FIELD OF THE INVENTION

The invention relates to devices for measuring pressure and making adjustments to compensate for varia¬ tions in pressure. More particularly, the invention re- lates to an automatic pressure sensitive regulation ap¬ paratus for use in a system employing a flow of partic¬ ulate solids. As explained further herein, the subject invention is particularly well adapted for use with ex¬ isting solids flow regulators. The invention automati- cally senses the height of particulate solids, and causes an immediate adjustment to the flow rate.

This application is related to United States Patent Application Serial No. 342,393 filed January 25, 1982 by Richard Norton and Paul Koppel entitled "SOLIDS FLOW REGULATOR".

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BACKGROUND OF THE INVENTION

Particulate solids are used in a variety of applications including chemical processing and steam generation. For example, particulate solids are widely used to accomplish hydrocarbon cracking and heat trans¬ fer. In many applications, the particulate solids are heated to a very high temperature, typically above 1500°F., and are caused to move through the system at high flow rates.

In the past, problems have been encountered in regulating the flow of particulate solids. Spec¬ ifically, the high temperatures and high flow rates of the solids adversely affect the performance and life of mechanical valves. Consequently, various non-mechanical flow control means have been developed to appropriately regulate the flow of particulate solids.

United States Patent Application Serial No.

342,393, filed January 25, 1982, discloses a recently developed system that operates without moving mechanical parts to regulate the flow of particulate solids. The system described therein is well adapted to a high mass flow, high temperature environment, and effectively functions as a non-mechanical valve. More specifically, the non-mechanical valve described in application Serial No. 342,393 includes a standpipe located intermediate an upstream source of particulate solids and a downstream passage into which the particulate solids pass. The standpipe functions as a seal between the pressure at the upstream and downstream locations. The downstream end of the standpipe is configured to accommodate a slumped mass of particulate solids at its lowest point. source of pressurized fluid communicates with a

chamber connected to the standpipe immediately upstream from the slumped mass.

In operation, the standpipe is always filled with particulate solids from the upstream source. Pres¬ surized fluid imposes a pressure on the slumped mass of particulate solids to cause the particulate solids from the slumped mass to move downstream and into the down¬ stream passage.

The rate of flow of particulate solids into the downstream passage varies directly with the magnitude of the pressure differential between the respective up¬ stream and downstream sides of the slumped mass. There- fore, the rate of flow of particulate solids into the downstream passage can be varied by changing the pres¬ sure from the source of pressurized fluid. To change the pressure, a mechanical valve can be provided inter¬ mediate the source of pressurized fluid and the plenum chamber. Appropriate adjustments to the valve then can be made to affect the rate of flow of particulate solids into the downstream passage. Alternatively, in applica¬ tion Serial No. 342,393 it is shown that in certain ap¬ plications a sensing line can extend from the pressure source to the steam lines in the associated furnace. The pressure then can be varied as a function of the steam conditions.

SUMMARY OF THE INVENTION

Experience has shown that in many applications it is desirable to vary the rate of flow of particulate solids to match the rate of solids received from upstream.

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Accordingly, it is an object of the subject invention to provide an apparatus that will automati¬ cally regulate the flow of particulate solids.

It is another object of the subject invention to provide an apparatus that will automatically regulate the flow of particulate solids without relying upon mov¬ ing mechanical parts.

It is an additional object of the subject in¬ vention to provide an apparatus that will automatically regulate the flow of particulate solids at a rate pro¬ portional to the height of particulate solids to be moved.

It is still another object of the subject in¬ vention to provide an apparatus to automatically regulate the flow of particulate solids in a high temperature, high mass flow environment.

It is still a further object of the subject in¬ vention to provide an apparatus to automatically regulate the flow of particulate solids, which apparatus is com¬ patible with recently developed systems for causing the flow of particulate solids.

The subject invention is compatible with a va¬ riety of particulate solids flow systems. It is partic¬ ularly well adapted to the system discussed above and described and claimed in United States Patent Application Serial No. 342,393. Briefly, the system described in that application includes a standpipe extending from a source of particulate solids to a downstream passage for the particulate solids. The downstream end of the standpipe is adapted to accommodate a slumped mass of

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particulate solids. A source of pressurized fluid is directed into the standpipe through .a plenum chamber immediately upstream of the slumped mass. As explained above, the higher pressure caused by the pressurized fluid urges the particulate solids from the slumped mass to the downstream passage, with a resultant flow of particulate solids from the source thereof and through the standpipe.

The apparatus of the subject invention com¬ prises first and second pressurized fluid distributors located at the upstream end of the standpipe substan¬ tially adjacent the source of particulate solids. The pressurized fluid distributors may either be connected to a common or to separate sources of pressurized fluid.

The first pressurized fluid distributor de¬ livers pressurized fluid into the bed of particulate solids located adjacent thereto at a flow rate sufficient to develop fluidization of the bed of particulate solids. More specifically, the flow rate of pressurized fluid is just above incipient fluidization of the particulate solids, but below the amount required for bubbling fluidization.

The second pressurized fluid distributor in¬ cludes apertures for directing pressurized fluid, sup¬ plied through a fluid flow limiter, into the bed of particulate solids, and also includes a through line which connects to the plenum chamber at the downstream end of the standpipe. Pressurized fluid directed into the second pressurized fluid distributor is partially directed through the apertures therein and into the bed of particulate solids, and partially directed to the through line and into the plenum chamber at the

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downstream end of the standpipe. The proportional dis¬ tribution of pressurized fluid between the apertures and the through line of the second pressurized fluid dis¬ tributor is determined by the height of particulate sol- ids in the source of particulate solids. More specifi¬ cally, the pressurized fluid directed by the first and second pressurized fluid distributors into the bed of particulate solids creates a fluidized environment with a hydrostatic pressure that varies directly with the height of particulate solids in the source of particu¬ late solids. This hydrostatic pressure is sensed by the apertures in the second pressurized fluid distributor. When the height of particulate solids is great, the hydrostatic pressure adjacent the apertures also will be great. As a result, a smaller proportion of the pressurized fluid that is directed into the second pres¬ surized fluid distributor will pass through the apertures therein, and a correspondingly greater amount will be directed into the through line and to the plenum chamber. This increased rate of flow to the plenum chamber at the downstream end of the standpipe will increase the pres¬ sure on the upstream side of the slumped mass causing a greater flow of particulate solids into the downstream passage. Thus, a greater height of particulate solids in the source of particulate solids will be sensed by the second pressurized fluid distributor of the subject invention, which in turn will cause an increased flow rate of particulate solids at the downstream end of the standpipe.

As the height of particulate solids in the source of particulate solids decreases, the hydrostatic pressure adjacent the first and second pressurized fluid distributors also will decrease. This decrease in hydro- static pressure will cause a greater proportion of the

pressurized fluid that is directed into the second pres¬ surized fluid distributor to pass through the apertures therein, and a correspondingly lower proportion to be directed to the through line. As a result, the flow rate of pressurized fluid to the plenum chamber at the downstream end of the standpipe will decrease causing a decreased pressure on the slumped mass,, and a corre¬ spondingly lower flow rate of particulate solids into the downstream passage.

DESCRIPTION OF THE DRAWINGS

FIGURE 1 is a schematic system for the flow of particulate solids in which the subject automatic pres¬ sure sensitive regulation assembly is employed.

FIGURE 2 is a partial cross-sectional view of a fluidized bed furnace in which the subject automatic pressure sensitive regulation assembly is employed.

FIGURE 3 is a cross-sectional side view of the subject automatic pressure sensitive regulation assembly employed in a particulate solids flow apparatus.

FIGURE 4 is a plan view partially in section of the subject automatic pressure sensitive regulation assembly employed in a particulate solids flow apparatus.

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS

The subject automatic pressure sensitive

regulation assembly can be employed in many particulate solids flow devices. For example, in FIGURE 1, the sub¬ ject automatic pressure sensitive regulation assembly 60 is employed in a basic particulate solids flow system. The system 2 shown in FIGURE 1 includes a particulate solids reservoir 6, a valve assembly indicated generally by the numeral 4, a particulate solids use system 8 and a particulate solids receiver reservoir 10. The valve assembly 4 of the system 2 shown in FIGURE 1 includes a standpipe 12 which extends from the particulate solids reservoir 6 at the upstream end of valve 4 to a control hopper 14 located within valve 4. Control hopper 14 is in communication with line 66 which accommodates a flow of pressurized fluid into plenum chamber 18. In opera- tion, particulate solids from particulate solids reser¬ voir 6 flow through standpipe 12 and into control hop¬ per 14. Pressurized fluid flows through line 66 into plenum chamber 18, and exerts a pressure upon the par¬ ticulate solids in control hopper 14. This pressure urges the particulate solids from control hopper 14 through discharge fixture 24 and into particulate sol¬ ids use system 8 and through solids receiver reservoir 10.

The subject automatic pressure sensitive reg- ulation assembly 60 is located at the upstream end of standpipe 12 adjacent to particulate solids reservoir 6. As explained in greater detail below, the automatic pres¬ sure sensitive regulation assembly 60 is in communication with a source of pressurized fluid 62. Pressurized fluid from the source of pressurized fluid 62 is directed through line 64 and into the automatic pressure sensitive regula¬ tion assembly 60. In the manner described below, the au¬ tomatic pressure sensitive regulation assembly 60 causes at least a local and incipient fluidization of the particu- late solids 28 adjacent to it. The hydrostatic pressure

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in the fluidized particulate solids, adjacent to the automatic pressure sensitive regulation assembly 60, varies according to the height of the particulate solids in the particulate solids reservoir 6. Automatic pres- sure sensitive regulation assembly 60 also is in communi¬ cation with the pressurized fluid line 66 which extends to the plenum chamber 18. As mentioned above, and as de¬ scribed further herein, automatic pressure sensitive reg¬ ulation assembly 60 operates to vary the flow rate of pres- surized fluid through line 66 directly in proportion to the height of particulate solids in the particulate sol¬ ids reservoir 6. This greater flow rate of pressurized fluid to line 66 will cause an increased pressure in plenum 18 and thereby will increase the flow rate of par- ^" ticulate solids through control hopper 14 and into dis¬ charge fixture 24 and particulate solids receiver reser¬ voir 10. Thus, the flow rate of particulate solids through the valve assembly 4 of the system 2 varies di¬ rectly and automatically with the height of the particu- late solids in the particulate solids reservoir 6.

FIGURE 2 shows another example of the subject automatic pressure sensitive regulation assembly 60 in an operational environment. In this example, automatic pressure sensitive regulation assembly 60 is employed to return collected solids to a fluidized bed furnace. Parts of the system shown in FIGURE 2 that are comparable to parts of the system shown in FIGURE 1 are numbered identically. Briefly, the fluidized bed furnace 32 of FIGURE 2 emits a mixture of gas and suspended particu¬ late solids which are separated by a cyclone or other equivalent device from which the particulate solids are directed into a solids collection reservoir 6. The solids collection reservoir contains a fluidized bed of particu- late solids 28 which flow by gravity into standpipe 12

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extending to control hopper 14, and thence return to the fluidized bed furnace 32. Pressurized fluid line 64 ex¬ tends from a source of pressurized fluid 62 to the auto¬ matic pressure sensitive regulation assembly 60, and ac- commodates the flow of pressurized fluid thereto. Pres¬ surized fluid line 66 in turn extends from the automatic pressure sensitive regulation assembly 60 to the plenum chamber 18, and accommodates the flow of pressurized fluid flow into the plenum chamber 18 as described above. This example employs the same principles described above. Briefly, pressurized fluid flowing through line 64 and into the automatic pressure sensitive regulation assem¬ bly 60 causes incipient fluidization of the particulate solids adjacent to the automatic pressure sensitive reg- ulation assembly 60. The hydrostatic pressure in these fluidized particulate solids varies according to the height of the particulate solids in the fluidized bed 28. The rate of flow of pressurized fluid through line 66 to the plenum chamber 18 varies directly with the hydrostatic pressure sensed by the automatic pressure sensitive reg¬ ulation assembly 60. Thus, as with the example described in FIGURE 1, as the height of particulate solids in flu¬ idized bed 28 increases, a greater flow of pressurized fluid is directed through the plenum chamber 18 causing a more rapid flow of particulate solids into the flu¬ idized bed furnace 32.

Turning to FIGURES 3 and 4, the preferred em¬ bodiment of the subject automatic pressure sensitive reg- ulation assembly 60 is shown in greater detail. This par¬ ticular embodiment of the automatic pressure sensitive reg¬ ulation assembly 60 is shown with the valve assembly 4 of the fluidized bed furnace 32 described above and shown generally in FIGURE 2.

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As shown in FIGURE 3, the automatic pressure sensitive regulation assembly is located at the upstream end of a standpipe 12 adjacent the fluidized bed of par¬ ticulate solids 28. The automatic pressure sensitive regulation assembly 60 includes first and second pres¬ surized fluid distributors, which are defined by an in¬ ner chamber 68 and an outer ring 70. The inner cham¬ ber 68 and the outer ring 70 are dimensioned and dis¬ posed to be substantially centrally located within the outlet of solids collection reservoir 6, such that par¬ ticulate solids may easily pass by the automatic pressure sensitive regulation assembly 60. Pressurized fluid lines 72 and 74 extend from the pressurized fluid line 64 directly to inner chamber 68 and via fluid flow limiter 82 to the outer ring 70. Thus, pressuri-zed fluid from the pressure source 62 flows through the pressurized fluid line 64 and into both lines 72 and 74 to both inner chamber 68 and outer ring 70. Alter¬ natively, the inner chamber 68 and the outer ring 70 of the automatic pressure sensitive regulation assembly 60 can be connected to separate pressure sources, pro¬ vided flow limiter 82 is included in the outer ring fluid supply.

Inner chamber 68 has a plurality of apertures

76 through which pressurized fluid may pass. The sizes of apertures 76 and line 74 are sufficient to enable a rate of flow of pressurized fluid that will cause in¬ cipient fluidization of the particulate solids adjacent the automatic pressure sensitive regulation assembly 60.

Outer ring 70 is connected, via flow limiter 82, to pressurized fluid lines 72 and directly to control line 66. The inner chamber 68 and the outer ring 70 are maintained in their proper positions with respect to one

another by support struts 78.

The outer ring 70 is provided with a plurality of pressure sensing apertures 80. In operation, a por- tion of the pressurized fluid flowing into the outer ring 70 exits therefrom through pressure sensing aper¬ tures 80, and the remainder of the pressurized fluid exits through pressurized fluid control line 66. A flow limiter 82, such as a restricting orifice, is provided in pressurized fluid line 72 to fix the total rate of flow of pressurized fluid to outer ring 70.

In operation, pressurized fluid is directed through the pressurized fluid line 64 from the pressure source 62 into both lines 72 and 74. The pressurized fluid that flows through line 74 enters inner chamber 68 and exits therefrom through the plurality of holes 76. As explained above, this rate of flow of pressurized fluid through the holes 76 is sufficient to cause in- cipient fluidization of the particulate solids adjacent the automatic pressure sensitive regulation assembly 60.

The pressurized fluid from pressure source 62 enters line 72, and passes through the restricting ori- fice 82 and flows at a near constant rate into the outer ring 70. Part of the pressurized fluid that enters outer ring 70 exits therefrom through pressure sensing apertures 80, while the remainder of the pressurized fluid enter¬ ing outer ring 70 continues into pressurized line 66. Consequently, as the flow through pressure sensing ap¬ ertures 80 decreases, the flow through pressurized fluid line 66 will increase. The opposite, of course, is also true.

The amount of pressurized fluid exiting

pressure sensing apertures 80 on outer ring 70 is pro¬ portional to the height of particulate solids in the fluidized bed of particulate solids 28. Specifically, the particulate solids that have been fluidized by pressurized fluid directed through holes 76 of inner chamber 68 will have a hydrostatic pressure that varies directly with the height of particulate solids in flu¬ idized bed 28. Therefore, as the height of particulate solids in fluidized bed 28 increases, the hydrostatic pressure in the fluidized particulate solids also will increase. The variations in hydrostatic pressure are sensed by the pressure sensing apertures 80 in outer ring 70. As the hydrostatic pressure increases, less pressurized fluid will exit from outer ring 70 through pressure sensing apertures 80, and a correspondingly greater amount will flow into pressurized fluid line 66.

As explained above, pressurized fluid line 66 ' is connected to plenum chamber 18. Thus, as flow in- creases in pressurized fluid line 66, it also will in¬ crease in plenum chamber 18. This increased flow through plenum chamber 18 causes a greater pressure on the slumped mass 30 at the downstream end of standpipe 12, thereby causing a greater rate of flow of particulate solids from standpipe 12 into discharge passage 24.

To summarize this facet of the operation, the increased height of particulate solids raises the hydro¬ static pressure at automatic pressure sensitive regulation assembly 60. The increased hydrostatic pressure causes less pressured fluid to be directed through pressure sensing apertures 80 in outer ring 70 and a correspond¬ ing increase in pressurized fluid to be directed through pressurized fluid line 66. This increased flow of pres- surized fluid is directed through line 66 and into

plenum chamber 18 - to cause an increased flow of par¬ ticulate solids from standpipe 12 to discharge passage 24.

Automatic pressure sensitive regulation as¬ sembly 60 similarly reacts to decreases in the height of particulate solids in the fluidized bed 28. Specif¬ ically, as the height of particulate solids in fluidized bed 28 decreases, due to the flow through standpipe 12, the hydrostatic pressure adjacent automatic pressure sensitive regulation assembly 60 also decreases. Pres¬ surized fluid in outer ring 70 automatically will adapt to these changed hydrostatic pressure conditions so that more pressurized fluid will pass through pressure sensing apertures 80, and less will pass through pressurized flu¬ id line 66. As a result, the pressure in plenum cham¬ ber 18 will decrease and the rate of flow of particulate solids from standpipe 12 to discharge passage 24 also will decrease.

It has been found that with scintered aluminum (Norton Co. 60/F) particulate solids in solids collec¬ tion reservoir 6 and with 0 inches water gage (WG) pres¬ sure in the space above the solids and with the particular size and number of holes 76 used in inner ring 68, a flu¬ id pressure of 40-50 WG delivered through line 74 will be sufficient to provide incipient fluidization when the height of solids above the inner chamber 68 is in the range of 10 to 20 inches. It also has been found, for example, that when the height of solids above the inner chamber 68 is 16.5 inches, the hydrostatic pressure sensed by outer ring 70 will be 33 WG, and the pressure at the control plenum chamber 18 will approach 33 inches. The hydrostatic pressure at the outer ring 70 will vary from 2 WG to 40 WG according to changes in the height of

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solids in reservoir 6 and backpressure beyond discharge passage 24.

The hydrostatic pressure in outer ring 70 and corresponding pressure, via line 66, in plenum chamber 18 will always be equal to or higher than the pressure beyond discharge passage 24 and is determined by the receiver pressure and differential pressure required to discharge the particulate solids at the same rate as collected in the solids collection reservoir 6.