
Free format text: AMENDMENT TO A PREVIOUSLY RECORDED SECURITY AGREEMENT DATED APRIL 27, 1989;;ASSIGNORS:BARBER-GREENECOMPANY;ROADTEC, INC.;TRENCOR JETCO, INC.;REEL/FRAME:006113/0075
Effective date: 19910301
|Dec 9, 1991||AS99||Other assignments|
Free format text: FIRST NATIONAL BANK OF CHICAGO, THE ONE FIRST NATIONAL PLAZA SUITE 0173 CHICAGO, * BARBER-GREENE COMPANY : 19910301; ROADTEC, INC. : 19910301; TRENCOR JETCO, INC. : 19910301 OTHER CASES: NONE; AMENDMENT TO A PREVIOUSLY RECORDED SECURITY AGREEMENT DATED
|Jun 14, 1990||AS||Assignment|
Owner name: FIRST NATIONAL BANK OF CHICAGO, THE
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|Jul 18, 1988||AS||Assignment|
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|Jul 6, 1987||AS||Assignment|
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|May 27, 1987||AS||Assignment|
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|Jan 16, 1987||AS||Assignment|
Owner name: BARBER-GREENE COMPANY, 400 N. HIGHLAND AVE., AUROR
Free format text: RELEASED BY SECURED PARTY;ASSIGNOR:FIRST NATIONAL BANK OF CHICAGO AS AGENT FOR SEE DOCUMENT FORNAMES;REEL/FRAME:004688/0001
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