X-rheometer mixer and its use

Abstract

The application discloses an X rheological mixing device and application thereof in an injection molding machine, and belongs to the technical field of injection molding machines.The X rheological mixing device is a mixing device for an injection nozzle of an injection molding machine or a discharging mixing adapter device of an extruder, and comprises a mixing cylinder and an integrated X rheological mixing valve core arranged in the mixing cylinder, wherein the integrated X rheological mixing valve core comprises a circular ring type end portion, at least one X type valve core rheological portion and a V type rheological end portion which are integrally formed from a proximal end to a distal end, and the integrated X rheological mixing valve core has an overall structure of an alternating distribution structure of a combined cross X type middle quadrilateral large hole and an outer circle V type; and a plurality of small holes are uniformly distributed on the inclined surfaces of the X type valve core rheological portion and the V type rheological end portion.The X rheological mixing device solves the problems of easy misalignment between contact surfaces of multiple valve cores, generation of black spots, black lines and yellow lines due to hidden glue, easy deformation and cracking of split valve cores, has better use effect, is simpler to process and has a wide application range.

Description

TECHNICAL FIELD

[0001] The present application relates to a mixing device, in particular to an X rheological mixing device and its application in injection molding machines and extruders. BACKGROUND

[0002] Nowadays, the types of plastics in the injection molding industry are constantly updated, the performance is constantly improved, and the plastic additives are constantly changing and increasing, making it more and more difficult to improve product quality by relying entirely on injection molding process or screw design. One of the most difficult problems to solve is uneven mixing of products and poor plasticization. Moreover, the overall plastic raw material price is rising, and the proportion of many enterprises using recycled materials is increasing. However, foreign objects such as iron filings inevitably enter the recycled materials during use, causing blockage in the hot runner of the mold during production, causing unnecessary losses and a large amount of downtime for maintenance and waiting time for customers. The methods used to solve the above two problems in the market are to increase the device for filtering iron filings and to increase the mixing effect device. Both can only solve a single technical problem, causing great distress to injection molding machine manufacturers and end users.

[0003] To solve the above two technical problems, the applicant has previously developed a filtering mixing nozzle disclosed in patent CN110091469A, which includes a rheological valve core head and at least one prismatic rheological valve core assembled together. By the double flow change of the prismatic rheological valve core and the rheological valve core head, the melted plastic can be guided, cross-fused, and compressed to guide the flow in the through hole of the sub-nozzle and the flange connector. The continuous flow guidance not only compensates for the incomplete fusion and color unevenness of the plastic in the screw pipe.

[0004] However, in actual application, it is found that the filtering mixing nozzle disclosed in patent CN110091469A has another problem after solving the above two problems, that is, the valve core in the nozzle is prone to carbon deposition and produces some black spots, which inevitably increases the product failure rate. The solution of coating a coating on the surface of the valve core cannot effectively improve the product pass rate.

[0005] Therefore, how to solve the problem of carbon deposition and black spot generation in the valve core of the existing mixing device after long-term use has become another big technical problem for technicians in the field to solve. SUMMARY

[0006] The technical problem to be solved by the present application is that the existing mixing device is prone to carbon deposition and black spot generation in the valve core after long-term use. An X rheological mixing device and its application in injection molding machines and extruders are proposed.

[0007] To achieve the above purpose, the present application adopts the following technical scheme:

[0008] The first aspect of the present application provides an X rheological mixer, comprising a mixing cylinder and an integrated X rheological valve core arranged in the mixing cylinder, wherein:

[0009] The integrated X rheological valve core comprises a circular ring type end portion, at least one X type valve core rheological portion and a V type rheological end portion integrally formed from the proximal end to the distal end, which are alternately distributed in the structure of the middle quadrilateral large hole combined cross X type and outer circle V type;

[0010] And a plurality of small holes are uniformly distributed on the inclined surface of the X type valve core rheological portion and the V type rheological end portion.

[0011] Further, in the X rheological mixer, the outer circle diameter of the integrated X rheological valve core is 10-600 mm, and the thickness of the X type column is 1-50 mm.

[0012] Further, in the X rheological mixer, the aperture of the small hole is 0.5-20 mm, and the depth is 1-50 mm.

[0013] Further, in the X rheological mixer, the number of small holes on a single inclined surface of the X type valve core rheological portion is 1-200.

[0014] Further, in the X rheological mixer, the number of X type valve core rheological portions is 1-100.

[0015] Further, in the X rheological mixer, the included angle of the quadrilateral formed on the left and right sides of the X type valve core rheological portion is 5-150°, and the included angle of the V type formed on the upper and lower sides is 5-150°.

[0016] Further preferably, in the X rheological mixer, the quadrilateral large hole is a shape of a harp, or a rhombus, or a square.

[0017] Further, in the X rheological mixer, the side end face of the circular ring type end portion is a ring type inclined surface.

[0018] The second aspect of the present application provides an X rheological mixer, which is an injection nozzle mixer of an injection machine, comprising a sub-nozzle, a flange connecting body and an integrated X rheological valve core as described above, wherein:

[0019] The integrated X rheological valve core is arranged in the through hole between the sub-nozzle and the flange connecting body, and the side end face of the circular ring type end portion is in close contact with the inner hole wall of the sub-nozzle.

[0020] Further, in the X rheological mixer, the inner hole wall of the sub-nozzle is provided with a nozzle inclined surface, and the nozzle inclined surface is in inclined surface contact with the ring type inclined surface of the side end face of the circular ring type end portion.

[0021] The third aspect of the present application is to provide an X rheological mixer, which is an extruder discharge mixing adapter device, comprising an adapter die and an integrated X rheological mixing valve core as described above, wherein:

[0022] The integrated X rheological mixing valve core is arranged in the through hole of the adapter die, and the annular end surface of the annular end portion is in close contact with the inner hole wall of the adapter die.

[0023] Further, on the X rheological mixer, the inner hole wall of the adapter die is provided with an adapter inclined surface, which is in inclined surface contact with the annular inclined surface of the annular end surface.

[0024] The fourth aspect of the present application is to provide an application of the injection nozzle mixer of the injection molding machine or the extruder discharge mixing adapter device as described above in the mixing of liquid silicone, chemical agents, flow paste, fluid food and beverage, fluid food and medicine.

[0025] The present application adopts the above technical scheme, compared with the prior art, has the following technical effects:

[0026] (1) better use effect: compared with the split valve core, the valve core is designed as an integrated type, which completely solves the problem of easy misalignment between the contact surfaces of multiple valve cores and the generation of black spots, black lines and yellow lines, and also solves the problem of easy deformation and cracking of the split valve core;

[0027] (2) convenient maintenance and replacement: since an integrated filter mixing valve core is used, it can be installed and removed at will, which is convenient, fast, time-saving and labor-saving;

[0028] (3) simpler processing: compared with the split structure of the valve core head and the prismatic rheological valve core, the integrated filter mixing valve core can save multiple surface processing procedures, improve processing efficiency and reduce production cost;

[0029] (4) wide application range: the integrated filter mixing valve core is designed according to the size of the injection rate of the machine, and is used on the injection nozzle mixer of the injection molding machine or the extruder discharge mixing adapter device, to realize the mixing function of any flowable material. BRIEF DESCRIPTION OF DRAWINGS

[0030] Figure 1 is a structural schematic view of the integrated X rheological mixing valve core in the X rheological mixer of the present application;

[0031] Figure 2 is a structural schematic view of the integrated X rheological mixing valve core in the X rheological mixer of the present application;

[0032] Figure 3This is a schematic diagram of the sub-nozzle structure in the injection nozzle mixer of the injection machine of the present invention;

[0033] Figure 4 This is a schematic diagram of the flange connection body in the injection nozzle mixer of the injection machine of the present invention;

[0034] Figure 5 This is a schematic diagram of the overall structure of the X rheological mixer of the present invention as an extruder discharge mixing adapter device;

[0035] Figure 6 This is a schematic diagram of the structure of the adapter die in the extruder discharge mixing adapter device of the present invention;

[0036] The accompanying figures are labeled as follows:

[0037] 100-Integrated X-type rheological mixing valve core, 101-Annular end, 102-X-type valve core rheological section, 103-V-type rheological end, 104-Small hole, 105-Annular bevel; 200-Sub-nozzle, 201-Nozzle bevel; 300-Flange connector; 400-Transfer die head, 401-Transfer bevel. Detailed Implementation

[0038] The present invention will now be described in detail and specifically through specific embodiments to enable a better understanding of the invention. However, the following embodiments do not limit the scope of the invention.

[0039] Example 1

[0040] Please see Figure 1 As shown, this embodiment provides an X-rheology mixer for mixing flowable substances such as liquid silicone, chemical agents, flowable pastes, fluid beverages, fluid substances, or pharmaceutical solutions. The X-rheology mixer includes a mixing cylinder and an integrated X-rheology mixing valve core 100 disposed within the mixing cylinder. The mixing cylinder can be any mounting cylinder with mixing functions, such as an injection nozzle for an injection molding machine, or a mixing adapter for an extruder discharge.

[0041] As a preferred technical solution in this embodiment, please refer to Figure 1As shown, the integrated X rheological mixing valve core 100 can be made of a metal round bar as a raw material and integrally processed, or integrally cast into shape, which includes a circular ring type end portion 101, at least one X type valve core rheological portion 102 and a V type rheological end portion 103 integrally formed from the proximal end to the distal end, and the overall is an alternating distribution structure of a combined cross X type of a middle quadrilateral large hole and an outer circle V type. The cross-sectional shape of the circular ring type end portion 101, the X type valve core rheological portion 102 and the V type rheological end portion 103 are all circular with the same diameter, that is, the end portion of at least one X type valve core rheological portion 102 of the X type cylinder structure is connected with the end portion of the V type rheological end portion 103 to form a quadrilateral large hole shape with two sides through, and a continuous V type groove is formed between the upper and lower two side ends. And the X type valve core rheological portion 102 and the V type rheological end portion 103 are uniformly distributed with a plurality of small holes 104 for mixing the rheological material. By using the integrated X rheological mixing valve core 100 with the special structure design, compared with the existing split type mixing valve core, the problem of easy misalignment of multiple valve core contact surfaces and black spots, black lines and yellow lines caused by hidden glue is solved, and the problem of easy deformation and cracking of the split valve core is also solved.

[0042] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, according to the production needs, the outer circle diameter of the integrated X rheological mixing valve core 100 is 10-600mm, and the thickness of the X type cylinder is 1-50mm; preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 20-500mm, and the thickness of the X type cylinder is 5-45mm; more preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 20-100mm, and the thickness of the X type cylinder is 4-10mm; more preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 26-50mm, and the thickness of the X type cylinder is 4-6mm.

[0043] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, the hole diameter of the small hole 104 is 0.5-20mm, and the depth is 1-50mm; preferably, the hole diameter of the small hole 104 is 1-5mm, and the depth is 4-20mm; more preferably, the hole diameter of the small hole 104 is 1-4mm, and the depth is 4-10mm; more preferably, the hole diameter of the small hole 104 is 1-3mm, and the depth is 4-6mm.

[0044] As a preferred technical solution of the embodiment, please refer to Figure 1As shown, the number of small holes on the single inclined surface of the X-shaped valve core rheological part varies from 1 to 200 according to the size of the plane area and the reasonable stress distribution; preferably, the number of small holes on the single inclined surface of the X-shaped valve core rheological part is 5-180; more preferably, the number of small holes on the single inclined surface of the X-shaped valve core rheological part is 8-160; more preferably, the number of small holes on the single inclined surface of the X-shaped valve core rheological part is 15-150; more preferably, the number of small holes on the single inclined surface of the X-shaped valve core rheological part is 25-120.

[0045] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, the number of X-shaped valve core rheological parts 102 is 1-100 integrally formed; preferably, the number of X-shaped valve core rheological parts 102 is 3-90; more preferably, the number of X-shaped valve core rheological parts 102 is 4-80; more preferably, the number of X-shaped valve core rheological parts 102 is 5-10.

[0046] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, the included angle of the quadrilateral formed on the left and right sides of the X-shaped valve core rheological part 102 is 5-150°, and the included angle of the V-shaped formed on the upper and lower sides is 5-150°; preferably, the included angle of the quadrilateral formed on the left and right sides of the X-shaped valve core rheological part 102 is 10-145°, and the included angle of the V-shaped formed on the upper and lower sides is 10-145°; more preferably, the included angle of the quadrilateral formed on the left and right sides of the X-shaped valve core rheological part 102 is 30-135°, and the included angle of the V-shaped formed on the upper and lower sides is 35-110°; more preferably, the included angle of the quadrilateral formed on the left and right sides of the X-shaped valve core rheological part 102 is 55-120°, and the included angle of the V-shaped formed on the upper and lower sides is 65-100°; more preferably, the included angle of the quadrilateral formed on the left and right sides of the X-shaped valve core rheological part 102 is 80-100°, and the included angle of the V-shaped formed on the upper and lower sides is 85-105°.

[0047] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, the quadrilateral large hole formed by the right angles of the two adjacent X-shaped valve core rheological parts 102 is a harp shape, preferably a rhombus, and more preferably a square. The best large hole shape can be selected according to the raw materials and mixing process, and it is worth noting that the harp-shaped or rhombus-shaped large hole design is more helpful to improve the mixing effect.

[0048] As a preferred technical solution of the embodiment, please refer to Figure 1 As shown, the side end face of the circular ring type end part 101 is a ring type inclined surface 105, which is an outer circular ring shape and can tightly fit the inner hole wall of the mixing cylinder body, ensuring the sealing performance of the connection between the circular ring type end part 101 and the mixing cylinder body.

[0049] Embodiment two

[0050] As shown in Figure 2 , Figure 3 and Figure 4 , different from the first embodiment, the embodiment specifically provides an injection nozzle mixer of an injection machine, which mainly comprises a sub-nozzle 200, a flange connecting body 300 and an integrated X rheological mixing valve core 100. The integrated X rheological mixing valve core 100 is arranged in a through hole between the sub-nozzle 200 and the flange connecting body 300, and a side end face of a circular ring type end part 101 is in close contact with an inner hole wall of the sub-nozzle 200.

[0051] As a preferred technical solution of the embodiment, as shown in Figure 2 and Figure 3 , the inner hole wall of the sub-nozzle 200 is provided with a nozzle inclined surface 201, and the nozzle inclined surface 201 is in close contact with a ring type inclined surface 105 of the side end face of the circular ring type end part 101. The nozzle inclined surface 201 is in the form of an inner circular ring, which can be in close contact with the ring type inclined surface 105 of the side end face of the circular ring type end part 101, thereby ensuring the sealing performance of the connection between the circular ring type end part 101 and the inner hole of the sub-nozzle 200.

[0052] The same as the above-mentioned first embodiment, the integrated X rheological mixing valve core 100 is integrally formed from the circular ring type end part 101, at least one X type valve core rheological part 102 and a V type rheological end part 103 from the proximal end to the distal end, and the whole is in the form of an alternating distribution structure of a middle quadrilateral large hole combined cross X type and an outer circle V type. The cross-sectional shapes of the circular ring type end part 101, the X type valve core rheological part 102 and the V type rheological end part 103 are all in the form of circles with the same diameter, that is, the end part of the at least one X type valve core rheological part 102 of the X type cylinder structure is connected with the end part of the V type rheological end part 103, thereby forming a quadrilateral large hole shape with two sides through, and a continuous V type groove is formed between the upper and lower two side ends. By using the integrated X rheological mixing valve core 100 with the special structure design, the problems of easy misalignment of multiple valve core contact surfaces and generation of black points, black lines and yellow lines caused by hidden glue of the existing split type mixing valve core are completely solved, and the problem of easy deformation and cracking of the split valve core is also solved.

[0053] As a preferred technical solution of the embodiment, as shown in Figure 2As shown, the outer diameter of the integrated X rheological mixing valve core 100 on the injection nozzle mixer of the injection machine is 10-600 mm, and the thickness of the X-shaped column is 1-50 mm according to the production needs; preferably, the outer diameter of the integrated X rheological mixing valve core 100 is 20-450 mm, and the thickness of the X-shaped column is 5-40 mm; more preferably, the outer diameter of the integrated X rheological mixing valve core 100 is 20-100 mm, and the thickness of the X-shaped column is 4-10 mm; more preferably, the outer diameter of the integrated X rheological mixing valve core 100 is 26-50 mm, and the thickness of the X-shaped column is 4-6 mm.

[0054] As a preferred technical solution of the present embodiment, the hole diameter of the small hole 104 on the injection nozzle mixer of the injection machine is 0.5-20 mm, and the depth is 1-50 mm; preferably, the hole diameter of the small hole 104 is 1-5 mm, and the depth is 4-20 mm; more preferably, the hole diameter of the small hole 104 is 1-4 mm, and the depth is 4-10 mm; more preferably, the hole diameter of the small hole 104 is 1-3 mm, and the depth is 4-6 mm.

[0055] As a preferred technical solution of the present embodiment, the number of X-shaped valve core rheological parts 102 on the injection nozzle mixer of the injection machine is 1-100 integrally formed; preferably, the number of X-shaped valve core rheological parts 102 is 5-80; more preferably, the number of X-shaped valve core rheological parts 102 is 4-80; more preferably, the number of X-shaped valve core rheological parts 102 is 5-10.

[0056] As a preferred technical solution of the present embodiment, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 on the injection nozzle mixer of the injection machine is 5-150°, and the included angle of the V-shaped formed by the upper and lower sides is 5-150°; preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 15-140°, and the included angle of the V-shaped formed by the upper and lower sides is 15-145°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 35-130°, and the included angle of the V-shaped formed by the upper and lower sides is 40-120°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 60-110°, and the included angle of the V-shaped formed by the upper and lower sides is 55-100°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 85-100°, and the included angle of the V-shaped formed by the upper and lower sides is 75-105°; most preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 90°, and the included angle of the V-shaped formed by the upper and lower sides is 90°.

[0057] As a preferred technical solution of the embodiment, the quadrilateral large hole formed by the right angles of the two adjacent X-shaped valve core rheological parts 102 on the injection nozzle mixer of the injection machine is preferably square, which is more helpful to improve the mixing effect of the injection machine.

[0058] Please continue to refer to Figure 2 、 Figure 3 and Figure 4 , the working process of the injection nozzle mixer of the injection machine provided by the embodiment is as follows:

[0059] Before the injection starts, the injection machine advances the front end of the R spherical surface of the sub-injection nozzle 200 to contact and press the R spherical surface of the mold gate, and the melted plastic is forced to flow into the inner hole of the flange connector 300 under the push of the screw rod, and then flows into the quadrilateral cavity through the small holes 104 on the V-shaped rheological end part 103;

[0060] Then the flow direction of the plastic is branched into multiple paths through the X-shaped valve core rheological part 102, and the plastic is extruded into the V-shaped cavity of the outer circle of the integrated X-shaped rheological mixing valve core 100 through the several small holes 104 on the inclined surface of the X-shaped valve core rheological part 102, and then enters the large hole surrounded in front through the X-shaped valve core rheological part 102.

[0061] After multiple cross-flow fusion, the plastic is finally compressed into the triangular cavity between the X-shaped valve core rheological part 102 and the circular ring end part 101, and then flows into the mold through the sub-injection nozzle 200.

[0062] The injection nozzle mixer of the injection machine is provided with a heating ring and a temperature sensing wire outside the entire injection nozzle, and the temperature can be adjusted and corrected in the computer to ensure that the plastic is not easily decomposed under the condition of better fusion.

[0063] Embodiment Three

[0064] Please refer to Figure 5 and Figure 6 , which is different from the above-mentioned embodiment one, the embodiment specifically provides an extrusion machine discharge mixing adapter device, which comprises an adapter die head 400 and an integrated X-shaped rheological mixing valve core 100 as described above. The integrated X-shaped rheological mixing valve core 100 is arranged in the through hole of the adapter die head 400, and the side end face of the circular ring end part 101 is in close contact with the inner hole wall of the adapter die head 400.

[0065] As a preferred technical solution of the embodiment, please refer to Figure 5 and Figure 6As shown, the inner hole wall of the adapter die 400 is provided with an adapter bevel 401 which is bevel-fitted with the annular bevel 105 of the side end face of the circular ring-shaped end portion 101. The adapter bevel 401 is in the form of an inner annular ring which can be tightly fitted with the annular bevel 105 of the side end face of the circular ring-shaped end portion 101, thereby ensuring the sealing performance of the connection between the circular ring-shaped end portion 101 and the inner hole of the adapter die 400.

[0066] As the same as the embodiment one, the circular ring-shaped end portion 101, the at least one X-shaped valve core rheological portion 102 and the V-shaped rheological end portion 103 of the integrated X rheological mixing valve core 100 are integrally formed from the proximal end to the distal end, and the whole is in the form of an alternating distribution structure of a middle quadrilateral large hole combined cross X and an outer circle V. The cross-sectional shapes of the circular ring-shaped end portion 101, the X-shaped valve core rheological portion 102 and the V-shaped rheological end portion 103 are all in the form of a circle with the same diameter, i.e. the end portion of the at least one X-shaped valve core rheological portion 102 and the end portion of the V-shaped rheological end portion 103 are cross-connected to form a quadrilateral large hole shape with two sides through, and a continuous V-shaped groove is formed between the upper and lower two side ends. By using the integrated X rheological mixing valve core 100 with the special structure design, the problems of easy misalignment of multiple valve core contact surfaces and black spots, black lines and yellow lines caused by hidden glue of the existing split type mixing valve core are completely solved, and the problem of easy deformation and cracking of the split valve core is also solved.

[0067] As a preferred technical solution of the embodiment, please refer to Figure 5 As shown, on the extruder discharge mixing adapter device, the outer circle diameter of the integrated X rheological mixing valve core 100 is 10-550mm, and the thickness of the X-shaped cylinder thereof is 1-50mm; preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 20-450mm, and the thickness of the X-shaped cylinder thereof is 5-40mm; more preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 20-100mm, and the thickness of the X-shaped cylinder thereof is 4-10mm; more preferably, the outer circle diameter of the integrated X rheological mixing valve core 100 is 26-50mm, and the thickness of the X-shaped cylinder thereof is 4-6mm.

[0068] As a preferred technical solution of the embodiment, on the extruder discharge mixing adapter device, the hole diameter of the small hole 104 is 0.5-18mm, and the depth thereof is 1-45mm; preferably, the hole diameter of the small hole 104 is 1-5mm, and the depth thereof is 4-20mm; more preferably, the hole diameter of the small hole 104 is 1-4mm, and the depth thereof is 4-10mm; more preferably, the hole diameter of the small hole 104 is 1-3mm, and the depth thereof is 4-6mm.

[0069] As a preferred technical solution of the embodiment, the number of the X-shaped valve core rheological parts 102 on the extruder discharge mixing adapter device is 1-100 integrally formed; preferably, the number of the X-shaped valve core rheological parts 102 is 5-80; more preferably, the number of the X-shaped valve core rheological parts 102 is 4-60; and more preferably, the number of the X-shaped valve core rheological parts 102 is 5-10.

[0070] As a preferred technical solution of the embodiment, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 22-140°, and the included angle of the V-shaped formed by the upper and lower sides is 10-140°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 40-130°, and the included angle of the V-shaped formed by the upper and lower sides is 30-110°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 65-110°, and the included angle of the V-shaped formed by the upper and lower sides is 60-100°; more preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 80-90°, and the included angle of the V-shaped formed by the upper and lower sides is 90-100°; and most preferably, the included angle of the quadrilateral formed by the left and right sides of the X-shaped valve core rheological part 102 is 90°, and the included angle of the V-shaped formed by the upper and lower sides is 90°.

[0071] As a preferred technical solution of the embodiment, the quadrilateral large hole formed by the right angles of the two adjacent X-shaped valve core rheological parts 102 is preferably a rhombic structure, which is more helpful to improve the mixing effect of the extruder discharge mixing adapter.

[0072] Please continue to refer to Figure 5 and Figure 6 The working process of the extruder discharge mixing adapter device provided by the embodiment is as follows:

[0073] Before the extrusion molding starts, the extruder machine advances to contact and press the front end of the adapter die head 400 with the glue inlet of the mold. The plastic is forced to melt and flow into the inner hole of the adapter die head 400 under the pushing of the screw rod. The melted plastic flows into the quadrilateral cavity through the small holes 104 on the V-shaped rheological end part 103 at the same time;

[0074] Then the flow direction of the plastic is branched into multiple paths through the X-shaped valve core rheological part 102. The plastic is extruded into the V-shaped cavity of the integral X-shaped rheological mixing valve core 100 through the several small holes 104 on the inclined surface of the X-shaped valve core rheological part 102, and then enters the large hole surrounded in front through the X-shaped valve core rheological part 102.

[0075] After multiple cross-flow fusion, the plastic is finally compressed into the triangular cavity between the X-shaped valve core rheological part 102 and the circular ring-shaped end part 101, and then flows into the mold through the adapter die head 400.

[0076] Comparative Example 1

[0077] The filter mixing nozzle disclosed in the patent CN110091469A of the company is used as a comparative example for injection molding production. The injection molding process is as follows: before starting injection molding, the injection machine moves forward to the front of the nozzle, the R spherical surface at the front end of the sub nozzle is in contact with and pressed against the R spherical surface of the mold glue inlet, and the melted plastic is forced to flow into the inner hole of the prismatic rheological valve core under the push of the screw rod, and then into the inner cavity of the prismatic rheological valve core. The prismatic rheological valve core branches the flow direction of the plastic into two paths, the plastic is extruded into the middle cavity of the prismatic rheological valve core through several small holes on the prismatic shape of the prismatic rheological valve core, and then enters the large hole in front of it after crossing. After several times of crossing and merging, the plastic is finally compressed into the cavity between the rheological valve core head and the sub nozzle, and then injected into the mold.

[0078] Performance test:

[0079] The integrated injection machine injection nozzle mixer of Example 2 of the present application is used as the test group, and the split filter mixing nozzle of Comparative Example 1 is used as the control group. The overall size and structure of the mixing nozzles used in the two groups are the same. The processing production cycle, service life under the same plastic raw material and the same process conditions, disassembly and cleaning time, failure rate and maintenance cycle are tested respectively. The test results are shown in Table 1 below.

[0080] Table 1 Performance test results of integrated nozzle mixer and split mixing nozzle

[0081]

[0082] As can be seen from the test data in Table 1 above, compared with the existing split filter mixing nozzle, the X rheological mixer of the present application greatly shortens the processing cycle and reduces the production cost. The average service life is extended by more than 2 times, the disassembly and cleaning time of the equipment is reduced from 3 hours to 1 hour, the occurrence of faults is avoided, and the maintenance cycle is extended from half a year to one year.

[0083] In addition, the X rheological mixer completely solves the problem of misalignment between the contact surfaces of multiple valve cores and the problem of black spots, black lines and yellow lines caused by hidden glue, and also solves the problem of deformation and cracking of split valve cores. The use effect is better: only one integrated filter mixing valve core is used, which can be installed and disassembled at will, is convenient and fast, saves time and effort, is convenient for maintenance and replacement, improves the processing efficiency, and reduces the manufacturing cost.

[0084] The above detailed description of the application is only as an example, and the application is not limited to the above described specific embodiments. Any equivalent modifications and substitutions made by those skilled in the art to the application are also within the scope of the application. Therefore, equivalent transformations and modifications made without departing from the spirit and scope of the application should be covered within the scope of the application.

Claims

1. An X rheomixer characterized in that, The application relates to an integrated X rheological mixing valve core (100) arranged in a mixing cylinder, wherein the integrated X rheological mixing valve core (100) comprises a circular ring type end (101), at least one X type valve core rheological part (102) and a V type rheological end (103) integrally formed from a proximal end to a distal end, and the integrated X rheological mixing valve core (100) has an overall structure of an alternating distribution structure of a middle quadrilateral large hole combined cross X type and an outer circle V type. The side end face of the circular ring type end (101) is a ring type inclined surface (105); the outer circle diameter of the integrated X rheological mixing valve core (100) is 10-600 mm, and the thickness of the X type column is 1-50 mm; the included angle of the quadrilateral formed on the left and right sides of the X type valve core rheological part (102) is 5-150 DEG, and the included angle of the V type formed on the upper and lower sides is 5-150 DEG; and the inclined surfaces of the X type valve core rheological part (102) and the V type rheological end (103) are uniformly distributed with a plurality of small holes (104), the hole diameter of the small holes (104) is 0.5-20 mm, and the depth is 1-50 mm. The number of the X type valve core rheological parts (102) is 1-100.

2. The X-rheometric mixer of claim 1, wherein, The quadrilateral large hole is a shape of a harp, a rhombus or a square.

3. The X-rheometric mixer of claim 1, wherein, The injection machine injection nozzle mixing device comprises a sub nozzle (200), a flange connecting body (300) and the integrated X rheological mixing valve core (100) according to any one of claims 1-3, wherein the integrated X rheological mixing valve core (100) is arranged in a through hole between the sub nozzle (200) and the flange connecting body (300), and the side end face of the circular ring type end (101) is attached to the inner hole wall of the sub nozzle (200); the inner hole wall of the sub nozzle (200) is provided with a nozzle inclined surface (201), and the nozzle inclined surface (201) is attached to the ring type inclined surface (105) of the side end face of the circular ring type end (101) in an inclined surface manner.

4. An injection-molding machine injection nozzle compounder characterized by, The extruder discharge mixing adapter device comprises an adapter die (400) and the integrated X rheological mixing valve core (100) according to any one of claims 1-3, wherein the integrated X rheological mixing valve core (100) is arranged in a through hole of the adapter die (400), and the side end face of the circular ring type end (101) is attached to the inner hole wall of the adapter die (400); the inner hole wall of the adapter die (400) is provided with an adapter inclined surface (401), and the adapter inclined surface (401) is attached to the ring type inclined surface (105) of the side end face of the circular ring type end (101) in an inclined surface manner. ​ 5. An extruder discharge compound transfer adapter apparatus, characterized by, ​ ​

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