JPH10216529A - Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material - Google Patents

Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material

Info

Publication number
JPH10216529A
JPH10216529A JP9020671A JP2067197A JPH10216529A JP H10216529 A JPH10216529 A JP H10216529A JP 9020671 A JP9020671 A JP 9020671A JP 2067197 A JP2067197 A JP 2067197A JP H10216529 A JPH10216529 A JP H10216529A
Authority
JP
Japan
Prior art keywords
inorganic fiber
woven fabric
catalyst
rollers
base material
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
JP9020671A
Other languages
Japanese (ja)
Inventor
Koichi Yokoyama
公一 横山
Naomi Yoshida
直美 吉田
Yasuyoshi Kato
泰良 加藤
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.)
Mitsubishi Power Ltd
Original Assignee
Babcock Hitachi KK
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 Babcock Hitachi KK filed Critical Babcock Hitachi KK
Priority to JP9020671A priority Critical patent/JPH10216529A/en
Publication of JPH10216529A publication Critical patent/JPH10216529A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a method for producing an inorganic fiber catalytic base material which retainss a strength equal to or more than a conventional catalyst and can have its thickens reduced further. SOLUTION: An inorganic fiber woven cloth 1 is fed by each specified length to an impregnation tank 4 by a woven cloth feeder machine 2, then is impregnated with a reinforcing liquid 3 containing an inorganic binder using an impregnating machine 4, and an excess reinforcing liquid is removed with the held of a liquid draining roller 5. Further, a woven cloth impregnated with the reinforcing liquid thus obtained is supplied, in a tensionless state, between a pair of thickness-limiting rollers 7 heated at a specified temperature, while a space between the rollers 7 or a pressure between the rollers 7 is kept at a specified value. The inorganic fiber woven cloth is thinned and, at the same time, has its strength increased by causing the woven cloth to pass between the thickness limiting rollers 7.

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、無機繊維触媒基材
の製造方法および製造装置ならびに無機繊維触媒基材を
用いた板状触媒の製造方法に係り、特に曲げ強度を低下
させることなく触媒の厚さを薄くして触媒を装着した装
置内の被処理ガス通過圧力損失を低下させることがで
き、さらに同一容積の装置内に装着できる触媒の枚数を
増加させて、その処理能力を向上させることを可能とし
た無機繊維触媒基材の製造方法および製造装置ならびに
無機繊維触媒基材を用いた板状触媒の製造方法に関す
る。
The present invention relates to a method and an apparatus for producing an inorganic fiber catalyst substrate and a method for producing a plate-shaped catalyst using the inorganic fiber catalyst substrate. The thickness can be reduced to reduce the pressure loss of the gas to be treated in a device equipped with a catalyst, and the number of catalysts that can be mounted in a device of the same volume can be increased to improve the processing capacity. The present invention relates to a method and an apparatus for producing an inorganic fiber catalyst base material, and a method for producing a plate catalyst using the inorganic fiber catalyst base material.

【0002】[0002]

【従来の技術】図3に無機繊維織布を使った従来の触媒
用基材の製造方法および装置を示す。図3において、織
布送り出し機2の軸に巻き付けられた無機繊維織布1
は、ガイドローラ13、14を介して含浸槽4内に導入
され、ここで無機結合剤(例えばシリカ、チタニヤ、ア
ルミナなど)を含有する強化液3に浸漬されたのち、液
切りローラ5で余分の液が除去され、さらにテンショナ
6を経て熱風乾燥機9にて乾燥され、巻取り機8に巻取
られる。このような処理をすることにより無機繊維織布
は所望の引張強度、曲げ強度、剛性を有する帯状の触媒
用基材となる。
2. Description of the Related Art FIG. 3 shows a conventional method and apparatus for producing a substrate for a catalyst using an inorganic fiber woven fabric. In FIG. 3, the inorganic fiber woven fabric 1 wound around the shaft of the woven fabric feeder 2 is shown.
Is introduced into the impregnation tank 4 via the guide rollers 13 and 14, where it is immersed in the strengthening liquid 3 containing an inorganic binder (for example, silica, titania, alumina, etc.), Is removed, further dried by a hot-air dryer 9 via a tensioner 6, and wound up by a winder 8. By performing such treatment, the inorganic fiber woven fabric becomes a belt-shaped catalyst substrate having desired tensile strength, bending strength, and rigidity.

【0003】高温の被処理ガスにさらされる板状の触媒
は、図7に示すように、上記した方法によって得られた
帯状の触媒基材15を一対の塗布ローラ21、22の間
に、あらかじめ混練してペースト状に調製した触媒組成
物16とともに供給して、基材15上に触媒組成物16
を塗布して触媒塗布体17とし、これを乾燥、焼成して
板状触媒とすることが知られている。ここで23は受け
台、24は塗布補助紙である。
As shown in FIG. 7, a plate-shaped catalyst exposed to a high-temperature gas to be treated is prepared by preliminarily placing a belt-shaped catalyst base material 15 obtained by the above-described method between a pair of application rollers 21 and 22. It is supplied together with the kneaded paste-form catalyst composition 16 to form the catalyst composition 16 on the substrate 15.
It is known that a catalyst-coated body 17 is applied to the resultant and then dried and fired to obtain a plate-shaped catalyst. Here, reference numeral 23 denotes a receiving stand, and 24 denotes an application assisting paper.

【0004】[0004]

【発明が解決しようとする課題】図4に示すように、板
状触媒においては、触媒積層時にスペーサーの役割を持
つ山部に平行な方向では構造的に曲げ強度は大きいが、
山部に垂直な方向では触媒自体の曲げ強度で強度が決ま
るため、板状触媒自体の充分な曲げ強度が要求される。
板状触媒において、一定方向の曲げ強度は、その方向に
平行な繊維の引張強度に依存している。そのため図3の
液切りローラ5、テンショナ6のように織布を一定方向
に引張り、図5における繊維束12を引張ることにより
繊維同士を密着させ、シリカやチタニアのゾルやスラリ
のような無機結合剤で互いに充分結合された状態にする
ことで一定方向の繊維を強化し、繊維の引張強度を向上
させることにより板状触媒の曲げ強度を向上することが
行われていた。
As shown in FIG. 4, a plate-like catalyst has a structurally large bending strength in a direction parallel to a hill portion serving as a spacer when laminating the catalyst.
In the direction perpendicular to the peak, the strength is determined by the bending strength of the catalyst itself, so that a sufficient bending strength of the plate-shaped catalyst itself is required.
In a plate-like catalyst, the bending strength in a certain direction depends on the tensile strength of a fiber parallel to that direction. Therefore, the woven fabric is pulled in a certain direction like the draining roller 5 and the tensioner 6 in FIG. 3, and the fibers are brought into close contact by pulling the fiber bundle 12 in FIG. 5, and inorganic binding such as silica or titania sol or slurry is performed. It has been practiced to reinforce fibers in a certain direction by making them sufficiently bonded to each other with an agent, and to improve the bending strength of the plate catalyst by improving the tensile strength of the fibers.

【0005】近年、板状触媒をより薄肉化することによ
り、例えば排ガス中の窒素酸化物を除去するための排ガ
ス処理用の脱硝触媒の場合、反応面積に比例する脱硝活
性を維持し、触媒量に比例するSO2 酸化率を低減する
ことを目指した研究が行われているが、図3に示した従
来の織布強化方法では、張力のかかっていない繊維束
(図5における繊維束12′)同士の空隙に無機結合剤
が固形物として残存するため、織布全体として強化する
前よりも厚くなるということがわかっていた。そのため
触媒を薄肉化する場合、従来の触媒に用いていた織布よ
りも繊維束自体を薄くするため、繊維束を構成する繊維
の本数を減少させるかまたはより細い繊維を用いる以外
に方法がなく、基材の強度ひいては触媒の強度を低下さ
せる原因になっていた。
In recent years, by reducing the thickness of the plate catalyst, for example, in the case of a denitration catalyst for exhaust gas treatment for removing nitrogen oxides in exhaust gas, the denitration activity proportional to the reaction area is maintained, and the amount of catalyst is reduced. Research has been conducted to reduce the SO 2 oxidation rate proportional to the fiber bundle. However, in the conventional woven fabric reinforcing method shown in FIG. 3, a fiber bundle without tension (the fiber bundle 12 ′ in FIG. 5) is used. It has been found that since the inorganic binder remains as a solid substance in the space between the woven fabrics, the woven fabric as a whole becomes thicker than before reinforcement. Therefore, when thinning the catalyst, in order to make the fiber bundle itself thinner than the woven fabric used for the conventional catalyst, there is no other way but to reduce the number of fibers constituting the fiber bundle or use thinner fibers. This has been a cause of lowering the strength of the base material and thus the strength of the catalyst.

【0006】本発明の目的は、上記従来技術の課題を解
決し、従来の触媒と同等以上の強度を保持し、しかも触
媒をより薄くすることができる無機繊維触媒基材の製造
方法および製造装置ならびに無機繊維触媒基材を用いた
板状触媒の製造方法を提供することにある。
An object of the present invention is to solve the above-mentioned problems of the prior art, to maintain a strength equal to or higher than that of a conventional catalyst, and to further reduce the thickness of the catalyst. Another object of the present invention is to provide a method for producing a plate catalyst using an inorganic fiber catalyst substrate.

【0007】[0007]

【課題を解決するための手段】上記目的を達成するため
本願で特許請求される発明は以下のとおりである。 (1)無機繊維織布を含浸槽に所定量ずつ送り出す工程
と、該含浸槽にて前記送り出された織布に無機結合剤を
含有する強化液を含浸する工程と、加熱された一対のロ
ーラの間隔またはローラ間の圧力を所定値に保持しつつ
該ローラ間に前記強化液含浸織布を通過させて所定厚さ
の基材を得る工程とを備えたことを特徴とする無機繊維
触媒基材の製造方法。
The invention claimed in the present application to achieve the above object is as follows. (1) a step of feeding a predetermined amount of an inorganic fiber woven fabric to an impregnation tank, a step of impregnating the sent woven cloth with a reinforcing liquid containing an inorganic binder in the impregnation tank, and a pair of heated rollers A step of passing the reinforcing liquid-impregnated woven fabric between the rollers to obtain a base material having a predetermined thickness while maintaining the interval between the rollers or the pressure between the rollers at a predetermined value. The method of manufacturing the material.

【0008】(2)(1)において、前記強化液を含浸
した織布を前記加熱ローラ間に供給する前に、強化液含
浸織布の表面を乾燥する工程を備えたことを特徴とする
無機繊維触媒基材の製造方法。 (3)無機繊維織布を含浸槽に送る織布送り出し機と、
送り出された前記織布を受取りこれに結合剤を含有する
強化液を含浸させる含浸槽と、強化液を含浸された前記
織布中の余分の強化液を除去する液切り手段と、液切り
された前記無機繊維織布を所定の間隔または所定圧力で
加熱しつつ加圧する加熱加圧手段とを備えていることを
特徴とする無機繊維触媒基材の製造装置。
(2) The method according to (1), further comprising a step of drying a surface of the woven fabric impregnated with the reinforcing liquid before supplying the woven cloth impregnated with the reinforcing liquid between the heating rollers. A method for producing a fiber catalyst substrate. (3) a woven cloth feeder that sends the inorganic fiber woven cloth to the impregnation tank;
An impregnating tank for receiving the sent-out woven fabric and impregnating it with a reinforcing liquid containing a binder, a draining means for removing excess reinforcing liquid in the woven cloth impregnated with the reinforcing liquid; A heating and pressurizing means for heating and pressurizing the inorganic fiber woven fabric at a predetermined interval or at a predetermined pressure.

【0009】(4)(3)において、前記加熱加圧手段
が、加熱された一対の加圧ローラであり、該加圧ローラ
の表面が撥水性かつ耐熱性を有する樹脂で被覆されてい
ることを特徴とする無機繊維触媒基材の製造装置。 (5)織布送り出し手段により無機繊維織布を含浸槽に
所定量ずつ送り出し、送り出された織布に無機結合剤を
含有する強化液を含浸し、加熱された一対のローラの間
隔またはローラ間の圧力を所定値に保持しつつ該ローラ
間に前記強化液含浸織布を張力を除去した状態で供給し
て該ローラ間を通過させて所定厚さの無機繊維触媒基材
とし、該無機繊維触媒基材の1枚または複数枚にペース
ト状の触媒原料を塗布し、乾燥、焼成することを特徴と
する無機繊維触媒基材を用いた板状触媒の製造方法。
(4) In (3), the heating / pressing means is a pair of heated pressure rollers, and the surfaces of the pressure rollers are coated with a water-repellent and heat-resistant resin. An apparatus for producing an inorganic fiber catalyst substrate. (5) A predetermined amount of the inorganic fiber woven fabric is sent out to the impregnation tank by the woven fabric sending means, and the sent woven fabric is impregnated with a reinforcing liquid containing an inorganic binder, and the distance between the heated pair of rollers or between the rollers is adjusted. While maintaining the pressure at a predetermined value, the reinforcing liquid-impregnated woven fabric is supplied between the rollers in a state where the tension is removed, and is passed between the rollers to form an inorganic fiber catalyst base material having a predetermined thickness. A method for producing a plate-shaped catalyst using an inorganic fiber catalyst substrate, wherein a paste-like catalyst material is applied to one or a plurality of catalyst substrates, dried and calcined.

【0010】本発明においては、無機結合剤を含有する
強化液に無機繊維織布を含浸し、充分液切りした後、加
熱した一対のローラの隙間を通すことにより無機繊維触
媒基材を作製する。ここで、ローラの間隔を一定にする
か、またはローラ間に一定の圧力を加えることにより、
通過する無機繊維織布の厚さを制限する。さらに、厚さ
制限ローラを通す前の織布にかかる張力をできるだけ弱
くすることも重要であり、これにより織布を構成する繊
維束はローラにより自由に変形され易くなる。また、加
熱することも重要で、これにより織布中の水分が蒸発
し、無機結合剤により織布の形状が固定化される。これ
らの効果の重畳により、従来の基材と同等の引張強度を
持ち、かつ従来よりも薄い触媒基材を得ることが可能に
なる。
In the present invention, an inorganic fiber woven fabric is impregnated with a reinforcing liquid containing an inorganic binder, sufficiently drained, and then passed through a gap between a pair of heated rollers to prepare an inorganic fiber catalyst base material. . Here, by keeping the interval between the rollers or applying a constant pressure between the rollers,
Limit the thickness of the inorganic fiber woven fabric that passes. It is also important to reduce the tension applied to the woven fabric before passing through the thickness limiting roller as much as possible, so that the fiber bundle constituting the woven fabric can be easily deformed by the roller. It is also important to heat, whereby moisture in the woven fabric evaporates, and the shape of the woven fabric is fixed by the inorganic binder. By superimposition of these effects, it is possible to obtain a catalyst base material having a tensile strength equivalent to that of the conventional base material and being thinner than the conventional base material.

【0011】本発明において、乾燥機によりローラを通
過する前の無機繊維織布の表面を乾燥させれば、ローラ
が汚れにくくなる。さらにローラ表面に耐熱性かつ撥水
性を持つフッ素系やシリコン系の樹脂で被覆してもロー
ラ表面は汚れにくくなる。このようにして作製した基材
に、ペースト状の触媒粉末を圧延塗布することにより従
来の触媒よりも薄く、かつ曲げ強度は同等以上の触媒を
得ることができる。
In the present invention, if the surface of the inorganic fiber woven fabric before passing through the rollers is dried by the dryer, the rollers are less likely to become dirty. Further, even if the roller surface is coated with a heat-resistant and water-repellent fluorine-based or silicon-based resin, the roller surface is hardly stained. By rolling and applying the paste-like catalyst powder to the base material thus produced, a catalyst having a thickness smaller than that of a conventional catalyst and having the same or higher bending strength can be obtained.

【0012】[0012]

【発明の実施の形態】本発明の内容を具体的実施例によ
りさらに詳細に説明する。本実施例が記載する触媒原料
および触媒基材は本願発明を限定するものではない。ま
た、本実施例では、脱硝触媒の用途に合わせて触媒組成
および構造を記載しているが、この用途および構造に限
定されるものではなく、例えば排ガス酸化触媒や燃焼触
媒に用いてもよい。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The contents of the present invention will be described in more detail with reference to specific examples. The catalyst raw materials and catalyst bases described in this example do not limit the present invention. Further, in this embodiment, the catalyst composition and structure are described according to the use of the denitration catalyst. However, the present invention is not limited to this use and structure, and may be used for, for example, an exhaust gas oxidation catalyst or a combustion catalyst.

【0013】ここで、記載している加圧ローラ以外の構
造も同様な機能を果たすものであればどのようなもので
もかまわない。 実施例1 本実施例で用いた無機繊維触媒基材の製造装置は、図1
に示すように、無機繊維織布1の送り出し機2、織布1
にシリカゾルを含んだ強化液3を含浸するための含浸槽
4、強化液3含浸後の織布1の余分な強化液を除去する
ための一対のスポンジ製液切りローラ5、液切りした織
布1が撓まない最小限の張力を加えるテンショナ6、織
布1を加熱成形する一対の加熱した厚さ制限ローラ7お
よび強化された織布1の巻き取り機8で構成される。本
実施例では無機繊維織布1としてシリカアルミナガラス
織布(繊維径は6μm、繊維束は厚さ0.4mm、繊維束
の間隔2mm)を、強化液3としてシリカゾル10wt
%、ポリビニルアルコール1wt%、チタニア50wt
%となるように水分を調整した混合液をそれぞれ用い、
上記触媒基材の製造装置における厚さ制限ローラ7の表
面温度を150℃、隙間間隔を0.3mmに固定して、前
記無機繊維織布1に強化液3を含浸させて触媒基材を得
た。 実施例2 液切りした織布1の表面を乾燥させることにより、加熱
成形の際厚さ制限ローラ7の表面を汚れにくくするた
め、図2のように、厚さ制限ローラ7の上流に熱風乾燥
機9を設置した触媒基材製造装置を用いた以外は上記実
施例と同様にして触媒基材を得た。 実施例3 厚さ制限ローラ7の表面が汚れにくいように厚さ制限ロ
ーラ7の表面に0.05mmのフッ素樹脂コートを行った
触媒基材製造装置を用いた以外は実施例1と同様にして
触媒基材を得た。 比較例1 厚さ制限ローラ7の代わりに熱風乾燥機9を設置した図
3の装置を用い、液切りローラ5で液切りした後、テン
ショナ6で織布1の送り方向の繊維束に300g/1本
の張力を加えて触媒基材を得た。
Here, the structure other than the described pressure roller may be any structure as long as it performs the same function. Example 1 An apparatus for producing an inorganic fiber catalyst substrate used in this example is shown in FIG.
As shown in the figure, the feeder 2 of the inorganic fiber woven fabric 1 and the woven fabric 1
Impregnating tank 4 for impregnating reinforcing liquid 3 containing silica sol, a pair of sponge draining rollers 5 for removing excess reinforcing liquid from woven cloth 1 impregnated with reinforcing liquid 3, and drained cloth 1 comprises a tensioner 6 for applying a minimum tension that does not bend, a pair of heated thickness limiting rollers 7 for thermoforming the woven fabric 1, and a winder 8 for the reinforced woven fabric 1. In the present embodiment, a silica-alumina glass woven fabric (fiber diameter: 6 μm, fiber bundle thickness: 0.4 mm, fiber bundle interval: 2 mm) is used as the inorganic fiber woven fabric 1, and silica sol 10 wt.
%, Polyvinyl alcohol 1wt%, titania 50wt
%, Each using a mixture of which the water content has been adjusted,
The catalyst substrate is obtained by impregnating the inorganic fiber woven fabric 1 with the reinforcing liquid 3 while fixing the surface temperature of the thickness limiting roller 7 to 150 ° C. and the gap interval to 0.3 mm in the above-mentioned catalyst base material manufacturing apparatus. Was. Example 2 Drying the surface of the drained woven fabric 1 makes it difficult for the surface of the thickness-limiting roller 7 to become dirty during heat molding. Therefore, hot air drying is performed upstream of the thickness-limiting roller 7 as shown in FIG. A catalyst base material was obtained in the same manner as in the above example, except that a catalyst base material manufacturing apparatus equipped with a machine 9 was used. Example 3 In the same manner as in Example 1 except that a catalyst substrate manufacturing apparatus in which the surface of the thickness limiting roller 7 was coated with a 0.05 mm fluororesin so as to prevent the surface of the thickness limiting roller 7 from becoming dirty was used. A catalyst substrate was obtained. COMPARATIVE EXAMPLE 1 Using the apparatus shown in FIG. One tension was applied to obtain a catalyst substrate.

【0014】上記の実施例の効果を確認するため、酸化
チタン粉末(以下、チタニア粉末、比表面積約100m
2 /g)と硫酸バナジルを100:12の重量比となる
ように秤量した後、酸化チタンに対して60重量パーセ
ントの水を加え、30分間ニーダで混練を行った後、原
料の酸化チタンに対して15および21重量パーセント
の割合でシリカアルミナ繊維と酸化モリブデンを同時に
加え、さらに30分間混練を行った触媒ペーストを実施
例1〜3および比較例1で作製した触媒基材に塗布し、
乾燥後500℃で2時間焼成して板状触媒とし、得られ
た板状触媒について曲げ強度および板厚の比較を行っ
た。なお、触媒ペーストの塗布は2枚の基材の間にペー
ストを挟み、ローラで圧延し、触媒ペーストを基材に展
延圧着する方法で行った。
In order to confirm the effects of the above embodiment, a titanium oxide powder (hereinafter, titania powder, specific surface area of about 100 m) was used.
2 / g) and vanadyl sulfate were weighed so as to have a weight ratio of 100: 12, water of 60% by weight was added to the titanium oxide, and the mixture was kneaded with a kneader for 30 minutes. Silica alumina fiber and molybdenum oxide were simultaneously added at a ratio of 15 and 21% by weight, and the catalyst paste kneaded for further 30 minutes was applied to the catalyst base materials prepared in Examples 1 to 3 and Comparative Example 1,
After drying, the plate catalyst was calcined at 500 ° C. for 2 hours to obtain a plate catalyst, and the obtained plate catalyst was compared in bending strength and plate thickness. The application of the catalyst paste was carried out by sandwiching the paste between two base materials, rolling with a roller, and spreading and pressing the catalyst paste on the base material.

【0015】曲げ試験の試験条件を表1、結果を表2に
示す。なお、比較例1で作製した触媒基材に実施例と同
じ条件で触媒ペーストを塗布したところ、上下の基材が
剥離したため、比較例1は基材が剥離しないで塗布でき
た最も薄い試料の試験結果を用いた。
The test conditions of the bending test are shown in Table 1, and the results are shown in Table 2. In addition, when the catalyst paste was applied to the catalyst base material manufactured in Comparative Example 1 under the same conditions as in the example, the upper and lower base materials were separated, so that Comparative Example 1 was the thinnest sample that could be applied without separating the base material. The test results were used.

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【表2】 表2において、触媒基材の厚さおよび板状触媒の板厚は
比較例1よりも実施例1〜3のほうが薄くなっており、
本発明による無機繊維触媒基材の平板化により触媒を塗
布した後の厚みが減少することがわかる。また曲げ試験
において実施例1〜3の曲げ強度は比較例1に比べて著
しく向上していることがわかる。
[Table 2] In Table 2, the thickness of the catalyst substrate and the plate thickness of the plate catalyst are smaller in Examples 1 to 3 than in Comparative Example 1,
It can be seen that the flatness of the inorganic fiber catalyst substrate according to the present invention reduces the thickness after the application of the catalyst. In addition, it can be seen that the bending strengths of Examples 1 to 3 are significantly improved in the bending test as compared with Comparative Example 1.

【0018】すなわち、図3の装置を用いた比較例1で
は、無機繊維織布1に強化液3を含浸後、液切りをして
熱風乾燥機9で加熱した後、織布は図5のように送り方
向の繊維束12のみが引張られて円形の断面になり、そ
れ以外の方向の繊維束12′は過剰な強化液で厚肉化し
ていると考えられる。一方、図1の装置またはその改良
装置を用いた実施例1〜3では、一対の加熱したローラ
7の間を通過させる際、ローラ7より上流側の繊維には
張力がほとんどかからないため、いずれの方向の繊維束
12、12′もローラ7により図6のように平板状に成
形される。そのため基材を巻き取る際に一定の張力で引
張ってもこの形状は維持される。また、加圧しているた
め繊維間は従来法と同様に密着した状態である。従っ
て、実施例1〜3で作製した繊維束はいずれの方向も従
来法の繊維束より薄くなる。
That is, in Comparative Example 1 using the apparatus of FIG. 3, after impregnating the reinforcing liquid 3 into the inorganic fiber woven cloth 1, draining the liquid and heating it with the hot air drier 9, the woven cloth is Thus, it is considered that only the fiber bundle 12 in the feed direction is pulled to have a circular cross section, and the fiber bundle 12 'in the other direction is thickened by an excessive reinforcing liquid. On the other hand, in Examples 1 to 3 using the apparatus of FIG. 1 or the improved apparatus thereof, when passing between the pair of heated rollers 7, almost no tension is applied to the fiber upstream of the roller 7. The fiber bundles 12 and 12 'in the directions are also formed into flat plates by the rollers 7 as shown in FIG. Therefore, this shape is maintained even if the substrate is pulled with a constant tension when winding the substrate. Since the fibers are pressurized, the fibers are in close contact with each other as in the conventional method. Therefore, the fiber bundles produced in Examples 1 to 3 are thinner in all directions than the fiber bundles of the conventional method.

【0019】[0019]

【発明の効果】本発明によれば、無機繊維触媒基材を従
来と同等またはそれ以上の強度を保ったまま薄肉化でき
るので、板状触媒自体の薄肉化が可能となり、例えば触
媒反応装置の低圧損化を図ることができる。
According to the present invention, it is possible to reduce the thickness of the inorganic fiber catalyst substrate while maintaining the same or higher strength as that of the conventional one, so that the thickness of the plate catalyst itself can be reduced. Low pressure loss can be achieved.

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

【図1】本発明の一実施例における無機繊維触媒基材の
製造装置の説明図。
FIG. 1 is an explanatory diagram of an apparatus for producing an inorganic fiber catalyst base material according to one embodiment of the present invention.

【図2】本発明の他の実施例における無機繊維触媒基材
の製造装置の説明図。
FIG. 2 is an explanatory diagram of an apparatus for manufacturing an inorganic fiber catalyst base material according to another embodiment of the present invention.

【図3】従来の無機繊維触媒基材製造装置の説明図。FIG. 3 is an explanatory view of a conventional inorganic fiber catalyst base material manufacturing apparatus.

【図4】板状触媒の説明図。FIG. 4 is an explanatory view of a plate catalyst.

【図5】従来の無機繊維触媒基材の繊維束の形状を示す
説明図。
FIG. 5 is an explanatory view showing the shape of a fiber bundle of a conventional inorganic fiber catalyst substrate.

【図6】本発明の加圧ローラを通過するときの繊維束の
形状を示す説明図。
FIG. 6 is an explanatory diagram showing a shape of a fiber bundle when passing through a pressure roller of the present invention.

【図7】無機繊維織布基材への触媒ペーストの塗布状態
を説明する図。
FIG. 7 is a diagram illustrating a state in which a catalyst paste is applied to an inorganic fiber woven fabric base material.

【符号の説明】[Explanation of symbols]

1…無機繊維織布、2…織布送り出し機、3…強化液、
4…含浸槽、5…液切りローラ、6…テンショナ、7…
厚さ制限ローラ、8…巻き取り機、9…熱風乾燥機、1
0…板状触媒、11…板状触媒山部、12、12′…繊
維束、13、14…ガイドローラ、15…基材、16…
ペースト状触媒組成物、17…触媒塗布体、21、22
…塗布ローラ、23…塗布台、24…塗布補助紙。
1: inorganic fiber woven fabric, 2: woven fabric feeder, 3: reinforcing liquid,
4: impregnation tank, 5: draining roller, 6: tensioner, 7:
Thickness limiting roller, 8: winder, 9: hot air dryer, 1
0: plate-shaped catalyst, 11: plate-shaped catalyst peak, 12, 12 ': fiber bundle, 13, 14: guide roller, 15: base material, 16:
Paste catalyst composition, 17 ... catalyst coated body, 21, 22
... Coating roller, 23 ... Coating table, 24 ... Coating auxiliary paper.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI D06C 29/00 D06C 29/00 A ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI D06C 29/00 D06C 29/00 A

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 無機繊維織布を含浸槽に所定量ずつ送り
出す工程と、該含浸槽にて前記送り出された織布に無機
結合剤を含有する強化液を含浸する工程と、加熱された
一対のローラの間隔またはローラ間の圧力を所定値に保
持しつつ該ローラ間に前記強化液含浸織布を通過させて
所定厚さの基材を得る工程とを備えたことを特徴とする
無機繊維触媒基材の製造方法。
1. A step of feeding a predetermined amount of an inorganic fiber woven fabric to an impregnation tank, a step of impregnating the sent-out woven cloth with a reinforcing liquid containing an inorganic binder in the impregnation tank, A step of passing the reinforcing liquid impregnated woven fabric between the rollers to obtain a base material having a predetermined thickness while maintaining the distance between the rollers or the pressure between the rollers at a predetermined value. A method for producing a catalyst substrate.
【請求項2】 請求項1において、前記強化液を含浸し
た織布を前記加熱ローラ間に供給する前に、強化液含浸
織布の表面を乾燥する工程を備えたことを特徴とする無
機繊維触媒基材の製造方法。
2. The inorganic fiber according to claim 1, further comprising a step of drying the surface of the woven fabric impregnated with the reinforcing liquid before supplying the woven cloth impregnated with the reinforcing liquid between the heating rollers. A method for producing a catalyst substrate.
【請求項3】 無機繊維織布を含浸槽に送る織布送り出
し機と、送り出された前記織布を受取りこれに結合剤を
含有する強化液を含浸させる含浸槽と、強化液を含浸さ
れた前記織布中の余分の強化液を除去する液切り手段
と、液切りされた前記無機繊維織布を所定の間隔または
所定圧力で加熱しつつ加圧する加熱加圧手段とを備えて
いることを特徴とする無機繊維触媒基材の製造装置。
3. A woven fabric feeder for feeding an inorganic fiber woven fabric to an impregnation bath, an impregnation bath for receiving the fed woven fabric and impregnating the woven fabric with a reinforcement liquid containing a binder, and an impregnation liquid impregnated with the reinforcement liquid. It is provided with a draining means for removing excess reinforcing liquid in the woven fabric, and a heating and pressurizing means for applying pressure while heating the drained inorganic fiber woven fabric at a predetermined interval or a predetermined pressure. Characteristic equipment for manufacturing inorganic fiber catalyst base material.
【請求項4】 請求項3において、前記加熱加圧手段
が、加熱された一対の加圧ローラであり、該加圧ローラ
の表面が撥水性かつ耐熱性を有する樹脂で被覆されてい
ることを特徴とする無機繊維触媒基材の製造装置。
4. The method according to claim 3, wherein the heating / pressurizing means is a pair of heated pressure rollers, and the surface of the pressure roller is coated with a resin having water repellency and heat resistance. Characteristic equipment for manufacturing inorganic fiber catalyst base material.
【請求項5】 織布送り出し手段により無機繊維織布を
含浸槽に所定量ずつ送り出し、送り出された織布に無機
結合剤を含有する強化液を含浸し、加熱された一対のロ
ーラの間隔またはローラ間の圧力を所定値に保持しつつ
該ローラ間に前記強化液含浸織布を張力を除去した状態
で供給して該ローラ間を通過させて所定厚さの無機繊維
触媒基材とし、該無機繊維触媒基材の1枚または複数枚
にペースト状の触媒原料を塗布し、乾燥、焼成すること
を特徴とする無機繊維触媒基材を用いた板状触媒の製造
方法。
5. A method for feeding a predetermined amount of an inorganic fiber woven fabric to an impregnation tank by a woven fabric sending means, impregnating the sent woven fabric with a reinforcing liquid containing an inorganic binder, and heating the space between a pair of heated rollers. While maintaining the pressure between the rollers at a predetermined value, the reinforcing liquid-impregnated woven fabric is supplied between the rollers in a state where the tension is removed, and is passed through the rollers to form an inorganic fiber catalyst substrate having a predetermined thickness. A method for producing a plate-shaped catalyst using an inorganic fiber catalyst substrate, wherein a paste-like catalyst material is applied to one or a plurality of inorganic fiber catalyst substrates, dried and calcined.
JP9020671A 1997-02-03 1997-02-03 Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material Pending JPH10216529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9020671A JPH10216529A (en) 1997-02-03 1997-02-03 Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9020671A JPH10216529A (en) 1997-02-03 1997-02-03 Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material

Publications (1)

Publication Number Publication Date
JPH10216529A true JPH10216529A (en) 1998-08-18

Family

ID=12033674

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9020671A Pending JPH10216529A (en) 1997-02-03 1997-02-03 Production of inorganic fiber catalytic base material and device for producing the base material and production of plate-like catalyst using inorganic fiber catalytic base material

Country Status (1)

Country Link
JP (1) JPH10216529A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012121386A1 (en) * 2011-03-10 2012-09-13 株式会社エフ・シ-・シ- Exhaust gas cleaning device
JP2016204815A (en) * 2015-04-21 2016-12-08 ソフォス カンパニー,リミテッド Ultraviolet curing method applied high fastness coloring method of fiber yarn

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2012121386A1 (en) * 2011-03-10 2012-09-13 株式会社エフ・シ-・シ- Exhaust gas cleaning device
JP2012187501A (en) * 2011-03-10 2012-10-04 F C C:Kk Exhaust gas cleaning device
US9500112B2 (en) 2011-03-10 2016-11-22 Kabushiki Kaisha F.C.C. Exhaust gas purifying apparatus
JP2016204815A (en) * 2015-04-21 2016-12-08 ソフォス カンパニー,リミテッド Ultraviolet curing method applied high fastness coloring method of fiber yarn

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