Material or article handling – Process – Of emptying portable receptacle
Reexamination Certificate
2002-03-22
2003-05-06
Werner, Frank E. (Department: 3652)
Material or article handling
Process
Of emptying portable receptacle
C406S038000, C406S075000, C414S800000, C414S809000, C414S403000, C414S415000, C414S363000, C414S421000, C220S001500, C222S196000, C222S203000
Reexamination Certificate
active
06558111
ABSTRACT:
BACKGROUND OF THE INVENTION
Transport of bulk powders from the manufacturing location to user location often pose problems particularly for powders that are by nature cohesive.
To transport bulk powders economically, they are typically shipped in metric ton bags commonly called semi-bulk containers (SBC's) or large bulk containers commonly called COFC's (container on railway flat car) or IMC's (intermodal containers). But, these alternatives have associated problems that increase transportation and handling costs, particularly for cohesive powders.
Use of SBC's offer efficiencies if the end user is willing to accept the SBC for direct use in their operations. If the end user prefers bulk delivery, the SBC must be dumped into large storage containers or into bulk trucks for delivery or use. This operation requires time and potentially represents some loss of product due to the incomplete emptying of the bag. The residual material (known as a heel) is often discarded with the bags.
IMC's may be used to efficiently transport bulk powders by rail or by sea, but on receipt at the receiving location the bulk powder must be transferred to storage or to bulk trucks for delivery. Economical unloading of bulk materials from IMC's at a transfer terminal or end user must be accomplished rapidly (ideally in one or two hours) in order to make effective use of labor and the expensive capital equipment needed to handle or unload the IMC. Any connection between the IMC and an unloading system must be made (and later removed) rapidly in order to minimize the impact on the total unloading cycle time. Spillage or airborne dust is not permissible due to product losses and environmental and housekeeping concerns.
Free flowing bulk materials such as plastic pellets and agricultural grains can easily be unloaded from IMC's containing 20 tons or more of material. Cohesive powders, on the other hand, are extremely difficult to unload from IMC's due to their bulk handling properties. These properties fall into four categories—dustiness, wall friction, gas permeability, and cohesive strength.
Discharging a load of cohesive bulk powder requires long times and presents unloading problems even when gravity unloading is assisted by the extensive use of vibrators or the use of pneumatic aeration systems. Such assisted unloading methods generally lead to dusting problems. Often, in spite of much effort directed to discharging all the powder stored in the IMC, substantial heels remain in the liner unavailable for use.
U.S. Pat. No. 3,999,741 teaches a method of unloading pigments from a bulk container by adding liquid to the container and removing the pigment as dispersion.
German Patent Publication DE 34 29 167 A1 teaches a method and apparatus for unloading a flexible container (such as a big bag) by placing the container on a vibrating element.
U.S. Pat. No. 4,781,513 teaches an apparatus for unloading and spreading a bulk material such as asphalt over the ground.
U.S. Pat. Nos. 4,875,811; 5,096,336; and 5,378,047 teach related inventions. In each case the invention is directed to unloading a bulk container using a pneumatic conveying apparatus. In the apparatus and process taught in these patents, bulk material such as polycarbonate resin is directed through a flexible conduit to a rotary valve that feeds the particulate material into a lower hopper for pneumatic conveying into a suitable storage facility.
U.S. Pat. No. 4,301,943 teaches a container and process to unload melamine powder from a bulk container. According to this patent melamine powder is unloaded through a discharge device having a hopper portion, a connector portion and a rotary pump assembly wherein certain hopper dimensions of angle, height and opening diameters are required.
The present invention provides an unloading system that is fully effective even with cohesive bulk powders such as pigmentary titanium dioxide.
BRIEF SUMMARY OF THE INVENTION
The present invention is directed to a bulk unloading system comprising:
(a) a bulk container removably mounted on a platform, the container having surrounding walls and a floor mounted on a structural frame and two ends, a front end and a rear end, wherein the front end is closed and rear end is least partially open; and the platform having a means of tilting the container at an angle from about 0 to at least 40 degrees;
(b) optionally a removable, flexible liner within the container where the bulk powder is sealed;
(c) optionally vibrators mounted on the container floor structural frame; and
(d) a manifold having inlet and discharge sections, the manifold being mounted on the rear end of the container or on the platform, wherein at least a portion of the manifold is lined with a pneumatic conditioning membrane having a means of gas supply.
The present invention includes a method to unload bulk powder from a large bulk container removably mounted on a platform, the container having surrounding walls and a floor mounted on a structural frame and two ends, a front end and a rear end, wherein the front end is closed and rear end is least partially open, the powder being stored in the container or in a removable, flexible liner within the container; the platform having a means of tilting the container at an angle from about 0 to at least 40 degrees; and optionally vibrators mounted the container floor structural frame, the method comprising the steps of;
(a) connecting to the rear end of the container a manifold having a inlet and discharge sections wherein at least a portion of the manifold is lined with a pneumatic conditioning membrane having a means of gas supply;
(b) when the powder is stored within a liner, cutting the liner where the liner is exposed by the opening in the top plate of the manifold;
(c) tilting the container to an angle between 0 and at least 40 degrees;
(d) activating the pneumatic conditioning membrane by supplying gas to the membrane, with the proviso that if the angle of tilt is fixed and is an angle less than the angle of repose of the bulk powder the vibrators are activated.
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George P. Fotou, Quint H. Powell, Toivo T. Kodas, “Gas-Phase Coating of Titania with Metal Oxides in an Aerosol Flow Reactor”, Center for Micro-Engineered Ceramics, Department of Chemical Engineering, University of New Mexico, Albuquerque, NM.
Bell Timothy Allan
Clark Peter Carl
Connolly, Jr. John D.
Wilson Catherine Marie
E. I. du Pont de Nemours and Company
Werner Frank E.
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