JP2003326138A - End sealing method of porous ceramic hollow-fiber membrane - Google Patents

End sealing method of porous ceramic hollow-fiber membrane

Info

Publication number
JP2003326138A
JP2003326138A JP2002136469A JP2002136469A JP2003326138A JP 2003326138 A JP2003326138 A JP 2003326138A JP 2002136469 A JP2002136469 A JP 2002136469A JP 2002136469 A JP2002136469 A JP 2002136469A JP 2003326138 A JP2003326138 A JP 2003326138A
Authority
JP
Japan
Prior art keywords
fiber membrane
hollow fiber
porous ceramic
porous
ceramic hollow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002136469A
Other languages
Japanese (ja)
Inventor
Hirokata Mizuta
裕賢 水田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nok Corp
Original Assignee
Nok Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nok Corp filed Critical Nok Corp
Priority to JP2002136469A priority Critical patent/JP2003326138A/en
Publication of JP2003326138A publication Critical patent/JP2003326138A/en
Pending legal-status Critical Current

Links

Abstract

<P>PROBLEM TO BE SOLVED: To provide an end sealing method of a porous ceramic hollow-fiber membrane which is easily produced, extremely low in leakage of gas and effectively used for gas separation. <P>SOLUTION: One end of the porous ceramic hollow-fiber membrane is immersed in an organic solvent solution of a polymer material in which a ceramic powder is highly dispersed, and then is immersed in a coagulation bath, thus the ceramic powder and the polymer material are attached to the end of the hollow-fiber membrane. A composite membrane composed of the ceramic powder and the polymer material is sintered, and the opening of the porous ceramic hollow-fiber membrane is closed, thus a deadend structure is formed. <P>COPYRIGHT: (C)2004,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、多孔質セラミック
ス中空糸膜の端部封止方法に関する。更に詳しくは、ガ
ス分離装置などに有効に用いられる多孔質セラミックス
中空糸膜の端部封止方法に関する。
TECHNICAL FIELD The present invention relates to a method for sealing an end portion of a porous ceramic hollow fiber membrane. More specifically, the present invention relates to a method for sealing an end portion of a porous ceramic hollow fiber membrane which is effectively used in a gas separation device or the like.

【0002】[0002]

【従来の技術】多孔質セラミックスは、化学的安定性お
よび熱安定性が高いため、有機分離膜が適用できない工
程への分離膜あるいはその支持体としての利用が期待さ
れている。この多孔質セラミックス中空管を用いた分離
モジュールのうち、高温で使用されるものについては、
熱膨張差によるセラミックスの破損を防止する目的で、
多孔質セラミックス中空糸の一端をフランジなどで閉じ
たデットエンド構造とする場合がある(特開平7-112111
号公報)。
2. Description of the Related Art Since porous ceramics have high chemical and thermal stability, they are expected to be used as a separation membrane or a support thereof in a process in which an organic separation membrane cannot be applied. Of the separation modules that use this porous ceramic hollow tube, those that are used at high temperatures are:
In order to prevent damage to the ceramics due to the difference in thermal expansion,
In some cases, one end of the porous ceramic hollow fiber is closed with a flange or the like to form a dead end structure (Japanese Patent Laid-Open No. 7-112111).
Issue).

【0003】一端を閉塞させる方法としては、特開平11
-226370号公報において、開口部に無機接着剤を充填
し、さらにその部分をガラスでコーティングし、気密性
を確保する方法が開示しているが、工程が複雑であり多
孔質部分に分離機能層を形成させる場合にガラス成分が
機能層側へ拡散したり、またガラス軟化点以上に長期間
保つとリークが発生しやすいなどの問題がみられた。
As a method for closing one end, Japanese Patent Laid-Open No.
-226370 discloses a method of filling an opening with an inorganic adhesive and further coating the portion with glass to ensure airtightness, but the process is complicated and a separation functional layer is formed in the porous portion. However, there were problems such that the glass component was diffused to the functional layer side when forming the film, and if the glass component was kept at a temperature above the glass softening point for a long time, a leak was likely to occur.

【0004】また、本出願人は先に、図1〜2に示され
るような金属とセラミックスとの複合体を用いたガス分
離モジュールを提案している(特願2000-347689号)。
Further, the present applicant has previously proposed a gas separation module using a composite of metal and ceramics as shown in FIGS. 1 and 2 (Japanese Patent Application No. 2000-347689).

【0005】図1には、多孔質セラミックス管状体1の一
端側2が管状金属部材3に挿入され、また他端側2が閉塞
された金属部材4に挿入され、これらの挿入個所がInお
よびTiを含有する活性金属ロウ材5で接合された態様が
示されている。多孔質セラミックス管状体1の非接合部
分表面には、ガス分離膜6が形成されており、このよう
なガス分離膜6を形成させた多孔質セラミックス管状体1
を挿入した管状金属部材3は、前述の如き活性金属ロウ
材の他銀ロウ、ニッケルロウ、金ロウ、パラジウムロウ
等の汎用金属ロウ材7を用いて、金属支持体8に接合され
ている。この金属支持体としては、ステンレス鋼等の汎
用金属を用いることができる。
In FIG. 1, one end side 2 of a porous ceramic tubular body 1 is inserted into a tubular metal member 3 and the other end side 2 is inserted into a closed metal member 4, and these insertion points are In and An embodiment in which the active metal brazing material 5 containing Ti is bonded is shown. A gas separation membrane 6 is formed on the surface of the non-bonded portion of the porous ceramics tubular body 1, and the porous ceramics tubular body 1 on which such a gas separation membrane 6 is formed is formed.
The tubular metal member 3 in which is inserted is joined to the metal support 8 by using a general-purpose metal brazing material 7 such as silver brazing, nickel brazing, gold brazing, and palladium brazing in addition to the active metal brazing material as described above. As this metal support, a general-purpose metal such as stainless steel can be used.

【0006】図2には、このような多孔質セラミックス
管状体挿入管状金属部材の複数本が金属支持体によって
接合されて形成するガス分離モジュール11を装着した水
素分離装置が断面図として示されている。このガス分離
モジュール11は、筒状容器12内に吊り下げられた状態で
収容され、この筒状容器は金属支持体8によって被処理
ガス供給部13と分離ガス取出部14とに分離されている。
FIG. 2 is a sectional view showing a hydrogen separation device equipped with a gas separation module 11 formed by joining a plurality of such tubular metal members for inserting a porous ceramic tubular body with a metal support. There is. The gas separation module 11 is accommodated in a cylindrical container 12 in a suspended state, and the cylindrical container is separated by a metal support 8 into a to-be-processed gas supply section 13 and a separated gas extraction section 14. .

【0007】水素を含有する被処理ガスは、パイプ15か
ら筒状容器12内のモジュール11の外側に導入され、水素
のみがガス分離膜6および多孔質セラミックス1を透過
し、モジュールの各多孔質セラミックス管状体1の内部
空間を経由して、分離・精製された水素が分離ガス取出
部14に設けられたパイプ16から取り出される。一方、精
製されなかったガスは、被処理ガス供給部13に設けられ
たパイプ17から排出される。
The gas to be treated containing hydrogen is introduced from the pipe 15 to the outside of the module 11 in the cylindrical container 12, and only hydrogen permeates the gas separation membrane 6 and the porous ceramics 1 and each porous of the module. The separated and purified hydrogen is taken out from the pipe 16 provided in the separated gas taking-out section 14 via the internal space of the ceramic tubular body 1. On the other hand, the gas that has not been purified is discharged from the pipe 17 provided in the processing target gas supply unit 13.

【0008】この図2に示されるように、ガス分離モジ
ュール11が、筒状容器12内に吊り下げられた状態で収容
されるため、閉塞金属部材の重みにより多孔質セラミッ
クス中空糸膜が破損する可能性が考えられる。
As shown in FIG. 2, since the gas separation module 11 is accommodated in the cylindrical container 12 in a suspended state, the porous ceramic hollow fiber membrane is damaged by the weight of the closed metal member. There is a possibility.

【0009】[0009]

【発明が解決しようとする課題】本発明の目的は、作製
が容易でしかもガス漏れが極めて少なく、ガス分離に有
効に用いられる多孔質セラミックス中空糸膜の端部封止
方法を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a method for sealing an end portion of a porous ceramic hollow fiber membrane which is easy to manufacture, has extremely little gas leakage, and is effectively used for gas separation. is there.

【0010】[0010]

【課題を解決するための手段】かかる本発明の目的は、
多孔質セラミックス中空糸膜の一端を、セラミックス粉
末を高分散させた高分子物質の有機溶媒溶液中に浸漬し
た後、凝固浴中に浸漬することにより中空糸膜端部に付
着させたセラミックス粉末と高分子物質からなる複合膜
を焼結させ、多孔質セラミックス中空糸膜の開口部を閉
塞させたデッドエンド構造にすることによって達成され
る。
The object of the present invention is as follows.
One end of the porous ceramic hollow fiber membrane is immersed in a solution of a high-dispersion ceramic powder in an organic solvent, and then immersed in a coagulation bath to form a ceramic powder adhered to the end of the hollow fiber membrane. This is achieved by sintering a composite membrane made of a polymer substance to form a dead end structure in which the openings of the porous ceramic hollow fiber membrane are closed.

【0011】[0011]

【発明の実施の形態】一端が閉塞処理される多孔質セラ
ミックス中空糸膜としては、アルミナ、シリカ、ムライ
ト、ジルコニア等の酸化物セラミックスまたは多孔質ガ
ラスなどの管状体が用いられる。
BEST MODE FOR CARRYING OUT THE INVENTION As a porous ceramics hollow fiber membrane whose one end is closed, an oxide ceramics such as alumina, silica, mullite, zirconia or a tubular body such as porous glass is used.

【0012】セラミックス粉末を高充填させる高分子物
質の有機溶媒溶液としては、例えば次のような組み合わ
せのものが用いられる。
As the organic solvent solution of the polymer substance which is highly filled with the ceramic powder, the following combinations are used, for example.

【0013】これらの高分子物質の有機溶媒溶液に高分
散されるセラミックス粉末としては、例えば粒径が0.1
〜5μm、好ましくは0.2〜1μmのアルミナ、シリカ、ム
ライト、ジルコニアなどの酸化物セラミックスの少なく
とも一種が用いられる。
The ceramic powder highly dispersed in an organic solvent solution of these polymer substances has, for example, a particle size of 0.1.
At least one kind of oxide ceramics having a particle size of ˜5 μm, preferably 0.2 to 1 μm, such as alumina, silica, mullite, and zirconia is used.

【0014】製膜原液は、約3〜20重量%の濃度に調整
された高分子物質の有機溶媒溶液に、最終的に調製され
た製膜原液中で15〜50体積%を占めるセラミックス粉末
を添加することにより得られる。
The stock solution for film formation is obtained by adding a ceramic powder that occupies 15 to 50% by volume in the finally prepared stock solution for film formation to an organic solvent solution of a polymer substance adjusted to a concentration of about 3 to 20% by weight. It is obtained by adding.

【0015】次に、調製された製膜原液に、多孔質セラ
ミックス中空糸膜の一端を浸漬し、その後水などの凝固
浴中に投入することで相分離によって開口部を塞ぐよう
に複合膜を形成させた後、必要に応じて高分子物質を分
解させるために約500〜700℃で加熱され、さらに焼結が
行われる。焼結は、複合膜を形成させた端部について、
用いられるセラミックス粉末の焼結温度で行われるが、
例えばセラミックス粉末としてアルミナが用いられる場
合には、1500〜1750℃で2〜24時間、好ましくは1650〜1
700℃で6〜12時間加熱することにより行われる。焼結温
度がこれより低い場合には、閉塞部の気密性を十分に確
保することができず、また焼結時間がこれより短い場合
にも、閉塞部の気密性を十分に確保することができな
い。また焼結は、中空糸膜端部のみ行うこともできる
が、多孔質セラミックス中空糸膜の分離機能層として用
いられる部分以外を緻密化する作業と同時に行うことも
できる。
Next, one end of the porous ceramic hollow fiber membrane is immersed in the prepared membrane-forming raw material solution and then put into a coagulation bath of water or the like to form a composite membrane so as to close the opening by phase separation. After being formed, if necessary, it is heated at about 500 to 700 ° C. to decompose the polymer material, and further sintered. Sintering is performed on the end part where the composite film is formed,
It takes place at the sintering temperature of the ceramic powder used,
For example, when alumina is used as the ceramic powder, it is 1500 to 1750 ° C. for 2 to 24 hours, preferably 1650 to 1
It is carried out by heating at 700 ° C for 6 to 12 hours. If the sintering temperature is lower than this, it is not possible to ensure sufficient airtightness of the closed part, and even if the sintering time is shorter than this, it is possible to ensure sufficient airtightness of the closed part. Can not. Further, the sintering can be performed only at the end portions of the hollow fiber membranes, but can also be performed at the same time as the work of densifying the portions of the porous ceramics hollow fiber membranes other than those used as the separation functional layer.

【0016】[0016]

【発明の効果】本発明によって、作製が容易でしかも高
温、高圧下でもガス漏れが極めて少なく、ガス分離に有
効に用いられる多孔質セラミックス中空糸膜の端部封止
方法が提供され、このようにして端部が封止された多孔
質セラミックス中空糸膜は水素含有ガスから水素ガスを
選択的に分離するためなどに用いられるガス分離装置な
どの作製に有効に用いられる。
According to the present invention, there is provided a method for sealing an end portion of a porous ceramic hollow fiber membrane which is easy to produce, has extremely little gas leakage even under high temperature and high pressure, and is effectively used for gas separation. The porous ceramic hollow fiber membrane whose ends are sealed as described above is effectively used for producing a gas separator used for selectively separating hydrogen gas from hydrogen-containing gas.

【0017】また、以上の操作は、多孔質セラミックス
中空糸膜の分離機能層を形成させる部分以外を緻密化さ
せて気密封止させる操作と同時に行うことができるた
め、操作時間の大幅な短縮を図ることが可能となる。
Further, the above operation can be performed simultaneously with the operation of densifying and hermetically sealing the portion of the porous ceramic hollow fiber membrane other than the portion where the separation functional layer is formed, so that the operation time is greatly shortened. It is possible to plan.

【0018】[0018]

【実施例】次に、実施例について本発明を説明する。EXAMPLES The present invention will now be described with reference to examples.

【0019】実施例 ポリスルホン(ユニオンカーバイト社製品P-1700)20gに
アルミナ微粉末(平均粒径0.3μm)350g(24体積%)およ
びジメチルホルムアミド250gを混合し、製膜原液を調
製した。この製膜原液に、多孔質アルミナ中空糸膜(外
径2.0mm、内径1.4mm、長さ300mm、平均細孔径0.2μm、
写真実測による表面開口率44%)の一端部約5mmを数秒間
浸漬した後、凝固浴である水に浸漬し、中空糸膜端部に
ポリスルホンとアルミナ微粉末の複合膜を形成させた。
このようにして複合膜を形成させた端部を含む片端約50
mmを電気炉内に挿入し、1650℃で12時間加熱して焼結さ
せた。焼結された片端約50mmは緻密化され、その端部は
閉塞されていた。
Example A 20 g of polysulfone (P-1700 manufactured by Union Carbide) was mixed with 350 g (24% by volume) of alumina fine powder (average particle size 0.3 μm) and 250 g of dimethylformamide to prepare a stock solution for film formation. In this membrane forming solution, a porous alumina hollow fiber membrane (outer diameter 2.0 mm, inner diameter 1.4 mm, length 300 mm, average pore diameter 0.2 μm,
Approximately 5 mm at one end with a surface aperture ratio of 44% measured by a photograph was immersed for several seconds and then immersed in water as a coagulation bath to form a composite membrane of polysulfone and alumina fine powder on the end of the hollow fiber membrane.
Approximately 50 on one end including the end where the composite film was formed in this way
mm was inserted into an electric furnace and heated at 1650 ° C. for 12 hours for sintering. About 50 mm of one end of the sintered body was densified and its end was closed.

【0020】緻密化され、端部が閉塞された部分約50mm
を切り出して、その部分のヘリウムリーク量を測定した
ところ、リーク量は1×10-10Pa・m3/s未満であり、高
いガス気密性を示した。
Approximately 50 mm, which is densified and has closed ends
When the helium leak amount was measured by cutting it out, the leak amount was less than 1 × 10 −10 Pa · m 3 / s, and high gas tightness was exhibited.

【図面の簡単な説明】[Brief description of drawings]

【図1】金属-セラミックス接合体の一態様の縦断面図
である。
FIG. 1 is a vertical cross-sectional view of one embodiment of a metal-ceramic bonding body.

【図2】ガス分離モジュールを用いたガス分離装置の縦
断面図である。
FIG. 2 is a vertical cross-sectional view of a gas separation device using a gas separation module.

【符号の説明】[Explanation of symbols]

1 多孔質セラミックス管状体 3 管状金属部材 4 閉塞金属部材 5 活性金属ロウ材 6 ガス分離膜 7 汎用金属ロウ材 8 金属支持体 11 ガス分離モジュール 12 筒状容器 13 被処理ガス供給部 14 分離ガス取出部 1 Porous ceramic tubular body 3 Tubular metal members 4 Blocking metal member 5 Active metal brazing material 6 Gas separation membrane 7 General-purpose metal brazing material 8 Metal support 11 Gas separation module 12 cylindrical container 13 Processed gas supply unit 14 Separation gas extraction part

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 多孔質セラミックス中空糸膜の一端を、
セラミックス粉末を高分散させた高分子物質の有機溶媒
溶液中に浸漬した後、凝固浴中に浸漬することにより中
空糸膜端部に付着させたセラミックス粉末と高分子物質
からなる複合膜を焼結させ、多孔質セラミックス中空糸
膜の開口部を閉塞させたデッドエンド構造にすることを
特徴とする多孔質セラミックス中空糸膜の端部封止方
法。
1. One end of the porous ceramic hollow fiber membrane is
After immersing the ceramic powder in a highly dispersed organic solvent solution of a polymer substance, immerse it in a coagulation bath to sinter the composite film consisting of the ceramic powder and polymer substance attached to the end of the hollow fiber membrane. And a dead end structure in which the opening of the porous ceramics hollow fiber membrane is closed, and a method for sealing the end portion of the porous ceramics hollow fiber membrane.
【請求項2】 焼結が複合膜を形成させた端部について
1500〜1750℃、2〜24時間の条件下で行われる請求項1
記載の多孔質セラミックス中空糸膜の端部封止方法。
2. About the end where the sintering forms a composite film
It is performed under the condition of 1500 to 1750 ° C. and 2 to 24 hours.
The method for sealing an end portion of the porous ceramic hollow fiber membrane described.
【請求項3】 請求項1または2記載の方法により得ら
れた端部封止多孔質セラミックス中空糸膜を用いたガス
分離装置。
3. A gas separation device using the end-sealed porous ceramics hollow fiber membrane obtained by the method according to claim 1.
JP2002136469A 2002-05-13 2002-05-13 End sealing method of porous ceramic hollow-fiber membrane Pending JP2003326138A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002136469A JP2003326138A (en) 2002-05-13 2002-05-13 End sealing method of porous ceramic hollow-fiber membrane

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002136469A JP2003326138A (en) 2002-05-13 2002-05-13 End sealing method of porous ceramic hollow-fiber membrane

Publications (1)

Publication Number Publication Date
JP2003326138A true JP2003326138A (en) 2003-11-18

Family

ID=29698479

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002136469A Pending JP2003326138A (en) 2002-05-13 2002-05-13 End sealing method of porous ceramic hollow-fiber membrane

Country Status (1)

Country Link
JP (1) JP2003326138A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007269600A (en) * 2006-03-31 2007-10-18 Ngk Spark Plug Co Ltd Hydrogen separation apparatus and hydrogen production system
CN100361730C (en) * 2005-01-14 2008-01-16 山东理工大学 Ceramic hollow fiber membrane reactor for making oxygen by air separation, and its preparing method and use
JP2008259928A (en) * 2007-04-10 2008-10-30 Nok Corp Housing-mounted hollow fiber membrane module
CN113926320A (en) * 2021-09-09 2022-01-14 浙江浙能天然气运行有限公司 Hollow fiber ceramic composite membrane for VOCs recovery and preparation process thereof

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100361730C (en) * 2005-01-14 2008-01-16 山东理工大学 Ceramic hollow fiber membrane reactor for making oxygen by air separation, and its preparing method and use
JP2007269600A (en) * 2006-03-31 2007-10-18 Ngk Spark Plug Co Ltd Hydrogen separation apparatus and hydrogen production system
JP2008259928A (en) * 2007-04-10 2008-10-30 Nok Corp Housing-mounted hollow fiber membrane module
CN113926320A (en) * 2021-09-09 2022-01-14 浙江浙能天然气运行有限公司 Hollow fiber ceramic composite membrane for VOCs recovery and preparation process thereof

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