CN105885081A - Plasma modification method for polytetrafluoroethylene microporous membrane - Google Patents
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- 238000002715 modification method Methods 0.000 title claims abstract description 15
- 229920001343 polytetrafluoroethylene Polymers 0.000 title abstract description 67
- 239000004810 polytetrafluoroethylene Substances 0.000 title abstract description 67
- 239000012982 microporous membrane Substances 0.000 title abstract description 62
- -1 polytetrafluoroethylene Polymers 0.000 title abstract description 8
- 238000000034 method Methods 0.000 claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 8
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 18
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 12
- 239000002131 composite material Substances 0.000 claims description 3
- 239000004809 Teflon Substances 0.000 claims 13
- 229920006362 Teflon® Polymers 0.000 claims 13
- 210000004379 membrane Anatomy 0.000 claims 13
- 239000004568 cement Substances 0.000 claims 1
- 238000009832 plasma treatment Methods 0.000 abstract description 40
- 238000012986 modification Methods 0.000 abstract description 6
- 230000004048 modification Effects 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000007789 gas Substances 0.000 description 31
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 10
- 239000012528 membrane Substances 0.000 description 9
- 238000002360 preparation method Methods 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 238000002203 pretreatment Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 5
- 238000012545 processing Methods 0.000 description 5
- 239000000126 substance Substances 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000012360 testing method Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910010413 TiO 2 Inorganic materials 0.000 description 2
- 239000003011 anion exchange membrane Substances 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000003566 sealing material Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/36—After-treatment
- C08J9/40—Impregnation
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J9/00—Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
- C08J9/36—After-treatment
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2327/00—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers
- C08J2327/02—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment
- C08J2327/12—Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by a halogen; Derivatives of such polymers not modified by chemical after-treatment containing fluorine atoms
- C08J2327/18—Homopolymers or copolymers of tetrafluoroethylene
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- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
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- Treatments Of Macromolecular Shaped Articles (AREA)
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
Description
技术领域technical field
本发明属于燃料电池的质子交换膜材料领域,具体涉及一种聚四氟乙烯微孔膜的等离子体改性方法。The invention belongs to the field of proton exchange membrane materials for fuel cells, and in particular relates to a plasma modification method for polytetrafluoroethylene microporous membranes.
背景技术Background technique
聚四氟乙烯(PTFE)由四氟乙烯聚合而成的,只含有C-C键和C-F化学键,两个化学键都含有非常高的化学键能,因此聚四氟乙烯化学性质非常稳定,可作为防腐蚀剂材料,降解率非常小,使用寿命比较长,在医学应用材料、阴离子交换膜、密封材料、过滤材料等领域应用广泛。Polytetrafluoroethylene (PTFE) is polymerized from tetrafluoroethylene and only contains C-C bonds and C-F chemical bonds. Both chemical bonds contain very high chemical bond energy, so PTFE is very stable in chemical properties and can be used as an anti-corrosion agent material , the degradation rate is very small, the service life is relatively long, and it is widely used in medical application materials, anion exchange membranes, sealing materials, filter materials and other fields.
聚四氟乙烯微孔膜疏水性强,表面能较低,粘结性和润湿性较弱,限制了其应用,因此需对其进行亲水性改性。【Materials Research Bulletin,2009,44(6):1437-1440】采用在PTFE微孔膜上面负载CeO2,水热合成CeO2/PTFE复合膜,该方法操作过程繁琐,制备时间长,改性后的水接触角只能达到80°,改性的效果不够理想。【Energy Procedia,2011,9:539-544】以钛酸四丁酯为原料,通过水热合成法在PTFE微孔膜上负载TiO2,形成TiO2/PTFE复合微孔膜,该方法合成时间较长,过程也比较繁琐,水接触角只可以达到70°,并且微孔膜的机械强度减小。【Vacuum,2012,86(6):643-647】采用单独的氩气等离子处理PTFE膜,处理后的膜的接触角为60°,同时对微孔膜的损伤较大,机械强度降低。【Applied Surface Science,2008,254(6):1614-1621】采用氮气等离子处理,改性后的PTFE膜的接触角为55°,并且微孔膜的机械强度略有下降。Polytetrafluoroethylene microporous membrane has strong hydrophobicity, low surface energy, weak adhesion and wettability, which limit its application, so it needs to be modified by hydrophilicity. 【Materials Research Bulletin,2009,44(6):1437-1440】CeO 2 /PTFE composite membrane is hydrothermally synthesized by loading CeO 2 on the PTFE microporous membrane. The water contact angle can only reach 80°, and the effect of modification is not ideal enough. [Energy Procedia, 2011, 9:539-544] Using tetrabutyl titanate as raw material, TiO 2 is loaded on PTFE microporous membrane by hydrothermal synthesis method to form TiO 2 /PTFE composite microporous membrane. The synthesis time of this method is Longer, the process is more cumbersome, the water contact angle can only reach 70°, and the mechanical strength of the microporous membrane is reduced. 【Vacuum,2012,86(6):643-647】The PTFE membrane is treated with argon plasma alone, the contact angle of the treated membrane is 60°, and the damage to the microporous membrane is relatively large, and the mechanical strength is reduced. 【Applied Surface Science,2008,254(6):1614-1621】The contact angle of the modified PTFE membrane was 55° after nitrogen plasma treatment, and the mechanical strength of the microporous membrane decreased slightly.
发明内容Contents of the invention
针对现有的聚四氟乙烯微孔膜的亲水改性方法中,改性效果不佳,改性后微孔膜的机械强度降低的不足,本发明提供了一种聚四氟乙烯微孔膜的等离子体改性方法,采用低温等离子体处理方法对PTFE微孔膜进行表面改性,通过控制低温等离子体处理的工艺参数,包括低温等离子气体种类、处理距离、射频功率、处理时间和气体流通量,改善PTFE微孔膜的亲水性,将原疏水性很强的PTFE微孔膜改性成亲水性较强的PTFE微孔膜,水接触角由原来的130°左右降至40°左右,同时保持PTFE微孔膜的机械强度。In view of the existing hydrophilic modification method of polytetrafluoroethylene microporous membrane, the modification effect is not good, and the mechanical strength of the modified microporous membrane is reduced. The present invention provides a polytetrafluoroethylene microporous The plasma modification method of the membrane uses the low-temperature plasma treatment method to modify the surface of the PTFE microporous membrane. By controlling the process parameters of the low-temperature plasma treatment, including the type of low-temperature plasma gas, treatment distance, radio frequency power, treatment time and gas Throughput, improve the hydrophilicity of PTFE microporous membrane, modify the original highly hydrophobic PTFE microporous membrane into a more hydrophilic PTFE microporous membrane, and reduce the water contact angle from about 130° to about 40° , while maintaining the mechanical strength of the PTFE microporous membrane.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
一种聚四氟乙烯微孔膜的等离子体改性方法,具体步骤如下:A method for plasma modification of a polytetrafluoroethylene microporous membrane, the specific steps are as follows:
步骤1,PTFE微孔膜的预处理:将PTFE微孔膜在丙酮溶液中浸泡12~24h,再在80%-98%的乙醇溶液中浸泡3~12h,乙醇溶液多次浸泡除去丙酮后,去离子水清洗除去乙醇,最后在30~70℃下干燥10~24h,得到清洗干净的PTFE微孔膜;Step 1, pretreatment of PTFE microporous membrane: soak PTFE microporous membrane in acetone solution for 12-24 hours, then soak in 80%-98% ethanol solution for 3-12 hours, after soaking in ethanol solution several times to remove acetone, Wash with deionized water to remove ethanol, and finally dry at 30-70°C for 10-24 hours to obtain a cleaned PTFE microporous membrane;
步骤2,等离子体处理:将清洗干净的PTFE微孔膜置于等离子体高真空制备室中,抽真空后,通入CH4和N2,控制CH4和N2的体积比为3:1~1:3,气体的总流量为10cm3/s~50cm3/s,功率为20w~100w,处理距离为1cm~100cm,处理时间为20s~100s,最终得到改性后的PTFE微孔膜。Step 2, plasma treatment: place the cleaned PTFE microporous membrane in the plasma high-vacuum preparation chamber, after vacuuming, feed CH 4 and N 2 , and control the volume ratio of CH 4 and N 2 to 3:1~ 1:3, the total gas flow rate is 10cm 3 /s-50cm 3 /s, the power is 20w-100w, the treatment distance is 1cm-100cm, the treatment time is 20s-100s, and finally the modified PTFE microporous membrane is obtained.
优选地,步骤2中,所述的CH4和N2的体积比为2:1~1:2,更优选为1:1。Preferably, in step 2, the volume ratio of CH 4 and N 2 is 2:1˜1:2, more preferably 1:1.
优选地,步骤2中,所述的气体的总流量为20cm3/s~40cm3/s。Preferably, in step 2, the total flow rate of the gas is 20cm 3 /s-40cm 3 /s.
优选地,步骤2中,所述的功率为40w~80w。Preferably, in step 2, the power is 40w-80w.
优选地,步骤2中,所述的处理距离为20cm~80cm,更优选为40cm~60cm。Preferably, in step 2, the treatment distance is 20cm-80cm, more preferably 40cm-60cm.
优选地,步骤2中,所述的处理时间为40s~80s。Preferably, in step 2, the processing time is 40s-80s.
与现有技术相比,本发明具有以下显著优点:本发明采用甲烷和氮气混合气体等离子体处理的方法对PTFE微孔膜进行改性,改性后接触角可降至40°,显著改善了PTFE微孔膜的亲水性,同时维持了PTFE微孔膜优异的机械性能。本发明方法周期短、成本低廉,可进行商业化生产。Compared with the prior art, the present invention has the following significant advantages: the present invention uses methane and nitrogen mixed gas plasma treatment method to modify the PTFE microporous membrane, after modification, the contact angle can be reduced to 40°, significantly improving the The hydrophilicity of the PTFE microporous membrane maintains the excellent mechanical properties of the PTFE microporous membrane. The method of the invention has short period and low cost, and can be used for commercial production.
附图说明Description of drawings
图1是未处理的PTFE微孔膜(a)与等离子体处理后的PTFE微孔膜(b)的接触角图。Fig. 1 is the contact angle diagram of untreated PTFE microporous membrane (a) and plasma treated PTFE microporous membrane (b).
图2是等离子功率与PTFE微孔膜接触角的关系图。Fig. 2 is a relation diagram of plasma power and contact angle of PTFE microporous membrane.
图3是等离子处理时间与PTFE微孔膜接触角的关系图。Fig. 3 is a graph showing the relationship between the plasma treatment time and the contact angle of the PTFE microporous membrane.
图4是等离子体进气的比例与PTFE微孔膜接触角的关系图。Fig. 4 is a graph showing the relationship between the ratio of plasma gas inlet and the contact angle of PTFE microporous membrane.
图5是等离子处理进气的气体流量与PTFE微孔膜接触角的关系图。Fig. 5 is a graph showing the relationship between the gas flow rate of the plasma treatment inlet and the contact angle of the PTFE microporous membrane.
图6是等离子处理距离与PTFE微孔膜接触角的关系图。Fig. 6 is a graph showing the relationship between the plasma treatment distance and the contact angle of the PTFE microporous membrane.
图7是等离子处理后的PTFE微孔膜拉伸强度测试的结果图。Fig. 7 is a graph showing the results of the tensile strength test of the PTFE microporous membrane after plasma treatment.
具体实施方式detailed description
下面结合实施例和附图对本发明作进一步详细说明。The present invention will be described in further detail below in conjunction with the embodiments and accompanying drawings.
实施例1Example 1
PTFE微孔膜的预处理:Pretreatment of PTFE microporous membrane:
将PTFE微孔膜弄平整用两个A4纸夹着,放在平板切纸机下,切成若干个5×5cm的PTFE微孔膜,将切好的PTFE微孔膜浸没于丙酮溶液中,在通风橱中浸泡12~24h,然后在80%~98%的乙醇溶液中浸泡3~12h,多次更换乙醇溶液,除去丙酮,然后用去大量离子水多次清洗除去乙醇,最后放入到真空干燥箱中,在30~70℃的条件下干燥10~24h,将干燥好的PTFE微孔膜冷却至室温,然后将微孔膜放在玻璃板上固定,进行下一步等离子体改性。Flatten the PTFE microporous membrane with two A4 papers, place it under a flat paper cutter, cut into several 5×5cm PTFE microporous membranes, immerse the cut PTFE microporous membranes in acetone solution, Soak in a fume hood for 12-24 hours, then soak in 80%-98% ethanol solution for 3-12 hours, replace the ethanol solution several times, remove acetone, then wash with a large amount of ionized water to remove ethanol, and finally put it in In a vacuum drying oven, dry at 30-70°C for 10-24 hours, cool the dried PTFE microporous membrane to room temperature, and then fix the microporous membrane on a glass plate for the next step of plasma modification.
实施例2Example 2
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
先将预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,调节等离子处理距离为40cm,选择处理时间100s,气体流量选择20cm3/s,进气比例选择1:1,即甲烷和氮气的气体流量都为10cm3/s,控制等离子体功率,功率分别选择20w,40w,60w,80w,100w。First place the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the mixed gas of N 2 +CH 4 , adjust the plasma treatment distance to 40cm, select the treatment time to be 100s, and select the gas flow rate to be 20cm 3 /s. The gas ratio is selected as 1:1, that is, the gas flow rate of both methane and nitrogen is 10cm 3 /s, and the plasma power is controlled, and the power is respectively selected as 20w, 40w, 60w, 80w, and 100w.
将等离子体处理的PTFE微孔膜分别用JY-82接触角测定仪(承德市试验机厂)进行测量,分别取6点不同位置分别测量水的接触角,最后取其平均值。接触角与等离子体处理功率的关系图如图2所示。由图2可以知道,20w~100w时接触角在40°~60°之间。从等离子处理的功率20w到40w,接触角逐渐变小,到40w时接触角达到最小,接触角达到42.84°,40w到100w接触角开始逐渐变大。The plasma-treated PTFE microporous membrane was measured with a JY-82 contact angle measuring instrument (Chengde Testing Machine Factory) respectively, and the contact angle of water was measured at 6 different positions respectively, and finally the average value was taken. The relationship between contact angle and plasma treatment power is shown in Fig. 2 . It can be seen from Figure 2 that the contact angle is between 40° and 60° at 20w to 100w. From the plasma treatment power of 20w to 40w, the contact angle gradually decreases, and at 40w, the contact angle reaches the minimum, and the contact angle reaches 42.84°, and the contact angle begins to gradually increase from 40w to 100w.
实施例3Example 3
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
把预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,调节等离子处理距离为40cm,气体流量选择30cm3/s,进气比例选择1:1,即甲烷和氮气的气体流量都为10cm3/s,等离子处理的功率为40w,控制等离子处理时间,时间分别为20s,40s,60s,80s,100s。Put the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the mixed gas of N 2 +CH 4 , adjust the plasma treatment distance to 40cm, select the gas flow rate to be 30cm 3 /s, and select the gas inlet ratio to be 1:1 , that is, the gas flow rates of methane and nitrogen are both 10cm 3 /s, the power of plasma treatment is 40w, and the plasma treatment time is controlled, and the time is 20s, 40s, 60s, 80s, 100s respectively.
图1是未处理的PTFE微孔膜(a)与等离子体处理后的PTFE微孔膜(b)的接触角图。接触角与等离子体处理时间的关系图如图3所示。从图1可以看出,等离子处理前PTFE膜接触角为130°,最终处理后的接触角达到40°。从图3可知,在20s之前,随着处理时间的增加,接触角都是先迅速减小,在20s时到达最小,接触角为41.82°。20s到40s慢慢变大,40s之后就趋向于稳定。Fig. 1 is the contact angle diagram of untreated PTFE microporous membrane (a) and plasma treated PTFE microporous membrane (b). The relationship between contact angle and plasma treatment time is shown in Fig. 3. It can be seen from Figure 1 that the contact angle of PTFE film before plasma treatment is 130°, and the contact angle after final treatment reaches 40°. It can be seen from Figure 3 that before 20s, as the processing time increases, the contact angle decreases rapidly first, and reaches the minimum at 20s, and the contact angle is 41.82°. From 20s to 40s, it gradually increases, and after 40s, it tends to be stable.
实施例4Example 4
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
把预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,调节等离子处理距离为40cm,气体流量选择30cm3/s,处理功率40w,处理时间20s,控制进气比例,甲烷和氮气进气比例分别为3:1,2:1,1:1,1:2,1:3,即甲烷和氮气的进气量分别为22.5cm3/s和7.5cm3/s,20cm3/s和10cm3/s,15cm3/s和15cm3/s,10cm3/s和20cm3/s,7.5cm3/s和22.5cm3/s。Put the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the mixed gas of N 2 +CH 4 , adjust the plasma treatment distance to 40cm, select the gas flow rate to 30cm 3 /s, process power 40w, and process time 20s , to control the intake ratio, the intake ratios of methane and nitrogen are 3:1, 2:1, 1:1, 1:2, 1:3 respectively, that is, the intake volumes of methane and nitrogen are 22.5cm 3 /s and 7.5cm 3 /s, 20cm 3 /s and 10cm 3 /s, 15cm 3 /s and 15cm 3 /s, 10cm 3 /s and 20cm 3 /s, 7.5cm 3 /s and 22.5cm 3 /s.
接触角与进气比例的关系图如图4所示。从图4可以看出,接触角是一个先减小后增加的过程,在气体比例为1:1时,接触角达到了最小。The relationship between contact angle and intake ratio is shown in Fig. 4. It can be seen from Figure 4 that the contact angle is a process of first decreasing and then increasing. When the gas ratio is 1:1, the contact angle reaches the minimum.
实施例5Example 5
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
把预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,调节等离子处理距离为40cm,进气比例为1:1,等离子体处理时间为20s,等离子体处理功率为40w,控制气体流量,气体总流量分别为10cm3/s,20cm3/s,30cm3/s,40cm3/s,50cm3/s。Put the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the N 2 +CH 4 mixed gas, adjust the plasma treatment distance to 40cm, the gas inlet ratio to 1:1, and the plasma treatment time to 20s. The plasma processing power is 40w, and the gas flow is controlled. The total gas flow is 10cm 3 /s, 20cm 3 /s, 30cm 3 /s, 40cm 3 /s, 50cm 3 /s respectively.
接触角与气体总流量的关系图如图5所示。从图5可知,当等离子体的气体流量变化时,在一定的条件下,接触角随着气体流量的增大而逐渐减小,但当气体流量为20cm3/s,接触角到达最小为40.83°,随后接触角反而开始增大。The relationship between the contact angle and the total gas flow is shown in Figure 5. It can be seen from Figure 5 that when the gas flow rate of the plasma changes, under certain conditions, the contact angle gradually decreases with the increase of the gas flow rate, but when the gas flow rate is 20cm 3 /s, the contact angle reaches a minimum of 40.83 °, then the contact angle began to increase instead.
实施例6Example 6
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
把预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,调节进气比例为1:1,等离子体处理时间为20s,等离子体处理功率为40w,等离子处理气体流量为20cm3/s,控制等离子处理距离,等离子处理距离分别为1cm,20cm,40cm,60cm,80cm,100cm。Put the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the mixed gas of N 2 +CH 4 , adjust the intake ratio to 1:1, the plasma treatment time is 20s, and the plasma treatment power is 40w , the plasma treatment gas flow rate is 20cm 3 /s, and the plasma treatment distance is controlled. The plasma treatment distances are 1cm, 20cm, 40cm, 60cm, 80cm, and 100cm.
接触角与等离子处理距离的关系图如图6所示。从图6可知,等离子处理距离从1cm到40cm处接触角表现出先增加后减小的趋势,等离子处理距离40cm到100cm接触角逐渐变大,在40cm处接触角达到最小。The relationship between contact angle and plasma treatment distance is shown in Fig. 6. It can be seen from Figure 6 that the contact angle shows a trend of first increasing and then decreasing at the plasma treatment distance from 1cm to 40cm, the contact angle gradually increases from the plasma treatment distance of 40cm to 100cm, and the contact angle reaches the minimum at 40cm.
实施例7Example 7
PTFE微孔膜的预处理方法如实施例1。The pretreatment method of PTFE microporous membrane is as embodiment 1.
等离子体处理:Plasma treatment:
把预处理后的PTFE微孔膜放在等离子体高真空制备室中,在N2+CH4混合气体下,处理功率40w,气体比例为1:1,气体流量为20cm3/s,等离子处理距离为40cm的条件下,控制等离子体处理时间,20s,40s,60s,80s,100s进行等离子体处理。将处理好的PTFE微孔膜,取2cm×5cm的条状微孔膜,采用的拉伸强度仪器(深圳市新三思材料检测有限公司拉伸强度测试仪)进行拉伸强度测试。拉伸强度随等离子体处理时间的关系图,结果如图7所示。从图7可以看出,等离子体处理后,PTFE微孔膜的拉伸强度保持不变,说明本发明的改性方法对PTFE微孔膜的机械性能无影响。Put the pretreated PTFE microporous membrane in the plasma high-vacuum preparation chamber, under the mixed gas of N 2 +CH 4 , the processing power is 40w, the gas ratio is 1:1, the gas flow rate is 20cm 3 /s, and the plasma processing distance Under the condition of 40cm, control the plasma treatment time, 20s, 40s, 60s, 80s, 100s for plasma treatment. With the treated PTFE microporous membrane, get 2cm * 5cm strip microporous membrane, and adopt the tensile strength instrument (tensile strength tester of Shenzhen Xinsansi Material Testing Co., Ltd.) to carry out tensile strength test. The relationship between tensile strength and plasma treatment time is shown in Figure 7. As can be seen from Figure 7, after the plasma treatment, the tensile strength of the PTFE microporous membrane remains unchanged, indicating that the modification method of the present invention has no effect on the mechanical properties of the PTFE microporous membrane.
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