US1616547A - Handling dry pulverulent materials - Google Patents
Handling dry pulverulent materials Download PDFInfo
- Publication number
- US1616547A US1616547A US99677A US9967726A US1616547A US 1616547 A US1616547 A US 1616547A US 99677 A US99677 A US 99677A US 9967726 A US9967726 A US 9967726A US 1616547 A US1616547 A US 1616547A
- Authority
- US
- United States
- Prior art keywords
- vessel
- under
- air
- pulverulent materials
- handling dry
- 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.)
- Expired - Lifetime
Links
- 239000000463 material Substances 0.000 title description 36
- 238000000034 method Methods 0.000 description 4
- 239000004568 cement Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 238000013019 agitation Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/34—Details
- B65G53/40—Feeding or discharging devices
- B65G53/48—Screws or like rotary conveyors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65G—TRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
- B65G53/00—Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
- B65G53/04—Conveying materials in bulk pneumatically through pipes or tubes; Air slides
- B65G53/16—Gas pressure systems operating with fluidisation of the materials
- B65G53/18—Gas pressure systems operating with fluidisation of the materials through a porous wall
- B65G53/22—Gas pressure systems operating with fluidisation of the materials through a porous wall the systems comprising a reservoir, e.g. a bunker
Definitions
- the object of this invention is to facilitate the handling of dry, pulverulent materials, such as dry Portland cementand coal dust, for example, for various purposes such a for example, as the bagging or barreling oi cement or the delivery of coal dustas fuel to a furnace or kiln.
- the particular purpose 4 has been to make it possible to deliver such material at a uniform rate and thereby to m facilitate themeasuring or the packaging of the material or the maintenance of predetermined conditions of combustion.
- the material to be handled or treated or dealt with is maintained in-mass in a fluent condition by the admixture therewith of air, with or without mechanical agitation, and at a constant head and is then discharged into the measuring devices or the packaging machine or the furnace or kiln or elsewhere as the case may be.
- the material is discharged at a uniform rate and, if in the form of powdered fuel, can be admixed with air and delivered into the furnace or kiln under such conditions as to insure practically perfect control of combustion, and, if dry cement or other merchantable commodity, can be measured, either by timing devices or weighing devices or otherwise, or delivered into barrels or bags or other packages, with great facility and with as certainty in delivery.
- Figures 1 and 2 are respectively views in outline, representing somewhat conventionally different forms of apparatus in which the method may be practiced.
- a container a such as a bin or tank, which stands as the source of supply of the material to be handled or treated.
- the material is delivered by any suitable means, represented generally by a screw conveyor 6, into a vessel 0 in which the material is to he maintained in a fluent condition and under a constant head and from which such -fluent material is to be permitted to flow at a uniform rate under the influence of such constant head.
- the vessel -'0 is provided with means, represented as air nozzlesd, through which air or any other suitable or desired aeriform fluid, is admitted and admixed'with the pulverulent material in the vessel.
- any other aeriform fluid either of a neutral character or of a character calculated to have some influence or eflect on the material may be employed.
- the air is supplied under such pressure differential and in such volume as to be thoroughl admixed with the pulverulentmaterial an thereby to maintain the mass of such material in a fluent or mobile cndition in which it will be ca- -which the movement of the material to the desired point may be continued, 'but it will be understood that a. conduit of any sort is not essential in all cases, it being ssible that the material might flow direct y from the discharge opening 7 into a measuring device or a suitable receptacle.
- the vessel 0 In order that a uniform rate of flow 'of the fluent or mobile material from the vessel 6' may be attained, it is necessary that the material in the vessel 0 be maintained at a constant level or under a constant head.
- the vessel 0 In 100 the form of apparatus indicated in Figure 1, the vessel 0 is provided at some suitable point inits upper portion with an overflow outlet it, through which the excess of material delivered to the vessel 0 by the feeding device 1 5 d may be returned to the container or source of supply a.
- the vessel 0 is shown as provided with a float z, of any suitable material, which rests on the surface of 10 $0 the material a fluent condition by i the column of fluent material in the vessel 0 and is operatively connected with a rheostat k for the control, through suitable circuit connections, of a variable s (1 motor I by which the feeding device is driven.
- a float z of any suitable material, which rests on the surface of 10 $0 the material a fluent condition by i the column of fluent material in the vessel 0 and is operatively connected with a rheostat k for the control, through suitable circuit connections, of a variable s (1 motor I by which the feeding device is driven.
- the method of handling dry pulverulent material which consists in imparttling to a material in said vessel under mixture of air, maintaining the mass of material admixed with air under a constant head, and discharging from the mass at a uniform rate under the influence of such constanthead the material so admixed with air.
- An apparatus for handling dry pulverulent material which comprises a source of supply for the material, a vessel, means to de iver the material from the source of supply to said vessel, means to impart to the material in said vessel a fluent condition by the admixture of air, means to maintain the a constant head, and means whereby the material is disghaaged from the vessel under such constant ea a
- This specification signed this 19th day of March A. D. 1926. 4
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Basic Packing Technique (AREA)
Description
. 1,616,547 9 c. PONTOPPIDAN HANDLING DRY PULV ERULENT MATERIALS Filed April 5, 1926 2 'Shets-Sheet 1 L J I L C V VXtXg E d $5 F 1 1,616,547 eb c. PONTOPPIDAN v I HANDLING DRY PULVBRULENT MATERIALS Filed April 5, 1926 2 Sheets-Sheet 2 IN VEN TOR Patented Feb. 8 1 927.
" UNITED STATES I 1,616,547 PATENT OFFICE.
CARL PONTOPPIDAN, OE COPENHAGEN, DENMARK, ASSIGNOR TO F. I. SIIDTH a CO.,
\ OF NEW YORK, N. Y., A CORPORATION 01' NEW JERSEY.
HANDLING DRY PULVERULENT MATERIALS.
Application and April a, 1926. Serial-No. 99,677.
. The object of this invention is to facilitate the handling of dry, pulverulent materials, such as dry Portland cementand coal dust, for example, for various purposes such a for example, as the bagging or barreling oi cement or the delivery of coal dustas fuel to a furnace or kiln. The particular purpose 4 has been to make it possible to deliver such material at a uniform rate and thereby to m facilitate themeasuring or the packaging of the material or the maintenance of predetermined conditions of combustion. In accordance with the invention, the material to be handled or treated or dealt with is maintained in-mass in a fluent condition by the admixture therewith of air, with or without mechanical agitation, and at a constant head and is then discharged into the measuring devices or the packaging machine or the furnace or kiln or elsewhere as the case may be. By thus maintaining the material in mass in a fluent condition and at a constant level or under a constant head and permitting it to flow under such conditions, the material is discharged at a uniform rate and, if in the form of powdered fuel, can be admixed with air and delivered into the furnace or kiln under such conditions as to insure practically perfect control of combustion, and, if dry cement or other merchantable commodity, can be measured, either by timing devices or weighing devices or otherwise, or delivered into barrels or bags or other packages, with great facility and with as certainty in delivery. The method in which the invention finds its best expression, obviously can be practiced in various forms of apparatus, suited to the character of the material and the ultimate purposes inview and it will be understood that so far as the invention finds expression in apparatus, such apparatus embodies certain essential features which take form and character according to the conditions under which the method is practiced.
In the accompanying drawings, Figures 1 and 2 are respectively views in outline, representing somewhat conventionally different forms of apparatus in which the method may be practiced.
c In both forms of apparatus'represented, .there is indicated a container a, such as a bin or tank, which stands as the source of supply of the material to be handled or treated. 'From the container or source of supply the material is delivered by any suitable means, represented generally by a screw conveyor 6, into a vessel 0 in which the material is to he maintained in a fluent condition and under a constant head and from which such -fluent material is to be permitted to flow at a uniform rate under the influence of such constant head. In .both forms of apparatus represented, the vessel -'0 is provided with means, represented as air nozzlesd, through which air or any other suitable or desired aeriform fluid, is admitted and admixed'with the pulverulent material in the vessel. The term-air is employed onlyfor convenience and brevity and it will be'understood that any other aeriform fluid, either of a neutral character or of a character calculated to have some influence or eflect on the material may be employed. The air is supplied under such pressure differential and in such volume as to be thoroughl admixed with the pulverulentmaterial an thereby to maintain the mass of such material in a fluent or mobile cndition in which it will be ca- -which the movement of the material to the desired point may be continued, 'but it will be understood that a. conduit of any sort is not essential in all cases, it being ssible that the material might flow direct y from the discharge opening 7 into a measuring device or a suitable receptacle.
In order that a uniform rate of flow 'of the fluent or mobile material from the vessel 6' may be attained, it is necessary that the material in the vessel 0 be maintained at a constant level or under a constant head. In 100 the form of apparatus indicated in Figure 1, the vessel 0 is provided at some suitable point inits upper portion with an overflow outlet it, through which the excess of material delivered to the vessel 0 by the feeding device 1 5 d may be returned to the container or source of supply a. In the form of apparatus shown in Figure 2, however, the vessel 0 is shown as provided with a float z, of any suitable material, which rests on the surface of 10 $0 the material a fluent condition by i the column of fluent material in the vessel 0 and is operatively connected with a rheostat k for the control, through suitable circuit connections, of a variable s (1 motor I by which the feeding device is driven. By either of such means or by other means which will suggest themselves, the fluent or mobile material in the vessel 0 is maintained at a constant level or under a constant head so that it flows from such vessel at a uniform rate.
It will be understood that the term handling is used herein in a broad sense and without any intention of limiting the invention by thelit'eral and restricted meaning of the term.
I claim as my invention 1. The method of handling dry pulverulent material which consists in imparttling to a material in said vessel under mixture of air, maintaining the mass of material admixed with air under a constant head, and discharging from the mass at a uniform rate under the influence of such constanthead the material so admixed with air.
2. An apparatus for handling dry pulverulent material which comprises a source of supply for the material, a vessel, means to de iver the material from the source of supply to said vessel, means to impart to the material in said vessel a fluent condition by the admixture of air, means to maintain the a constant head, and means whereby the material is disghaaged from the vessel under such constant ea a This specification signed this 19th day of March A. D. 1926. 4
- CARL PONTOPPIDAN.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US99677A US1616547A (en) | 1926-04-03 | 1926-04-03 | Handling dry pulverulent materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US99677A US1616547A (en) | 1926-04-03 | 1926-04-03 | Handling dry pulverulent materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US1616547A true US1616547A (en) | 1927-02-08 |
Family
ID=22276100
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US99677A Expired - Lifetime US1616547A (en) | 1926-04-03 | 1926-04-03 | Handling dry pulverulent materials |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US1616547A (en) |
Cited By (39)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2437694A (en) * | 1946-05-15 | 1948-03-16 | Nasa | Method for blending powder grains |
| US2438728A (en) * | 1944-06-10 | 1948-03-30 | Standard Oil Dev Co | Temperature control in fluidized catalyst systems |
| US2448272A (en) * | 1943-08-11 | 1948-08-31 | Socony Vacuum Oil Co Inc | Method and apparatus for separation of vapors from a contact mass |
| US2448745A (en) * | 1943-11-16 | 1948-09-07 | Struckmann Holger | Conveying pulverized material |
| US2492401A (en) * | 1945-02-24 | 1949-12-27 | Lummus Co | Gas adsorption |
| US2509431A (en) * | 1949-07-14 | 1950-05-30 | Shawinigan Chem Ltd | Dispensing fluidized pulverulent materials |
| US2559557A (en) * | 1944-07-12 | 1951-07-03 | Babcock & Wilcox Co | Aerating feeding of pulverized materials |
| US2568400A (en) * | 1946-09-18 | 1951-09-18 | Standard Oil Dev Co | Process for subdividing solid particles |
| US2576177A (en) * | 1948-12-30 | 1951-11-27 | Herr Joseph Stanley | Feed mixing apparatus |
| US2609185A (en) * | 1949-07-04 | 1952-09-02 | F S Smidth & Co | Method and apparatus for increasing fluidity of material |
| US2641574A (en) * | 1949-07-21 | 1953-06-09 | Standard Oil Co | Process and apparatus for decolorizing oil |
| US2651602A (en) * | 1948-11-04 | 1953-09-08 | Lummus Co | Process and apparatus for clay contacting in the refining of lubricating oil |
| US2668365A (en) * | 1949-12-31 | 1954-02-09 | Standard Oil Dev Co | Apparatus for determining densities of finely divided solid materials in a fluidized body of such materials |
| US2687343A (en) * | 1949-12-19 | 1954-08-24 | Phillips Petroleum Co | Fluidized bed floating baffle |
| US2710232A (en) * | 1950-06-14 | 1955-06-07 | Lawrence D Schmidt | Method for filling cavities with granular solids |
| US2718471A (en) * | 1952-08-01 | 1955-09-20 | Nat Plastic Products Company | Blending method and apparatus |
| US2730407A (en) * | 1950-10-23 | 1956-01-10 | Union Oil Co | Conveyance of granular solids |
| US2741546A (en) * | 1952-07-02 | 1956-04-10 | Exxon Research Engineering Co | Floating control for fluidized solids system |
| US2746810A (en) * | 1953-05-07 | 1956-05-22 | Exxon Research Engineering Co | Standpipe for coarse solids and method of operating |
| US2764316A (en) * | 1952-10-02 | 1956-09-25 | Smidth & Co As F L | Apparatus for conveying pulverulent material |
| US2767030A (en) * | 1951-12-21 | 1956-10-16 | Atkinson Bulk Transp Company | Apparatus for conveying pulverulent material in fixed installations |
| US2772864A (en) * | 1954-12-08 | 1956-12-04 | John P Rich | Method and apparatus for evacuating pulp from high density storage towers |
| US2855246A (en) * | 1955-04-22 | 1958-10-07 | Ruston & Hornsby Ltd | Gas-turbo engines |
| US2905362A (en) * | 1954-09-17 | 1959-09-22 | Fmc Corp | Apparatus for filling powdered or granular materials into containers |
| US2914357A (en) * | 1953-12-31 | 1959-11-24 | Exxon Research Engineering Co | Method of dispensing solids in polymerization mixtures |
| US2919159A (en) * | 1956-06-08 | 1959-12-29 | Pechiney Prod Chimiques Sa | Pneumatic conveying method and system |
| US2919160A (en) * | 1957-10-25 | 1959-12-29 | American Cyanamid Co | Apparatus for dispensing material |
| US2924489A (en) * | 1954-11-09 | 1960-02-09 | Beckmann Heinrich | Process and apparatus for conveying finely divided material |
| US3062589A (en) * | 1959-12-14 | 1962-11-06 | Shell Oil Co | Feeding powder at uniform rates |
| US3304127A (en) * | 1965-08-20 | 1967-02-14 | Ma Tran Corp | Material handling apparatus |
| US3463553A (en) * | 1966-11-18 | 1969-08-26 | Siderurgie Fse Inst Rech | Pneumatic conveyor |
| US3870375A (en) * | 1971-11-02 | 1975-03-11 | Nordson Corp | Powder spray system |
| US3955907A (en) * | 1970-12-07 | 1976-05-11 | Keniti Yamasita | Apparatus for molding layered concrete slabs |
| US3985263A (en) * | 1972-04-05 | 1976-10-12 | Research Corporation | Apparatus and method for metering particles |
| US4037877A (en) * | 1975-02-18 | 1977-07-26 | Allen Foster | Down-loading device |
| WO1990008723A1 (en) * | 1989-01-25 | 1990-08-09 | Alcan International Limited | Feeder for particulate material |
| US5299888A (en) * | 1991-11-27 | 1994-04-05 | Finn Corporation | Apparatus for conveying and discharging bulk materials |
| WO1997048629A1 (en) * | 1996-06-18 | 1997-12-24 | Kohlenstaubtechnik Dr. Schoppe Gmbh | Process and device for fluidising fine-grained bulk products |
| EP0953525A3 (en) * | 1998-04-28 | 2001-04-18 | Spies, Klaus, Prof. Dr.-Ing.Dr. hc. | Method and device for introducing a granular or paste like material into a processing plant, in particular high pressure transporting systems |
-
1926
- 1926-04-03 US US99677A patent/US1616547A/en not_active Expired - Lifetime
Cited By (40)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2448272A (en) * | 1943-08-11 | 1948-08-31 | Socony Vacuum Oil Co Inc | Method and apparatus for separation of vapors from a contact mass |
| US2448745A (en) * | 1943-11-16 | 1948-09-07 | Struckmann Holger | Conveying pulverized material |
| US2438728A (en) * | 1944-06-10 | 1948-03-30 | Standard Oil Dev Co | Temperature control in fluidized catalyst systems |
| US2559557A (en) * | 1944-07-12 | 1951-07-03 | Babcock & Wilcox Co | Aerating feeding of pulverized materials |
| US2492401A (en) * | 1945-02-24 | 1949-12-27 | Lummus Co | Gas adsorption |
| US2437694A (en) * | 1946-05-15 | 1948-03-16 | Nasa | Method for blending powder grains |
| US2568400A (en) * | 1946-09-18 | 1951-09-18 | Standard Oil Dev Co | Process for subdividing solid particles |
| US2651602A (en) * | 1948-11-04 | 1953-09-08 | Lummus Co | Process and apparatus for clay contacting in the refining of lubricating oil |
| US2576177A (en) * | 1948-12-30 | 1951-11-27 | Herr Joseph Stanley | Feed mixing apparatus |
| US2609185A (en) * | 1949-07-04 | 1952-09-02 | F S Smidth & Co | Method and apparatus for increasing fluidity of material |
| US2509431A (en) * | 1949-07-14 | 1950-05-30 | Shawinigan Chem Ltd | Dispensing fluidized pulverulent materials |
| US2641574A (en) * | 1949-07-21 | 1953-06-09 | Standard Oil Co | Process and apparatus for decolorizing oil |
| US2687343A (en) * | 1949-12-19 | 1954-08-24 | Phillips Petroleum Co | Fluidized bed floating baffle |
| US2668365A (en) * | 1949-12-31 | 1954-02-09 | Standard Oil Dev Co | Apparatus for determining densities of finely divided solid materials in a fluidized body of such materials |
| US2710232A (en) * | 1950-06-14 | 1955-06-07 | Lawrence D Schmidt | Method for filling cavities with granular solids |
| US2730407A (en) * | 1950-10-23 | 1956-01-10 | Union Oil Co | Conveyance of granular solids |
| US2767030A (en) * | 1951-12-21 | 1956-10-16 | Atkinson Bulk Transp Company | Apparatus for conveying pulverulent material in fixed installations |
| US2741546A (en) * | 1952-07-02 | 1956-04-10 | Exxon Research Engineering Co | Floating control for fluidized solids system |
| US2718471A (en) * | 1952-08-01 | 1955-09-20 | Nat Plastic Products Company | Blending method and apparatus |
| US2764316A (en) * | 1952-10-02 | 1956-09-25 | Smidth & Co As F L | Apparatus for conveying pulverulent material |
| US2746810A (en) * | 1953-05-07 | 1956-05-22 | Exxon Research Engineering Co | Standpipe for coarse solids and method of operating |
| US2914357A (en) * | 1953-12-31 | 1959-11-24 | Exxon Research Engineering Co | Method of dispensing solids in polymerization mixtures |
| US2905362A (en) * | 1954-09-17 | 1959-09-22 | Fmc Corp | Apparatus for filling powdered or granular materials into containers |
| US2924489A (en) * | 1954-11-09 | 1960-02-09 | Beckmann Heinrich | Process and apparatus for conveying finely divided material |
| US2772864A (en) * | 1954-12-08 | 1956-12-04 | John P Rich | Method and apparatus for evacuating pulp from high density storage towers |
| US2855246A (en) * | 1955-04-22 | 1958-10-07 | Ruston & Hornsby Ltd | Gas-turbo engines |
| US2919159A (en) * | 1956-06-08 | 1959-12-29 | Pechiney Prod Chimiques Sa | Pneumatic conveying method and system |
| US2919160A (en) * | 1957-10-25 | 1959-12-29 | American Cyanamid Co | Apparatus for dispensing material |
| US3062589A (en) * | 1959-12-14 | 1962-11-06 | Shell Oil Co | Feeding powder at uniform rates |
| US3304127A (en) * | 1965-08-20 | 1967-02-14 | Ma Tran Corp | Material handling apparatus |
| US3463553A (en) * | 1966-11-18 | 1969-08-26 | Siderurgie Fse Inst Rech | Pneumatic conveyor |
| US3955907A (en) * | 1970-12-07 | 1976-05-11 | Keniti Yamasita | Apparatus for molding layered concrete slabs |
| US3870375A (en) * | 1971-11-02 | 1975-03-11 | Nordson Corp | Powder spray system |
| US3985263A (en) * | 1972-04-05 | 1976-10-12 | Research Corporation | Apparatus and method for metering particles |
| US4037877A (en) * | 1975-02-18 | 1977-07-26 | Allen Foster | Down-loading device |
| WO1990008723A1 (en) * | 1989-01-25 | 1990-08-09 | Alcan International Limited | Feeder for particulate material |
| AU624220B2 (en) * | 1989-01-25 | 1992-06-04 | Alcan International Limited | Feeder for particulate material |
| US5299888A (en) * | 1991-11-27 | 1994-04-05 | Finn Corporation | Apparatus for conveying and discharging bulk materials |
| WO1997048629A1 (en) * | 1996-06-18 | 1997-12-24 | Kohlenstaubtechnik Dr. Schoppe Gmbh | Process and device for fluidising fine-grained bulk products |
| EP0953525A3 (en) * | 1998-04-28 | 2001-04-18 | Spies, Klaus, Prof. Dr.-Ing.Dr. hc. | Method and device for introducing a granular or paste like material into a processing plant, in particular high pressure transporting systems |
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