US1971853A - Apparatus for conveying powdered material - Google Patents
Apparatus for conveying powdered material Download PDFInfo
- Publication number
- US1971853A US1971853A US716135A US71613534A US1971853A US 1971853 A US1971853 A US 1971853A US 716135 A US716135 A US 716135A US 71613534 A US71613534 A US 71613534A US 1971853 A US1971853 A US 1971853A
- Authority
- US
- United States
- Prior art keywords
- conduit
- support
- gas
- conveyed
- conveying
- 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
- 239000012254 powdered material Substances 0.000 title description 4
- 239000000463 material Substances 0.000 description 65
- 239000011148 porous material Substances 0.000 description 7
- 239000004568 cement Substances 0.000 description 4
- 238000010276 construction Methods 0.000 description 4
- 239000012530 fluid Substances 0.000 description 4
- 238000005192 partition Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 235000011089 carbon dioxide Nutrition 0.000 description 1
- 239000002817 coal dust Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 230000005070 ripening Effects 0.000 description 1
- 238000009827 uniform distribution 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
- B65G53/04—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
- B65G53/20—Gas pressure systems operating with fluidisation of the materials through a porous wall of an air slide, e.g. a trough
Definitions
- This invention relates to a process of and apparatus for the conveying of material in pulverulent or finely divided form, for instance cement, coal dust, or farinaceous material. It is the principal object of the invention to provide a simple and effective means whereby the material can be rapidly conveyed and whereby resistance to fiow of the material may be reduced to a minimum.
- a conveying trough or conduit which consists at least in part of a support for the material formed of aporous or gas pervious substance, and a gaseous medium under pressure is forced through this support to maintain the material being conveyed in a suspended state approximating a fluid condition. It is in fact possible to form in this manner a blanket of air adjacent the upper surface of the support on which the finely divided material is carried along so that little or no resistance is offered to the movement of-the material.
- a conveying conduit which may be generally horizontally disposed, having an inlet for the material to be conveyed and a discharge outlet, this conduit having a lower wall formed of porous or gas pervious material through which gas may be forced under pressure in a finely divided state and in an upward direction, whereby the material to be conveyed 3 is maintained in a condition analogous to that of an emulsion and may flow freely through the conduit, being discharged with the gaseous medium at the conduit outlet.
- the construction is such as to permit variation of the pressure with which the gaseous medium is forced through the porous material at difierent points in the length of the conveyor, it having been found by experimentation that most efiicient operation may be effected by gradually reducing this pressure in the direction of movement of the material to be conveyed.
- Theinvention also contemplates the subjection of the gaseous medium to various temperatures differing substantially from that of the material to be conveyed or the inclusion in the gaseous medium of a gas capable of reacting with the material to be conveyed whereby a change in the temperature of the material may be effected or a chemical reaction produced concurrently with the feeding of the material. For instance,
- carbonic acid gas may form a part or all of the gaseous medium so that the ripening of the cement can be partially or wholly completed as the cement is conveyed, this process ensuring a prompt physical or chemical reaction as the result of the intimate commingling of the gaseous medium and the powdered material.
- Figure 2 is a plan view of the structure shown in Figure 1;
- Figure 3 is a transverse sectional view taken substantially on the line 3-3 of Figure 2;
- Figure 4 is a corresponding view illustrating a slightly modified form of conveyor.
- FIG. 1 of the drawing the elongated conveying trough or conduit indicated generally at 10 is illustrated as carried on a plurality of supports 11 and as provided with an inlet port 12 and an outlet port 13. While the conduit 10 is generally horizontal and is shown for convenience as substantially straight, it will be understood that conduits of other configuration may be employed if desired, and that the inclination of the conduit may be altered tofacilitate the conveying of materials of different characteristics.
- the supports 11 are each represented as comprising cooperating threaded elements 15 and 16 which may be relatively rotated to alter the angular disposition of the conduit with respect to the horizontal.
- the material is preferably delivered through the inlet port 12 by means of a telescoping supply duct 18, and the discharge duct 19 leading from the outlet port 13 is preferably constructed as shown in Figure 1 to provide a rocking connection between the separate parts thereof so that communication of the duct with a storage bin or receptacle 20 into which the material is delivered is not disturbed by manipulation of the supports 11.
- the conduit 10 may be open at its upper side, but in the preferred form of the'invention affords a closed passage 21 which is sealed to prevent escape of the powdered material.
- the conduit may be substantially rectangular in cross-section, longitudinally extending structural members 22 being provided, one leg of each member being secured to the associated side wall of the conduit and the other leg serving as a support to which a cover 24 may be applied and secured.
- the transverse shape of the conduit is not an essential element of the invention, and while the construction shown herein is preferred, it is possible to employ a cylindrical conduit.
- a support 26 for the material to be conveyed extends laterally between the side walls of the conduit and longitudinally of the latter, this support being spaced from the bottom wall 27 of the conduit to provide a gas passage 32 therebetween.
- the support 26 is illustrated as carried by the structural L-shaped members 28 secured to the side walls of the conduit, but the support 26 may be carried solely by partitions 30 extending transversely of the conduit and arranged in spaced relation longitudinally thereof, these partitions separating the passage 32 into a plurality of isolated compartments for a purpose hereinafter explained.
- the support 26 is formed of gas pervious material for instance filter stones, porous brick, porous rubber, porous porcelain, or-similar substances, the nature of the material preferably being such that gas may flow upwardly through the support and may emerge therefrom in a finely divided state, the development of individual jets or streams of gas being preferably avoided.
- gas pervious material for instance filter stones, porous brick, porous rubber, porous porcelain, or-similar substances, the nature of the material preferably being such that gas may flow upwardly through the support and may emerge therefrom in a finely divided state, the development of individual jets or streams of gas being preferably avoided.
- the gaseous medium under pressure is supplied to the passage 32 by means of a gas conduit 35 extending longitudinally of the conduit 10, a pump or other suitable gas pressure device delivering the gas to the conduit 35 through the flexible pipe 36, the latter permitting adjustment of the inclination of the conduit 10 as hereinbefore explained without interruption of the supply of gas.
- the conduit 35 is connected with the passage 32 by means of pipes 38, the latter affording communication between the conduit 35 and each of the separate compartments formed by the partitions 30 in the passage 32.
- This construction is to permit variation in the pressure under which gas is supplied to thepassage 32 longitudinally of the conduit 10, the conveyor functioning in a more efiicient manner when a pressure gradient is established so that the pressureis less at the discharge than at the inlet end of the conduit.
- a valve 40 in the conduit 35 controls the flow of gas through the latter and if desired separate valves as indicated at 39 in Figure 3 may be inserted in each of the pipes 38 to effect control of the pressure in the several compartments beneath the support 26.
- the difference in pressure in the several compartments may be controlled by proper design of the conduit 35 and the pipes 38, reduction in pressure longitudinally of the conduit 10 taking place for instance as the result of variation in cross-sec tional area and consequent frictional resistance to flow of gas within the conduit 35 and the pipes 38.
- the support 26 may be either flat as shown in Figure 3 or curvedlaterally as shown at 25 in the conveyor 9 of Figure 4, it being possible under some conditions .to provide a support of sufficient curvature to permit the elimination of the side walls and cover of the conduit, the material flowing readily along the trough-shaped support by the maintenance of the material in a substantially fluid condition.
- the operation of the device will now be understood from the foregoing description.
- the material to be conveyed is discharged downwardly through the duct 18 and passes along the support 26, the gaseous medium under pressure supplied in the passage 32 beneath the latter being forced upwardly through the support and maintaining the material to be conveyed in such condition that it assumes the characteristics of a fluid emulsion.
- the nature of the support 26 is such that a blanket of gas is established on the upper surface thereof which effectively prevents clogging of the material and reduces resistance of flow of the material to a minimum.
- the invention contemplates the provision of a porous support on which the material to be conveyed may rest, together with means for forcing a gaseous medium such as air upwardly through the support with suflicient pressure to maintain the material to be conveyed in a condition of fluidity, the material being thus simultaneously conveyed and agitated.
- a gaseous medium such as air upwardly through the support with suflicient pressure to maintain the material to be conveyed in a condition of fluidity, the material being thus simultaneously conveyed and agitated.
- the apparatus is particularly useful in the event a mixture of different materials is conveyed, the
- apparatus for conveying finely divided material the combination with a generally horizontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for introducing a gaseous medium into said conduit and beneath said support, whereby the gaseous medium may pass through said support and cause the finely divided material to flow along the conduit.
- a support for said conduit adjustable vertically to vary the inclination of the conduit to-facilitate the conveying of material of different characteristics.
- a generally horizontally disposed trough having a lower wall of a porous substance, of means for introducing a gaseous medium under pressure through said lower wall into said trough, said trough having an inlet for the material to be conveyed and an outlet through which the material and the gaseous medium may be discharged, whereby the material may be conveyed through said trough from the inlet to the outlet and simultaneously agitated.
- apparatus for conveying finely divided material the combination with a generally hori-- zontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for introducing a gaseous medium beneath said support and establishing a pressure gradient decreasing from the inlet to the outlet therein, whereby the latter will be forced through said support to maintain the finely divided material in a state of suspension and flow.
- apparatus for conveying finely divided material the combination with a generally horizontally disposed conduit having an inlet for the material and a' discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and extending laterally across and longitudinally 01' said conduit to form isolated upper and lower chambers therein, and means for introducing a gaseous medium under pressure into said lower chamber.
- apparatus for conveying finely divided material the combination with a generally horizontally disposed conduit having an inlet for the material and a. discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and extending laterally across and longitudinally of said conduit to form isolated upper and lower chambers therein, partitions in said lower chamber spaced longitudinally thereoi to form a plurality of isolated compartments therein, and separate means for introducing air under pressure into the several compartments.
Description
Aug. 28, 1934. J. IHLEFELDT APPARATUS FOR CONVEYING POWDERED MATERIAL Filed March 17, 1934 Patented Aug. 28, 1934 UNITED STATES PATENT OFFICE Johannes Ihlefeldt, Dessau, Germany, assignor to the firm G. Polysius, Aktien'gesellsohaft,
Dessau, Germany Application March 17, .1934, Serial No. 716,135
Germany March 24, 1933 9 Claims.
This invention relates to a process of and apparatus for the conveying of material in pulverulent or finely divided form, for instance cement, coal dust, or farinaceous material. It is the principal object of the invention to provide a simple and effective means whereby the material can be rapidly conveyed and whereby resistance to fiow of the material may be reduced to a minimum.
It is a feature of the invention that the material is thoroughly mixed and agitated during the process of conveying the same. Thus in the preferred form of the invention a conveying trough or conduit is provided which consists at least in part of a support for the material formed of aporous or gas pervious substance, and a gaseous medium under pressure is forced through this support to maintain the material being conveyed in a suspended state approximating a fluid condition. It is in fact possible to form in this manner a blanket of air adjacent the upper surface of the support on which the finely divided material is carried along so that little or no resistance is offered to the movement of-the material.
More specifically, it is an object of the invention to provide a conveying conduit, which may be generally horizontally disposed, having an inlet for the material to be conveyed and a discharge outlet, this conduit having a lower wall formed of porous or gas pervious material through which gas may be forced under pressure in a finely divided state and in an upward direction, whereby the material to be conveyed 3 is maintained in a condition analogous to that of an emulsion and may flow freely through the conduit, being discharged with the gaseous medium at the conduit outlet.
It is a further feature of the invention that the construction is such as to permit variation of the pressure with which the gaseous medium is forced through the porous material at difierent points in the length of the conveyor, it having been found by experimentation that most efiicient operation may be effected by gradually reducing this pressure in the direction of movement of the material to be conveyed.
Theinvention also contemplates the subjection of the gaseous medium to various temperatures differing substantially from that of the material to be conveyed or the inclusion in the gaseous medium of a gas capable of reacting with the material to be conveyed whereby a change in the temperature of the material may be effected or a chemical reaction produced concurrently with the feeding of the material. For instance,
in the event cement is being conveyed, carbonic acid gas may form a part or all of the gaseous medium so that the ripening of the cement can be partially or wholly completed as the cement is conveyed, this process ensuring a prompt physical or chemical reaction as the result of the intimate commingling of the gaseous medium and the powdered material.
Further objects and features of the invention will be apparent from the following description taken in connection with the accompanying drawing, in which Figure 1 is a longitudinal vertical sectional view of apparatus constructed in accordance with the principles of the invention;
Figure 2 is a plan view of the structure shown in Figure 1;
Figure 3 is a transverse sectional view taken substantially on the line 3-3 of Figure 2; and
Figure 4 is a corresponding view illustrating a slightly modified form of conveyor.
In order to facilitate an understanding of the invention reference is made herein to the specific forms thereof illustrated in the drawing and detailed descriptive language is employed. It will nevertheless be understood that no limitation of the invention is thereby intended and that various alterations and changes in the structure shown may be made without departing from the principles of the invention as defined in the appended claims.
In Figure 1 of the drawing the elongated conveying trough or conduit indicated generally at 10 is illustrated as carried on a plurality of supports 11 and as provided with an inlet port 12 and an outlet port 13. While the conduit 10 is generally horizontal and is shown for convenience as substantially straight, it will be understood that conduits of other configuration may be employed if desired, and that the inclination of the conduit may be altered tofacilitate the conveying of materials of different characteristics. Thus the supports 11 are each represented as comprising cooperating threaded elements 15 and 16 which may be relatively rotated to alter the angular disposition of the conduit with respect to the horizontal. To facilitate such adjustment the material is preferably delivered through the inlet port 12 by means of a telescoping supply duct 18, and the discharge duct 19 leading from the outlet port 13 is preferably constructed as shown in Figure 1 to provide a rocking connection between the separate parts thereof so that communication of the duct with a storage bin or receptacle 20 into which the material is delivered is not disturbed by manipulation of the supports 11. These details of the construction whereby the inclination of the conduit 10 maybe altered are not important and form no essential part ofthe present invention."
The conduit 10 may be open at its upper side, but in the preferred form of the'invention affords a closed passage 21 which is sealed to prevent escape of the powdered material. Thus as shown more particularly in Figures 1 and 3 of the drawing, the conduitmay be substantially rectangular in cross-section, longitudinally extending structural members 22 being provided, one leg of each member being secured to the associated side wall of the conduit and the other leg serving as a support to which a cover 24 may be applied and secured. It will be understood that the transverse shape of the conduit is not an essential element of the invention, and while the construction shown herein is preferred, it is possible to employ a cylindrical conduit.
A support 26 for the material to be conveyed extends laterally between the side walls of the conduit and longitudinally of the latter, this support being spaced from the bottom wall 27 of the conduit to provide a gas passage 32 therebetween. In the form of the invention shown in Figure 3 of the'drawing the support 26 is illustrated as carried by the structural L-shaped members 28 secured to the side walls of the conduit, but the support 26 may be carried solely by partitions 30 extending transversely of the conduit and arranged in spaced relation longitudinally thereof, these partitions separating the passage 32 into a plurality of isolated compartments for a purpose hereinafter explained.
The support 26 is formed of gas pervious material for instance filter stones, porous brick, porous rubber, porous porcelain, or-similar substances, the nature of the material preferably being such that gas may flow upwardly through the support and may emerge therefrom in a finely divided state, the development of individual jets or streams of gas being preferably avoided.
The gaseous medium under pressure is supplied to the passage 32 by means of a gas conduit 35 extending longitudinally of the conduit 10, a pump or other suitable gas pressure device delivering the gas to the conduit 35 through the flexible pipe 36, the latter permitting adjustment of the inclination of the conduit 10 as hereinbefore explained without interruption of the supply of gas. In the preferred form of the invention the conduit 35 is connected with the passage 32 by means of pipes 38, the latter affording communication between the conduit 35 and each of the separate compartments formed by the partitions 30 in the passage 32. The purpose of this construction is to permit variation in the pressure under which gas is supplied to thepassage 32 longitudinally of the conduit 10, the conveyor functioning in a more efiicient manner when a pressure gradient is established so that the pressureis less at the discharge than at the inlet end of the conduit.
A valve 40 in the conduit 35 controls the flow of gas through the latter and if desired separate valves as indicated at 39 in Figure 3 may be inserted in each of the pipes 38 to effect control of the pressure in the several compartments beneath the support 26. Alternatively, the difference in pressure in the several compartments may be controlled by proper design of the conduit 35 and the pipes 38, reduction in pressure longitudinally of the conduit 10 taking place for instance as the result of variation in cross-sec tional area and consequent frictional resistance to flow of gas within the conduit 35 and the pipes 38.
The support 26 may be either flat as shown in Figure 3 or curvedlaterally as shown at 25 in the conveyor 9 of Figure 4, it being possible under some conditions .to provide a support of sufficient curvature to permit the elimination of the side walls and cover of the conduit, the material flowing readily along the trough-shaped support by the maintenance of the material in a substantially fluid condition.
The operation of the device will now be understood from the foregoing description. The material to be conveyed is discharged downwardly through the duct 18 and passes along the support 26, the gaseous medium under pressure supplied in the passage 32 beneath the latter being forced upwardly through the support and maintaining the material to be conveyed in such condition that it assumes the characteristics of a fluid emulsion. Obviously the nature of the support 26 is such that a blanket of gas is established on the upper surface thereof which effectively prevents clogging of the material and reduces resistance of flow of the material to a minimum.
In its broadest aspect the invention contemplates the provision of a porous support on which the material to be conveyed may rest, together with means for forcing a gaseous medium such as air upwardly through the support with suflicient pressure to maintain the material to be conveyed in a condition of fluidity, the material being thus simultaneously conveyed and agitated. The apparatus is particularly useful in the event a mixture of different materials is conveyed, the
suspension of the particles of the mixture in the gas facilitating a uniform distribution of the several materials.
Having thus described the invention, what is claimed as new and desired to be secured by Letters Patent is:
1. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for forcing a gaseous medium upwardly through said support.
2. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for introducing a gaseous medium into said conduit and beneath said support, whereby the gaseous medium may pass through said support and cause the finely divided material to flow along the conduit.
3. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for forcing a gaseous medium upwardly through said support, a support for said conduit adjustable vertically to vary the inclination of the conduit to-facilitate the conveying of material of different characteristics.
4. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed trough, having a lower wall of a porous substance, of means for introducing a gaseous medium under pressure through said lower wall into said trough, said trough having an inlet for the material to be conveyed and an outlet through which the material and the gaseous medium may be discharged, whereby the material may be conveyed through said trough from the inlet to the outlet and simultaneously agitated.
5. In apparatus for conveying finely divided material, the combination with a generally hori-- zontally disposed conduit having an inlet for the material and a discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and means for introducing a gaseous medium beneath said support and establishing a pressure gradient decreasing from the inlet to the outlet therein, whereby the latter will be forced through said support to maintain the finely divided material in a state of suspension and flow.
6. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed conduit having an inlet for the material and a' discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and extending laterally across and longitudinally 01' said conduit to form isolated upper and lower chambers therein, and means for introducing a gaseous medium under pressure into said lower chamber.
7. In apparatus for conveying finely divided material, the combination with a generally horizontally disposed conduit having an inlet for the material and a. discharge outlet, of a support for said material disposed within said conduit in the lower portion thereof, said support being formed of porous material, and extending laterally across and longitudinally of said conduit to form isolated upper and lower chambers therein, partitions in said lower chamber spaced longitudinally thereoi to form a plurality of isolated compartments therein, and separate means for introducing air under pressure into the several compartments.
8. In apparatus for conveying finely divided material, the combination with means affording a passage for the material having a lower wall of gas pervious material, and means for forcing a gaseous medium under pressure through said wall, the degree of pressure being lessened in the direction of movement of the finely divided material.
9. In apparatus for conveying finely divided material, the combination with a generally horizontal elongated support formed of gas pervious material, of means for forcing gas under sumcient pressure through said support to maintain the finely dividedjmaterial thereon in a substantially fluid condition.
JOHANNES IHLEFELDT.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE1971853X | 1933-03-24 |
Publications (1)
Publication Number | Publication Date |
---|---|
US1971853A true US1971853A (en) | 1934-08-28 |
Family
ID=7828394
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US716135A Expired - Lifetime US1971853A (en) | 1933-03-24 | 1934-03-17 | Apparatus for conveying powdered material |
Country Status (1)
Country | Link |
---|---|
US (1) | US1971853A (en) |
Cited By (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2448745A (en) * | 1943-11-16 | 1948-09-07 | Struckmann Holger | Conveying pulverized material |
US2527488A (en) * | 1950-04-10 | 1950-10-24 | Huron Portland Cement Company | Apparatus for conveying materials |
US2527455A (en) * | 1950-02-18 | 1950-10-24 | Huron Portland Cement Company | Apparatus for conveying materials |
US2527466A (en) * | 1949-02-21 | 1950-10-24 | Huron Portland Cement Company | Air activated conveyer |
US2545766A (en) * | 1948-09-02 | 1951-03-20 | Cline Theodore William | Bulk granular material transporting vehicle |
US2589968A (en) * | 1946-12-23 | 1952-03-18 | Huron Portland Cement Company | Self-unloading vehicle body |
US2609125A (en) * | 1948-09-25 | 1952-09-02 | Huron Portland Cement Company | Self-unloading bin |
US2624069A (en) * | 1948-10-08 | 1953-01-06 | Ind Sound Systems Inc | Method and apparatus for fabricating seamless capsules |
US2695815A (en) * | 1951-02-16 | 1954-11-30 | Socony Vacuum Oil Co Inc | Method of and apparatus for pneumatic transfer of granular contact material in moving bed hydrocarbon conversion processes |
US2708602A (en) * | 1951-12-18 | 1955-05-17 | Smidth & Co As F L | Discharge apparatus for pulverulent or granular material |
US2735725A (en) * | 1956-02-21 | Apparatus for discharging pulverulent | ||
US2785018A (en) * | 1951-02-17 | 1957-03-12 | Diamond Alkali Co | Material handling method |
US2804349A (en) * | 1956-01-26 | 1957-08-27 | Beaumont Birch Company | Pulverized material feeder apparatus |
US2805898A (en) * | 1955-01-18 | 1957-09-10 | Jr Edward A Willis | Fluid current conveyor for fragile articles |
US2897005A (en) * | 1957-03-11 | 1959-07-28 | Sumner D Wiltse | Fluidized pressure system |
US3056632A (en) * | 1958-11-07 | 1962-10-02 | Holderbank Cement | Pneumatic conveyor |
US3156398A (en) * | 1961-06-30 | 1964-11-10 | Rca Corp | Tape handling apparatus |
US3180688A (en) * | 1963-05-22 | 1965-04-27 | Rudolph E Futer | Air-lift conveying of solids |
US3253865A (en) * | 1965-03-11 | 1966-05-31 | Kanics Andras | Apparatus for handling bulk material |
US3268264A (en) * | 1964-08-13 | 1966-08-23 | Arthur M Squires | Apparatus and method for conveying dry pulverulent solid in liquidlike state |
US3279864A (en) * | 1964-03-23 | 1966-10-18 | Wyatt J Weeks | Pneumatic conveyor |
US3304619A (en) * | 1965-01-27 | 1967-02-21 | Rudolph E Futer | Method and means for changing the temperature of granular material by gas jets |
US3362755A (en) * | 1962-08-23 | 1968-01-09 | Macks Elmer Fred | Conveying device utilizing pressurized fluid flow |
US3393943A (en) * | 1966-06-29 | 1968-07-23 | American Colloid Co | Apparatus and methods for fluidizing granular or pulverate materials |
US3395943A (en) * | 1965-10-22 | 1968-08-06 | Pilkington Brothers Ltd | Methods of and apparatus for carrying glass sheets |
US3414331A (en) * | 1967-02-09 | 1968-12-03 | Rapistan Inc | Valve for air film conveyors |
US3475058A (en) * | 1967-03-13 | 1969-10-28 | Roy Oliver Sanders | Conveying apparatus |
US3514158A (en) * | 1968-04-15 | 1970-05-26 | Fuller Co | Pneumatic conveying apparatus |
US3929379A (en) * | 1973-02-02 | 1975-12-30 | Waeschle Maschf Gmbh | Method and apparatus for the pneumatic conveying of bulk material |
US5360297A (en) * | 1991-03-25 | 1994-11-01 | Norsk Hydro A.S. | Apparatus for automatic level control in a closed channel or container for transport and/or distribution of fluidizable material |
US5588787A (en) * | 1994-06-22 | 1996-12-31 | Norsk Hydro A.S. | Pulse-operated point feeder |
US20090010720A1 (en) * | 2007-07-02 | 2009-01-08 | Flsmidth A/S | Use of air activated gravity conveyors in a continuous particulate removal process from an ESP or baghouse |
-
1934
- 1934-03-17 US US716135A patent/US1971853A/en not_active Expired - Lifetime
Cited By (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2735725A (en) * | 1956-02-21 | Apparatus for discharging pulverulent | ||
US2448745A (en) * | 1943-11-16 | 1948-09-07 | Struckmann Holger | Conveying pulverized material |
US2589968A (en) * | 1946-12-23 | 1952-03-18 | Huron Portland Cement Company | Self-unloading vehicle body |
US2545766A (en) * | 1948-09-02 | 1951-03-20 | Cline Theodore William | Bulk granular material transporting vehicle |
US2609125A (en) * | 1948-09-25 | 1952-09-02 | Huron Portland Cement Company | Self-unloading bin |
US2624069A (en) * | 1948-10-08 | 1953-01-06 | Ind Sound Systems Inc | Method and apparatus for fabricating seamless capsules |
US2527466A (en) * | 1949-02-21 | 1950-10-24 | Huron Portland Cement Company | Air activated conveyer |
US2527455A (en) * | 1950-02-18 | 1950-10-24 | Huron Portland Cement Company | Apparatus for conveying materials |
US2527488A (en) * | 1950-04-10 | 1950-10-24 | Huron Portland Cement Company | Apparatus for conveying materials |
US2695815A (en) * | 1951-02-16 | 1954-11-30 | Socony Vacuum Oil Co Inc | Method of and apparatus for pneumatic transfer of granular contact material in moving bed hydrocarbon conversion processes |
US2785018A (en) * | 1951-02-17 | 1957-03-12 | Diamond Alkali Co | Material handling method |
US2708602A (en) * | 1951-12-18 | 1955-05-17 | Smidth & Co As F L | Discharge apparatus for pulverulent or granular material |
US2805898A (en) * | 1955-01-18 | 1957-09-10 | Jr Edward A Willis | Fluid current conveyor for fragile articles |
US2804349A (en) * | 1956-01-26 | 1957-08-27 | Beaumont Birch Company | Pulverized material feeder apparatus |
US2897005A (en) * | 1957-03-11 | 1959-07-28 | Sumner D Wiltse | Fluidized pressure system |
US3056632A (en) * | 1958-11-07 | 1962-10-02 | Holderbank Cement | Pneumatic conveyor |
US3156398A (en) * | 1961-06-30 | 1964-11-10 | Rca Corp | Tape handling apparatus |
US3362755A (en) * | 1962-08-23 | 1968-01-09 | Macks Elmer Fred | Conveying device utilizing pressurized fluid flow |
US3180688A (en) * | 1963-05-22 | 1965-04-27 | Rudolph E Futer | Air-lift conveying of solids |
US3279864A (en) * | 1964-03-23 | 1966-10-18 | Wyatt J Weeks | Pneumatic conveyor |
US3268264A (en) * | 1964-08-13 | 1966-08-23 | Arthur M Squires | Apparatus and method for conveying dry pulverulent solid in liquidlike state |
US3304619A (en) * | 1965-01-27 | 1967-02-21 | Rudolph E Futer | Method and means for changing the temperature of granular material by gas jets |
US3253865A (en) * | 1965-03-11 | 1966-05-31 | Kanics Andras | Apparatus for handling bulk material |
US3395943A (en) * | 1965-10-22 | 1968-08-06 | Pilkington Brothers Ltd | Methods of and apparatus for carrying glass sheets |
US3393943A (en) * | 1966-06-29 | 1968-07-23 | American Colloid Co | Apparatus and methods for fluidizing granular or pulverate materials |
US3414331A (en) * | 1967-02-09 | 1968-12-03 | Rapistan Inc | Valve for air film conveyors |
US3475058A (en) * | 1967-03-13 | 1969-10-28 | Roy Oliver Sanders | Conveying apparatus |
US3514158A (en) * | 1968-04-15 | 1970-05-26 | Fuller Co | Pneumatic conveying apparatus |
US3929379A (en) * | 1973-02-02 | 1975-12-30 | Waeschle Maschf Gmbh | Method and apparatus for the pneumatic conveying of bulk material |
US5360297A (en) * | 1991-03-25 | 1994-11-01 | Norsk Hydro A.S. | Apparatus for automatic level control in a closed channel or container for transport and/or distribution of fluidizable material |
US5588787A (en) * | 1994-06-22 | 1996-12-31 | Norsk Hydro A.S. | Pulse-operated point feeder |
US20090010720A1 (en) * | 2007-07-02 | 2009-01-08 | Flsmidth A/S | Use of air activated gravity conveyors in a continuous particulate removal process from an ESP or baghouse |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US1971853A (en) | Apparatus for conveying powdered material | |
US2316814A (en) | Feeder | |
US1971852A (en) | Process for stirring up farinaceous materials in receptacles of any kind by compressed air, compressed gas, or the like | |
US2586818A (en) | Progressive classifying or treating solids in a fluidized bed thereof | |
US2844361A (en) | Method and apparatus for blending pulverulent material | |
US1472314A (en) | Process of and apparatus for drying and treating materials | |
US2766534A (en) | Method and apparatus for treating granular materials with gases | |
US2192287A (en) | Apparatus for feeding finely divided material | |
US2219283A (en) | Apparatus for conveying powdered material | |
US2527488A (en) | Apparatus for conveying materials | |
GB834052A (en) | Method of and apparatus for conveying particulate material | |
US3804250A (en) | Stratifier with discharge means for maintaining stratified layers | |
US4334898A (en) | Device for the production of solid aluminum chloride | |
US3003752A (en) | Method and apparatus for conditioning pulverulent or granular material | |
US3648380A (en) | Fluidized bed level control | |
US3266870A (en) | Bypass chemical dissolver with slantedslot jet agitators | |
US2735725A (en) | Apparatus for discharging pulverulent | |
US2226958A (en) | Apparatus for carbonating liquids | |
RU2060216C1 (en) | Closed channel or conveyor for transportation and/or distribution of fluidized material | |
US2740671A (en) | Pulverulent material supply for volumetric feeders | |
US2326276A (en) | Method and apparatus for feeding hygroscopic and reactive materials | |
US2244195A (en) | Apparatus and process for fluidifying and mixing by means of compressed air | |
US2319457A (en) | Apparatus for gravity separation of granular material | |
US2067335A (en) | Gas control and feeding unit | |
US2976997A (en) | Means for separating heavy particles from sands |