CN1036767C - A hydrogen permeable membrane and its preparation method - Google Patents
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 53
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 53
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 47
- 239000012528 membrane Substances 0.000 title claims abstract description 41
- 238000002360 preparation method Methods 0.000 title claims abstract description 17
- 239000000178 monomer Substances 0.000 claims abstract description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 12
- 238000006116 polymerization reaction Methods 0.000 claims abstract description 11
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- 239000004693 Polybenzimidazole Substances 0.000 claims abstract description 5
- 229920002480 polybenzimidazole Polymers 0.000 claims abstract description 5
- 150000001875 compounds Chemical class 0.000 claims abstract description 4
- 229910001220 stainless steel Inorganic materials 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 6
- 229920000642 polymer Polymers 0.000 claims description 6
- 125000003118 aryl group Chemical group 0.000 claims description 4
- 238000006068 polycondensation reaction Methods 0.000 claims description 4
- 239000002798 polar solvent Substances 0.000 claims description 3
- KAESVJOAVNADME-UHFFFAOYSA-N 1H-pyrrole Natural products C=1C=CNC=1 KAESVJOAVNADME-UHFFFAOYSA-N 0.000 claims description 2
- KSSJBGNOJJETTC-UHFFFAOYSA-N COC1=C(C=CC=C1)N(C1=CC=2C3(C4=CC(=CC=C4C=2C=C1)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)C1=CC(=CC=C1C=1C=CC(=CC=13)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)C1=CC=C(C=C1)OC Chemical compound COC1=C(C=CC=C1)N(C1=CC=2C3(C4=CC(=CC=C4C=2C=C1)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)C1=CC(=CC=C1C=1C=CC(=CC=13)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)N(C1=CC=C(C=C1)OC)C1=C(C=CC=C1)OC)C1=CC=C(C=C1)OC KSSJBGNOJJETTC-UHFFFAOYSA-N 0.000 claims description 2
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical group CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 2
- GTDPSWPPOUPBNX-UHFFFAOYSA-N ac1mqpva Chemical compound CC12C(=O)OC(=O)C1(C)C1(C)C2(C)C(=O)OC1=O GTDPSWPPOUPBNX-UHFFFAOYSA-N 0.000 claims description 2
- OLAPPGSPBNVTRF-UHFFFAOYSA-N naphthalene-1,4,5,8-tetracarboxylic acid Chemical compound C1=CC(C(O)=O)=C2C(C(=O)O)=CC=C(C(O)=O)C2=C1C(O)=O OLAPPGSPBNVTRF-UHFFFAOYSA-N 0.000 claims description 2
- 239000010935 stainless steel Substances 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims 2
- 239000011159 matrix material Substances 0.000 claims 1
- 230000035699 permeability Effects 0.000 abstract description 6
- 150000002431 hydrogen Chemical class 0.000 abstract description 5
- 125000006615 aromatic heterocyclic group Chemical group 0.000 abstract description 4
- 238000000926 separation method Methods 0.000 abstract description 3
- HNJBEVLQSNELDL-UHFFFAOYSA-N pyrrolidin-2-one Chemical compound O=C1CCCN1 HNJBEVLQSNELDL-UHFFFAOYSA-N 0.000 abstract description 2
- 239000002184 metal Substances 0.000 abstract 1
- 229920000620 organic polymer Polymers 0.000 abstract 1
- 230000002787 reinforcement Effects 0.000 abstract 1
- 239000010408 film Substances 0.000 description 18
- 239000007789 gas Substances 0.000 description 11
- 239000011248 coating agent Substances 0.000 description 7
- 238000000576 coating method Methods 0.000 description 7
- 239000011347 resin Substances 0.000 description 7
- 229920005989 resin Polymers 0.000 description 7
- 229930195733 hydrocarbon Natural products 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000010409 thin film Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001369 Brass Inorganic materials 0.000 description 1
- 239000011825 aerospace material Substances 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000003209 petroleum derivative Substances 0.000 description 1
- -1 pyrrole ketone Chemical class 0.000 description 1
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Abstract
一种具有高强度的选择性透氢膜及其制备方法,它是将聚苯并咪唑吡咯酮的预聚单体的溶液均匀地涂布在金属丝网上,在氮气的保护下经过聚合及高温固化,即制得用金属丝网增强的选择性高强度透氢膜。这种透氢膜与不用金属丝网增强的均质透氢膜有同样的氢选择性,但在机械强度、透氢率、成膜条件及成品的成功率等多方面都有很大的改善,因而使这种芳杂环有机高分子化合物透氢膜可扩大在膜分离技术领域中的应用。A high-strength selective hydrogen permeable membrane and its preparation method, which is to uniformly coat the solution of the pre-polymerized monomer of polybenzimidazole pyrrolidone on the wire mesh, and undergo polymerization and high temperature under the protection of nitrogen. Curing, that is, a selective high-strength hydrogen permeable membrane reinforced with a wire mesh is produced. This hydrogen permeable membrane has the same hydrogen selectivity as the homogeneous hydrogen permeable membrane without metal mesh reinforcement, but it has greatly improved in many aspects such as mechanical strength, hydrogen permeability rate, film forming conditions and the success rate of finished products. , so that the aromatic heterocyclic organic polymer compound hydrogen permeable membrane can expand the application in the field of membrane separation technology.
Description
本发明涉及一种高强度的选择性透氢膜及其制备方法,更确切地说,本发明是一种用金属丝网增强的选择性透氢膜及其制备方法,属于膜分离技术的领域。The invention relates to a high-strength selective hydrogen permeable membrane and a preparation method thereof, more precisely, the invention relates to a selective hydrogen permeable membrane reinforced with a wire mesh and a preparation method thereof, belonging to the field of membrane separation technology .
聚苯并咪唑吡咯酮(Polypyrrones)是由芳族四酸二酐和芳族四胺在极性溶剂中缩聚,并经过高温处理而得到的一种阶梯型芳杂环高分子化合物(卢凤才等,宇航材料工艺,第2期,15~18页,1984年)。用它制得的均质薄膜是一种对氢有较好选择性透过的富氢膜(卢凤才等,高分子学报,第5期,342~346页。1987年),由于这种均质薄膜的良好选择性,CN91217597.4实用新型专利用它作为选择性氢检测器的预分离器件。然而,由于以下不利因素的存在,这种均质膜的制备条件要求比较苛刻,难以批量生产:Polybenzimidazole pyrrole ketone (Polypyrrones) is a kind of stepped aromatic heterocyclic polymer compound obtained by polycondensation of aromatic tetraacid dianhydride and aromatic tetraamine in a polar solvent and treated at high temperature (Lu Fengcai et al., Aerospace Materials Technology, No. 2, pp. 15-18, 1984). The homogeneous membrane prepared by it is a hydrogen-rich membrane with good selective permeation to hydrogen (Lu Fengcai et al., Acta Polymer Sinica, No. 5, pp. 342-346. 1987), due to this homogeneous Good selectivity of thin film, CN91217597.4 utility model patent uses it as the pre-separation device of selective hydrogen detector. However, due to the existence of the following unfavorable factors, the preparation conditions of this homogeneous membrane are relatively harsh and difficult to produce in batches:
1、由于水份能使预聚单体水解并终止缩聚反应,成膜过程中要求严格控制环境湿度。1. Since water can hydrolyze the pre-polymerized monomer and terminate the polycondensation reaction, it is required to strictly control the environmental humidity during the film forming process.
2、成膜时预聚单体需要以一定的厚度均匀铺展在水平放置的平板上,进行初步聚合并除去溶剂(时间约需1.5~2小时),在这过程中,易受环境条件的干扰。此外,这种成品膜的均匀性也不易控制,常常是周边厚、中间薄,致使成膜的收率很低。2. When forming a film, the pre-polymerized monomer needs to be evenly spread on a flat plate with a certain thickness, and the initial polymerization is carried out and the solvent is removed (the time is about 1.5 to 2 hours). During this process, it is easily disturbed by environmental conditions. . In addition, the uniformity of the finished film is not easy to control, and it is often thick at the periphery and thin at the middle, resulting in a very low yield of film formation.
3、成膜越薄,氢的渗透率越好, 但为了保证得到的成品膜有足够的强度、膜又不能太薄,因此限制了进一步提高膜渗透率的这条途径。3. The thinner the film is, the better the hydrogen permeability is. However, in order to ensure that the finished film has sufficient strength and the film cannot be too thin, this way of further improving the film permeability is limited.
针对以上存在的实际问题,本发明的目的就是要提出一种以这种新的富氢材料为基体的膜及成膜方法,使其能更好地应用于实际。In view of the above practical problems, the purpose of the present invention is to propose a film and a film forming method based on this new hydrogen-rich material, so that it can be better applied in practice.
本发明是以一定浓度的聚苯并咪唑吡咯酮的预聚单体溶液,在一定的条件下,均匀地涂敷在金属丝网上,经过初步聚合及蒸除溶剂后,置于老化箱内,在氮气的保护下高温缩聚成用金属丝网增强的透氢膜。由于这种透氢膜是以依附在金属丝网上的高分子聚合物为基体,与单一的均质膜相比,其机械强度大为增加。此外,在制备时可以多次涂敷,因此透氢膜厚度的调节范围也比单一的均质膜宽得多,既可涂制厚膜,也可涂制超薄膜。这种透氢膜在制备时,其初聚过程所需要的时间仅是均质膜的三分之一或更短(10至25分钟)。在制备本发明透氢膜时,可最大限度地不受环境湿度的干扰。本发明所用的金属丝网有两个作用,一是作为膜的骨架,增加成品膜的强度,二是提供使有机高分子的预聚体能均匀分布的网孔,使成品膜的厚度均匀,因而避免了均质膜成膜时必然要发生的周边厚、中间薄的缺点。In the present invention, the pre-polymerized monomer solution of polybenzimidazole pyrrolidone with a certain concentration is evenly coated on the wire mesh under certain conditions, and after preliminary polymerization and evaporation of the solvent, it is placed in an aging box. Under the protection of nitrogen, high-temperature polycondensation forms a hydrogen permeable membrane reinforced with wire mesh. Since this hydrogen permeable membrane is based on a high molecular polymer attached to a wire mesh, compared with a single homogeneous membrane, its mechanical strength is greatly increased. In addition, it can be coated multiple times during preparation, so the adjustment range of the thickness of the hydrogen permeable membrane is much wider than that of a single homogeneous membrane, and it can be coated with thick films or ultra-thin films. When the hydrogen permeable membrane is prepared, the time required for the initial polymerization process is only one-third or shorter (10 to 25 minutes) than that of the homogeneous membrane. When preparing the hydrogen permeable membrane of the present invention, it can be freed from the interference of ambient humidity to the greatest extent. The wire mesh used in the present invention has two effects, the one, as the skeleton of film, increases the strength of finished film, the 2nd, provides the mesh that makes the prepolymer of organic macromolecule evenly distributed, makes the thickness of finished film uniform, thus It avoids the disadvantage that the periphery is thick and the middle is thin which inevitably occurs when the homogeneous film is formed.
本发明透氢膜制备示意见附图。在附图中,1是上滚筒,2是下滚筒,3、6是固定压轴,4是预聚单体溶液,5是金属丝网。制备方法步骤如下:The preparation of the hydrogen permeable membrane of the present invention is shown in the accompanying drawings. In the accompanying drawings, 1 is an upper drum, 2 is a lower drum, 3 and 6 are fixed pinches, 4 is a pre-polymerized monomer solution, and 5 is a wire mesh. The preparation method steps are as follows:
1、按照上述卢凤才等发表的方法,合成芳杂环高分子单体树脂。1. According to the above method published by Lu Fengcai et al., synthesize aromatic heterocyclic polymer monomer resin.
2、用N,N′-二甲基甲酰胺(水含量小于500ppm)将树脂稀释成浓度在3~15%(重),最好是5~8%(重)范围的溶液,密封备用。2. Dilute the resin with N,N'-dimethylformamide (water content is less than 500ppm) to a solution with a concentration of 3-15% (weight), preferably 5-8% (weight), and seal it for subsequent use.
3、将市售的金属丝网(300~800目),其材质如不锈钢、黄铜、镍等均可,以不锈钢较好,裁成长、宽适度的尺寸,用丙酮浸泡清洗,晾干待用。3. Cut the commercially available wire mesh (300-800 mesh), such as stainless steel, brass, nickel, etc., to a suitable length and width, soak it in acetone, and dry it to wait. use.
4、将上述的金属丝网在附图示意的涂布设备中装好,并调整滚筒1与两固定压轴3及6的间隙,至移动时松紧适合。4. Install the above-mentioned wire mesh in the coating equipment shown in the attached drawing, and adjust the gap between the roller 1 and the two
5、在涂布罐中加入适量的树脂溶液。5. Add an appropriate amount of resin solution into the coating tank.
6、以均速往复拉动金属丝网数次,使丝网孔为树脂溶液均匀涂布。6. Pull the wire mesh back and forth several times at an even speed, so that the mesh holes are evenly coated with resin solution.
7、用吹风机吹干涂布有树脂溶液的金属丝网。7. Use a hair dryer to dry the wire mesh coated with the resin solution.
8、将吹干的金属丝网放在一密封容器中,在氮气保护下升温至300℃,然后维持恒温2~3小时,使金属丝网表面涂布的芳杂环高分子单体树脂充分聚合固化成膜。8. Put the dried wire mesh in a sealed container, raise the temperature to 300°C under the protection of nitrogen, and then maintain a constant temperature for 2 to 3 hours, so that the aromatic heterocyclic polymer monomer resin coated on the surface of the wire mesh is fully Polymerization solidifies into a film.
9、将温度降至室温,即得到本发明金属丝网增强的选择性透氢膜。9. The temperature is lowered to room temperature, and the selective hydrogen permeable membrane reinforced by the wire mesh of the present invention is obtained.
在上述制备的过程中,第2、6、7步对透氢膜的厚度及均匀性有直接的影响。为保证涂层的均匀,第6、7两步在通常的情况下至少要重复操作两次。较低的树脂浓度、多次的涂布、吹干的过程对制成均匀涂布的透氢膜是关键的因素。由以下的实施例及透氧膜的使用性能数据可以看出,本发明金属丝网增强的选择性透氢膜对氢的选择性能及其它性能与均质膜相同,但机械强度及透氢率有显著的改善。In the above preparation process,
实施例1Example 1
预聚单体浓度为7.9%(重),325目不锈钢丝网,按上述制备方法涂布成膜,其中的6、7两步重复两次。用制得的透氢膜安装在CN9l217597.4实用新型专利的“氢含量检测器”上,以本发明的金属丝网增强透氢膜代替均质膜,热导检测器(TCD)桥流112mA,温度80℃,氮气为载气,流量30ml/分,金属丝网增强膜面积4.3cm2,温度80℃,样品气为北京市北分科学气体公司配制的氢和氮混和气,氢浓度为20.9%(体积)。Pre-polymerization monomer concentration is 7.9% (weight), 325 order stainless steel wire mesh, is coated into film by above-mentioned preparation method, wherein 6, 7 two steps are repeated twice. Install the obtained hydrogen permeable membrane on the "hydrogen content detector" of CN91217597.4 utility model patent, replace the homogeneous membrane with the wire mesh reinforced hydrogen permeable membrane of the present invention, and the thermal conductivity detector (TCD) bridge current 112mA , temperature 80°C, nitrogen as carrier gas, flow rate 30ml/min, wire mesh reinforced membrane area 4.3cm 2 , temperature 80°C, sample gas is hydrogen and nitrogen mixed gas prepared by Beijing Beifen Scientific Gas Company, hydrogen concentration is 20.9% (volume).
对氢的定量响应关系式为:Y=0.456XThe quantitative response relation to hydrogen is: Y=0.456X
式中:Y为响应信号,mV;In the formula: Y is the response signal, mV;
X为氢的体积百分浓度。X is the volume percent concentration of hydrogen.
以液化气为样品时,信号响应为0.82mV。When liquefied gas is used as a sample, the signal response is 0.82mV.
在同样条件下,厚度为30μ的均质透氢膜对氢的定量响应关系式为Y=0.167XUnder the same conditions, the quantitative response relationship of a homogeneous hydrogen permeable membrane with a thickness of 30μ to hydrogen is Y=0.167X
实施例2Example 2
预聚单体浓度为10%(重),325目不锈钢丝网,按上述制备方法涂布成膜,其中的6、7两步重复三次。在同样的氢含量检测器上测定。操作条件均和实施例1相同。Pre-polymerization monomer concentration is 10% (weight), 325 mesh stainless steel wire mesh, coating film-forming by the above-mentioned preparation method, wherein 6, 7 two steps are repeated three times. Measured on the same hydrogen content detector. Operating conditions are all identical with embodiment 1.
对氢的定量响应关系式为:Y=0.133XThe quantitative response relation to hydrogen is: Y=0.133X
以液化气为样品时,信号响应为0.04mVWhen using liquefied gas as a sample, the signal response is 0.04mV
实施例3Example 3
预聚单体浓度为5.4%(重),325目不锈钢丝岗,按上述制备方法涂布成膜,其中的6、7两步重复一次。其测定条件同实施例1。The concentration of pre-polymerization monomer is 5.4% (weight), 325 mesh stainless steel wire posts, coating film formation according to the above-mentioned preparation method, wherein 6, 7 two steps are repeated once. Its measuring condition is with embodiment 1.
对氢的定量响应关系式为:Y=2.21XThe quantitative response relation to hydrogen is: Y=2.21X
以液化气为样品时,信号响应为0.61mVWhen using liquefied gas as a sample, the signal response is 0.61mV
实施例4Example 4
预聚单体浓度为5.4%(重),325目不锈钢丝网,按上述制备方法涂布成膜,其中的6、7两步重复三次。其测定条件同实施例1。Pre-polymerization monomer concentration is 5.4% (weight), 325 mesh stainless steel wire mesh, coating film-forming by the above-mentioned preparation method, wherein 6, 7 two steps are repeated three times. Its measuring condition is with embodiment 1.
对氢的定量响应关系式为:Y=0.986XThe quantitative response relation to hydrogen is: Y=0.986X
实施例5Example 5
预聚单体浓度为5.0%(重),400目不锈钢丝网,按上述制备方法涂布成膜,其中的6、7两步重复六次,其测定条件同实施例1。Pre-polymerized monomer concentration is 5.0% (weight), 400 order stainless steel wire mesh, is coated film-forming by above-mentioned preparation method, wherein 6,7 two steps are repeated six times, and its measuring condition is with embodiment 1.
对氢的定量响应关系式为:Y=0.4XThe quantitative response relation to hydrogen is: Y=0.4X
以液化气为样品时,信号响应为0.72mVWhen using liquefied gas as a sample, the signal response is 0.72mV
实施例6Example 6
预聚单体浓度为5.0%(重),800目不锈钢丝网,按上述制备方法涂布成膜,其中的6、7两步重复三次,其测定条件同实施例1。Pre-polymerized monomer concentration is 5.0% (weight), 800 order stainless steel wire mesh, is coated film-forming by above-mentioned preparation method, wherein 6,7 two steps are repeated three times, and its measuring condition is with embodiment 1.
对氢的定量响应关系式为:Y=0.797XThe quantitative response relation to hydrogen is: Y=0.797X
以液化气为样品时,信号响应为0.91mVWhen using liquefied gas as a sample, the signal response is 0.91mV
在以上列举的实施例中, 对氢的定量响应关系Y=kX中的斜率k与透氢膜的透氢率有关,透氢率越大,相应的k值也就越大。而对石油液化气的响应值则反映了透氢膜对烃类气体(一般为C1~C5烃)的选择性。可以看出,所给例子中除个别情况外,对石油液化气的响应值均小于1%氢浓度气体的响应值。这样就说明了当这种透氢膜用于检测石油气中的氢含量时,烃组分的干扰是很小的。In the examples listed above, the slope k in the quantitative response relationship to hydrogen Y=kX is related to the hydrogen permeability rate of the hydrogen permeable membrane, and the greater the hydrogen permeability rate, the greater the corresponding k value. The response value to petroleum liquefied gas reflects the selectivity of the hydrogen permeable membrane to hydrocarbon gases (generally C 1 -C 5 hydrocarbons). It can be seen that in the examples given, except for individual cases, the response value to liquefied petroleum gas is lower than that of gas with 1% hydrogen concentration. This shows that when this hydrogen permeable membrane is used to detect the hydrogen content in petroleum gas, the interference of hydrocarbon components is very small.
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| CN93108889A CN1036767C (en) | 1993-07-29 | 1993-07-29 | A hydrogen permeable membrane and its preparation method |
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| Publication Number | Publication Date |
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| CN1098024A CN1098024A (en) | 1995-02-01 |
| CN1036767C true CN1036767C (en) | 1997-12-24 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN93108889A Expired - Fee Related CN1036767C (en) | 1993-07-29 | 1993-07-29 | A hydrogen permeable membrane and its preparation method |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4337154A (en) * | 1979-04-04 | 1982-06-29 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Crosslinked composite semipermeable membrane |
| US5262056A (en) * | 1992-11-30 | 1993-11-16 | Board Of Regents, The University Of Texas System | Polyamides and polypyrrolones for fluid separation membranes |
-
1993
- 1993-07-29 CN CN93108889A patent/CN1036767C/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4337154A (en) * | 1979-04-04 | 1982-06-29 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Crosslinked composite semipermeable membrane |
| US5262056A (en) * | 1992-11-30 | 1993-11-16 | Board Of Regents, The University Of Texas System | Polyamides and polypyrrolones for fluid separation membranes |
Non-Patent Citations (1)
| Title |
|---|
| 高分子学报,[5] 1987.1.1 卢凤才等 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1098024A (en) | 1995-02-01 |
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