USRE23880E - Extruder - Google Patents
Extruder Download PDFInfo
- Publication number
- USRE23880E USRE23880E US23880DE USRE23880E US RE23880 E USRE23880 E US RE23880E US 23880D E US23880D E US 23880DE US RE23880 E USRE23880 E US RE23880E
- Authority
- US
- United States
- Prior art keywords
- cylinder
- screw
- extruder
- control means
- feed screw
- 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
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/68—Barrels or cylinders
- B29C48/685—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads
- B29C48/686—Barrels or cylinders characterised by their inner surfaces, e.g. having grooves, projections or threads having grooves or cavities
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
- B29B7/428—Parts or accessories, e.g. casings, feeding or discharging means
- B29B7/429—Screws
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/58—Component parts, details or accessories; Auxiliary operations
- B29B7/72—Measuring, controlling or regulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/82—Heating or cooling
- B29B7/826—Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/80—Component parts, details or accessories; Auxiliary operations
- B29B7/84—Venting or degassing ; Removing liquids, e.g. by evaporating components
- B29B7/845—Venting, degassing or removing evaporated components in devices with rotary stirrers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/03—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/52—Screws with an outer diameter varying along the longitudinal axis, e.g. for obtaining different thread clearance
- B29C48/525—Conical screws
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/56—Screws having grooves or cavities other than the thread or the channel
Definitions
- the present invention while relating generally as indicated to an extruder, is more particularly concerned with certain improvements in a screwtype extruder for thermoplastic and like material which render the same more emcient in operation to produce a superior extruded product, and which in some instances render possible the extrusion of materials with which difficulty has been heretofore experienced.
- Screw-type extruders of the type currently in use are usually provided with a strainer or breaker plate assembly between the extrusion end of the feed screw and the die to hold back unplasticized particles of material as well as other foreign matter, such ⁇ plate also functioning to build up back pressure on the material to promote frictional heating, mixing, and smearing of the material.
- a strainer or breaker plate assembly between the extrusion end of the feed screw and the die to hold back unplasticized particles of material as well as other foreign matter, such ⁇ plate also functioning to build up back pressure on the material to promote frictional heating, mixing, and smearing of the material.
- One object of this invention is to provide an extruder in which, contrary to the prior extruders aforesaid, the required back pressure on the material is built up in the early stages of the extruding process to effect a more eflicient heating, mixing, and smearing of the material.
- Another object of this invention is to provide an extruder which has novel means therein for effecting de-volatilization of the material and removal of trapped air bubbles therefrom during the course of the travel of the material through the extruder.
- Another object of this invention is to provide an extruder in which there is included a narrow annular orifice defined between relatively rotating parts of the extruder and disposed ahead of the extrusion die orifice, the material which is forced through such annular orifice being sub- Jected to a grinding or smearing action to thereby effect a uniform and thorough dispersion or blending of the material.
- Another object of this invention is to provide an extruder in which the aforesaid annular 2 orifice is adjustable to enable variation of the grinding action in accordance with the properties of the material being extruded.
- Another object of this invention is to provide an extruder which has therein a tempering or low pressure zone through which the devolatilized material passes prior to extrusion to transform the material to an ideal condition for extrusion and to relieve the pulsation or uneven flow of the material as is occasionally encountered in prior art extruders wherein there is choking of the material at the extrusion end and sudden releasing of the pressure on the material just prior to the point of extrusion.
- Fig. l is a cross-section view of one embodiment of this invention.
- Fig. 2 is a cross-section view of a modification
- Fig. 3 is a fragmentary cross-section view of another modification.
- the extruder illustrated therein comprises a base I adapted to mount a suitable drive motor and speed reduction gearing therein (not shown). Journalled in said base and extending rearwardly therebeyond is a drive quill 2 which has a drive gear 3 keyed thereonto adapted to mesh with the motor drive gearing aforesaid.
- a cylinder assembly I Coaxial with said quill is a cylinder assembly I comprising for example a cylinder bushing 5 fixed within said base and which is preferably, though not necessarily, formed with an internally ribbed or threaded bore E, the threads thereof preferably being inclined in the same general direction as the feeding ribs of the feed screw to be described hereafter.
- Said cylinder bushing 5 is formed with a lateral feed opening 1 adjacent its rear end which communicates with an opening 8 in said base, through which openings thermoplastic or like material in pellet,
- granular. powder or chip form is adapted to be introduced into said cylinder bushing.
- a cylinder extension 9 coaxial with cylinder bushing 5.
- Said extension is provided with a vent III adjacent one end and has secured at the other end a suitable extrusion die I I.
- Said cylinder extension 9 is preferably formed with a smooth wall bore I2 therethrough.
- valve ring Il Clamped between said cylinder bushing 5 and said cylinder extension 9 is a valve ring Il which is formed with a tapered bore I4V therethrough smoothly joining the bores B and I2 of said bushing and extension.
- a feed screw I5 Within said cylinder extension 9 and cylinder bushing yIi and extending through said quill I also rearwardly beyond said base I is a feed screw I5.
- Said feed screw is formed with an extension Il vin cylinder extension D which has a helical feeding rib I1 thereon, said extension being of slight taper as shown so as to be slightly larger at the die end thereof whereby to define an annular space Il with bore I2 in said cylinder extension which may for certain materials gradually decrease in cross-sectional area in accordance with the reduction in the buik of the material as it is advanced through said cylinder extension Iby said feeding rib I1.
- a tapered plug valve portion Is Adjacent the small end of said extension i8 is a tapered plug valve portion Is disposed within the tapered bore I4 of said valve ring Il and as will hereinafter appear sa-id valve ring Il and tav pered plug portion I9 constitute a valve assembly which upon axial adjustment of feed screw Il provides an adjustable annular orifice Ill to control the rate of ilow of material through the apparatus.
- Said feed screw is further provided with a main body portion 2
- Said feed screw Il is slidably keyed as at Il to said quill l whereby driving of said quill through gear 3 will effect rotation of said feed screw.
- a conduit Il which is threaded into said feed screw whereby the latter may be of hollow construction and a suitable coolant circulated therethrough to prevent excessive transmission of heat thereto such as would interfere with the feeding action.
- the thrust block 2i is provided with a handle 2
- suitable temperature control zones will be provided. as for example a cooling zone which herein is shown as comprising a chamber Il disposed around the feed openings 1 and 8 through which s. suitable temperature modifying medium is adapted to be circulated to prevent the material introduced into the cylinder bushing II from becoming "tacky" and sticking to said feed screw and with separate heating zones provided as by the electric heating units II and I! which during the initial period of operation of the extruder, supply heat to the plasticized material disposed around said feed screw and which during later periods of operation after the apparatus has reached operating temperature are shut oil'.
- passages Il for circulation of temperature modifying medium to dissipate excess frictional heat which is generated by the working of the material by the screw. Bald cylinder extension 8 and die I I may be provided with similar temperature modifying devices. viz. units 32 and passages il.
- said feed screw Il is adjusted longitudinally within cylinder extension a and cylinder bushing I by means of nut I4 so as to desirably adjust the annular orifice 2l between the tapered surfaces of the plug portion I 9 and the tapered bore Il.
- Ihe restriction to free flow provided at this point effects the necessary build-up of back pressure on the material in the cylinder bushing and because of the relative rotation of said feed screw Il in said valve ring Il there is effected a screening. homogenizing, and a iinal plasticization of the material by the smearing action of the closely spaced tapered surfaces.
- the material now in a thoroughly plasticized and homogenized condition enters cylinder extension I but at a much reduced pressure whereby the volatile ingredients and trapped air and gas bubbles in the material are vented through the vent opening I0 from the very thin tubular stream cf material which issues from the aforesaid annular orifice III.
- Said thin stream of material fills the annular chamber Il between said cylinder extension bore Il and extension IB and said feeding rib I1 on said extension advances the material toward die II. Because of the relatively large cross-section of such annular chamber IB and the relatively smaller pitch of the helical rib I1, the material is advanced rather slowly.
- the annular body of material thus advanced slowly and at desired pressure becomes slightly thinner toward die II in order to compensate for the reduction in the bulk thereof and thus maintains a uniform rate of flow.
- the plasticized material after flowing through this so-cailed "tempering" zone finally enters and nils the chamber adjacent die Il and then is extruded at a uniform pressure through said die.
- the cylinder assembly 34 is of integral form. and the tapered bore 35 between the temperaturecontrol zone 36 and tempering zone 31 cooperates with the tapered portion 38 of feed screw 39 to control the rate of flo-w of material therethrough and thus to control the :back pressure build-up in the zone 35 and along the main portion 40 of said feed screw.
- and said feed screw 39 are provided with tapered bore and tapered extension portions 42 and 43 respectively which are spaced further apart than the tapered portions 35 and 38 which constitute the flow control valve so that the pressure buildup is in the zone 36 where desired rather than in the tempering zone 31 between the vent 44 and die 4I.
- helical ribs 6 in the cylinder bushing which as previously indicated may be included or not, as described, are preferably inclined in the same general direction as the feeding rib 22 of feed screw I5 whereby to induce a counterflow of the material which creates turbulence and thus facilitates more thorough blending o-r mixing and working of the material.
- Such counterilow improves the mixing and blending characteristics of the extruder so that the material as it emerges from the flow control valve orifice 20 is in a thoroughly plasticized and worked condition ready for tempering and elimination of bubbles :by passage at low pressure through the cylinder extension 9.
- the modification illustrated in Fig. 2 may also be formed with an internally threaded or ribbed bore 45 to cooperate with the feed screw as Just indicated.
- the tapered plug valve portion I9 in Fig. 1 or the corresponding portion 39 in Fig. 2 may, if desired, be provided with a helical rib 46 of opposite inclination to the feeding rib 22 on screw I5 (or the rib on screw 39 in Fig. 2).
- rib 46 creates additional mixing action at the control valve due to grinding or smearing action and counterilow action t-hereat to supplement or supplant similar action along the preceding portion of the screw.
- Fig. 3 is shown a modification in which the cylinder bushing 41 is formed with a smooth bore 48 therethrough as distinguished from the bushing 5 in Fig. 1 which has a threaded bore 6 therethrough.
- the counterflo-w action of the material may be entirely dispensed with when extruding certain materials or it may be found that by providing the ribs 46 on the valve portion sufficient counterflow action is obtained so as not to require the threaded or ribbed bore 6.
- An extruder comprising a cylinder having a feed opening at one end for the introduction of Cil material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means, said flow control means comprising opposed tapered surfaces on said screw and in said cylinder, said cylinder and said screw, in advance of said flow control means, being of smaller diameter than beyond said flow contro-l means and such tapered surfaces joining the large and small diameter portions of said cylinder and screw respectively.
- An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said sere-w impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means, said flow control means comprising opposed surfaces on said screw and in said cylinder which are movable toward and away from each other to vary the size of the passageway therebetween upon relative axial adjustment of said cylinder and screw, and means for adjusting said cylinder and screw axially with respect to each other.
- An extruder comprising a cylinder which includes a feed opening at one end for the introduction of material to be extruded from the other end and successive zones along which the material is adapted to be advanced from such feed opening for plasticizing and working while under pressure in one zone and for conditioning for extrusion while under a substantially reduced pressure in the other zone, a feed screw extending through such successive zones and provided with a feeding rib for continuously advancing the material through such zones upon rotation of said screw, and a flow control means between such zones operative to maintain a backpressure on the material in such one zone and to pass the material at a lower pressure to such other zone, said iiow control means comprising axially spaced .and opposed surfaces on said feed screw and in said cylinder respectively, defining a passageway therebetween for flow of material from one zone to the other zone, said screw being mounted for axial adjustment in said cylinder whereby to vary the spacing between such opposed surfaces and thus to vary the size of the passageway, and means for locking said screw in desired axially adjusted position in said cylinder.
- An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means.
- said ow control means comprising opposed surfaces on said screw and in said cylinder defining a passageway therebetween of cross-sectional area less than that between adjacent portions of said screw and cylinder, said feed screw being formed with a rib along its passageway defining surface inducing counterflow of material for intimate mixing and blending of the material prior toand during now through said ilow control means] 5.
- An extruder comprising a cylinder having a feed opening at one end for the introduction oi material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and ilow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said now control means.
- said now control means comprising opposed tapered surfaces on said screw and in said cylinder.
- An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, ilow control means in the intermediate portion of said extruder providing a passageway which impedes free ilow of material and thereby builds up a back pressure on the material in advance of said now control means, and means for varying the flow area of such passageway including passageway-defining surfaces relatively movable closer to and further from each other whereby the ilow area of such passageway may be varied to predeterminedly impede free ilow oi material therethrough in accordance with the characteristics of the material being extruded] [7.
- An extruder according to claim 8 characterized further in that vent means are provided in the intermediate portion o! said -extruder toilowing said flow control means for discharge o1 volatile ingredients and trapped gas bubbles in the material prior to extrusion of the material from the other end of said cylinder.
- An extruder according to claim 2 character- 8 ized further in that a rib is formed on at least one oi said opposed surfaces disposed to induce counteriiow of material for intimate mixing and blending of the material prior to and during now through said ilow control means.
- An extruder comprising a cylinder, a feed screw rotatable in said cylinder, and now control means in an intermediate portion of said extruder effeta to impede free flow of the material being extruded along said cylinder and screw and thereby to build up a back pressure on the material in advance of said flow control means, said flow control means comprising axially spaced and relatively axially movable surfaces on said screw and in said cylinder defining a completely annular passageway of cross-sectional area less than that between adjacent portions of said screw and cylinder, said feed screw being formed with a rib along its annular passageway defining surface egective to induce counterfiow a! the material ,for intimate blending and mixing thereof prior to and during ,flow through said flow control means.
- An extruder comprising a cylinder, a feed screw rotatable in said cylinder, flow control means in an intermediate portion of said extruder eective to impede free flow of the material being extruded along said cylinder and screw and thereby to build up a back pressure on the material in advance o! said flow control means, said flow control means comprising complementary axially spaced annular portions on said screw and in said cylinder respectively defining a flow control passageway therebetween, and means for adiustably varying the axial spacing between said annular portions to thereby vary the flow area of such passageway so as to predeterminedly impede free )low of material in accordance with the characteristics thereof.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
Description
Sept. 28, 1954 a I N mm n mm 9 mm N e M 1E. t ...A l Q M 6 \\\\\\\\m\\\ u Y a B wm mv mm n .S A .HHHJ m. 1 n on n :n N m om 9 Hm l N m- .T f Q A Tf: n .n
Reissued Sept. 28, 1954 UNITED STATES PATENT OFFICE EXTRUDER Eugene E. Heston, Akron,
tional Rubber Machinery Company,
Ohio, assigner to Na- Akron,
Ohio, a corporation of Ohio Original No. 2,595,455, dated May 6, 1952, Serial No. 148,235, March 7, 1950. Application for reissue February 8, 1954, Serial No. 409,014
Matter enclosed in heavy brackets appears in the original patent but forms no part of this reissue specification; matter printed in italics indicates the additions made by reissue.
8 Claims.
The present invention, while relating generally as indicated to an extruder, is more particularly concerned with certain improvements in a screwtype extruder for thermoplastic and like material which render the same more emcient in operation to produce a superior extruded product, and which in some instances render possible the extrusion of materials with which difficulty has been heretofore experienced.
Screw-type extruders of the type currently in use are usually provided with a strainer or breaker plate assembly between the extrusion end of the feed screw and the die to hold back unplasticized particles of material as well as other foreign matter, such \plate also functioning to build up back pressure on the material to promote frictional heating, mixing, and smearing of the material. It has also been proposed heretofore in the extrusion of certain materials such as vinylidene chloride, for example, to omit the strainer plate assembly and in lieu thereof to mount the feed screw for longitudinal ad- Justment in the cylinder and to form the screw with a tapered end portion for cooperation with a conical bore located adjacent to the die orifice and in this way to effect a desired control of the rate of flow of material. As in the other example, there is created an increased back pressure on the material which surrounds the screw. An extruder of the last-mentioned type is disclosed in the Allen L. Heston Patent No. 2,449,652, dated September 2l, 1948.
One object of this invention is to provide an extruder in which, contrary to the prior extruders aforesaid, the required back pressure on the material is built up in the early stages of the extruding process to effect a more eflicient heating, mixing, and smearing of the material.
Another object of this invention is to provide an extruder which has novel means therein for effecting de-volatilization of the material and removal of trapped air bubbles therefrom during the course of the travel of the material through the extruder.
Another object of this invention is to provide an extruder in which there is included a narrow annular orifice defined between relatively rotating parts of the extruder and disposed ahead of the extrusion die orifice, the material which is forced through such annular orifice being sub- Jected to a grinding or smearing action to thereby effect a uniform and thorough dispersion or blending of the material.
Another object of this invention is to provide an extruder in which the aforesaid annular 2 orifice is adjustable to enable variation of the grinding action in accordance with the properties of the material being extruded.
Another object of this invention is to provide an extruder which has therein a tempering or low pressure zone through which the devolatilized material passes prior to extrusion to transform the material to an ideal condition for extrusion and to relieve the pulsation or uneven flow of the material as is occasionally encountered in prior art extruders wherein there is choking of the material at the extrusion end and sudden releasing of the pressure on the material just prior to the point of extrusion.
Other objects and advantages of the present invention will become apparent as the following description proceeds.
To the accomplishment of the foregoing and related ends, said invention, then, comprises the features hereinafter fully described and particularly pointed out in the claims, the following description and the annexed drawing setting forth in detail certain illustrative embodiments of the invention, these being indicative, however,
of but a few of the various ways in which the principle of the invention may be employed.
In said annexed drawing:
Fig. l is a cross-section view of one embodiment of this invention;
Fig. 2 is a cross-section view of a modification; and
Fig. 3 is a fragmentary cross-section view of another modification.
Referring now to the drawing and first to the form of the invention illustrated in Fig. 1, the extruder illustrated therein comprises a base I adapted to mount a suitable drive motor and speed reduction gearing therein (not shown). Journalled in said base and extending rearwardly therebeyond is a drive quill 2 which has a drive gear 3 keyed thereonto adapted to mesh with the motor drive gearing aforesaid.
Coaxial with said quill is a cylinder assembly I comprising for example a cylinder bushing 5 fixed within said base and which is preferably, though not necessarily, formed with an internally ribbed or threaded bore E, the threads thereof preferably being inclined in the same general direction as the feeding ribs of the feed screw to be described hereafter. Said cylinder bushing 5 is formed with a lateral feed opening 1 adjacent its rear end which communicates with an opening 8 in said base, through which openings thermoplastic or like material in pellet,
granular. powder or chip form is adapted to be introduced into said cylinder bushing.
Secured to said base and extending forwardly therefrom is a cylinder extension 9 coaxial with cylinder bushing 5. Said extension is provided with a vent III adjacent one end and has secured at the other end a suitable extrusion die I I. Said cylinder extension 9 is preferably formed with a smooth wall bore I2 therethrough.
Clamped between said cylinder bushing 5 and said cylinder extension 9 is a valve ring Il which is formed with a tapered bore I4V therethrough smoothly joining the bores B and I2 of said bushing and extension.
Within said cylinder extension 9 and cylinder bushing yIi and extending through said quill I also rearwardly beyond said base I is a feed screw I5. Said feed screw is formed with an extension Il vin cylinder extension D which has a helical feeding rib I1 thereon, said extension being of slight taper as shown so as to be slightly larger at the die end thereof whereby to define an annular space Il with bore I2 in said cylinder extension which may for certain materials gradually decrease in cross-sectional area in accordance with the reduction in the buik of the material as it is advanced through said cylinder extension Iby said feeding rib I1.
Adjacent the small end of said extension i8 is a tapered plug valve portion Is disposed within the tapered bore I4 of said valve ring Il and as will hereinafter appear sa-id valve ring Il and tav pered plug portion I9 constitute a valve assembly which upon axial adjustment of feed screw Il provides an adjustable annular orifice Ill to control the rate of ilow of material through the apparatus. Said feed screw is further provided with a main body portion 2| disposed within cylinder bushing 8, said portion 2| likewise being provided with a helical feeding rib I! thereon adapted to advance material forwardly from the lateral feed openin 1 and I toward die I I.
Said feed screw Il is slidably keyed as at Il to said quill l whereby driving of said quill through gear 3 will effect rotation of said feed screw.
Longitudinal adjustment of said feed screw IB to vary the size of the annular orifice 20 between the tapered plug 'portion Il and the tapered bore Il in said valve ring II is effected in much the same manner as disclosed in theaforesaid Allen L. Heston patent, viz. by means of a nut 24 which is threaded onto the rear end portion of said quill I and which bears against the end of said screw through the intermediary of a thrust block Il fitted into a slot Il in said nut. The rear face of said block Il bears against the rear wall of the slot Il and the front face of which is shaped to embrace the rear end of said feed screw Il. Extending through an opening 21 in the end of said nut 2l is a conduit Il which is threaded into said feed screw whereby the latter may be of hollow construction and a suitable coolant circulated therethrough to prevent excessive transmission of heat thereto such as would interfere with the feeding action. The thrust block 2i is provided with a handle 2| by which said block may be manipulated during assembly and disassembly of the machine. It is to be noted that the thrust of said feed screw Il during operation of the machine is transmitted through said block to the quill. said quill being provided with suitable anti-friction thrust bearings (not shown) to withstand such force.
It is to be understood that suitable temperature control zones will be provided. as for example a cooling zone which herein is shown as comprising a chamber Il disposed around the feed openings 1 and 8 through which s. suitable temperature modifying medium is adapted to be circulated to prevent the material introduced into the cylinder bushing II from becoming "tacky" and sticking to said feed screw and with separate heating zones provided as by the electric heating units II and I! which during the initial period of operation of the extruder, supply heat to the plasticized material disposed around said feed screw and which during later periods of operation after the apparatus has reached operating temperature are shut oil'. In addition to units 3| and 32 there may be provided passages Il for circulation of temperature modifying medium to dissipate excess frictional heat which is generated by the working of the material by the screw. Bald cylinder extension 8 and die I I may be provided with similar temperature modifying devices. viz. units 32 and passages il.
Having thus described one embodiment of the invention reference will now be made to the operation thereof.
Upon rotation of feed screw Il and introduction of material in desired form through lateral feed openings 1 and l. the action of the feeding rib 22 supplemented by -the action of the ribs l in said cylinder bushing l, if provided. will be to effect compressing of the material to increase its heat conductivity and to effect frictional heating, mixing, and smearing of the material, the material thus being worked or churned being at the same time advanced toward said cylinder extension l. It has been discovered that for better results the necessary back pressure on the material should be built up in the very early stages of the process.
In order to obtain such back pressure build-up as well as to secure a screening or straining action, said feed screw Il is adjusted longitudinally within cylinder extension a and cylinder bushing I by means of nut I4 so as to desirably adjust the annular orifice 2l between the tapered surfaces of the plug portion I 9 and the tapered bore Il. Ihe restriction to free flow provided at this point effects the necessary build-up of back pressure on the material in the cylinder bushing and because of the relative rotation of said feed screw Il in said valve ring Il there is effected a screening. homogenizing, and a iinal plasticization of the material by the smearing action of the closely spaced tapered surfaces.
Thereafter, the material now in a thoroughly plasticized and homogenized condition enters cylinder extension I but at a much reduced pressure whereby the volatile ingredients and trapped air and gas bubbles in the material are vented through the vent opening I0 from the very thin tubular stream cf material which issues from the aforesaid annular orifice III. Said thin stream of material fills the annular chamber Il between said cylinder extension bore Il and extension IB and said feeding rib I1 on said extension advances the material toward die II. Because of the relatively large cross-section of such annular chamber IB and the relatively smaller pitch of the helical rib I1, the material is advanced rather slowly. As shown, the annular body of material thus advanced slowly and at desired pressure becomes slightly thinner toward die II in order to compensate for the reduction in the bulk thereof and thus maintains a uniform rate of flow. The plasticized material after flowing through this so-cailed "tempering" zone finally enters and nils the chamber adjacent die Il and then is extruded at a uniform pressure through said die.
In the form of the invention illustrated in Fig. 2, the cylinder assembly 34 is of integral form. and the tapered bore 35 between the temperaturecontrol zone 36 and tempering zone 31 cooperates with the tapered portion 38 of feed screw 39 to control the rate of flo-w of material therethrough and thus to control the :back pressure build-up in the zone 35 and along the main portion 40 of said feed screw. A further difference in the Fig. 2 construction is that the die 4| and said feed screw 39 are provided with tapered bore and tapered extension portions 42 and 43 respectively which are spaced further apart than the tapered portions 35 and 38 which constitute the flow control valve so that the pressure buildup is in the zone 36 where desired rather than in the tempering zone 31 between the vent 44 and die 4I.
With respect to the helical ribs 6 in the cylinder bushing which as previously indicated may be included or not, as described, are preferably inclined in the same general direction as the feeding rib 22 of feed screw I5 whereby to induce a counterflow of the material which creates turbulence and thus facilitates more thorough blending o-r mixing and working of the material. Such counterilow, as indicated, improves the mixing and blending characteristics of the extruder so that the material as it emerges from the flow control valve orifice 20 is in a thoroughly plasticized and worked condition ready for tempering and elimination of bubbles :by passage at low pressure through the cylinder extension 9. The modification illustrated in Fig. 2 may also be formed with an internally threaded or ribbed bore 45 to cooperate with the feed screw as Just indicated.
As a further feature of this invention the tapered plug valve portion I9 in Fig. 1 or the corresponding portion 39 in Fig. 2 may, if desired, be provided with a helical rib 46 of opposite inclination to the feeding rib 22 on screw I5 (or the rib on screw 39 in Fig. 2). Such rib 46 creates additional mixing action at the control valve due to grinding or smearing action and counterilow action t-hereat to supplement or supplant similar action along the preceding portion of the screw.
In Fig. 3 is shown a modification in which the cylinder bushing 41 is formed with a smooth bore 48 therethrough as distinguished from the bushing 5 in Fig. 1 which has a threaded bore 6 therethrough. In such modification, that is the Fig. 3 modification, the counterflo-w action of the material may be entirely dispensed with when extruding certain materials or it may be found that by providing the ribs 46 on the valve portion sufficient counterflow action is obtained so as not to require the threaded or ribbed bore 6. In any event, it is within the contemplation of this invention to only provide feeding ribs on the feed screw without the counterflow action afforded by ribs 6 or 4E.
Other modes of applying the principle of the invention may be employed, change being made as regards the details described, providing the features stated in any of the following claims, or the equivalent of such, be employed.
I therefore particularly point out and distinctly claim as my invention:
1. An extruder comprising a cylinder having a feed opening at one end for the introduction of Cil material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means, said flow control means comprising opposed tapered surfaces on said screw and in said cylinder, said cylinder and said screw, in advance of said flow control means, being of smaller diameter than beyond said flow contro-l means and such tapered surfaces joining the large and small diameter portions of said cylinder and screw respectively.
2. An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said sere-w impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means, said flow control means comprising opposed surfaces on said screw and in said cylinder which are movable toward and away from each other to vary the size of the passageway therebetween upon relative axial adjustment of said cylinder and screw, and means for adjusting said cylinder and screw axially with respect to each other.
3. An extruder comprising a cylinder which includes a feed opening at one end for the introduction of material to be extruded from the other end and successive zones along which the material is adapted to be advanced from such feed opening for plasticizing and working while under pressure in one zone and for conditioning for extrusion while under a substantially reduced pressure in the other zone, a feed screw extending through such successive zones and provided with a feeding rib for continuously advancing the material through such zones upon rotation of said screw, and a flow control means between such zones operative to maintain a backpressure on the material in such one zone and to pass the material at a lower pressure to such other zone, said iiow control means comprising axially spaced .and opposed surfaces on said feed screw and in said cylinder respectively, defining a passageway therebetween for flow of material from one zone to the other zone, said screw being mounted for axial adjustment in said cylinder whereby to vary the spacing between such opposed surfaces and thus to vary the size of the passageway, and means for locking said screw in desired axially adjusted position in said cylinder.
[4. An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and flow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said flow control means. said ow control means comprising opposed surfaces on said screw and in said cylinder defining a passageway therebetween of cross-sectional area less than that between adjacent portions of said screw and cylinder, said feed screw being formed with a rib along its passageway defining surface inducing counterflow of material for intimate mixing and blending of the material prior toand during now through said ilow control means] 5. An extruder comprising a cylinder having a feed opening at one end for the introduction oi material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, and ilow control means between the ends of said screw impeding free flow of material along said cylinder and screw and thereby building up a back pressure on the material in advance of said now control means. said now control means comprising opposed tapered surfaces on said screw and in said cylinder.
[6. An extruder comprising a cylinder having a feed opening at one end for the introduction of material to be extruded from the other end thereof, a feed screw rotatable in said cylinder and adapted when rotated to advance and to condition the material for extrusion, ilow control means in the intermediate portion of said extruder providing a passageway which impedes free ilow of material and thereby builds up a back pressure on the material in advance of said now control means, and means for varying the flow area of such passageway including passageway-defining surfaces relatively movable closer to and further from each other whereby the ilow area of such passageway may be varied to predeterminedly impede free ilow oi material therethrough in accordance with the characteristics of the material being extruded] [7. An extruder according to claim 8 characterized further in that vent means are provided in the intermediate portion o! said -extruder toilowing said flow control means for discharge o1 volatile ingredients and trapped gas bubbles in the material prior to extrusion of the material from the other end of said cylinder.]
8. An extruder according to claim 2 characterized further in that said cylinder in advance of said flow control means is formed with internal helical ribs inclined in a direction. to induce counterlow of material in said cylinder and thereby to eiect intimate blending o! the material prior to advance thereof through said now control means.
9. An extruder according to claim 2 character- 8 ized further in that a rib is formed on at least one oi said opposed surfaces disposed to induce counteriiow of material for intimate mixing and blending of the material prior to and during now through said ilow control means.
10. An extruder comprising a cylinder, a feed screw rotatable in said cylinder, and now control means in an intermediate portion of said extruder efectiva to impede free flow of the material being extruded along said cylinder and screw and thereby to build up a back pressure on the material in advance of said flow control means, said flow control means comprising axially spaced and relatively axially movable surfaces on said screw and in said cylinder defining a completely annular passageway of cross-sectional area less than that between adjacent portions of said screw and cylinder, said feed screw being formed with a rib along its annular passageway defining surface egective to induce counterfiow a! the material ,for intimate blending and mixing thereof prior to and during ,flow through said flow control means.
11. An extruder comprising a cylinder, a feed screw rotatable in said cylinder, flow control means in an intermediate portion of said extruder eective to impede free flow of the material being extruded along said cylinder and screw and thereby to build up a back pressure on the material in advance o! said flow control means, said flow control means comprising complementary axially spaced annular portions on said screw and in said cylinder respectively defining a flow control passageway therebetween, and means for adiustably varying the axial spacing between said annular portions to thereby vary the flow area of such passageway so as to predeterminedly impede free )low of material in accordance with the characteristics thereof.
References Cited in the file of this patent or the-original patent UNITED STATES PATENTS Number Name Date 1,283,947 Steinle Nov. 5, 1918 1.936.050 Gordon Nov. 14, 1933 2.200.997 Royle May 14, 1940 2,449,652 Heston Sept. 2l. 1948 2,496,825 Henning Feb. 7, 1950 2,519,014 Bankey Aug. 15, i950 2,015,199 Fuller Oct. 2B. 1952
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US148235A US2595455A (en) | 1950-03-07 | 1950-03-07 | Extruder |
Publications (1)
Publication Number | Publication Date |
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USRE23880E true USRE23880E (en) | 1954-09-28 |
Family
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Family Applications (2)
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US23880D Expired USRE23880E (en) | 1950-03-07 | Extruder | |
US148235A Expired - Lifetime US2595455A (en) | 1950-03-07 | 1950-03-07 | Extruder |
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US148235A Expired - Lifetime US2595455A (en) | 1950-03-07 | 1950-03-07 | Extruder |
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Cited By (7)
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US3008184A (en) * | 1959-04-10 | 1961-11-14 | Werner & Pfleiderer | Worm press |
US3078824A (en) * | 1960-04-04 | 1963-02-26 | Potdevin Machine Co | Hot melt adhesive extruder |
US3110930A (en) * | 1960-05-27 | 1963-11-19 | Alpine Ag | Apparatus for producing plastic filaments |
US3252182A (en) * | 1963-01-22 | 1966-05-24 | Lavorazione Mat Plast | Screw press for extrusion of plastics |
US3300810A (en) * | 1964-01-29 | 1967-01-31 | Nrm Corp | Extruder |
US6103290A (en) | 1996-07-18 | 2000-08-15 | Wenger Manufacturing, Inc. | Method of extrusion cooking an edible material |
US20100034917A1 (en) * | 2006-04-27 | 2010-02-11 | Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H. | Device For Degassing And Filtering Plastic Melts |
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US2662243A (en) * | 1950-07-07 | 1953-12-15 | Farrel Birmingham Co Inc | Blending and/or warming extrusion device for plastics or the like |
US2719325A (en) * | 1951-12-13 | 1955-10-04 | Hercules Powder Co Ltd | Method and apparatus for mixing plastic compositions |
US2767437A (en) * | 1952-02-11 | 1956-10-23 | Donald E Marshall | Method of amalgamating and extruding soap |
US2752633A (en) * | 1952-05-28 | 1956-07-03 | Western Electric Co | Apparatus for simultaneously advancing and working plastic material |
BE521347A (en) * | 1952-07-12 | 1900-01-01 | ||
BE523705A (en) * | 1952-10-23 | 1900-01-01 | ||
US2765491A (en) * | 1953-05-04 | 1956-10-09 | Nat Rubber Machinery Co | Extrusion apparatus |
DE1187010B (en) * | 1953-07-28 | 1965-02-11 | Horst Heidrich | Process for the processing of injectable masses and screw extruder to carry out this process |
BE535316A (en) * | 1954-07-12 | 1900-01-01 | ||
US2842796A (en) * | 1954-08-31 | 1958-07-15 | Us Rubber Co | Rubber shaping and vulcanizing apparatus |
US2836851A (en) * | 1955-09-09 | 1958-06-03 | Danielson Mfg Company | Apparatus for extrusion |
NL224151A (en) * | 1957-01-22 | 1900-01-01 | ||
DE1095515B (en) * | 1957-06-13 | 1960-12-22 | Battenfeld Geb | Injection molding machine for processing thermoplastics |
US2970341A (en) * | 1957-11-27 | 1961-02-07 | Nat Rubber Machinery Co | Extruder with adjustable choke |
US3001233A (en) * | 1959-01-22 | 1961-09-26 | Ohio Commw Eng Co | Apparatus for plastic injection |
DE1145787B (en) * | 1959-03-10 | 1963-03-21 | Kloeckner Humboldt Deutz Ag | Screw extruder with a damming section, the cross section of which is variable |
BE596143A (en) * | 1959-11-27 | 1900-01-01 | ||
US3233288A (en) * | 1963-03-21 | 1966-02-08 | Pennsalt Chemicals Corp | Molding apparatus |
FR1371923A (en) * | 1963-07-29 | 1964-09-11 | Etablissements Andouart Soc D | Improvements to plastic extruders |
CH420580A (en) * | 1965-02-08 | 1966-09-15 | Buss Ag | Device for degassing plastic masses in screw machines |
DE1502335B2 (en) * | 1965-02-13 | 1971-10-21 | Werner & Pfleiderer, 7000 Stuttgart | SCREW EXTRUSION PRESS FOR THE PROCESSING OF PLASTIC |
US3475787A (en) * | 1968-03-06 | 1969-11-04 | Nrm Corp | Extruder |
US3826477A (en) * | 1971-04-13 | 1974-07-30 | Meiki Seisakusho Kk | Injection molding machine with a venting device |
JPS4982754A (en) * | 1972-12-12 | 1974-08-09 | ||
DE2612827C3 (en) * | 1976-03-26 | 1982-11-18 | Werner & Pfleiderer, 7000 Stuttgart | Screw extruder for the continuous preparation and degassing of elastomers and polymers with a viscosity of more than 1000 d Pa s |
US4075712A (en) * | 1976-08-08 | 1978-02-21 | Paul Geyer | Extrusion and mixing apparatus |
US4107048A (en) * | 1977-02-04 | 1978-08-15 | The Weatherhead Company | Turbulence amplifier baffle |
CH612375A5 (en) * | 1977-03-29 | 1979-07-31 | Maillefer Sa | |
FR2395133A1 (en) * | 1977-06-22 | 1979-01-19 | Geyer Paul | Screw extrusion and mixing appts. - having cooperating grooved barrel and screw, for extrusion of thermoplastic or thermosetting materials |
DE3026842C2 (en) * | 1980-07-16 | 1984-02-16 | Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover | Twin screw venting extruder for thermoplastic materials |
DE3133708C2 (en) * | 1981-08-26 | 1986-07-03 | Semen Il'ič Gdalin | Extruder for processing polymer materials |
US4981364A (en) * | 1988-05-12 | 1991-01-01 | Paul Geyer | Extrusion apparatus |
US6280667B1 (en) | 1999-04-19 | 2001-08-28 | Andersen Corporation | Process for making thermoplastic-biofiber composite materials and articles including a poly(vinylchloride) component |
JP4907366B2 (en) * | 2007-01-26 | 2012-03-28 | 株式会社神戸製鋼所 | Extruder screw, bearing segment used therefor, and twin screw extruder provided with extruder screw |
DE102018130102B4 (en) * | 2018-11-28 | 2022-06-09 | Gneuss Gmbh | Process for processing solid plastic particles from a polycondensate using a multi-rotation system and multi-rotation system therefor |
KR102267692B1 (en) * | 2020-09-02 | 2021-06-22 | 이재호 | Apparatus for manufacturing and this using method of organic and inorganic mixture composition |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US1283947A (en) * | 1915-04-24 | 1918-11-05 | Rubber Regenerating Co | Treatment of materials. |
US1935050A (en) * | 1930-11-29 | 1933-11-14 | Farrel Birmingham Co Inc | Machine for plasticating materials |
US2200997A (en) * | 1937-01-29 | 1940-05-14 | Vernon E Royle | Extruding machine |
US2519014A (en) * | 1946-05-20 | 1950-08-15 | Lucas County Bank | Compounding and molding machine |
US2496625A (en) * | 1946-11-13 | 1950-02-07 | Western Electric Co | Apparatus for advancing and working plastic materials |
-
0
- US US23880D patent/USRE23880E/en not_active Expired
-
1950
- 1950-03-07 US US148235A patent/US2595455A/en not_active Expired - Lifetime
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3008184A (en) * | 1959-04-10 | 1961-11-14 | Werner & Pfleiderer | Worm press |
US3078824A (en) * | 1960-04-04 | 1963-02-26 | Potdevin Machine Co | Hot melt adhesive extruder |
US3110930A (en) * | 1960-05-27 | 1963-11-19 | Alpine Ag | Apparatus for producing plastic filaments |
US3252182A (en) * | 1963-01-22 | 1966-05-24 | Lavorazione Mat Plast | Screw press for extrusion of plastics |
US3300810A (en) * | 1964-01-29 | 1967-01-31 | Nrm Corp | Extruder |
US6103290A (en) | 1996-07-18 | 2000-08-15 | Wenger Manufacturing, Inc. | Method of extrusion cooking an edible material |
US20100034917A1 (en) * | 2006-04-27 | 2010-02-11 | Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H. | Device For Degassing And Filtering Plastic Melts |
US7866876B2 (en) * | 2006-04-27 | 2011-01-11 | Erema Engineering Recycling Maschinen Und Anlagen Gesellschaft M.B.H. | Device for degassing and filtering plastic melts |
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US2595455A (en) | 1952-05-06 |
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