US1971853A - Apparatus for conveying powdered material - Google Patents

Apparatus for conveying powdered material Download PDF

Info

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
Application number
US716135A
Inventor
Ihlefeldt Johannes
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
FIRM G POLYSIUS AG
Original Assignee
FIRM G POLYSIUS AG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by FIRM G POLYSIUS AG filed Critical FIRM G POLYSIUS AG
Application granted granted Critical
Publication of US1971853A publication Critical patent/US1971853A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/04Conveying materials in bulk pneumatically through pipes or tubes; Air slides
    • B65G53/16Gas pressure systems operating with fluidisation of the materials
    • B65G53/18Gas pressure systems operating with fluidisation of the materials through a porous wall
    • B65G53/20Gas 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.
US716135A 1933-03-24 1934-03-17 Apparatus for conveying powdered material Expired - Lifetime US1971853A (en)

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)

* Cited by examiner, † Cited by third party
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

Cited By (32)

* Cited by examiner, † Cited by third party
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