CN1640527A - Preparation method of filter membrane of palladium-based alloy/aperture gradient titanium-aluminum intermetallic compound homogeneous support body for hydrogen separation - Google Patents
Preparation method of filter membrane of palladium-based alloy/aperture gradient titanium-aluminum intermetallic compound homogeneous support body for hydrogen separation Download PDFInfo
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- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 title claims abstract description 52
- 239000012528 membrane Substances 0.000 title claims abstract description 46
- 229910000765 intermetallic Inorganic materials 0.000 title claims abstract description 36
- 229910045601 alloy Inorganic materials 0.000 title claims abstract description 30
- 239000000956 alloy Substances 0.000 title claims abstract description 30
- 229910052763 palladium Inorganic materials 0.000 title claims abstract description 26
- 239000001257 hydrogen Substances 0.000 title claims abstract description 25
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 25
- 238000000926 separation method Methods 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- 125000004435 hydrogen atom Chemical class [H]* 0.000 title abstract 2
- UQZIWOQVLUASCR-UHFFFAOYSA-N alumane;titanium Chemical compound [AlH3].[Ti] UQZIWOQVLUASCR-UHFFFAOYSA-N 0.000 title description 2
- 238000006243 chemical reaction Methods 0.000 claims abstract description 44
- 229910010038 TiAl Inorganic materials 0.000 claims abstract description 39
- 239000000843 powder Substances 0.000 claims abstract description 31
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 24
- 238000005240 physical vapour deposition Methods 0.000 claims abstract description 23
- 239000002131 composite material Substances 0.000 claims abstract description 13
- 238000005245 sintering Methods 0.000 claims abstract description 13
- 239000007788 liquid Substances 0.000 claims abstract description 10
- 230000007797 corrosion Effects 0.000 claims abstract description 8
- 238000005260 corrosion Methods 0.000 claims abstract description 8
- 238000000465 moulding Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 18
- 238000001816 cooling Methods 0.000 claims description 16
- 150000002431 hydrogen Chemical class 0.000 claims description 16
- 239000002245 particle Substances 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 13
- 150000001875 compounds Chemical class 0.000 claims description 11
- 230000008569 process Effects 0.000 claims description 11
- 238000002156 mixing Methods 0.000 claims description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 238000001914 filtration Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 239000011812 mixed powder Substances 0.000 claims description 3
- 230000008595 infiltration Effects 0.000 claims 10
- 238000001764 infiltration Methods 0.000 claims 10
- 230000014759 maintenance of location Effects 0.000 claims 8
- 238000007493 shaping process Methods 0.000 claims 8
- 229910004349 Ti-Al Inorganic materials 0.000 claims 6
- 229910004692 Ti—Al Inorganic materials 0.000 claims 6
- 238000005056 compaction Methods 0.000 claims 6
- 238000003825 pressing Methods 0.000 claims 4
- 230000003026 anti-oxygenic effect Effects 0.000 claims 2
- 230000000704 physical effect Effects 0.000 claims 1
- 238000010189 synthetic method Methods 0.000 claims 1
- 239000011148 porous material Substances 0.000 abstract description 16
- 239000011888 foil Substances 0.000 abstract description 12
- 238000009694 cold isostatic pressing Methods 0.000 abstract description 8
- 238000007654 immersion Methods 0.000 abstract description 6
- 239000003795 chemical substances by application Substances 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 238000005229 chemical vapour deposition Methods 0.000 abstract description 3
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 230000004907 flux Effects 0.000 abstract description 3
- 238000001471 micro-filtration Methods 0.000 abstract description 3
- 239000000126 substance Substances 0.000 abstract description 3
- 238000005374 membrane filtration Methods 0.000 abstract description 2
- 238000001728 nano-filtration Methods 0.000 abstract description 2
- 238000001308 synthesis method Methods 0.000 abstract description 2
- 239000003963 antioxidant agent Substances 0.000 abstract 1
- 230000003078 antioxidant effect Effects 0.000 abstract 1
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000000919 ceramic Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000001513 hot isostatic pressing Methods 0.000 description 2
- 238000003754 machining Methods 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000001272 pressureless sintering Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 230000007123 defense Effects 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000012982 microporous membrane Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 238000005191 phase separation Methods 0.000 description 1
- 231100000572 poisoning Toxicity 0.000 description 1
- 230000000607 poisoning effect Effects 0.000 description 1
- 238000004663 powder metallurgy Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
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Abstract
本发明涉及半渗透膜的生产,用于分离工艺的半透膜的专用制备方法。它通过模压或冷等静压,将Ti、Al元素粉末直接与Ti箔或Al箔复合成形片状或管状坯,或者先通过模压或冷等静压将Ti、Al元素粉末成形为片状坯或管状坯,然后通过Al液表面熔浸的方式制成复合成形坯;再通过低温预反应和高温短时反应两阶段真空烧结合成法,制备TiAl金属间化合物孔径梯度均质支撑体,随后,在其表面,采用化学或物理气相沉积(CVD或PVD)的方式,均匀镀上一层钯基合金膜,厚度为5~50μm。由此制得的膜具有良好的抗氧化性能、抗腐蚀性能和力学性能,提高了氢分离膜的渗透通量和使用寿命;其TiAl支撑体还可直接用作性能优异的微滤膜和纳滤膜。本发明制备过程不需要添加造孔剂,降低了能耗,几乎无污染。The invention relates to the production of semi-permeable membranes, and a special preparation method for semi-permeable membranes used in separation processes. It directly forms a sheet or tubular blank by molding or cold isostatic pressing Ti and Al element powders with Ti foil or Al foil, or first forms a sheet or tubular blank by molding or cold isostatic pressing Ti and Al element powders, and then forms a composite blank by Al liquid surface immersion; then prepares a TiAl intermetallic compound pore size gradient homogeneous support body by a two-stage vacuum sintering synthesis method of low-temperature pre-reaction and high-temperature short-time reaction, and then uniformly plates a layer of palladium-based alloy film on its surface by chemical or physical vapor deposition (CVD or PVD), with a thickness of 5 to 50 μm. The membrane prepared in this way has good antioxidant performance, corrosion resistance and mechanical properties, and improves the permeation flux and service life of the hydrogen separation membrane; its TiAl support body can also be directly used as a microfiltration membrane and nanofiltration membrane with excellent performance. The preparation process of the invention does not require the addition of a pore-forming agent, reduces energy consumption, and is almost pollution-free.
Description
技术领域:Technical field:
本发明涉及半渗透膜的生产,用于分离工艺的半透膜的专用制备方法,制备氢分离钯基合金与孔径梯度TiAl金属间化合物均质支撑体的过滤膜的制备方法。The invention relates to the production of a semi-permeable membrane, a special preparation method for the semi-permeable membrane used in a separation process, and a preparation method for preparing a filter membrane of a hydrogen separation palladium-based alloy and a TiAl intermetallic compound homogeneous support body with a pore size gradient.
背景技术:Background technique:
膜分离技术是借助于外界能量或化学位差的推动,对两组分或多组分混合的气体或液体进行分离、分级、提纯和富集,过程中大多无相变化,具有高效、节能、工艺简便、投资少、污染小等优点,广泛应用于国民经济各生产、研究部门以及国防建设领域。在气体膜分离领域中,应用最为广泛的是氢气的分离和回收。目前用于氢分离的无机膜以金属钯、银及其合金膜为主,按结构可分为非支撑膜和支撑膜。支撑体的引入,实现了钯膜的薄化,减少了钯的用量,降低了成本,提高了膜的透量,并保持了金属膜的耐高温和机械强度大等特点。Membrane separation technology is driven by external energy or chemical potential difference to separate, classify, purify and enrich the gas or liquid mixed with two or more components. Most of the process has no phase change, and it has high efficiency, energy saving, With the advantages of simple process, less investment and less pollution, it is widely used in various production and research departments of the national economy and in the field of national defense construction. In the field of gas membrane separation, the most widely used is the separation and recovery of hydrogen. At present, the inorganic membranes used for hydrogen separation are mainly metal palladium, silver and their alloy membranes, which can be divided into unsupported membranes and supported membranes according to their structures. The introduction of the support realizes the thinning of the palladium film, reduces the amount of palladium, reduces the cost, improves the permeability of the film, and maintains the high temperature resistance and high mechanical strength of the metal film.
目前氢分离用支撑体所用材料主要有:陶瓷体,如氧化铝和玻璃,以及铜、镍和不锈钢等金属。所采用的制备方法主要有:固态粒子烧结法制备载体及过渡膜;溶胶-凝胶法制备超滤、微滤膜;分相法制备玻璃膜;采用化学气相沉积、无电镀等制备微孔膜,这些方法工艺复杂,成本较高,过滤膜孔径难以控制;存在材料与钯膜的热膨胀系数不匹配,支撑体表面的非均匀活化,金属的氢脆,陶瓷的脆而不易焊接组件化等缺点。At present, the materials used for the support body for hydrogen separation mainly include: ceramic bodies, such as alumina and glass, and metals such as copper, nickel and stainless steel. The preparation methods used mainly include: preparation of carrier and transition membrane by solid particle sintering method; preparation of ultrafiltration and microfiltration membrane by sol-gel method; preparation of glass membrane by phase separation method; preparation of microporous membrane by chemical vapor deposition and electroless plating. , these methods are complex in process, high in cost, and difficult to control the pore size of the filter membrane; there are disadvantages such as the thermal expansion coefficient mismatch between the material and the palladium membrane, the non-uniform activation of the support surface, the hydrogen embrittlement of the metal, and the brittleness of the ceramic, which makes it difficult to weld and assemble. .
发明内容:Invention content:
本发明旨在提高氢分离膜的抗氧化性能、抗腐蚀性能和力学性能,提高氢分离膜的渗透通量,延长其使用寿命,降低成本,总之,本发明能够制备无裂缝、不脱落、均匀的致密复合膜,而且其制备工艺流程简便,能耗低,污染减少。The invention aims to improve the oxidation resistance, corrosion resistance and mechanical properties of the hydrogen separation membrane, increase the permeation flux of the hydrogen separation membrane, prolong its service life, and reduce the cost. The dense composite membrane, and its preparation process is simple, low energy consumption, and pollution reduction.
本发明采用以下方案:The present invention adopts following scheme:
向氢分离用钯基合金膜支撑体中引入物理性能及力学性能优异的TiAl金属间化合物,以制备氢分离用钯基合金/孔径梯度钛铝金属间化合物均质支撑体的过滤膜的方法,其特征在于:Introducing a TiAl intermetallic compound with excellent physical and mechanical properties into a palladium-based alloy membrane support for hydrogen separation to prepare a filter membrane for a homogeneous support of a palladium-based alloy/aperture gradient titanium-aluminum intermetallic compound for hydrogen separation, It is characterized by:
A.混料:A. Mixture:
以粒径200~10μm的Ti粉,粒径200~5μm的Al粉,按照50~60at.%Ti,40~50at.%Al的成分配比进行均匀混合。The Ti powder with a particle size of 200-10 μm and the Al powder with a particle size of 200-5 μm are uniformly mixed according to the composition distribution ratio of 50-60 at.% Ti and 40-50 at.% Al.
B.复合成形:B. Composite forming:
①采用模压成形或冷等静压成形的方式,将Ti、Al元素粉末直接与Ti箔或Al箔复合成形,制成片状或管状坯。具体过程为:将Ti箔或Al箔置于普通模压机的冲头端部,并与Ti、Al元素混合粉末直接接触,通过模压成形制得片状坯,模压压强为50~600MPa;或者采用冷等静压成形方式,压强为50~200MPa,芯杆成一定锥度,锥度为0.1~2°,将Ti箔或Al箔置于芯杆外侧并与之紧密接触,同时与Ti、Al元素混合粉末直接接触,通过冷等静压成形方式制得管状坯,Ti箔或Al箔的厚度为10~50μm,脱模后对冷等静压坯外径进行少量机加工,制成外径均匀,内径略成锥度,厚度为1~3mm的管状成形坯。①Using compression molding or cold isostatic pressing, the Ti and Al element powders are directly compounded with Ti foil or Al foil to form a sheet or tubular blank. The specific process is as follows: put Ti foil or Al foil at the end of the punch of a common molding machine, and directly contact with the mixed powder of Ti and Al elements, and form a sheet blank by molding, and the molding pressure is 50-600MPa; or use Cold isostatic pressing method, the pressure is 50-200MPa, the core rod forms a certain taper, the taper is 0.1-2°, the Ti foil or Al foil is placed on the outside of the core rod and in close contact with it, and it is mixed with Ti and Al elements at the same time The powder is in direct contact, and the tubular billet is made by cold isostatic pressing. The thickness of the Ti foil or Al foil is 10-50 μm. A tubular shaped blank with a slightly tapered inner diameter and a thickness of 1 to 3 mm.
②或者先将Ti、Al元素粉末模压成形或冷等静压成形为片状或管状坯,然后通过Al液表面熔浸的方式制成复合成形坯,Al液表面熔浸温度为670~900℃,熔浸时间为0.1~10min,熔浸层厚度为0.01~0.5mm。② Or first mold Ti, Al element powder or cold isostatic pressing into a sheet or tubular billet, and then make a composite billet by immersing the surface of Al liquid. The surface immersion temperature of Al liquid is 670-900 °C , the immersion time is 0.1-10min, and the thickness of the immersion layer is 0.01-0.5mm.
C.反应合成:C. Reactive synthesis:
通过低温预反应和高温短时反应两阶段真空烧结合成法,制备TiAl金属间化合物孔径梯度均质过滤膜,采用真空无压烧结时,真空度为1×10-1~1×10-3Pa,低温预反应阶段的温度为500~800℃,时间为20~60分钟;高温短时反应阶段的温度为1200~1400℃,时间为10~30分钟;冷却阶段,控制降温速度为10~50℃/min。Through the two-stage vacuum sintering synthesis method of low-temperature pre-reaction and high-temperature short-term reaction, TiAl intermetallic compound pore size gradient homogeneous filtration membrane is prepared. When vacuum pressureless sintering is used, the vacuum degree is 1×10 -1 ~ 1×10 -3 Pa , the temperature in the low-temperature pre-reaction stage is 500-800°C, and the time is 20-60 minutes; the temperature in the high-temperature short-term reaction stage is 1200-1400°C, and the time is 10-30 minutes; in the cooling stage, the cooling rate is controlled to be 10-50 °C/min.
或者通过低压热等静压进行反应合成,压强为0.01~5MPa,低温预反应阶段的温度为500~800℃,时间为20~40分钟;高温短时反应阶段的温度为1200~1300℃,时间为10~20分钟;冷却阶段,控制降温速度为10~50℃/min。Or carry out reaction synthesis by low-pressure hot isostatic pressing, the pressure is 0.01-5MPa, the temperature of the low-temperature pre-reaction stage is 500-800°C, and the time is 20-40 minutes; the temperature of the high-temperature short-time reaction stage is 1200-1300°C, and the time is 10 to 20 minutes; in the cooling stage, control the cooling rate to 10 to 50°C/min.
获得孔径梯度TiAl金属间化合物均质支撑体。A pore size gradient TiAl intermetallic compound homogeneous support is obtained.
D.TiAl金属间化合物均质支撑体表面,采用化学或物理气相沉积(CVD或PVD)的方法,均匀镀上一层钯基合金膜,厚度为5~50μm,组合成氢分离用钯基合金/孔径梯度TiAl金属间化合物均质支撑体的过滤膜。D. The surface of the homogeneous support body of TiAl intermetallic compound is uniformly coated with a layer of palladium-based alloy film by chemical or physical vapor deposition (CVD or PVD), with a thickness of 5-50 μm, and combined into a palladium-based alloy for hydrogen separation /Filtration membrane of gradient TiAl intermetallic compound homogeneous support.
本发明与现有技术相比,具有以下优点:Compared with the prior art, the present invention has the following advantages:
1.由于TiAl金属间化合物作为轻质高温结构材料,具有优良的力学性能,耐酸碱腐蚀性能和抗氧化性能,其抗氧化极限可达800~950℃,采用它制备氢分离钯基合金膜用支撑体,大幅度改善了氢分离膜的抗氧化性能、抗腐蚀性能和力学性能,提高了氢分离膜的渗透通量,延长了使用寿命,并降低了生产成本。此外,缘于TiAl金属间化合物的热膨胀系数为1.1~1.4(10-5/K(0~600℃)),与金属钯的热膨胀系数1.176(10-5/K)匹配,有利于TiAl金属间化合物孔径梯度均质支撑体与钯基合金膜的复合。1. Since TiAl intermetallic compound is a lightweight high-temperature structural material, it has excellent mechanical properties, acid and alkali corrosion resistance and oxidation resistance, and its oxidation resistance limit can reach 800-950 ° C. It is used to prepare palladium-based alloy membranes for hydrogen separation By using the support body, the oxidation resistance, corrosion resistance and mechanical properties of the hydrogen separation membrane are greatly improved, the permeation flux of the hydrogen separation membrane is improved, the service life is prolonged, and the production cost is reduced. In addition, due to the thermal expansion coefficient of TiAl intermetallic compounds is 1.1~1.4 (10 -5 /K (0 ~ 600 ℃)), which matches the thermal expansion coefficient of metal palladium 1.176 (10 -5 /K), which is beneficial to TiAl intermetallic Composite compound pore size gradient homogeneous support and palladium-based alloy membrane.
2.本发明采用TiAl金属间化合物制备孔径梯度均质过滤膜,有利于控制膜的孔径分布。采用Ti、Al元素粉末制备过滤膜的造孔机制是Al元素偏扩散引起Kirkendall效应。除了粉末冶金工艺本身带来一定量的孔隙外,Kirkendall效应可造成TiAl合金20~30%的开孔率,通过控制工艺条件:例如Ti、Al粉末粒度配比和成分配比,反应合成的温度和保温时间等,能够得到孔径精确控制的通孔。2. The present invention adopts TiAl intermetallic compound to prepare pore size gradient homogeneous filtration membrane, which is beneficial to control the pore size distribution of the membrane. The pore-forming mechanism of the filter membrane prepared by using Ti and Al element powders is the Kirkendall effect caused by partial diffusion of Al elements. In addition to a certain amount of porosity brought by the powder metallurgy process itself, the Kirkendall effect can cause a 20-30% porosity of the TiAl alloy. By controlling the process conditions: such as Ti, Al powder particle size ratio and composition ratio, reaction synthesis temperature and holding time, etc., can obtain through holes with precisely controlled pore diameters.
3.本发明的Ti、Al元素粉末复合成形和反应合成,制备氢分离用钯基合金TiAl金属间化合物孔径梯度均质支撑体,由于Al元素偏扩散所引起Kirkendall效应,在支撑体中可形成孔径由非复合端的1~10μm到复合端的0.01~0.5μm的孔径梯度,通过控制复合工艺条件和烧结工艺条件能够控制材料的孔径梯度状况,因此,TiAl金属间化合物孔径梯度均质过滤膜,也可以直接用作性能优异的微滤膜和纳滤膜。3. The compound forming and reaction synthesis of Ti and Al element powders of the present invention are used to prepare palladium-based alloy TiAl intermetallic compound pore size gradient homogeneous supports for hydrogen separation. Due to the Kirkendall effect caused by partial diffusion of Al elements, it can form in the supports. The pore size gradient is from 1-10 μm at the non-composite end to 0.01-0.5 μm at the composite end. The pore size gradient of the material can be controlled by controlling the composite process conditions and sintering process conditions. Therefore, the TiAl intermetallic compound pore size gradient homogeneous filter membrane is also It can be directly used as microfiltration membrane and nanofiltration membrane with excellent performance.
4.本发明的Ti、Al元素粉末复合成形和反应合成,制备氢分离用钯基合金TiAl金属间化合物孔径梯度均质支撑体过程中,不需要添加造孔剂即可获得40~50%的孔隙率,避免了传统工艺中的脱除造孔剂环节,降低了能耗,而且几乎无污染。4. In the compound forming and reaction synthesis of Ti and Al element powders of the present invention, in the process of preparing palladium-based alloy TiAl intermetallic compound pore size gradient homogeneous support for hydrogen separation, 40-50% of the pore-forming agent can be obtained without adding pore-forming agents. Porosity avoids the removal of pore-forming agents in the traditional process, reduces energy consumption, and is almost pollution-free.
5.本发明成分配比的TiAl金属间化合物在1300℃以下具有高的显微组织和晶粒尺寸稳定性,保证了TiAl无机膜的使用稳定性,并且有效的防止了钯膜的中毒;此外,TiAl金属间化合物的可焊接性能还可很好地解决陶瓷和玻璃在高温环境下难密封的问题。5. The TiAl intermetallic compound with the composition ratio of the present invention has high microstructure and grain size stability below 1300°C, which ensures the stability of the TiAl inorganic film in use and effectively prevents the poisoning of the palladium film; in addition , The weldability of TiAl intermetallic compounds can also well solve the problem of difficult sealing of ceramics and glass in high temperature environments.
具体实施方式:Detailed ways:
实施例1Example 1
采用粒度为100~150μm的Ti粉和粒度为50~100μm的Al粉,按Ti-46.5at.%Al的成分配比进行混料;随后在200MPa的压力下模压成形,同时将Al箔置于普通模压机的冲头端部,制成直径为50mm,厚1~2mm的复合片状坯;采用真空无压烧结进行反应合成,真空度控制在1×10-2~1×10-3Pa;低温预反应温度为600℃,保温时间为60min;高温短时反应温度为1300℃,保温时间为20min;反应完毕后冷却速度控制在40℃/min;由此制备的TiAl金属间化合物孔径梯度均质片状支撑体,孔隙率为40~45%,开孔率为30~35%,同时具有良好的抗氧化性能和抗腐蚀性能。随后,在所制备的TiAl金属间化合物支撑体表面,采用物理气相沉积(PVD)的方式,均匀镀上一层钯基合金膜,厚度为10μm。Ti powder with a particle size of 100-150 μm and Al powder with a particle size of 50-100 μm are used for mixing according to the composition ratio of Ti-46.5at.% Al; then molded under a pressure of 200 MPa, and the Al foil is placed in the The end of the punch of an ordinary molding machine is made into a composite sheet blank with a diameter of 50 mm and a thickness of 1 to 2 mm; the reaction is synthesized by vacuum pressureless sintering, and the vacuum degree is controlled at 1×10 -2 to 1×10 -3 Pa The low-temperature pre-reaction temperature is 600°C, and the holding time is 60min; the high-temperature short-term reaction temperature is 1300°C, and the holding time is 20min; the cooling rate is controlled at 40°C/min after the reaction; The homogeneous flaky support body has a porosity of 40-45%, an open porosity of 30-35%, and has good oxidation resistance and corrosion resistance. Subsequently, on the surface of the prepared TiAl intermetallic compound support, a layer of palladium-based alloy film was uniformly plated with a thickness of 10 μm by means of physical vapor deposition (PVD).
实施例2Example 2
采用粒度为20~50μm的Ti粉和粒度为50~100μm的Al粉,按Ti-48at.%Al的成分配比进行混料;随后采用冷等静压成形管状坯,将Al箔紧贴于芯杆外侧,芯杆锥度为0.5°,压强为150MPa;经少量机加工后,制得外径为30mm,内径为28~29mm,高为200mm的复合管状成形坯;烧结气氛为真空,真空度控制在1×10-2~1×10-3Pa;低温预反应温度为620℃,保温时间为40min;高温短时反应温度为1260℃,保温时间为30min;反应完毕后冷却速度控制在30℃/min;由此制得渗透性能良好的TiAl金属间化合物孔径梯度均质管状支撑体。随后,在所制备的TiAl金属间化合物支撑体表面,采用物理气相沉积(PVD)的方式,均匀镀上一层钯基合金膜,厚度为15μm。Ti powder with a particle size of 20-50 μm and Al powder with a particle size of 50-100 μm are used for mixing according to the composition ratio of Ti-48at.% Al; then cold isostatic pressing is used to form a tubular billet, and the Al foil is closely attached to the On the outside of the core rod, the taper of the core rod is 0.5°, and the pressure is 150MPa; after a small amount of machining, a composite tubular forming blank with an outer diameter of 30mm, an inner diameter of 28-29mm, and a height of 200mm is obtained; the sintering atmosphere is vacuum, and the vacuum degree Control at 1×10 -2 ~ 1×10 -3 Pa; low-temperature pre-reaction temperature is 620°C, holding time is 40min; high-temperature short-term reaction temperature is 1260°C, holding time is 30min; after the reaction is completed, the cooling rate is controlled at 30 °C/min; thus, a TiAl intermetallic compound pore size gradient homogeneous tubular support with good permeability is prepared. Subsequently, a layer of palladium-based alloy film was evenly plated on the surface of the prepared TiAl intermetallic compound support body by physical vapor deposition (PVD), with a thickness of 15 μm.
实施例3Example 3
采用粒度为150~200μm的Ti粉和粒度为20~50μm的Al粉,按Ti-48.5at.%Al的成分配比进行混料;在200MPa的压力下模压成形,制成直径为50mm,厚1~2mm的片状坯,随后采用Al液表面熔浸的方式制成复合成形坯,熔浸温度为700℃,熔浸时间为2min;烧结采用低压热等静压,气氛Ar气,压强为0.1MPa,低温预反应温度为620℃,保温时间为40min;高温短时反应温度为1300℃,保温时间为10min。反应完毕后冷却速度控制在20℃/min;由此制备的TiAl金属间化合物孔径梯度均质片状支撑体,孔隙率为35~40%,开孔率为25~35%,同时具有良好的抗氧化性能和抗腐蚀性能。随后,在所制备的TiAl金属间化合物支撑体表面,采用物理气相沉积(PVD)的方式,均匀镀上一层钯基合金膜,厚度为25μm。Ti powder with a particle size of 150-200μm and Al powder with a particle size of 20-50μm are used for mixing according to the composition ratio of Ti-48.5at.%Al; molded under a pressure of 200MPa to make a diameter of 50mm and a thickness of The 1-2mm flake billet is then made into a composite billet by immersing the surface of Al liquid, the immersion temperature is 700°C, and the immersion time is 2min; the sintering adopts low-pressure hot isostatic pressing, the atmosphere is Ar gas, and the pressure is 0.1MPa, the low-temperature pre-reaction temperature is 620°C, and the holding time is 40min; the high-temperature short-time reaction temperature is 1300°C, and the holding time is 10min. After the reaction is completed, the cooling rate is controlled at 20°C/min; the thus prepared TiAl intermetallic compound pore size gradient homogeneous sheet-like support has a porosity of 35-40%, an open porosity of 25-35%, and a good Oxidation resistance and corrosion resistance. Subsequently, a layer of palladium-based alloy film was evenly plated on the surface of the prepared TiAl intermetallic compound support by physical vapor deposition (PVD), with a thickness of 25 μm.
实施例4Example 4
采用粒度为10~40μm的Ti粉和粒度为10~40μm的Al粉,按Ti-47at.%Al的成分配比进行混料;采用冷等静压成形管状坯,芯杆锥度为1°,压强为150MPa;经少量机加工后,制得外径为40mm,内径为37.5~38.5mm,高为220mm的管状成形坯;随后采用对管状坯外径表面进行Al液熔浸的方式制成复合成形坯,管状坯的旋转速度为0.25rpm,熔浸温度为720℃,熔浸时间为4min;烧结气氛为真空,真空度控制在1×10-2~1×10-3Pa;低温预反应温度为630℃,保温时间为30min;高温短时反应温度为1300℃,保温时间为15min;反应完毕后冷却速度控制在30℃/min;由此制得渗透性能良好的TiAl金属间化合物孔径梯度均质管状支撑体。随后,在所制备的TiAl金属间化合物支撑体表面,采用物理气相沉积(PVD)的方式,均匀镀上一层钯基合金膜,厚度为20μm。Ti powder with a particle size of 10-40 μm and Al powder with a particle size of 10-40 μm are used for mixing according to the composition ratio of Ti-47at.% Al; cold isostatic pressing is used to form a tubular billet, and the taper of the core rod is 1°. The pressure is 150MPa; after a small amount of machining, a tubular forming blank with an outer diameter of 40mm, an inner diameter of 37.5-38.5mm, and a height of 220mm is produced; then the surface of the outer diameter of the tubular blank is immersed in Al liquid to make a composite Formed billet, the rotation speed of the tubular billet is 0.25rpm, the melting temperature is 720°C, and the melting time is 4min; the sintering atmosphere is vacuum, and the vacuum degree is controlled at 1×10 -2 ~ 1×10 -3 Pa; low temperature pre-reaction The temperature is 630°C, and the holding time is 30 minutes; the high-temperature short-term reaction temperature is 1300°C, and the holding time is 15 minutes; after the reaction is completed, the cooling rate is controlled at 30°C/min; thus, a TiAl intermetallic compound with a good permeability gradient is obtained. Homogeneous tubular support. Subsequently, a layer of palladium-based alloy film was evenly plated on the surface of the prepared TiAl intermetallic compound support by physical vapor deposition (PVD), with a thickness of 20 μm.
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| CN101985084A (en) * | 2010-11-18 | 2011-03-16 | 南京工业大学 | Preparation method of ceramic Ti-Al alloy composite membrane |
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| CN102574074A (en) * | 2009-09-14 | 2012-07-11 | 东京瓦斯株式会社 | Hydrogen separation membrane and hydrogen separation method |
| CN103657434A (en) * | 2012-09-12 | 2014-03-26 | 中国科学院大连化学物理研究所 | Palladium-based membrane with surface covered by molecular sieve membrane and preparation method thereof |
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| CN1059191C (en) * | 1996-05-08 | 2000-12-06 | 中国科学院大连化学物理研究所 | Palladium-ceramic composite film and nitrogen rich film coupling making catalytic dehydrogenation reaction |
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