The present disclosure relates to devices for detecting concentrations of particulate matter in air and more particularly to a mass loading monitor for real time detection and warning of potentially explosive concentrations of dust, powder or particulate matter in air from industrial and commercial processes.
The statements in this section merely provide background information related to the present disclosure and may or may not constitute prior art.
Airborne dust or powder of, for example, sugar, grain and wood, escaping from industrial process machinery in a sufficient concentration can support rapid combustion and explosions. Such explosions typically occur in a confined or semi-confined space although an unbounded cloud can also support an explosion. Agricultural processes which occur at grain handling facilities such as transfer and storage depots, grain mills and cereal plants are particularly prone to this phenomenon. The following table highlights the losses over a recent ten year period (1996 to 2005) attributed to dust explosions in agricultural processing facilities in the United States.
Spray dryers are particularly vulnerable to this problem since they purposefully concentrate the powdered material before transferring it. The current response to this problem is to accept the possibility of an explosive event and incorporate, for example, explosion panels. These may either be passive devices—simply a weak component of the confining surface that gives way upon an explosion—or active devices that sense pressure in the device and release a panel. Alternatively, a dust suppressant may be routinely deployed in the spray dryer chamber.
Consideration of the foregoing current solutions to this problem leads one to the conclusion that an apparatus and technique to avoid this problem rather than to mitigate its effects would be a welcome addition to these industrial and commercial enterprises. The following disclosed and claimed invention is so directed.
The present invention provides a mass loading monitor for measuring in real time the particulate, i.e., powder, dust and the like, content of air inside an industrial or commercial processing facility and providing a warning signal indicating the existence of a potentially explosive atmosphere in the facility. Optionally, the mass loading monitor may be configured to indicate the sensed level of particulate matter and to shut down the facility until the level of particulates drops to a safe level.
In an first embodiment, the mass loading monitor comprises two parallel cylinders, one of which is charged with clean, ambient air and the other of which is charged with air from within the facility containing dust, powder or other particulate matter. A piston resides within each cylinder and the pistons are commonly accelerated for a short distance during which time the pressure at each piston face is measured. The time integrals of the pressures from each of the piston faces are evaluated over the period: from rest to the time of discharge from the open end of the cylinders. The ratio of these integrals defines the difference in the densities within the cylinders. Lookup tables keyed to the type of material and relative humidity within the facility are then utilized to determine the explosion potential and provide an alarm or other indication that a predetermined concentration has been exceeded.
In a second embodiment, the same theory of operation is applied but only a single piston and cylinder assembly is utilized. Here, the single piston and cylinder assembly is first calibrated by determining the time integral of pressure with clean air at known temperature and barometric pressure. The assembly is then filled with particulate laden air and the time integral of pressure is compared to the calibration data and the density of the particulate laden air and its explosion potential is determined.
Thus it is an object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air.
It is a still further object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air in a processing facility for sugar, grain, wood and similar dust or powder producing materials.
It is a still further object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air in a processing facility for sugar, grain, wood and similar dust or powder producing materials and providing an alarm or other indication that a threshold concentration level has been reached or exceeded.
It is a still further object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air by accelerating samples of clean and particulate laden air to determine their time integrals of pressure and comparing the computed densities of the clean and particulate laden air.
It is a still further object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air having a pair of parallel cylinders in which a respective pair of pistons accelerate samples of clean and particulate laden air.
It is a still further object of the present invention to provide an apparatus for monitoring the concentration of particulate matter in air having a single piston and cylinder assembly that is calibrated with clean air and charged with particulate laden air.
It is a still further object of the present invention to provide a method for monitoring the concentration of particulate matter in air.
It is a still further object of the present invention to provide a method for monitoring the concentration of particulate matter in air by accelerating samples of clean and particulate laden air, determining the time integrals of pressure and comparing the computed air densities.
It is a still further object of the present invention to provide a method for monitoring the concentration of particulate matter in air in a processing facility for sugar, grain, wood and similar dust or powder producing materials and providing an alarm or other indication that a threshold concentration level has been reached or exceeded.
Further objects, advantages and areas of applicability will become apparent from the description provided herein. It should be understood that the description and specific examples are intended for purposes of illustration only and are not intended to limit the scope of the present disclosure.
The drawings described herein are for illustration purposes only and are not intended to limit the scope of the present disclosure in any way.
The following description is merely exemplary in nature and is not intended to limit the present disclosure, application, or uses.
With reference to
The grain processing facility 10 includes a building or superstructure 12 which typically encloses the processing machinery which is installed on one or more floors 14. Railway gondola cars 16, trucks or other vehicles may supply raw material(s) to the facility 10 and dump their contents onto one or more horizontal conveyors 18. The conveyors 18 carry the material to a bin or hopper 20 from where they are extracted by a vertical, bucket type conveyor 22 or similar device. Cooperating horizontal conveyors 24 then carry the material to, for example, grinding or milling equipment 26 for processing or to one or more silos 30 for storage. The silos 30 include controllable outlets 32 which selectively supply material to an additional conveyor or conveyors 34 which, for example, provide material to the bin or hopper 20 or other collecting points.
At eight locations within the grain processing facility 10 are preferably disposed a mass loading monitor 40 according to the present invention. It will be appreciated, however, that more or fewer mass loading monitors 40 may be suitable or desirable in this exemplary facility 10, and that the actual number of monitors 40 preferred or necessary in a given facility will depend upon the construction and layout of the facility, upon its machinery, upon the nature of the material processed in the facility and other variables.
Referring now to
An open end of the first cylinder 50 is enclosed within a first valve or control box 60. The air supply 52 communicates with the interior of the first control box 60 as does the open end of the first cylinder 50. A first hinged panel 62 controlled by a first two position actuator 64 opens and closes the first hinged panel 62 which acts as a valve to allow the air within the first cylinder 50 to be exhausted to the ambient through the control box 60.
The second cylinder 70 which is essentially identical to the first cylinder 50 is a measurement cylinder and is supplied with air that contains dust, powder or other particulate matter from a region of a facility such as the grain processing facility 10. The open end of the second cylinder 70 is enclosed within a second valve or control box 72. A second hinged panel 74 is controlled by a second two position actuator 76. The second hinged panel 74 opens and closes to allow the particulate laden ambient air to be drawn into the second cylinder 70 through the control box 72 and to be exhausted (returned) to the ambient. A third hinged panel and two position actuator 78 provide selective communication between the first valve or control box 62 and the second valve or control box 74 to allow clean air into the second control box 74 and the second cylinder 70.
Referring now to
As illustrated in
Disposed adjacent the flat face 84 of the main piston 82 in a rest or quiescent position but moveable axially relative thereto is a light or secondary piston 112. The light piston 112 includes a circular aperture or port 114 which is preferably the same size as the circular aperture or port 88 on the main piston 82 and is aligned therewith as illustrated in
An annular band of a plurality of ports or apertures 122 extend around each of the cylinders 50 and 70 at an axial location just beyond the limit of translation of the main pistons 82. The ports or apertures 122 may be round, as illustrated, rectangular or another configuration. Extending about the circumference of each of the cylinders 50 and 70 in general alignment with the ports or apertures 122 is an axially, bi-directionally movable sleeve 124. In the position illustrated in
Referring again to
When the linear drive motor 140 is activated, the first and second main pistons 82 and the first and second light pistons 112 translate together in the respective first and second cylinders 50 and 70. To translate only the light piston drive rod or shaft 116 and the light piston 112 of the first piston assembly 80 and the light piston drive rod or shaft 116 and the light piston 112 of the second piston assembly 120, only the light piston drive assembly 130 is activated. The linear drive motor 140 also includes a control assembly 148 which directs pneumatic or hydraulic flow or the supply of electrical energy to the linear drive motor 140 to achieve such bi-directional translation as those skilled in the art will readily understand.
In an alternative construction illustrated in
The mass loading monitor 40 is intended and designed to determine whether a particular concentration of particulate matter in the air of a facility such as the grain processing facility 10 is approaching the minimum explosive concentration (MEC). The MEC is specified as a density: X grams per cubic meter. The magnitude of X depends upon the material, for example, sugar, coal, sawdust, oats and wheat, and varies also with the relative humidity level. Nominal values are in the range of 30 to 80 grams per cubic meter. Typical sea level ambient density is on the order of 1.2 Kg per cubic meter and thus the resolution required is between 2.5 and 6.67%.
The measurement strategy of the mass loading monitor 40 follows from the recognition that a density difference (ρw−ρw/o) is sought and that discharging air with particulates (w) and without particulates (w/o) from a cylinder—by the action of an accelerating piston can yield (ρw−ρw/o). The following analysis illustrates how the pair of cylinders 50 and 70 can determine (ρw−ρw/o). Alternatively, a second embodiment 200, illustrated in
Referring now to
which leads to
where p is the pressure at the face of the piston, is the wall shear stress, u and ρ are the axial velocity and density of material within the cylinder 70. Experimental data reveal that the initial motion of the piston assemblies 80 and 120 compress and displace the air in the cylinders 50 and 70 in a progressive manner. That is, there is a time lag (approximately 0.01 sec. as presented in
The “small” dust or powder loading (≦80 g/m3) with respect to the density of the ambient air (≈1.1 Kg/m3) makes it rational to assume that the term γ will be unaffected by the presence or absence of particulate matter in the cylinders 50 and 70. In contrast, the basis for the measurement process is the dependence of the terms α and β on the presence or absence of particulate matter. The two conditions are designated by the symbols: with particulates ( )w: α, β and without particulates ( )w/o: α, β.
During calibration or at any time during its service life, the mass loading monitor 40 can be operated with clean air in both cylinders 50 and 70 to quantify minor differences in their operating characteristics. Specifically, the operating theory and computations presented herein do not require identical performances for (α), (β) and (γ) with identical cylinder charges of no particulates although this will be assumed for the analytical structure of the data processing. The correction scheme, to be utilized when the air only data are not the same for the cylinders 50 and 70, is to first form the ratio: [β1/β2]*, where β2 represents the cylinder 70 that ingests the particulate matter. Second, when the dust or powder loading is to be determined, the ratio of the measured β2 and β1 values will then be multiplied by [β1/β2]* as a correction coefficient. It is understood that β will represent the corrected β2 value in the subsequent text.
The air in both cylinders 50 and 70 will be at the same temperature and pressure (hence the same density). From Equation 3, the ratio of the (α) terms can be equated to the ratio of the spatially averaged densities since the integrals have identical kinematic features. This is the key step in the mass loading monitor 40 data processing algorithm. It should be appreciated that the time lag to accelerate the airborne particulate matter within the cylinder 70 will not only be small, but evaluating α at the discrete time T also ensures that the acceleration period will not alter the α value.
The desired information: Δρ=<ρw>−<ρw/o>, can be obtained from the ratio <ρw>/<ρw/o> and the separately measured ρw/o. That is, a barometric pressure reading (patm) and the ambient (absolute) temperature T can provide (ρw/o) as: ρw/o=patm/RT, and
From measured data (where βw represents the corrected β2* value)
The ratio γ/β is plausibly <1 since γ depends upon the viscosity of air and the large acceleration (about 15 g's) will create an inertially dominated flow field. With this condition, it is recognized that the bracketed term represents a converged series whereby the bracketed term can be expressed as
The coefficient K can be treated as a calibration constant. Known quantities of small particulates can be added to a vertically disposed cylinder 70 and the piston 120 accelerated before their “leading edge” reaches the piston face. Since (αw/αw/o) will therefore be known and (βw/βw/o) will be measured, K can be determined.
Referring now to
Referring now to
The ratio of the integrands from the integrators 174 is then established in a comparator 176 and this value is multiplied by the constant K in a process (multiplier) step 178. A programmable or read only memory or storage device 182 includes look up tables and other data utilized, for among other purposes, to calculate the minimum explosive concentration (MEC). The MEC, as noted above, varies with the type of material, for example, sugar, coal, sawdust, oats and wheat, and varies also with the relative humidity. This current, necessary information is provided to a computational comparator 184 in which the value of the stored MEC is multiplied by a safety factor 6 to avoid a false negative indication and this value is subtracted from K(βw/βw/o). If the result is greater than or equal to one, a warning signal is provided by an annunciator 186. If the result is less than one, no output or a null or safe signal may be provided by an annunciator 188. Alternatively, as noted above, the warning signal may directly control operations within a processing facility and shut down the machinery generating the MEC without human intervention.
The mechanical cycle of the piston assemblies 80 and 120 of the embodiment illustrated in
Operation of the alternate construction illustrated in
Referring now to
Referring now to
The double cam follower assembly 230, illustrated in
The first drive disc 222 includes a first complex cam track 224 utilized to rapidly accelerate the piston assembly 80′ to undertake a measurement as will be more fully described subsequently. The second drive disc 226 includes a second, bell shaped cam track 228A utilized to translate the piston assembly 80′ in cooperation the jet ejector assembly 300 to draw particulate laden air into the cylinder 210. When commanded, either the first, lower cam follower 240 is extended downwardly to engage the first complex cam track 224 to undertake a measurement of β or the second, upper cam follower 250 is extended upwardly to engage the second cam track 228A to facilitate ingestion of particulate laden air into the cylinder 210 as will be more full described subsequently.
Referring now to
As illustrated in
Referring now to
Referring again to
Secured to the upper end of the idler shaft 272 is a third timing belt drive pulley 284 which engages and drives a third timing belt 286. The third timing belt 286 engages and drives a third driven timing belt pulley 288. The sizes of the pulleys 284 and 288 are the same such that there is no speed increase or decrease between them. The third driven timing belt pulley 288 is secured to an upper shaft 290 which is coaxial with the output shaft 262 of the motor 260 and may be piloted therein in a suitable bearing assembly 292. Secured to the upper shaft 290 for rotation therewith are the second drive disc 226 and the third drive disc 340.
Referring now to
Normally closed valves are associated with the inner cam track 362A and normally open valves are associated with the outer cam track 362B. In
In
The sequence of operation of the second embodiment mass loading monitor 200 will now be presented with reference to all of the drawing Figures, especially
At the completion of a measurement cycle as described directly above, data from the MEMS pressure sensor 100 within the piston 82 is downloaded or read, the time integral of pressure is computed and compared with the stored reference or calibration data and the particulate content of the air is computed.
As
It should be understood that the sequencing assembly 350 may be replaced by an electronic timing or sequencing device (not illustrated) having, for example, an optical or magnetic marker attached to the first disc 222 and a proximate compatible sensor which provides timing or synchronizing pulses to a programmed sequencer such as a microprocessor having a plurality of outputs which drive solenoid valves on a manifold supplied with shop air and which selectively provide compressed air to the cam follower assemblies 230, 230′ and 230″ in accordance with the above described sequence of operation.
The description of the invention is merely exemplary in nature and variations that do not depart from the gist of the invention are intended to be within its scope. Such variations are not to be regarded as a departure from the spirit and scope of the invention
This patent application claims the benefit of U.S. Provisional Application No. 61/110,276, filed on Nov. 3, 2008. The disclosure of this provisional application is incorporated herein by reference.
Number | Date | Country | |
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61110726 | Nov 2008 | US |