JPS5851909B2 - Manufacturing method for titanium oxide molded products - Google Patents
Manufacturing method for titanium oxide molded productsInfo
- Publication number
- JPS5851909B2 JPS5851909B2 JP50093466A JP9346675A JPS5851909B2 JP S5851909 B2 JPS5851909 B2 JP S5851909B2 JP 50093466 A JP50093466 A JP 50093466A JP 9346675 A JP9346675 A JP 9346675A JP S5851909 B2 JPS5851909 B2 JP S5851909B2
- Authority
- JP
- Japan
- Prior art keywords
- titanium oxide
- alumina
- molded product
- acid
- titanium
- 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.)
- Expired
Links
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 title claims description 45
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 title claims description 25
- 238000004519 manufacturing process Methods 0.000 title claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 18
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 150000007933 aliphatic carboxylic acids Chemical class 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims description 8
- 238000010304 firing Methods 0.000 claims description 6
- 239000001913 cellulose Substances 0.000 claims description 5
- 229920002678 cellulose Polymers 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 150000007522 mineralic acids Chemical class 0.000 claims description 4
- 238000000465 moulding Methods 0.000 claims description 4
- -1 polyethylene Polymers 0.000 claims description 4
- 239000004698 Polyethylene Substances 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 229920002472 Starch Polymers 0.000 claims description 3
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 3
- 239000012736 aqueous medium Substances 0.000 claims description 3
- 239000004202 carbamide Substances 0.000 claims description 3
- 150000001875 compounds Chemical class 0.000 claims description 3
- 229920000573 polyethylene Polymers 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 229920002689 polyvinyl acetate Polymers 0.000 claims description 3
- 239000011118 polyvinyl acetate Substances 0.000 claims description 3
- 239000008107 starch Substances 0.000 claims description 3
- 235000019698 starch Nutrition 0.000 claims description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 21
- 239000003054 catalyst Substances 0.000 description 15
- 239000004408 titanium dioxide Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000000843 powder Substances 0.000 description 7
- 238000001035 drying Methods 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 6
- 238000010521 absorption reaction Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 235000010980 cellulose Nutrition 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- 239000000654 additive Substances 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- DCKVFVYPWDKYDN-UHFFFAOYSA-L oxygen(2-);titanium(4+);sulfate Chemical compound [O-2].[Ti+4].[O-]S([O-])(=O)=O DCKVFVYPWDKYDN-UHFFFAOYSA-L 0.000 description 3
- 229910000348 titanium sulfate Inorganic materials 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 2
- 235000021355 Stearic acid Nutrition 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- 230000003301 hydrolyzing effect Effects 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 230000003472 neutralizing effect Effects 0.000 description 2
- 229910017604 nitric acid Inorganic materials 0.000 description 2
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 description 2
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000008117 stearic acid Substances 0.000 description 2
- LLZRNZOLAXHGLL-UHFFFAOYSA-J titanic acid Chemical compound O[Ti](O)(O)O LLZRNZOLAXHGLL-UHFFFAOYSA-J 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 238000004438 BET method Methods 0.000 description 1
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 1
- 229920000168 Microcrystalline cellulose Polymers 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- AZDRQVAHHNSJOQ-UHFFFAOYSA-N alumane Chemical class [AlH3] AZDRQVAHHNSJOQ-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 229910001593 boehmite Inorganic materials 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001768 carboxy methyl cellulose Substances 0.000 description 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- FOCAUTSVDIKZOP-UHFFFAOYSA-N chloroacetic acid Chemical compound OC(=O)CCl FOCAUTSVDIKZOP-UHFFFAOYSA-N 0.000 description 1
- 229940106681 chloroacetic acid Drugs 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- FAHBNUUHRFUEAI-UHFFFAOYSA-M hydroxidooxidoaluminium Chemical compound O[Al]=O FAHBNUUHRFUEAI-UHFFFAOYSA-M 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229920000609 methyl cellulose Polymers 0.000 description 1
- 239000001923 methylcellulose Substances 0.000 description 1
- 235000019813 microcrystalline cellulose Nutrition 0.000 description 1
- 239000008108 microcrystalline cellulose Substances 0.000 description 1
- 229940016286 microcrystalline cellulose Drugs 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 150000003608 titanium Chemical class 0.000 description 1
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 229910001935 vanadium oxide Inorganic materials 0.000 description 1
Description
【発明の詳細な説明】
本発明は酸化チタン成型物の製造法に関するものである
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing a titanium oxide molded article.
さらに詳しくは、例えば、触媒担体として好適な表面積
、気孔率を有し、かつ実用上充分な強度の酸化チタンを
主成分とする成型物の製造方法に関するものである。More specifically, the present invention relates, for example, to a method for producing a molded article containing titanium oxide as a main component, which has a suitable surface area and porosity as a catalyst carrier, and has sufficient strength for practical use.
一般に、固体触媒は、適当な形状および粒径の担体上に
触媒成分を担持した形態、あるいは触媒成分自体を適当
な形状および粒径に成型した形態で使用し、固定層、移
動層、流動層等の方式が彩用されるが、いずれの場合に
おいても工業的規模で使用するには一定以上の強度が要
求される。In general, solid catalysts are used in the form of a catalyst component supported on a carrier with an appropriate shape and particle size, or in the form of a catalyst component itself molded into an appropriate shape and particle size. The following methods are widely used, but in either case, a certain level of strength is required for use on an industrial scale.
強度が充分でない場合は、反応塔への充填時に崩壊した
り、反応中の風圧、熱衝撃などによる粉化や破壊のため
に、閉塞などを起こして実際の使用に耐えることができ
ない。If the strength is not sufficient, it may collapse during filling into the reaction tower, or it may become clogged due to powdering or destruction due to wind pressure, thermal shock, etc. during the reaction, and cannot withstand actual use.
酸化チタンは触媒担体あるいは触媒自体としで、すぐれ
た性質を有しているが、優れた機械的強度を保持した成
型物を得ることが困難である。Titanium oxide has excellent properties as a catalyst carrier or as a catalyst itself, but it is difficult to obtain molded products that maintain excellent mechanical strength.
例えば、二酸化チタンを触媒担体用の成型物に成型する
には、通常、微細な粉状の二酸化チタンを水と混線し押
出成型機で押出し、適当な長さに切断後、焼成する方法
が採られるが、この場合、強固な凝集が生起し難く、強
度の高い成型物をうることは困難である。For example, in order to mold titanium dioxide into a molded product for use as a catalyst carrier, the usual method is to mix fine powdered titanium dioxide with water, extrude it in an extruder, cut it into appropriate lengths, and then sinter it. However, in this case, strong agglomeration is difficult to occur and it is difficult to obtain a molded product with high strength.
一方、二酸化チタンを1000℃以上の高温で焼結処理
することにより、硬度を非常に大きくし、熱衝撃に対し
ても強くすることができるが、得られる焼結体は極めて
緻密となり、表面積も小さく、触媒担体として適当でな
い。On the other hand, by sintering titanium dioxide at a high temperature of 1000°C or higher, it can be made extremely hard and resistant to thermal shock, but the resulting sintered body becomes extremely dense and has a small surface area. It is small and not suitable as a catalyst carrier.
本発明は触媒担体としてとくに好適な表面積、気孔率を
有し、かつ、実用上充分な強度を有する酸化チタンを主
成分とする成型物を得ることを目的として、種々慣討し
た結果、さきに、酸化チタンを無機酸又は低級脂肪族カ
ルボン酸を含む水性媒体と混合し、焼成する方法を提案
した。The present invention was developed as a result of various studies aimed at obtaining a molded product containing titanium oxide as a main component, which has a particularly suitable surface area and porosity as a catalyst carrier, and has sufficient strength for practical use. proposed a method in which titanium oxide is mixed with an aqueous medium containing an inorganic acid or a lower aliphatic carboxylic acid and then fired.
この方法によれば、強度の優れた酸化チタン成型物を得
ることができるが、触媒担体としての表面積、気孔率に
おいて必ずしも満足しうるものとはいい難い。According to this method, a titanium oxide molded product with excellent strength can be obtained, but it cannot be said that the surface area and porosity as a catalyst carrier are necessarily satisfactory.
本発明者等は上記事情にもとすき更に検討の結果、ある
種の威型助削を添加することにより表面積、気孔率が高
く、かつ強度においても実用上満足しつる酸化チタン成
型物を得ることができることを見い出し本発明に到達し
た。In view of the above circumstances, the inventors of the present invention made further studies and obtained a titanium oxide molded product that has a high surface area, high porosity, and is practically satisfactory in terms of strength by adding a certain type of shaping additive. The present invention was achieved by discovering that this can be done.
すなわち、本発明の要旨は、酸化チタンまたは酸化チタ
ンとアルミナの混合物を、水溶性セルロース系化合物、
ポリアクリルアミド、でんぷん、ポリエチレングリコー
ル、ポリ酢酸ビニル、高級脂肪族カルボン酸、ポリエチ
レン、尿素、活性炭から選ばれた少くとも一種と、無機
酸又は低級脂肪族カルボン酸との存在下、水性媒体と混
合し、成型したのち焼成することを特徴とする酸化チタ
ン成型物の製造法に存する。That is, the gist of the present invention is to combine titanium oxide or a mixture of titanium oxide and alumina with a water-soluble cellulose compound,
At least one selected from polyacrylamide, starch, polyethylene glycol, polyvinyl acetate, higher aliphatic carboxylic acids, polyethylene, urea, and activated carbon is mixed with an aqueous medium in the presence of an inorganic acid or lower aliphatic carboxylic acid. , a method for producing a titanium oxide molded product, characterized in that it is molded and then fired.
以下本発明を更に詳細に説明する。The present invention will be explained in more detail below.
本発明に使用される酸化チタンとしては、例えば四塩化
チタン、硫酸チタンむどのチタン塩を加水分解し、必要
に応じて中和洗浄することにより得られるが、本発明に
おいてはこのようにして得られる湿ケーキをそのまま、
あるいは、一部脱水もしくは乾燥した粉状で使用される
。The titanium oxide used in the present invention can be obtained, for example, by hydrolyzing titanium salts such as titanium tetrachloride and titanium sulfate, and neutralizing and washing as necessary. Leave the wet cake as it is,
Alternatively, it is used in partially dehydrated or dried powder form.
また、乾燥後さらに800℃程度未満の比較的低温で焼
成しして使用することもできる。Further, after drying, it can be further used by firing at a relatively low temperature of less than about 800°C.
酸化チタンは、単独で使用することができるが、アルミ
ナを混合して使用してもよい。Titanium oxide can be used alone, or may be used in combination with alumina.
酸化チタンとアルミナから戒る成型物を得る場合に使用
されるアルミナとしては、例えば常法1こよりアルミナ
水和物の熱分解で製造されたγ−アルミナ、θ−アルミ
ナ、θ−アルミナおよびベーマイトなどのアルミナ水和
物が使われるが、更にアルミナゾルや焼成によりアルミ
ナに転化する硝酸アルミニウムのようなアルミニウム塩
が使用される。Examples of alumina used to obtain a molded product from titanium oxide and alumina include γ-alumina, θ-alumina, θ-alumina, and boehmite produced by thermal decomposition of alumina hydrate using conventional method 1. An alumina hydrate is used, as well as an alumina sol or an aluminum salt such as aluminum nitrate, which is converted to alumina by calcination.
アルミナの添加量は通常、全量に対し0.1〜50重量
%である。The amount of alumina added is usually 0.1 to 50% by weight based on the total amount.
酸化チタンまたは酸化チタンとアルミナとの混合物の成
型に際し使用される助剤としては、結晶性セルロース、
メチルセルロース、カルボキシメチルセルロースおよび
その塩などの水溶性セルロース:ポリアクリルアミド;
でんぷん;ポリエチレングリコール:ポリ酢酸ビニル;
ステアリン酸、パルミチン酸などの高級脂肪族カルボン
酸:ポリエチレン;尿素および活性炭から選ばれた少な
くとも一種が挙げられる。Auxiliary agents used in molding titanium oxide or a mixture of titanium oxide and alumina include crystalline cellulose,
Water-soluble cellulose such as methylcellulose, carboxymethylcellulose and its salts: polyacrylamide;
Starch; Polyethylene glycol: Polyvinyl acetate;
Examples include at least one selected from higher aliphatic carboxylic acids such as stearic acid and palmitic acid; polyethylene; urea and activated carbon.
これらは焼成により炭酸ガスと水として焼失されるため
、二酸化チタン担体の本来の特性を損うことはなく、成
型、焼成後の成型物の表面積、気孔率を高くすることが
できるが、とくに水溶性セルロース化合物、ポリアクリ
ルアミドが好ましい。Since these are burnt off as carbon dioxide gas and water during firing, they do not impair the original properties of the titanium dioxide support and can increase the surface area and porosity of the molded product after molding and firing. Preferred are cellulose compounds and polyacrylamide.
これらの有効な添加量は、通常、酸化チタンまたは酸化
チタンとアルミナの混合物の0.1〜20重量%、好ま
しくは1〜10重量%である。Their effective addition amount is usually 0.1 to 20% by weight, preferably 1 to 10% by weight of the titanium oxide or the mixture of titanium oxide and alumina.
一方、上述の添加物とともに添加する酸とじては、硫酸
、硝酸、塩酸などが挙げられ、また低級脂肪族カルボン
酸としでは、蟻酸、酢酸、プロピオン酸、蓚酸、酪酸、
マレイン酸、クロル酢酸などが挙げられるが、とくに硝
酸または酢酸による効果が著しい。On the other hand, examples of acids added with the above-mentioned additives include sulfuric acid, nitric acid, hydrochloric acid, etc., and examples of lower aliphatic carboxylic acids include formic acid, acetic acid, propionic acid, oxalic acid, butyric acid,
Examples include maleic acid and chloroacetic acid, but nitric acid or acetic acid is particularly effective.
これらの添加量は、酸化チタンまたは酸化チタンとアル
ミナの混合物100部に対して0.01〜50部の範囲
から選ばれるが、通常は0.1〜10部程度添加するの
が効果的であり、水溶液として使用される。The amount of these additives is selected from the range of 0.01 to 50 parts per 100 parts of titanium oxide or a mixture of titanium oxide and alumina, but it is usually effective to add about 0.1 to 10 parts. , used as an aqueous solution.
酸化チタンまたは酸化チタンとアルミナ混合物、前述の
成型助剤および無機酸または低級脂肪族カルボン酸は水
とともに可及的均一に混合した後成型する。Titanium oxide or a mixture of titanium oxide and alumina, the above-mentioned molding aid, and an inorganic acid or lower aliphatic carboxylic acid are mixed as uniformly as possible with water and then molded.
例えば、押出成型機を使用して押出し、適当な寸法に切
断する。For example, it is extruded using an extrusion molding machine and cut into appropriate dimensions.
このようにして成型された成型物は乾燥後焼成される。The molded product thus molded is dried and then fired.
焼成は、通常、空気雰囲気下、1000℃未満、好まし
くは500℃から900℃の範囲で行なわれる。Firing is usually carried out in an air atmosphere at a temperature below 1000°C, preferably in the range from 500°C to 900°C.
加熱温度が1000°Cを越えた場合、強度は増大する
が強固な焼結が起こり、緻密となり表面積、気孔率とも
に著しく減少する。When the heating temperature exceeds 1000°C, the strength increases, but strong sintering occurs, the material becomes dense, and both the surface area and porosity decrease significantly.
焼成時間も、担体の物性および強度に影響を与えるが通
常は1時間ないし10時間で好適に行うことができる。Although the firing time also affects the physical properties and strength of the carrier, it is usually suitably 1 hour to 10 hours.
このようにして得られた成型物は、工業的使用に耐え得
るに充分な機械的強度を有し、かつ触媒担体として充分
な表面積、気孔率などの物理的諸性質を保持しており、
とくに気相接触反応用触媒または該触媒の担体として好
適である。The molded product thus obtained has sufficient mechanical strength to withstand industrial use, and maintains sufficient physical properties such as surface area and porosity as a catalyst carrier.
It is particularly suitable as a catalyst for gas phase catalytic reactions or a carrier for the catalyst.
たとえば、本発明によって得られた成型物に、酸化バナ
ジウムのような触媒金属を担持させた触媒は、窒素酸化
物のアンモニア還元分解用触媒として使用した場合、高
度の触媒活性を長時間保持することができ、しかも長時
間の使用により、破砕、粉化等を生ずるおそれがない。For example, a catalyst obtained by supporting a catalytic metal such as vanadium oxide on a molded product obtained by the present invention maintains a high level of catalytic activity for a long time when used as a catalyst for ammonia reduction and decomposition of nitrogen oxides. Moreover, there is no risk of crushing, pulverization, etc. due to long-term use.
以下、本発明を実施例により説明する。The present invention will be explained below using examples.
なお、実施例および比較例における圧縮強度は本屋式硬
度計により、成型物の長手方向の線耐圧強度として圧縮
強度を測定し、また、表面積はBET法N2ガス吸着に
よって測定した。The compressive strength in the Examples and Comparative Examples was determined by measuring the compressive strength as the linear compressive strength in the longitudinal direction of the molded product using a Honya type hardness tester, and the surface area was measured by N2 gas adsorption using the BET method.
実施例 1
硫酸チタンを加水分解し、中和、洗浄して得た水酸化チ
タンのウェットケーキを乾燥したのち500℃で3時間
焼成して二酸化チタン粉末を得た。Example 1 A wet cake of titanium hydroxide obtained by hydrolyzing, neutralizing and washing titanium sulfate was dried and then calcined at 500° C. for 3 hours to obtain titanium dioxide powder.
この二酸化チタン粉末200.9に微結晶セルロース(
アビセルTG−101、旭化戒工業■製品)6g(3重
量%)と5%酢酸溶液116rILlを加えてよく混練
した。Microcrystalline cellulose (
6 g (3% by weight) of Avicel TG-101 (product of Asahi Kakai Kogyo Co., Ltd.) and 116 rILl of a 5% acetic acid solution were added and kneaded well.
この混合物を押出成型機(不二パウダル■製エツクペレ
ツターEXKF−1)で押出し、カッターで5醋φxi
omiに成型し、乾燥後空気流中で700803時間焼
威した。This mixture was extruded using an extrusion molding machine (EXKPELLETTER EXKF-1 manufactured by Fuji Paudal ■), and a cutter was used to make 5 mm φxi.
After drying, it was baked in an air stream for 700803 hours.
焼成れた成型物の圧縮強度は8.6 kg、表口積は4
6、11 m/ g、吸水率は46%であった。The compressive strength of the fired molded product is 8.6 kg, and the surface area is 4.
6, 11 m/g, and the water absorption rate was 46%.
実施例 2
硫酸チタンを加水分解し、中和洗浄した水酸化チタンの
ウェットケーキを乾燥したのち、600℃で6時間焼成
して二酸化チタン粉末を得た。Example 2 Titanium sulfate was hydrolyzed, a wet cake of titanium hydroxide that had been neutralized and washed was dried, and then calcined at 600° C. for 6 hours to obtain titanium dioxide powder.
この二酸化チタン粉末190gにγ−アルミナ10gと
アゼヒル6gを加え、さらに1%酢酸溶液1287Vl
!を加えて混練した。Add 10 g of γ-alumina and 6 g of Azehil to 190 g of this titanium dioxide powder, and add 1287 Vl of 1% acetic acid solution.
! was added and kneaded.
続いて実施例1と同様に押出成型し、乾燥後空気流通下
800℃で3時間焼成した。Subsequently, extrusion molding was performed in the same manner as in Example 1, and after drying, the product was baked at 800° C. for 3 hours under air circulation.
得られた成型物の圧縮強度はs、 i kllであり、
触媒担体として充分使用しうる強度を有し、表面積は3
7.96 m1g、吸水率は53%であった。The compressive strength of the obtained molded product is s, i kll,
It has sufficient strength to be used as a catalyst carrier, and has a surface area of 3
7.96 ml/g, water absorption rate was 53%.
実施例 3
実施例4と同じ二酸化チタン粉末200gをとり、これ
にポリアクリルアマイド1gと5%酢酸溶液128−を
加え混線した。Example 3 200 g of the same titanium dioxide powder as in Example 4 was taken, and 1 g of polyacrylamide and 128 g of a 5% acetic acid solution were added thereto for crosstalk.
続いて実施例1と同様に押出成型し、乾燥後空気流通下
700℃で3時間焼成した。Subsequently, extrusion molding was performed in the same manner as in Example 1, and after drying, the product was baked at 700° C. for 3 hours under air circulation.
得られた成型物の圧縮強度は10.1kg、表面積は4
3.15m7g、吸水率は42%であった。The compressive strength of the molded product obtained was 10.1 kg, and the surface area was 4.
3.15m7g, water absorption rate was 42%.
実施例 4
実施例1と同じ二酸化チタン粉末20(lとステアリン
酸11をとり、これに1%酢酸溶液110M加えて混疎
し、ついで実施例1と同様に押出し成型し、乾燥後空気
流中で800℃3時間焼成した。Example 4 20 (l) of the same titanium dioxide powder as in Example 1 and 11 stearic acid were taken, 110M of 1% acetic acid solution was added thereto, mixed, and then extrusion molded in the same manner as in Example 1. After drying, the mixture was molded in an air stream. It was fired at 800°C for 3 hours.
得られた成型物の圧縮強度は10.9kg、表面積は3
3.11m/g、吸水率は37%であった。The compressive strength of the obtained molded product was 10.9 kg, and the surface area was 3
The water absorption rate was 3.11 m/g and 37%.
実施例 5
実施例1と同じ二酸化チタン粉末190.9をとり、こ
れに活性炭(成田薬品工業■製白鷺A)を11添加し、
さらに5%酢酸溶液137mA’77pえて混練し、実
施例1と同様にして押出成型した。Example 5 190.9% of the same titanium dioxide powder as in Example 1 was taken, and 11% of activated carbon (Shirasagi A manufactured by Narita Pharmaceutical Co., Ltd.) was added thereto.
Further, 137mA'77p of 5% acetic acid solution was added, kneaded, and extrusion molded in the same manner as in Example 1.
乾燥後これを空気流中でSOO℃3時間焼成した。After drying, it was calcined for 3 hours at SOO° C. in a stream of air.
得られた成型物の圧縮強度は9.7 kg、表面積は3
0、51 rrt/ 9、吸水率は38%であった。The compressive strength of the molded product obtained was 9.7 kg, and the surface area was 3
0.51 rrt/9, water absorption rate was 38%.
Claims (1)
、水溶性セルロース系化合物、ポリアクリルアミド、で
んぷん、ポリエチレングリコール、ポリ酢酸ビニル、高
級脂肪族カルボン酸、ポリエチレン、尿素、活性炭から
選ばれた少なくとも−と無機酸または低級脂肪族カルボ
ン酸との存在下、水性媒体と混合し、成型したのち焼成
することを特徴とする酸化チタン成型物の製造法。1. Titanium oxide or a mixture of titanium oxide and alumina is mixed with at least one selected from water-soluble cellulose compounds, polyacrylamide, starch, polyethylene glycol, polyvinyl acetate, higher aliphatic carboxylic acids, polyethylene, urea, and activated carbon and an inorganic acid. Alternatively, a method for producing a titanium oxide molded product, which comprises mixing it with an aqueous medium in the presence of a lower aliphatic carboxylic acid, molding it, and then firing it.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50093466A JPS5851909B2 (en) | 1975-07-31 | 1975-07-31 | Manufacturing method for titanium oxide molded products |
US05/636,983 US4061596A (en) | 1974-12-02 | 1975-12-02 | Process for preparing titanium oxide shaped carrier |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50093466A JPS5851909B2 (en) | 1975-07-31 | 1975-07-31 | Manufacturing method for titanium oxide molded products |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5216507A JPS5216507A (en) | 1977-02-07 |
JPS5851909B2 true JPS5851909B2 (en) | 1983-11-18 |
Family
ID=14083102
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50093466A Expired JPS5851909B2 (en) | 1974-12-02 | 1975-07-31 | Manufacturing method for titanium oxide molded products |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5851909B2 (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5395892A (en) * | 1977-02-03 | 1978-08-22 | Mizusawa Industrial Chem | Titanium oxide catalyst carrier mold product and manufacture thereof |
JPS56117637A (en) * | 1980-02-21 | 1981-09-16 | Sumitomo Rubber Ind Ltd | Manufacture of reclaimed tyre |
US4547487A (en) * | 1983-05-19 | 1985-10-15 | Gulf Research & Development Company | Process for preparing catalysts |
FR2633605B1 (en) * | 1988-07-01 | 1991-07-12 | Rhone Poulenc Chimie | PROCESS FOR THE PREPARATION OF TITANIUM OXIDE AND TITANIUM OXIDE ARTICLES |
JP2001096154A (en) * | 1999-09-29 | 2001-04-10 | Yamada Sangyo Kk | Vanadium oxide/titania hybrid photocatalyst and its manufacturing method |
-
1975
- 1975-07-31 JP JP50093466A patent/JPS5851909B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5216507A (en) | 1977-02-07 |
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