In the processing of bulk materials, including wet fibrous materials, it is often necessary to compress the materials to extract liquids and that is typically done with a screw press, which includes a screw operating within a cylindrical screen housing. As the screw compresses the fibrous materials by compacting them, liquid is expressed through the screen housing of the screw press. Each flight (360 degree wrap of flighting) of a screw can hold a certain volume of material as determined by its inner and outer diameter as well as its pitch (length). The compression ratio of the screw press is determined by dividing the volume of the flight entering, the screen housing by the volume of the flight leaving the screw housing on the other side. In the compression of wet corn fiber materials, it is desirable to use an optimum compression ratio between one which results in escape of fibrous solids through the screen housing and a smaller compression ratio which results in too little liquid being extracted. Because compressed fibrous materials must be dried, remaining liquids must be removed through evaporation accomplished thermally by use of rotary dryers. Because it is far more enemy efficient to remove liquid mechanically through use of a screw press than thermally in a diver, it is important to maximize compression without exceeding the limit which results in solids being forced through the cage structure. Generally, in the processing of wet corn fiber material, a nominally approximate compression ratio is 7.5 but materials vary and so use of that ratio may not be optimum for each processing site or each batch of material to be dewatered. However, varying the compression ratio of a screw press has heretofore only been accomplished by alteration of the pitch of the screw flighting at either the intake end or the outlet end, which necessarily requires disassembly of the screw press and reworking of the screw flighting. This is both time consuming and costly yet still typically yields only compromised results.
A need exists for an apparatus which allows variation in the compression ratio of a screw press without the need to alter the pitch of the screw on the intake end; preferably while the press is in operation
The invention comprises apparatus which effectively reduces the pitch of the pressure housing, feed flight thus changing its volume. The pressure housing feed flight is the screw flight entrance into the screw housing. A volume reduction member is placed within the intake hopper of the screw press to serve to reduce the intake volume of the pressure housing feed flight. The volume reduction member has a lower end which conforms to the periphery of the screw flighting such that the flighting may operate below the lower end while the volume reduction member restricts the intake volume into the pressure housing feed flight.
In one embodiment, a plate hinged at its top is inserted into the intake hopper. By altering the angle and location of the plate, the intake volume may be increased or lowered and the compression ratio thereby changed as needed without disassembling the screw press or even shutting it down temporarily.
in another embodiment, a shroud member is introduced into the intake hopper. The shroud member is adjustable within the intake hopper and may be moved forward into the hopper or moved rearward within the hopper to increase the volume of the intake hopper and thereby increase the compression ratio of the screw press. The shroud member is movable along side rails mounted within the intake hopper and can be moved ahead or back by use of a threaded rod which passes through an end wall of the intake hopper. By properly rotating the threaded rod, the shroud member is moved into or out of the intake volume of the intake hopper of the screw press.
In another embodiment which may be used alone or with the shroud member, block elements are mounted to the screw flighting within the intake hopper to reduce the volume of commodity which may be received in the pressure housing, feed flight, thereby reducing the compression ratio between intake and output of the compression screw press.
It is therefore an objective to provide a variable compression screw press which can be adjusted to vary the compression ratio between the intake hopper of the press and the discharge box of the press by altering the intake volume available to receive commodity at the intake hopper.
Another object of the invention is to provide a screw press which allows the effective pitch of the pressure housing feed flight to be reduced as desired without dismantling, the screw press or disrupting its operation.
A further object of the invention is to provide apparatus to further reduce the compression ratio of a screw press by installation of volume displacing, block elements on the pressure housing, feed flight of the press.
The objects of the invention will be better understood by reference to the detailed description which follows.
For purposes of the disclosure and claims which follow, the following definitions shall apply:
“Flight” shall mean one segment of screw flighting which consists of 360 degrees of the screw flighting.
“Pitch” shall mean the length along the screw pipe which a single flight extends.
Screw flighting 22 includes intake flight 25 which is located within intake hopper 52 immediately adjacent entrance 51 to screen housing 54.
intake hopper 52 provides a chute through which fibrous commodity is fed to screw 20. The pitch of intake flight 25 located within intake hopper 52, in relationship to the pitch of the final compression flight 26 near outlet 60, governs the compression ratio of the press 50. Intake flight 25 also may be referred to as pressure housing feed flight 25. All flights helically circumnavigate pipe 27 and are fixed in place thereon, typically by welding. Upstream end flight 23 is joined to upstream end 24 of intake flight 25 by a weld 29.
Depending on the nature of the material to be pressed, a preferred approximate compression ratio is determined. For instance, if wet corn fiber is to be compressed, a compression ratio of approximately 7.5 is often used but variations in condition of the material may require that the ratio be different in order to maximize the separation of liquid content front the material without applying so much compressive force that the solids in the material are forced through the screen housing 54. Lower moisture solids require less energy to finish the drying process than wetter solids so maximizing liquid separation is desired before solids are moved to a thermal dryer. The present invention allows selection of varying compression ratios without reworking the pitch of any flights.
Referring now additionally to
Gate 10 extends between first sidewall 53 and opposing second sidewall 55 of intake hopper 52. Its lower arched end 16 generally conforms to the circular periphery 21 of flighting 22 and is disposed over flight 25. Adjusting rod 14 extends through downstream end wall 57 of intake hopper 52 and is longitudinally moveable to change the angle of gate 10 to restrict more or less of the material volume flowing into flight 25. Other structures to vary the incline and span of gate 10 may be used.
The location of lower end 16 over flight 25 defines the effective feed area. Covering more of flight 25 with gate 10 decreases the compression ratio of press 50.
Therefore, it can be appreciated that variation of the compression ratio of screw press 50 can be controlled by insertion or withdrawal of control rod 14 through downstream end wall 57 and by selective horizontal positioning of shield 12, thereby moving hinge 28 and the upper end 18 of gate 10.
Screw flighting 122 includes pressure housing feed flight 125 which is located within intake hopper 152 immediately adjacent the free end 130 of screw tube 128 which is located upstream from entrance 51 to screen housing 54. The downstream end 129 of pressure housing feed flight 125 terminates at the free end 128 of screw tube 130.
intake hopper 152 receives commodity which is intended to be compressed, including fibrous commodity to be fed to screw 120. The pitch of pressure housing feed flight 125 located within intake hopper 152, in relationship to the pitch of the final compression flight 126 near outlet 60, governs the compression ratio of the press 150. All flights of screw 120 helically circumnavigate pipe 127 and are fixed in place thereon, typically by welding. Upstream end flight 123 is joined to pressure housing feed flight 125 and the upstream end 131 thereof.
Depending on the nature and condition of the material to be pressed, a preferred approximate compression ratio is determined. For instance, variations in condition of the material may require that the ratio be somewhat altered in order to maximize the separation of liquid content from the material without applying so much compressive force that the solids in the material are forced through the screen housing 54. The preferred embodiment of
The location of bottom end 117 of front wall 114 of shroud member 110 over pressure housing feed flight 125 defines the effective feed area. Covering more of pressure housing feed flight 125 with shroud 110 decreases the compression ratio of press 150.
Therefore, it can be appreciated that variation of the compression ratio of screw press 150 can be controlled by insertion or withdrawal of control rod 14 through downstream end wall 57 and by selective horizontal positioning of shroud member 110.
Referring, now particularly to
it can be observed that shroud member 110 can be moved to any location from its fully retracted position as illustrated in
Shroud member 110 may overlie none of the pressure housing feed flight 125 or as much as approximately thirty percent of the space over pressure housing feed flight 125.
In practice, the volume displacing shroud member 110 will be used to fine tune the compression ratio of screw press 150 to maximize its compression efficiency for any batch of fibrous commodity being compressed. For instance, in the case of some fibrous materials, a nominal compression ratio of 7.5 may be appropriate but for some batches of those materials, that compression ratio may be excessive causing fiber to be extruded through the screen housing 154. In that case dewatering of the materials may be better accomplished if the ratio is reduced by, for instance fifteen to thirty percent. The variable positioning of shroud member 110 permits the compression ratio of a given screw press to be reduced in continuous proportions and not necessarily incrementally.
Referring particularly to
Shroud member 110 includes side grooves 134, 136 on each sidewall 116, 118 which may receive rails 144, 146 which are mounted to each sidewall 153, 155 of intake hopper 152. Suitable bearing elements 142 may be installed on rails 144, 146 or within grooves 134, 136 to facilitate the sliding of the volume displacing shroud member 110 along the rails 144, 146. The location of the volume displacing shroud member 110 within intake hopper 152 may be adjusted by use of a threaded rod 180 having a hand wheel 182 thereon to facilitate its rotation. Threaded rod 180 is attached to shroud member 110 and passes through a nut 184 mounted to downstream end wall 157 so that rotation of threaded rod 180 will effect lateral movement of shroud member 110. Rotation of the hand wheel 182 allows the shroud member 110 to be moved further into intake hopper 152 or alternatively to be backed out of any blockage of the pressure housing feed flight 125.
Referring now particularly to
While the present invention has been particularly shown and described with reference to exemplary embodiments thereof it should be understood by those of ordinary skill in the art that various changes, substitutions and alterations can be made herein without departing from the scope of the invention as defined by appended claims and their equivalents. The invention can be better understood by reference to the following claims. For purpose of claim interpretation, the transitional phrases “including” and “having” are intended to be synonymous with the transitional phrase “comprising”.
This application claims priority under 35 U.S.C. §119 to copending non-provisional application Ser. No. 61/651,831 entitled “Adjustable Compression Screw Press” which was filed May 25, 2012. The disclosure of provisional application 61/651,831 is hereby incorporated its entirety.
Number | Date | Country | |
---|---|---|---|
61651831 | May 2012 | US |