METHOD FOR PREPARING POLYMER MOULD-FREE STEREOSTRUCTURE FOAMED PRODUCT FROM SUPERCRITICAL FLUID

Abstract

A method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid, containing a supercritical fluid delivery system, a stereoscopic foaming system and a preheating system, and has the following steps: performing pressure molding on a polymer material to obtain a foaming preform, then preheating the foaming preform in the preheating system, delivering the foaming preform to the stereoscopic foaming system after a temperature rises to a preheating temperature, introducing the supercritical fluid, and decompressing after the supercritical fluid is swelled and diffused to the polymer. The polymer is swelled using high-temperature medium-pressure supercritical fluid by utilizing a one-step method in a stereoscopic foaming tank and then subjected to free mould-free stereoscopic pressure-relief foam molding, so as to obtain a polymer microcellular foamed product with controllable product shape, size precision, pore fineness and product density.

Claims

1: A method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid, comprising a supercritical fluid delivery system, a stereoscopic foaming system and a preheating system, wherein the supercritical fluid delivery system is a supercritical CO.sub.2 or supercritical N.sub.2 delivery system, or a N.sub.2/CO.sub.2 mixed gas; the stereoscopic foaming system comprises a stereoscopic foaming tank, a temperature control device, a pressure control device and a pressure release device, and the supercritical fluid delivery system is connected with the stereoscopic foaming system; the preheating system comprises a preheating tank, a heating cycle device and a temperature control device; swelling and impregnating the polymer using high-temperature medium-pressure supercritical fluid by utilizing a one-step method in a stereoscopic foaming tank and then directly subjected to free mould-free stereoscopic pressure-relief foam molding specifically comprises the following steps: performing pressure molding on a polymer material to obtain a foaming preform, then preheating the foaming preform in the preheating system, delivering the foaming preform to the stereoscopic foaming system after a temperature rises to a preheating temperature, closing and sealing the stereoscopic foaming tank, opening an intake valve, introducing the supercritical fluid to be regulated to be at a target temperature and pressure, swelling and diffusing the supercritical fluid toward the polymer for 30-120 min, and opening the pressure release device for pressure relief and foaming, so as to obtain a polymer microcellular foamed product with controllable product shape, size precision, pore fineness and product density.

2: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 1, wherein the polymer is selected from but not limited to any one or a combination of polyethylene, polylactic acid, polypropylene, polystyrene, polymethyl methacrylate, polycarbonate, an acrylonitrile-butadiene-styrene copolymer, polyethylene terephthalate, polyamide, polyimide, polyphenylene sulfide, polyether sulfone, polyether ether ketone, rubber, silicone rubber, EPDM, an ethylene-vinyl acetate copolymer, thermoplastic polyurethane and a thermoplastic elastomer.

3: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 2, wherein the polymer selects an amorphous polymer, the target temperature is 1.0-50° C. below the melting temperature of the polymer, and the pressure is 5-15 MPa.

4: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 2, wherein the polymer selects a crystalline polymer, the target temperature is 1.0-50° C. below the melting temperature of the polymer, and the pressure is 5-15 MPa.

5-8. (canceled)

9: The method for preparing a polymer mould-ree stereostructure foamed product from supercritical fluid according to claim 3, wherein the pressure relief rate of the of the pressure release device of the stereoscopic foaming tank is 1-1000 MPa/s.

10: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 4, wherein the pressure relief rate of the of the pressure release device of the stereoscopic foaming tank is 1-1000 MPa/s.

11: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 3, wherein the supercritical CO.sub.2 delivery system comprises a CO.sub.2 liquid storage tank and a CO.sub.2 booster station, and the supercritical N.sub.2 delivery system comprises a N.sub.2 liquid storage tank and a N.sub.2 booster station.

12: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 4, wherein the supercritical CO.sub.2 delivery system comprises a CO.sub.2 liquid storage tank and a CO.sub.2 booster station, and the supercritical N.sub.2 delivery system comprises a N.sub.2 liquid storage tank and a N.sub.2 booster station.

13: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 1, wherein the supercritical CO.sub.2 delivery system is a N.sub.2/CO.sub.2 mixed gas in which the volume percentage of N.sub.2 is 50-99%.

14: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 3, wherein the volume expansion ratio of the polymer microcellular foamed product has a volume expansion ratio of 2-60 folds, an average pore diameter of 0.1-100 μm and a pore density of 1.0×10.sup.6-1.0×10.sup.15 pores/cm.sup.3.

15: The method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid according to claim 4, wherein the volume expansion ratio of the polymer microcellular foamed product has a volume expansion ratio of 2-60 folds, an average pore diameter of 0.1-100 μm and a pore density of 1.0×10.sup.6-1.0×10.sup.15 pores/cm.sup.3.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0027] For better illustrating the technical solution of embodiments of the disclosure, drawings required for describing embodiments will be explained below. Apparently, the drawings in the description below are only some embodiments, and those skilled in the art can also obtain other drawings according to these drawings without any creative efforts.

[0028] FIG. 1 is a structural flowchart of a supercritical fluid delivery system and a stereoscopic foaming system according to the disclosure.

[0029] FIG. 2 is a diagram of a preheating system according to the disclosure.

[0030] FIG. 3 is a scanning electron microscopy of a 1PLA foamed product according to an embodiment.

[0031] FIG. 4 is a scanning electron microscopy of a 2POPCOHERE 8102 foamed product according to an embodiment of the disclosure.

[0032] FIG. 5 is a scanning electron microscopy of a 3TPU 58315 foamed product according to an embodiment of the disclosure.

[0033] In the drawings, 1—supercritical fluid delivery system; 2—N2 liquid storage tank; 3—N2 booster station; 4—CO2 liquid storage tank; 5—CO2 booster station; 6—intake valve; 7—stereoscopic foaming system; 8—pressure control device; 9—temperature control device; 10—pressure release device; 11—silencer, 12—vant valve; 13—preheating system; 14—temperature control device; 15—heating cycle device

DETAILED DESCRIPTION OF THE INVENTION

[0034] To make the purpose, the features and the benefits of the disclosure more clear, the technical solution in embodiments of the disclosure will be dearly and completely described below in conjunction with embodiments of the disclosure. Based on embodiments of the disclosure, other embodiments obtained by those of ordinary skill in the art without any creative efforts all belong to the scope of protection of the disclosure.

[0035] A method for preparing a polymer mould-free stereostructure foamed product from supercritical fluid comprises a supercritical fluid delivery system, a stereoscopic foaming system and a preheating system, wherein the supercritical fluid delivery system is a supercritical CO2 or supercritical N2 delivery system, or a N2/CO2 mixed gas; the stereoscopic foaming system comprises a stereoscopic foaming tank, a temperature control device, a pressure control device and a pressure release device, and the stereoscopic foaming system is connected with the stereoscopic foaming system; the preheating system comprises a preheating tank, a heating cycle device and a temperature control device;

[0036] specific operation steps are as follows: a polymer material is subjected to pressure molding to obtain a foaming preform, then the foaming preform is preheated in the preheating system, the foaming preform is delivered to the stereoscopic foaming system after a temperature rises to 30-50° C. below a softening temperature or a melting point of a polymer, the stereoscopic foaming tank is closed and sealed, an intake valve is opened, the supercritical fluid is introduced to be regulated to be at a target temperature and pressure, the supercritical fluid is swelled and diffused toward the polymer for 30-120 min, a pressure release device is opened for pressure relief and foaming to obtain a polymer microcellular foamed product with controllable product shape, size precision, pore fineness and product density.

Embodiment 1

[0037] The polylactic acid particles having an average molecular weight of 100,000 and a melting point of 120° C. are subjected to injection molding via a mould of an injection molding machine to prepare a to-be-foamed polylactic acid special-shaped preform. The to-be-processed polylactic acid special-shaped preform is preheated in the preheating tank, and the preheating temperature is in a region of 105° C. below the melting point of polylactic acid. After the preheating temperature is reached, the polylactic acid special-shaped perform enters the stereoscopic foaming tank together with the material rack, and the stereoscopic foaming tank sealing cover is closed. The stereoscopic foaming tank is always maintained at the target temperature of 125° C. during the work. The intake valve is opened, supercritical fluid is introduced, and the ratio of supercritical carbon dioxide to supercritical nitrogen is 30:70. At the target temperature, the supercritical fluid is swelled and diffused toward the polymer for 80 min when the working pressure of the stereoscopic foaming tank is 10 MPa. The pressure release device is opened for exhausting, pressure relief and foaming, and the pressure-relief rate of the pressure release device of the stereoscopic foaming tank is 5 MPa/s, and therefore the polymer microcellular foamed product with controllable product shape, pore fineness and product density is obtained. The volume expansion ratio is 14 folds. Based on 100 parts of polymer weight, the content of supercritical fluid dissolved in the polymer is 15.0 parts after diffusion balance is reached. The average pore diameter is 6.3 μm by analyzing its interior pore morphology via scanning electron microscope, and the pore density obtained by calculation is 3.8×109 pores/cm3. The expansions of the polylactic acid special-shaped preform in all directions are basically uniform, and the linear expansion ratio is 2.33±0.15. A product having a foam density of 90 kg/m3 is finally obtained

Embodiment 2

[0038] Polyolefin plastic POP COHERE 8102 having a density of 902 kg/m3 and a melting point of 98° C. is subjected to injection molding via a mould of an injection molding machine to prepare a to-be-foamed polyolefin plastic special-shaped preform. The to-be-processed foaming polylactic acid special-shaped preform is preheated in the preheating tank, and the preheating temperature is in a region of 80° C. below the melting point of polylactic acid. After the preheating temperature is reached, the to-be-processed foaming polylactic acid special-shaped preform enters the stereoscopic foaming tank together with the material rack, and the stereoscopic foaming tank sealing cover is closed. The stereoscopic foaming tank is always maintained at the target temperature of 100° C. during the work. The intake valve is opened, supercritical fluid is introduced, and the ratio of supercritical carbon dioxide to supercritical nitrogen is 20:80. At the target temperature, the supercritical fluid is swelled and diffused toward the polymer for 100 min when the working pressure of the stereoscopic foaming tank is 12 MPa. The pressure release device is opened for exhausting, pressure relief and foaming, and the pressure relief rate of the pressure release device of the stereoscopic foaming tank is 200 MPa/s, and therefore the polymer microcellular foamed product with controllable product shape, pore fineness and product density is obtained. The volume expansion ratio is 20 folds. Based on 100 parts of polymer weight, the content of supercritical fluid dissolved in the polymer is 18.0 parts after diffusion balance is reached. The average pore diameter is 32.5 μm by analyzing its interior pore morphology via scanning electron microscope, and the pore density obtained by calculation is 5.2×108 pores/cm3. The expansions of the polyolefin plastic special-shaped preform in all directions are basically uniform, and the linear expansion ratio is 2.62±0.15. A product having a foam density of 45 kg/m3 is finally obtained.

Embodiment 3

[0039] TPU 58315 having a density of 1120 kg/m3 and a melting point of 135° C. is subjected to injection molding via a mould of an injection molding machine to prepare a to-be-foamed TPU special-shaped preform. The to-be-processed TPU special-shaped preform is preheated in the preheating tank, and the preheating temperature is in a region of 120° C. below the melting point. After the preheating temperature is reached, the TPU special-shaped perform enters the stereoscopic foaming tank together with the material rack, and the stereoscopic foaming tank sealing cover is closed. The stereoscopic foaming tank is always maintained at the target temperature of 140° C. during the work. The intake valve is opened, supercritical fluid is introduced, and the ratio of supercritical carbon dioxide to supercritical nitrogen is 50:50. At the target temperature, the supercritical fluid is swelled and diffused toward the polymer for 90 min when the working pressure of the stereoscopic foaming tank is 13 MPa. The pressure release device is opened for exhausting, pressure relief and foaming, and the pressure relief rate of the pressure release device of the stereoscopic foaming tank is 60 MPa/s, the pressure of the supercritical fluid in the tank is released to 2 MPa through the pressure release device of the stereoscopic foaming tank and then released to atmosphere, subsequently, the sealing cover is opened, and the polymer microcellular foamed product with controllable product shape, pore fineness and product density is obtained. The volume expansion ratio is 11 folds. Based on 100 parts of polymer weight, the content of supercritical fluid dissolved in the polymer is 12.0 parts after diffusion balance is reached. The average pore diameter is 72 μm by analyzing its interior pore morphology via scanning electron microscope, and the pore density obtained by calculation is 4.6×107 pores/cm3. The expansions of the TPU special-shaped preform in all directions is basically uniform, and the linear expansion ratio is 2.22±0.15. A product having a foam density of 101 kg/m3 is finally obtained.

[0040] The above embodiments are only for illustrating the technical solution of the disclosure but not limiting thereto. Although the disclosure is described in detail by reference to the above-mentioned embodiments, those of ordinary skill in the art should understand that they can still make amendments to the technical solution in the above-mentioned embodiments, or make equivalent substitutions to partial technical features; these amendments or substitutions do not make the nature of the corresponding technical solution depart from the spirit and scope of the technical solutions of various embodiments of the disclosure.

[0041] In the description of this specification, referring to terms the description of ‘one embodiment’, “example”, “specific example” and the like means specific features, structures, materials or characteristics described by combining this embodiment or example are included in at least one embodiment or example of the disclosure. In this specification, illustrative representation of the above terms does not necessarily refer to the same embodiment or example. Furthermore, the described specific features, structures, materials or characteristics can be combined in any one or more embodiments or examples in a proper manner.

[0042] The above disclosed preferred embodiments of the disclosure are only for helping to illuminate the disclosure. The preferred embodiments do not elaborate all the details, and do not limit concrete implementations of the disclosure. Apparently, many amendments and variations can be made according to contents of this specification. Selection and specific description of these embodiments by this specification are intended to better explain the principle and actual application of the disclosure, and therefore those skilled in the art can well understand and utilize the disclosure. The disclosure is limited only by claims and all the scopes and equivalents thereof.