The present invention relates to the filtering of fluids and, in particular, filters for molten polymer and the decompression of equipment downstream from such filters.
Injection molding systems typically include a molding machine, which is a source of molten polymer put under very high pressure, at least one mold including at least one cavity formed therein, and an assembly such as a hot runner assembly which (at the time of molding) joins the two. U.S. Pat. No. Re. 41,280, issued to the Applicant and fully incorporated by reference herein, discloses details of a representative injection molding assembly, in that instance a multiple-nozzle manifold meant to inject molten polymer into multiple cavities in a mold.
Prior to delivering the molten polymer to the mold, it is desirable to filter the molten polymer. Such filters are known in the industry (See, e.g., U.S. Pat. No. 4,434,053 to Osuma-Diaz and U.S. Pat. No. 4,906,360 to the Applicant), and remove contaminants occurring in recycled polymer or “regrind” such as unmelted plastic granules, dirt, and metal shavings or filings which could clog the gates, damage the downstream system components or affect the quality of the molded part. After filtration, the molten polymer passes into the mold. But the interposition of the filter across the stream of pressurized molten polymer causes a pressure drop in the line.
Molten polymer is a compressible fluid. After the completion of a polymer injection into the mold, the mold is allowed to cool. The mold is opened and the molded part removed. If the equipment upstream from the mold (such as the hot runner system) is not depressurized, there is a danger that the gates will blow out and that molten polymer will “drool” out of the mold openings. The conventional way to minimize this “drool” is to have the molding machine draw back, exerting negative pressure in the line, prior to opening the mold. To date this decompression step has been incompatible with the provision of a polymer filter, as the pressure drop across the filter element is too great to allow the polymer downstream from the filter to significantly decompress. Thus injection molders have had to either put up with “drool” or forgo the filter. A need therefore persists for injection apparatus which can filter the molten polymer but which also permits molten polymer decompression after the injection step.
In one aspect of the invention, filtration apparatus (such as a screen pack) for filtering molten polymer comprises a primary inlet, a primary outlet, a filter, and a filtration passage fluidly connecting the primary inlet and the primary outlet through the filter. The apparatus also has a decompression passage that connects the primary inlet and primary outlet and is operable to decompress the equipment downstream from the filter, including the machine nozzle and any hot runner assembly connecting to the mold. A valve is operable between a first position that forces polymer to flow through the preferably two-stage filter along the filtration passage from the primary inlet to the primary outlet, and a second position that permits polymer to flow from the primary outlet to the primary inlet along the decompression path, bypassing the filter and decompressing the downstream equipment.
In a further aspect of the invention, a method of using an injection molding filtration apparatus comprises the major steps of filtering molten polymer and thereafter decompressing the equipment downstream from the filter. The step of filtering includes the substeps of closing a check valve to close a decompression passage which circumvents the filter, and flowing polymer from the primary inlet toward the primary outlet along the filtration passage through the filter. The step of decompressing includes the substeps of opening the check valve to open the decompression passage and flowing polymer from the primary outlet toward the primary inlet through the decompression passage. The polymer downstream of the check valve pushes a second sealing surface of a check valve movable body away from a first sealing surface of the check valve, thereby opening the check valve and bypassing the filter.
Preferably, the valve is a filter check valve that is arranged along an axis. The filter has a cavity formed by a wall with an interior surface that receives unfiltered polymer from the primary inlet. The filter check valve is disposed to be radially inward from the interior surface of the filter wall, A first position of a movable body of the filter check valve is a forward position that is proximate to a filter check valve inlet and a second position thereof is a rear position that is remote from the filter check valve inlet.
More preferably, the apparatus has a decompression duct disposed on a central axis to be radially interior to the inside surface of the wall of the filter element. The forward end has an abutting surface adapted to receive the movable body of the check valve. An internal passage from a forward end of the shaft to a rear end of the shaft acts as the decompression passage, such that the filter check valve is forced closed in the forward position when a polymer flows through the filtration passage from the primary inlet toward the primary outlet and, and is pushed open to the rear position when the polymer flows through the internal passage from the primary outlet toward the primary inlet.
According to another aspect of the invention, injection molding filtration apparatus (such as a screen pack) has a primary inlet, a primary outlet, and a filtration passage in fluid communication with the two. The filtration passage has a preferably two-stage filter and a filter check valve that is open when a molten polymer flows from the primary inlet toward the primary outlet, and is closed when the polymer flows from the primary outlet toward the primary inlet.
In this embodiment, a bypass line is also provided which fluidly connects the primary inlet with the primary outlet. The bypass line has a bypass check valve that is closed when the polymer flows from the primary inlet toward the primary outlet and is open when the polymer flows from the primary outlet toward the primary inlet. Thus, the bypass and filtration check valves act in opposition one another, regardless of the direction of the fluid flow.
According to a further aspect of the invention, a method of using an injection molding apparatus includes the major steps of filtering a polymer and subsequently decompressing the equipment downstream from the filter. The method includes the substeps of closing a bypass check valve to close a bypass line which extends from the primary inlet to the primary outlet and which bypasses the filter. At this time, polymer flows from the primary inlet to the primary outlet through a filtration passage, as permitted by a filter check valve which is then in an open position.
The step of decompressing the downstream equipment includes the substeps of closing the filter check valve, opening the bypass check valve, and flowing the polymer from the primary outlet toward the primary inlet through the bypass line.
The present invention thus permits the filtration of molten polymer prior to its introduction into the machine nozzle, any hot runner assembly and the mold, and also allows the subsequent decompression of the polymer prior to opening the mold.
Further aspects of the invention and their advantages can be discerned in the following detailed description, in which like characters denote like parts and in which:
A filtration apparatus, or filter pack, indicated generally at 100 in
The filtration apparatus 100 has a primary inlet 102 connected to a polymer source 158, such as an injection molding machine. The primary outlet 124 is connected to a filtration passage 126 and a bypass line 116. The filtration passage 126 is fluidly connected between the primary inlet 102 and the primary outlet 124. As discussed herein, when two parts of the apparatus are said to be “fluidly connected,” this means that changes in the pressure and/or direction of the polymer flow in the first part affects the pressure and/or direction of the polymer flow in at least one section of the second part. Thus, by being “fluidly connected,” the physical aspects of the two parts are interrelated in some way. Further, “fluidly connected” is short form for “selectively fluidly connected”, as one or both of the filtration and decompression passages may be interrupted by a valve, depending on which embodiment of the invention is being considered and depending on the present step of the injection molding process.
The filtration passage 126 has a preferably two-stage filter 114 interposed across it and a filter check valve, indicated generally at 104, that is open when polymer flows from the primary inlet 102 toward the primary outlet 124. Correspondingly, the filter check valve 104 is closed when the polymer flows from the primary outlet 124 toward the primary inlet 102.
The bypass line 116 is also fluidly connected between the primary inlet 102 and the primary outlet 124 and has interposed across it a bypass check valve 106. The bypass check valve is closed when the polymer flows from the primary inlet 102 toward the primary outlet 124 and open when the fluid flow is reversed. Thus, the operation of the bypass check valve 106 and the filter check valve 104 ensure that the polymer flows either forward through the filtration passage 126 or backward through the bypass line 116. Polymer does not flow through both at the same time except during a time of transition when the valves are in the process of opening and closing.
Still referring to
The bypass check valve movable body 112 has a second bypass sealing surface 113 that seals with the first bypass sealing surface 130 when the movable body 112 is in the forward position. A bypass check valve outlet 134 provides fluid communication between the bypass valve chamber 128 and the primary inlet 102 through an exit opening 136 in an exit wall 138 of the bypass valve chamber 128. Thus, as polymer flows from the primary inlet 102 toward the primary outlet 124, the bypass check valve movable body 112 moves to the forward position and the second bypass sealing surface 113 mates with the first bypass sealing surface 130, sealing the bypass check valve 106 and closing the bypass line 116. As a result, the polymer is forced through the filtration passage 126 and filter 114. See
The filtration apparatus preferably further includes a heat-conductive band heater 137 which jackets a body 160 of the pack 100. This maintains the polymer flowing through the pack 100 at the correct processing temperature.
The filter check valve 104 is similar in function and structure to the bypass check valve 106 except that it is directionally reversed, i.e., it allows polymer to flow in the opposite direction of the bypass check valve 106. See
Referring to
A filter check valve movable body 146 (such as a sphere) is reciprocally movable within the filter valve chamber 140 between a rear position that is proximate to the entry wall 148 (
The filter check valve movable body 146 has a second filter valve sealing surface 153 that seals with the first filter valve sealing surface 142 when the movable body 146 is in the rear position. A filter check valve outlet 144 provides fluid communication between the filter valve chamber 140 and the primary outlet 124 through an exit opening 150 in an exit wall 152 of the filter valve chamber 140. The filter check valve outlet 144 is in fluid communication with the filter 114.
As above and referring again to
One or more of a plurality of filter check valve passages 210 are spaced from each other by the filter valve ridges 208. As with the bypass valve passages 204, the filter check valve passages 210 allow the polymer to flow between the filter check valve inlet 108 and the filter check valve outlet 144 when the filter check valve movable body 146 is not in the rear position (
The filter 114 is preferably a two-stage filter which has an internal cavity 156 that is formed by at least a portion of an interior surface 155 of a wall 154. The first filter stage is formed by a plurality of holes 120 which are formed in the wall 154. In operation, the polymer flows through the filter check valve 104 when the filter check valve movable body 146 is not in the rear position, into the internal cavity 156, and through the plurality of holes 120. Once the polymer passes through the holes 120, it flows through first stage filter outlet passages 118 that are aligned with but spaced from axis 212 and are circumferentially spaced around the filter. Larger-size particulate contaminants such as dirt, plastic particles, or metal filings are retained in the internal cavity 156 of the filter 114.
At least a portion of the filter check valve 104 is preferably integrated into the filter 114. As shown in
[check numbers] As shown in
Referring to
Referring to
After injection is completed, it is desirable to decompress (314) the molten polymer downstream from the filter pack 100 prior to opening the mold. This is accomplished by actuating the injection molding machine to draw back (315), thereby inducing molten polymer to flow back toward the primary inlet 102. Downstream molten polymer then pushes open (326) the bypass check valve 106 and preferably pushes closed (324) the filter check valve 104. Polymer may then flow (328) through the bypass line 116. Subsequent to decompression (314) the mold may be opened (330).
There is the possibility that the movable body 146 will not seal with wall 148 in the decompression step 314. This depends on the relative values of the pressure drop across the filter and the pressure drop occurring in the bypass line 116. If, as might occur if the filter is clogged, there is a much larger pressure drop across it than will be experienced through the bypass line 116, the polymer will largely flow through bypass line 116 rather than across the filter, and the movable body 146 may not be displaced enough or at all to seal with wall 148.
Referring to
Preferably, the filter 703 is cylindrical and arranged along an axis 501 and has a wall 704 with an interior surface 505 (see also
More preferably, the pack 500 has a decompression duct 516 disposed on the axis 501 to be radially inward of the interior surface 505 of the wall 704 of the filter 703. A forward end 520 of the duct 516 has an abutting surface 608 (see
Even more preferably, the duct 516 has the abutting surface 608 in the forward end and an internal passage 518 from a forward end 520 of the duct 516 to a rear end 522 of the duct. At least a portion of the duct 516 is axially radially inward from the interior surface 505 of the filter 703. The internal passage 518 defined by duct 516 acts as the main component of the decompression passage 506. Thus, the filter check valve 508 closes, with ball 510 in the forward position, when a polymer flows from the primary inlet 102 toward the primary outlet 124 down passage 518, and opens, with ball 510 in the rear position, when the polymer flows from the primary outlet 124 toward the primary inlet 102.
A first check valve sealing surface 524 of an entry wall 526 surrounds the check valve inlet 514 and a second sealing surface 528 of the filter check valve movable body 510 is sealable with the first check valve sealing surface 524 when the movable body 510 is in the forward position.
The filter pack 500 has a technical advantage in that its structure includes only one movable body or ball 510 rather than two, saving manufacturing and maintenance costs. The filter pack 500 is also more compact than the previously described embodiment in that no separate bypass line has to be provided for.
In a preferred embodiment and referring to
A method of using the injection molding apparatus 500, indicated generally at (1000) in
Preliminarily the mold is closed (1001) and equipment such as a sprue bar assembly is connected to it. At step 1002 an injection molding machine introduces molten polymer at high pressure to the primary inlet 102, flowing (1006) polymer from the primary inlet 102 toward the primary outlet 124 through the filter 114, and closing (1008) a check valve 508 to close a decompression passage which otherwise would circumvent the filter 502.
In the decompression phase 1010, the injection molding machine draws polymer back (1011) from the primary inlet 102. Downstream molten polymer will then push (1016) the filter check valve 508 open, opening the decompression passage 506. Polymer then flows (1020) through the decompression passage 506. The substep of pushing (1016) involves displacing a second sealing surface 528 of the check valve movable body 510 away from the first sealing surface 524 of the check valve 508, with the aid of polymer downstream of the check valve 508. This opens the check valve 508 and bypasses the filter 703. Polymer then flows (1020) through the decompression passage 506, decompressing the equipment downstream from the filter pack 500. After decompression (1010) the mold may be opened (1022).
In summary, the described apparatus and method permit molten polymer to be filtered and also allows the equipment downstream from the filter pack to be decompressed, thereby eliminating or reducing the amount of “drool” which would otherwise occur. While illustrated embodiments of the present invention have been described and illustrated in the appended drawings, the present invention is not limited thereto but only by the scope and spirit of the appended claims.