AU1881083A - Automatic pressure sensitive regulation assembly - Google Patents
Automatic pressure sensitive regulation assemblyInfo
- Publication number
- AU1881083A AU1881083A AU18810/83A AU1881083A AU1881083A AU 1881083 A AU1881083 A AU 1881083A AU 18810/83 A AU18810/83 A AU 18810/83A AU 1881083 A AU1881083 A AU 1881083A AU 1881083 A AU1881083 A AU 1881083A
- Authority
- AU
- Australia
- Prior art keywords
- pressurized fluid
- particulate solids
- solids
- flow
- downstream
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Description
AUTOMATIC PRESSURE SENSITIVE REGULATION ASSEMBLY
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.
Claims (9)
1. An automatic pressure sensitive regulation assembly for regulating the flow of particulate solids between upstream and downstream reservoirs of particulate solids by metering the flow of fluid provided to urge the particulate solids to flow from the upstream reservoir to the downstream reservoir comprising:
means for the passage of particulate solids between said upstream and downstream reservoir; at least one source of pressurized fluid; a first pressurized fluid distributor located in the particulate solids above the downstream solids reservoir; means for delivering pressurized fluid from said source of pressurized fluid to said first pressurized fluid distributor for dis¬ tributing the pressurized fluid to the partic- ulate solids adjacent said automatic pressure sensitive regulation assembly at a rate to cause incipient fluidization of said particulate solids and an attendant hydrostatic pressure; a second pressurized fluid distributor; means for delivering pressurized fluid from said source of pressurized fluid to the second pressurized fluid distributor at a rate to sense said hydrostatic pressure variation as a func¬ tion of the particulate solids above the first pressurized fluid distributor and thereby meter the flow of fluid provided to urge the partic¬ ulate solids to the downstream reservoir.
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2. An automatic pressure sensitive regula¬ tion assembly as in Claim 1 wherein the first pressur¬ ized fluid distributor is a chamber having a plurality of holes for directing pressurized fluids into said par- ticulate solids causing incipient fluidization thereof.
3. An automatic pressure sensitive regula¬ tion assembly as in Claim 1, further comprising a plenum chamber intermediate said automatic pressure sensitive regulation assembly and said downstream reservoir of particulate solids, and wherein the second pressurized fluid distributor is a ring having a plurality of pres¬ sure sensing apertures for sensing the hydrostatic pres¬ sure of the fluidized particulate solids, said ring being in communication with said plenum chamber such that changes in hydrostatic pressure sensed by said pressure sensing apertures causes a corresponding change in the flow of pressurized fluids to said plenum chamber thereby chang¬ ing the flow of particulate solids to said downstream reservoir of particulate solids.
4. An automatic pressure sensitive regulation assembly.as in Claim 3 wherein. said means for the passage for particulate solids from the upstream to the downstream reservoir is a passage between the upstream and downstream reservoirs, said assembly is located above the outlet of the upstream reservoir leading to the passage between the upstream and downstream reservoirs adjacent said passage for the particulate solids and wherein said plenum cham- ber is located adjacent said downstream reservoir of par¬ ticulate solids.
5. An automatic pressure sensitive regula¬ tion assembly as in Claim 3, further comprising a flow limiter in the means for delivering pressurized fluid to the second pressurized fluid distributor.
6. An automatic pressure sensitive regula¬ tion assembly as in Claim 1 having a single source of pressurized fluid in communication with both said first and second pressurized fluid distributors.
7. An automatic pressure sensitive regula¬ tion assembly for automatically regulating the flow of particulate solids from an upstream location, through a valve and to a downstream location, said automatic pres- sure sensitive regulation assembly being disposed in said valve and adjacent said upstream location, said au¬ tomatic pressure sensitive regulation assembly comprising:
a source of pressurized fluid; an inner chamber in communication with said source of pressurized fluid and having a plurality of holes disposed therein, pres¬ surized fluid from said source of pressurized fluid being distributed through said holes in said inner chamber at a sufficient rate to cause incipient fluidization of the particu¬ late solids adjacent thereto; an outer ring in communication with said source of pressurized fluid and having a plurality of pressure sensing apertures dis¬ posed therein for distributing into said fluidized particulate solids adjacent there¬ to a portion of the pressurized fluid directed into said outer ring;
a plenum chamber in communication with said outer ring and disposed in a portion of said valve adjacent said downstream location, said plenum chamber for directing into said particulate solids the pressurized fluid from said outer ring that is not distributed through the pressure sensing apertures thereof, such that the hydrostatic pressure of the fluidized particulate solids adjacent the automatic pres- sure sensitive regulation assembly varies di¬ rectly with the height of particulate solids in the upstream location, and such that the portion of pressurized fluid from said outer ring directed to said plenum chamber varies directly with the hydrostatic pressure ad¬ jacent said automatic pressure sensitive reg¬ ulation assembly.
8. A method for automatically regulating the flow of particulate solids through a valve from an up¬ stream location to a downstream location at a flow rate directly proportional to the height of particulate solids at the upstream location, said method comprising the steps of: creating incipient fluidization of the par¬ ticulate solids in said valve at a portion thereof adjacent said upstream location to produce hydrostatic pressure; varying the hydrostatic pressure as a func- tion of the height of the particulate solids above the location of incipient fluidization; directing a stream of pressurized fluid through the location of incipient fluidization;
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discharging a portion of the stream of pressurized fluid into the particulate solids as a function of the hydrostatic pressure; directing to a location on said valve ad- jacent said downstream location the remaining portion of said stream of pressurized fluid for urging into said downstream location an amount of particulate solids directly propor¬ tional to said remaining portion of said stream of pressurized fluid.
9. A method as in Claim 8 wherein the incip¬ ient fluidization of the particulate solids is created by fluid delivered through a distributor with apertures on the surface thereof and the stream of pressurized flu¬ id discharged into the particulate solids is discharged through apertures on the surface of a ring.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US06/400,397 US4453865A (en) | 1982-07-21 | 1982-07-21 | Automatic pressure sensitive regulation assembly |
| US400397 | 1982-07-21 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| AU1881083A true AU1881083A (en) | 1984-02-23 |
| AU546159B2 AU546159B2 (en) | 1985-08-15 |
Family
ID=23583447
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU18810/83A Ceased AU546159B2 (en) | 1982-07-21 | 1983-07-12 | Automatic pressure sensitive regulation assembly |
Country Status (18)
| Country | Link |
|---|---|
| US (1) | US4453865A (en) |
| EP (1) | EP0102329B1 (en) |
| JP (1) | JPS59501457A (en) |
| KR (1) | KR890001383B1 (en) |
| AU (1) | AU546159B2 (en) |
| CA (1) | CA1217523A (en) |
| DE (1) | DE3360888D1 (en) |
| ES (1) | ES524296A0 (en) |
| FI (1) | FI81318C (en) |
| GB (1) | GB2123982B (en) |
| GR (1) | GR78882B (en) |
| IL (1) | IL69162A (en) |
| MA (1) | MA19847A1 (en) |
| MX (1) | MX155876A (en) |
| PT (1) | PT77054B (en) |
| WO (1) | WO1984000532A1 (en) |
| YU (1) | YU154783A (en) |
| ZA (1) | ZA835174B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU570887B2 (en) * | 1984-05-21 | 1988-03-24 | Sumitomo Electric Industries, Ltd. | Liquid replenishing apparatus |
Families Citing this family (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT383582B (en) * | 1985-03-18 | 1987-07-27 | Lisec Peter | DEVICE FOR FILLING HOLLOW BODIES WITH GRANULES |
| JPS6221626A (en) * | 1985-07-17 | 1987-01-30 | Nippon Steel Corp | Granular body distributing device and using method thereof |
| JPS62130927A (en) * | 1985-12-02 | 1987-06-13 | Nippon Steel Corp | Distributor for powder material and gas and using method thereof |
| US4814067A (en) * | 1987-08-11 | 1989-03-21 | Stone & Webster Engineering Corporation | Particulate solids cracking apparatus and process |
| US4919898A (en) * | 1987-08-11 | 1990-04-24 | Stone & Webster Engineering Corp. | Particulate solids cracking apparatus |
| US4941779A (en) * | 1987-09-18 | 1990-07-17 | Shell Oil Company | Compartmented gas injection device |
| FR2667609B1 (en) * | 1990-10-03 | 1993-07-16 | Inst Francais Du Petrole | PROCESS AND DEVICE FOR CATALYTIC CRACKING IN DOWNFLOW BED. |
| DE69132062T2 (en) * | 1990-12-27 | 2000-09-07 | Matsuo Sangyo Co. Ltd., Osaka | Device for feeding powder paints |
| US5254788A (en) * | 1991-09-10 | 1993-10-19 | Stone And Webster Engineering Corporation | Process for the production of olefins from light paraffins |
| CN102180358B (en) * | 2011-04-18 | 2012-10-03 | 宝钢工程技术集团有限公司 | Blowing feeding system and method in mechanical stirring desulfurization |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2623793A (en) * | 1949-12-24 | 1952-12-30 | Dow Chemical Co | Pneumatic conveyer and feeder for loose solids |
| US2684869A (en) * | 1951-05-21 | 1954-07-27 | Dorr Co | Handling pulverulent materials |
| US2726137A (en) * | 1951-07-13 | 1955-12-06 | Gulf Oil Corp | Process and apparatus for transfer of solid particles |
| US2880170A (en) * | 1956-12-13 | 1959-03-31 | Socony Mobil Oil Co Inc | Method of sealing moving bed conversion reactor |
| GB1300935A (en) * | 1969-08-18 | 1972-12-29 | Dorr Oliver Company Ltd | Valves for controlled solids transfer |
| US4240377A (en) * | 1978-01-19 | 1980-12-23 | Johnson William B | Fluidized-bed compact boiler and method of operation |
| JPS5410290A (en) * | 1977-06-27 | 1979-01-25 | Daiya Kemifua Kk | Deoxidating agent |
| DE2749399C2 (en) * | 1977-11-04 | 1981-10-15 | Deutsche Babcock Ag, 4200 Oberhausen | Device for the thermal regeneration of loaded adsorbents |
| US4260298A (en) * | 1979-05-17 | 1981-04-07 | The Ducon Company, Inc. | Control of solids discharge from pressurized vessel |
-
1982
- 1982-07-21 US US06/400,397 patent/US4453865A/en not_active Expired - Fee Related
-
1983
- 1983-07-05 IL IL69162A patent/IL69162A/en not_active IP Right Cessation
- 1983-07-08 CA CA000432064A patent/CA1217523A/en not_active Expired
- 1983-07-12 JP JP58502655A patent/JPS59501457A/en active Granted
- 1983-07-12 WO PCT/US1983/001073 patent/WO1984000532A1/en active IP Right Grant
- 1983-07-12 AU AU18810/83A patent/AU546159B2/en not_active Ceased
- 1983-07-14 MX MX198041A patent/MX155876A/en unknown
- 1983-07-15 ZA ZA835174A patent/ZA835174B/en unknown
- 1983-07-18 YU YU01547/83A patent/YU154783A/en unknown
- 1983-07-19 PT PT77054A patent/PT77054B/en not_active IP Right Cessation
- 1983-07-19 GR GR71973A patent/GR78882B/el unknown
- 1983-07-19 KR KR1019830003312A patent/KR890001383B1/en not_active IP Right Cessation
- 1983-07-20 MA MA20068A patent/MA19847A1/en unknown
- 1983-07-20 ES ES524296A patent/ES524296A0/en active Granted
- 1983-07-20 DE DE8383830152T patent/DE3360888D1/en not_active Expired
- 1983-07-20 EP EP83830152A patent/EP0102329B1/en not_active Expired
- 1983-07-20 GB GB08319558A patent/GB2123982B/en not_active Expired
-
1984
- 1984-03-20 FI FI841111A patent/FI81318C/en not_active IP Right Cessation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU570887B2 (en) * | 1984-05-21 | 1988-03-24 | Sumitomo Electric Industries, Ltd. | Liquid replenishing apparatus |
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