Polyolefin porous separator and preparation method thereof

Abstract

A polyolefin porous separator includes a first surface and a second surface corresponding to the first surface. The surfaces of the polyolefin porous separator contain dendritic crystals and micropores, the dendritic crystals intersect with the micropores on the first surface or/and the second surface, and the dendritic crystals penetrate through the second surface from the first surface. A preparation method of the polyolefin porous separator includes: (1) a mixed melting of polyethylene resin and a mineral oil; (2) an extrusion of the mineral oil/polyethylene resin molten mixture; (3) a stretching of a thick sheet in a machine direction (MD); (4) a stretching of the separator in a transverse direction (TD); (5) immersing the separator into a solvent to extract the mineral oil; (6) a secondary stretching of the separator in the TD; and (7) subjecting the separator having the longitudinal crystals to a heat-setting treatment and then rolling up.

Claims

1. A polyolefin porous separator, comprising a first surface and a second surface corresponding to the first surface, wherein, the first surface and the second surface of the polyolefin porous separator contain dendritic crystals and micropores, the dendritic crystals intersect with the micropores on the first surface or/and the second surface, and the dendritic crystals penetrate through the second surface from the first surface; wherein a preparation method of the polyolefin porous separator comprises the following steps: (1) melt mixing polyethylene resin and a mineral oil comprising feeding the polyethylene resin and the mineral oil into a twin-screw extruder through two feed inlets, respectively, wherein the mineral oil is put into a first feed inlet of the two feed inlets, and a mixture of the mineral oil and the polyethylene resin is put into a second feed inlet of the two feed inlets, and setting a first temperature above a melting temperature of the polyethylene resin to form a mineral oil/polyethylene resin molten mixture; (2) extruding the mineral oil/polyethylene resin molten mixture into a thick sheet by a T-shaped die head of the twin-screw extruder; (3) performing a stretching of the thick sheet in a machine direction (MD) by passing the thick sheet through 6 sets of stretching rollers, keeping a second temperature between 150° C.-170° C., and controlling a speed ratio of two adjacent stretching rollers of the 6 sets of stretching rollers between 1.2-1.8, to form a separator intermediate; (4) performing a first stretching of the separator intermediate in a transverse direction (TD) 9-12 times; (5) immersing the separator intermediate into a solvent to extract the mineral oil; (6) performing a secondary stretching of the separator intermediate in the TD 1.2-1.4 times to form longitudinal crystals in the separator intermediate; and (7) subjecting the separator intermediate having the longitudinal crystals to a heat-setting treatment and then rolling up to obtain the polyolefin porous separator.

2. The polyolefin porous separator according to claim 1, wherein a width of the dendritic crystals is 0.25-0.5 μm.

3. The polyolefin porous separator according to claim 1, wherein an average number of the dendritic crystals contained in the polyolefin porous separator per square micron is 2-8.

4. A preparation method of a polyolefin porous separator, comprising the following steps: (1) melt mixing polyethylene resin and a mineral oil comprising feeding the polyethylene resin and the mineral oil into a twin-screw extruder through two feed inlets, respectively, wherein the mineral oil is put into a first feed inlet of the two feed inlets, and a mixture of the mineral oil and the polyethylene resin is put into a second feed inlet of the two feed inlets, and setting a first temperature above a melting temperature of the polyethylene resin to form a mineral oil/polyethylene resin molten mixture; (2) extruding the mineral oil/polyethylene resin molten mixture into a thick sheet by a T-shaped die head of the twin-screw extruder; (3) performing a stretching of the thick sheet in a machine direction (MD) by passing the thick sheet through 6 sets of stretching rollers, keeping a second temperature between 150° C.-170° C., and controlling a speed ratio of two adjacent stretching rollers of the 6 sets of stretching rollers between 1.2-1.8 to form a separator intermediate; (4) performing a first stretching of the separator intermediate in a transverse direction (TD) 9-12 times; (5) immersing the separator intermediate into a solvent to extract the mineral oil; (6) performing a secondary stretching of the separator intermediate in the TD 1.2-1.4 times to form longitudinal crystals in the separator intermediate; and (7) subjecting the separator intermediate having the longitudinal crystals to a heat-setting treatment and then rolling up to obtain the polyolefin porous separator.

5. The preparation method of the polyolefin porous separator according to claim 4, wherein the polyethylene resin in step (1) is a mixed resin of an ultra-high molecular weight polyethylene (UHMWPE) resin and high molecular weight polyethylene (HMWPE) resin, a molecular weight of the UHMWPE resin is more than 1,800,000, and a molecular weight of the HMWPE resin is 600,000-700,000.

6. The preparation method of the polyolefin porous separator according to claim 5, wherein, mass percentages of the UHMWPE resin, the HMWPE resin and the mineral oil are 15%-20%, 5%-10% and 70%-80%, respectively, and a total mass percentage of the UHMWPE resin, the HMWPE resin and the mineral oil is 100%.

7. The preparation method of the polyolefin porous separator according to claim 4, wherein an extrusion temperature in step (2) is 10-15° C. lower than the melting temperature of the polyethylene resin.

8. The preparation method of the polyolefin porous separator according to claim 4, wherein a pressure of the T-shaped die head in step (2) is 0.1-0.3 MPa.

9. The preparation method of the polyolefin porous separator according to claim 4, wherein the solvent in step (5) is dichloromethane.

Description

DETAILED DESCRIPTION OF THE EMBODIMENTS

(1) The present invention mainly makes the prepared separator have a specific crystal structure at the microscopic level by adjusting raw material formula and improving processing technology in the preparation process of the separator, and the prepared separator shows a dendritic crystal structure.

(2) The microstructure of the separator in a lithium-ion battery contains dendrite crystals and micropores that intersect on a flat surface. The dendrite crystals penetrate through both surfaces of the separator, and have a width of 0.25-0.5 μm. The number of dendrite crystals in the separator per unit area can be observed by scanning electron microscopy. The average number of dendrite crystals in the separator per square micron is 2-8.

(3) The raw materials used in the present invention are polyethylene and mineral oil, in which the polyethylene is a mixed resin of UHMWPE resin and HMWPE resin. The molecular weight of the UHMWPE is more than 1,800,000, and the molecular weight of the HMWPE is 600,000-700,000. The present invention has no special requirements for the mineral oil. Any industrial grade mineral oil or paraffin oil can be adopted. The mass percentages of the UHMWPE, the HMWPE and the mineral oil are 15%-20%, 5%-10% and 70%-80%, respectively.

(4) The preparation method adopts the thermally induced phase separation (TIPS) process, and the preparation steps are as follows.

(5) (1) In the mixed melting stage of polyethylene resin and a mineral oil, the polyethylene resin and the mineral oil are respectively fed into a twin-screw extruder through two feed inlets. Only the mineral oil is put into the first feed inlet, and a mixture of the mineral oil and the polyethylene resin is put into the second feed inlet. The temperature is set above the melting temperature of polyethylene. The specific temperature varies according to different raw materials, so the present invention does not make specific limits.

(6) (2) In the extrusion process of the mineral oil/polyethylene resin molten mixture, the molten mixture is extruded into a thick sheet by a T-shaped die head of the extruder. The extrusion temperature is 10-15° C. lower than the melting temperature, and the pressure of the die head is controlled between 0.1-0.3 MPa.

(7) (3) In the MD stretching process of the cast sheet, there are 6 sets of stretching rollers. In this process, the stretching temperature and the speed ratio between the stretching rollers need to be controlled. The temperature is kept between 150° C.-170° C., and the speed ratio of two adjacent stretching rollers is controlled between 1.2-1.8.

(8) (4) In the first TD (TD1) stretching process, the separator is stretched transversely to 9-12 times.

(9) (5) The separator is immersed into dichloromethane to extract the mineral oil.

(10) (6) In the second TD (TD2) stretching process, the separator is stretched transversely to 1.2-1.4 times to ensure the formation of longitudinal crystals in the separator.

(11) (7) The stretched separator is successively subjected to a heat-setting treatment and being rolled up.

(12) In order to make the above-mentioned objectives, features and advantages of the present invention more obvious and easy to understand, the present invention is further described in detail in combination with the specific implementation modes.

Example 1

(13) TABLE-US-00001 Raw materials and preparation process Properties of separator Mn (UHMWPE) 1,800,000/ n (number/μm.sup.2) 4 & w % 15 Mn (HDPE) 600,000/5 d (μm) 0.26 & w % Mineral oil (w %) 80 MD tensile strength 3104 (Kgf/cm.sup.2) MD speed ratio of TD tensile strength 3546 stretching rollers (Kgf/cm.sup.2) 1/2# roller speed ratio 1.2 MD elongation 212 ratio (%) 2/3# roller speed ratio 1.3 TD elongation 238 ratio (%) 3/4# roller speed ratio 1.5 Frontal puncture 496 strength (gf) 4/5# roller speed ratio 1.6 Reverse puncture 482 strength (gf) 5/6# roller speed ratio 1.5 TD1 stretching multiple 9 TD2 stretching multiple 1.2 Note: n is the number of dendritic crystals per unit area (number/μm.sup.2); d is the average width of dendritic crystals per unit area (μm).

Example 2

(14) TABLE-US-00002 Raw materials and Properties of preparation process separator Mn (UHMWPE) & w % 2,100,000/ n (number/μm.sup.2) 3.5 15 Mn (HDPE) & w % 650,000/5 d (μm) 0.31 Mineral oil (w %) 80 MD tensile strength 3304 (Kgf/cm.sup.2) MD speed ratio of TD tensile strength 3646 stretching rollers (Kgf/cm.sup.2) 1/2# roller speed ratio 1.2 MD elongation ratio (%) 246 2/3# roller speed ratio 1.3 TD elongation ratio (%) 273 3/4# roller speed ratio 1.5 Frontal puncture 527 strength (gf) 4/5# roller speed ratio 1.6 Reverse puncture 531 strength (gf) 5/6# roller speed ratio 1.5 TD1 stretching multiple 9 TD2 stretching multiple 1.2

Example 3

(15) TABLE-US-00003 Raw materials and preparation process Properties of separator Mn (UHMWPE) & 1,800,000/ n (number/μm.sup.2) 5.1 w % 15 Mn (HDPE) & w % 600,000/5 d (μm) 0.18 Mineral oil (w %) 75 MD tensile strength 2816 (Kgf/cm.sup.2) MD speed ratio of TD tensile strength 2934 stretching rollers (Kgf/cm.sup.2) 1/2# roller speed ratio 1.2 MD elongation ratio (%) 195 2/3# roller speed ratio 1.3 TD elongation ratio (%) 170 3/4# roller speed ratio 1.5 Frontal puncture 428 strength (gf) 4/5# roller speed ratio 1.6 Reverse puncture 437 strength (gf) 5/6# roller speed ratio 1.5 TD1 stretching multiple 9 TD2 stretching multiple 1.2

Example 4

(16) TABLE-US-00004 Raw materials and preparation process Properties of separator Mn (UHMWPE) 1,800,000/ n (number/μm.sup.2) 3.7 & w % 15 Mn (HDPE) & w % 600,000/5 d (μm) 0.28 Mineral oil (w %) 80 MD tensile strength 3209 (Kgf/cm.sup.2) MD speed ratio of TD tensile strength 3567 stretching rollers (Kgf/cm.sup.2) 1/2# roller speed ratio 1.3 MD elongation 216 ratio (%) 2/3# roller speed ratio 1.4 TD elongation 246 ratio (%) 3/4# roller speed ratio 1.4 Frontal puncture 514 strength (gf) 4/5# roller speed ratio 1.6 Reverse puncture 536 strength (gf) 5/6# roller speed ratio 1.6 TD1 stretching multiple 9 TD2 stretching multiple 1.2

Example 5

(17) TABLE-US-00005 Raw materials and preparation process Properties of separator Mn (UHMWPE) 1,800,000/ n (number/μm.sup.2) 6 & w % 15 Mn (HDPE) & w % 600,000/5 d (μm) 0.08 Mineral oil (w %) 80 MD tensile strength 2496 (Kgf/cm.sup.2) MD speed ratio of TD tensile strength 2671 stretching rollers (Kgf/cm.sup.2) 1/2# roller speed ratio 1.2 MD elongation ratio (%) 281 2/3# roller speed ratio 1.3 TD elongation ratio (%) 293 3/4# roller speed ratio 1.5 Frontal puncture 483 strength (gf) 4/5# roller speed ratio 1.6 Reverse puncture 467 strength (gf) 5/6# roller speed ratio 1.5 TD1 stretching multiple 10 TD2 stretching multiple 1.4

(18) The following is a comparison between example 4 and the prior art:

(19) TABLE-US-00006 Comparative Comparative Comparative Comparative Properties of separators Example 4 example 1 example 2 example 3 example 4 n (number/μm.sup.2) 3.7 7.4 6.1 5.4 4.7 d (μm) 0.28 0.04 0.11 0.21 0.34 MD tensile strength 3209 2416 1937 2739 3128 (Kgf/cm.sup.2) TD tensile strength (Kgf/cm.sup.2) 3567 2601 2483 2941 3309 MD elongation ratio (%) 216 239 223 169 143 TD elongation ratio (%) 246 240 249 184 169 Frontal puncture strength (gf) 514 386 409 372 412 Reverse puncture strength (gf) 536 361 394 393 429

(20) In conclusion, the polyolefin porous separator and its preparation method can ensure the thickness of the separator and meanwhile significantly improve its mechanical tensile properties and puncture resistance.

(21) Based on the above ideal embodiments of the present invention as an inspiration, technical personnel in this field may make various variations and modifications within the scope of not deviating from the technical idea of the present invention. The technical scope of the present invention is not limited to the contents in the description, and the technical scope shall be determined according to the scope of claims.