JPH0393634A - Preparation of porous sintered product having open pores - Google Patents
Preparation of porous sintered product having open poresInfo
- Publication number
- JPH0393634A JPH0393634A JP22449589A JP22449589A JPH0393634A JP H0393634 A JPH0393634 A JP H0393634A JP 22449589 A JP22449589 A JP 22449589A JP 22449589 A JP22449589 A JP 22449589A JP H0393634 A JPH0393634 A JP H0393634A
- Authority
- JP
- Japan
- Prior art keywords
- carbonaceous material
- mixture
- sintered product
- sintered
- 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.)
- Granted
Links
- 239000011148 porous material Substances 0.000 title abstract description 26
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 36
- 239000000463 material Substances 0.000 claims abstract description 36
- 239000000203 mixture Substances 0.000 claims abstract description 30
- 239000011521 glass Substances 0.000 claims abstract description 18
- 239000002994 raw material Substances 0.000 claims abstract description 15
- 239000000843 powder Substances 0.000 claims abstract description 14
- 239000007787 solid Substances 0.000 claims abstract description 8
- 238000003980 solgel method Methods 0.000 claims abstract description 5
- 230000001590 oxidative effect Effects 0.000 claims description 11
- 238000010438 heat treatment Methods 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 19
- 229910052799 carbon Inorganic materials 0.000 abstract description 9
- 238000005245 sintering Methods 0.000 abstract description 7
- 239000000919 ceramic Substances 0.000 abstract description 5
- 238000002156 mixing Methods 0.000 abstract description 4
- 239000003054 catalyst Substances 0.000 abstract description 3
- 229910002804 graphite Inorganic materials 0.000 abstract description 2
- 239000010439 graphite Substances 0.000 abstract description 2
- 239000003610 charcoal Substances 0.000 abstract 1
- 238000002844 melting Methods 0.000 abstract 1
- 230000008018 melting Effects 0.000 abstract 1
- 238000000034 method Methods 0.000 description 19
- 238000004519 manufacturing process Methods 0.000 description 11
- 239000000126 substance Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 238000010304 firing Methods 0.000 description 7
- 239000002245 particle Substances 0.000 description 6
- 230000029087 digestion Effects 0.000 description 5
- 241000894006 Bacteria Species 0.000 description 3
- 229920002134 Carboxymethyl cellulose Polymers 0.000 description 3
- 239000003570 air Substances 0.000 description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 150000004703 alkoxides Chemical class 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000001580 bacterial effect Effects 0.000 description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 description 2
- 239000008112 carboxymethyl-cellulose Substances 0.000 description 2
- 239000001913 cellulose Substances 0.000 description 2
- 229920002678 cellulose Polymers 0.000 description 2
- 229910010293 ceramic material Inorganic materials 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000005361 soda-lime glass Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000002562 thickening agent Substances 0.000 description 2
- 239000000080 wetting agent Substances 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 1
- 239000001888 Peptone Substances 0.000 description 1
- 108010080698 Peptones Proteins 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 description 1
- 230000010065 bacterial adhesion Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000008103 glucose Substances 0.000 description 1
- -1 graphite Chemical compound 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 229910052754 neon Inorganic materials 0.000 description 1
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 1
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 1
- 229910052575 non-oxide ceramic Inorganic materials 0.000 description 1
- 239000011225 non-oxide ceramic Substances 0.000 description 1
- 239000011224 oxide ceramic Substances 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 235000019319 peptone Nutrition 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000008279 sol Substances 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03B—MANUFACTURE, SHAPING, OR SUPPLEMENTARY PROCESSES
- C03B19/00—Other methods of shaping glass
- C03B19/06—Other methods of shaping glass by sintering, e.g. by cold isostatic pressing of powders and subsequent sintering, by hot pressing of powders, by sintering slurries or dispersions not undergoing a liquid phase reaction
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Dispersion Chemistry (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は開放気孔を有する多孔質焼結体の製造方法に関
し、より詳細には開放気孔の大きさと形状を広範囲かつ
精密に制御することができる多孔質焼結体の製造方法に
関する。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for manufacturing a porous sintered body having open pores, and more specifically, to a method for manufacturing a porous sintered body having open pores, and more specifically, to a method for manufacturing a porous sintered body having open pores, and more specifically, a method for manufacturing a porous sintered body having open pores, and more specifically, a method for manufacturing a porous sintered body having open pores. The present invention relates to a method for manufacturing a porous sintered body.
従来、開放気孔を有する多孔質焼結体の製造方法として
は、例えば下記の(1)および(2)の方法が知られて
いる。Conventionally, as a method for producing a porous sintered body having open pores, for example, methods (1) and (2) below are known.
(1)得られる多孔質焼結体の細孔径に合った粒度のガ
ラスを使用し、ガラス粒子同志が結合し、かつ粒子間の
孔がつぶれない程度の温度で焼成する方法。(1) A method of using glass with a particle size that matches the pore diameter of the porous sintered body to be obtained, and firing at a temperature that allows the glass particles to bond with each other and not collapse the pores between the particles.
《2)ガラスまたはセラミックスの母材と、焼成温度で
は固体で、かつ水に可熔性の物質、好ましくは塩類との
混合物を焼威し、大気中または酸化性雰囲気中で焼結し
、焼結完了後に可熔性の物質を水で溶出して多孔体を製
造する方法。[2] A mixture of a glass or ceramic base material and a substance that is solid at the firing temperature and is soluble in water, preferably salts, is sintered in the air or in an oxidizing atmosphere, and then sintered. A method of producing a porous body by dissolving the fusible substance with water after completion of solidification.
しかしながら上記+1)の方法では、適正な焼威温度幅
が狭く、母材の性質によって焼威温度が大きく変化する
.気孔率の大きい物を製造することができない.気孔の
形状の自由度が少ないなどの欠点がある。However, with method +1) above, the appropriate firing temperature range is narrow, and the firing temperature varies greatly depending on the properties of the base material. It is not possible to manufacture products with high porosity. There are drawbacks such as less freedom in the shape of the pores.
また上記(2)の方法では焼戒後に細孔が得られるので
、別途溶液による溶出処理が必要であり、このため設備
および工程が複雑となり、コストも高くなる欠点がある
。In addition, in the method (2) above, since pores are obtained after burning, a separate elution treatment with a solution is required, which has the drawback of complicating the equipment and process and increasing costs.
更に可溶性物質が母材と反応する恐れがあるので、母材
の選択の幅が狭くなり、焼戒温度も制約される欠点があ
る。Furthermore, since there is a possibility that the soluble substance may react with the base material, there is a drawback that the range of selection of the base material is narrowed and the firing temperature is also restricted.
本発明はかかる従来の欠点を解消し、開放気孔の大きさ
と形状を広範囲かつ精密に制御することができる多孔質
焼結体の製造方法を提供することを目的とする。An object of the present invention is to eliminate such conventional drawbacks and provide a method for manufacturing a porous sintered body in which the size and shape of open pores can be precisely controlled over a wide range.
上記課題を解決するため、本発明では、固体ガラス粉末
およびゾル・ゲル法用ガラス原料からなる群から選ばれ
た少なくとも1種の母材と炭素質材料とからなる原料混
合物を、還元性条件下で焼結して焼結混合物を製造し、
ついで該焼結混合物の形状を保持しながら該焼結混合物
を酸化性雰囲気内で加熱して前記炭素質材料を燃焼させ
ることを特徴とするものである.本発明においては、ま
ず、母材と炭素質材料を十分に混合して原料混合物を製
造する.ここで、母材としては固体ガラス粉末、ゾル・
ゲル法用ガラス原料が用いられ、これらは単一種でも良
いし、複数種を混合して使用することもできる。In order to solve the above problems, in the present invention, a raw material mixture consisting of at least one base material selected from the group consisting of a solid glass powder and a glass raw material for sol-gel method and a carbonaceous material is prepared under reducing conditions. sintering to produce a sintered mixture;
The method is characterized in that the sintered mixture is then heated in an oxidizing atmosphere to burn the carbonaceous material while maintaining the shape of the sintered mixture. In the present invention, first, a base material and a carbonaceous material are thoroughly mixed to produce a raw material mixture. Here, the base material is solid glass powder, sol,
Glass raw materials for the gel method are used, and these may be used alone or in a mixture of multiple types.
固体ガラス粉末としては、ほとんどのガラス粉末を使用
することができる.
ゾル・ゲル法用ガラス原料とは、乾燥または加熱するこ
とによってガラス状となるゾルまたはゲルを云い、例え
ばテトラエトキシシランSi(QC z H s )
4 、アルミニウムイソプロポキシド^1(QC 3
H ? ) 3などの金属アルコキシドと酸をアルコー
ルに溶かした溶液に水を加え攪拌することによって得ら
れたゾルまたはゲルである.
この金属アルコキシドから得られるゾルまたはゲルは、
400〜1000℃の温度下に加熱し、水分および気孔
を取り除くことによってガラス状となる。Most glass powders can be used as solid glass powders. The glass raw material for the sol-gel method refers to a sol or gel that becomes glassy by drying or heating, such as tetraethoxysilane Si (QC z H s ).
4, aluminum isopropoxide ^1 (QC 3
H? ) It is a sol or gel obtained by adding water to a solution of a metal alkoxide such as 3 and an acid dissolved in alcohol and stirring. The sol or gel obtained from this metal alkoxide is
It becomes glassy by heating at a temperature of 400 to 1000°C to remove moisture and pores.
また本発明においては、母材として上記以外にセラミッ
クス粉末を選択の対象に含めることもできる.セラミン
クス粉末は特に限定されるものではなく、金属酸化物系
セラミックス、金属非酸化物系セラミックス等が使用さ
れる。Furthermore, in the present invention, ceramic powders other than those mentioned above can also be selected as the base material. The ceramic powder is not particularly limited, and metal oxide ceramics, metal non-oxide ceramics, etc. are used.
炭素質材料としては、有利には黒鉛等の炭素、木炭、活
性炭等の多孔質炭素、セルロース、結晶性セルロース等
の有機物等の高温で炭化しえる物質が使用され、好まし
くは炭素、多孔質炭素である.
母材と炭素質材料との合比率は、使用する母材、炭素質
材料の種類によって異なり、本発明によって得られる多
孔質焼結体における気孔の大きさ、形状や焼結体全容積
に占める気孔の容積比率(気孔率〉を支配するものであ
るが、通常では母材として固体ガラス粉末を使用する場
合には、母材50重量部あたり炭素質材料1〜2500
重量部であり、例えば菌担体として用いる多孔質焼結体
の製造の場合には母材100重量部あたり炭素質材料5
〜200重量部である.また、母材がゾル・ゲル法用ガ
ラス原料の場合には、水分を除去した場合の重量と炭素
質材料の重量比率が100〜lと1〜100の間の範囲
である.
なお、母材としてセラミックス粉末を使用する場合にも
、母材100重量部あたり炭素質材料5〜200重量部
である。As the carbonaceous material, substances that can be carbonized at high temperatures are advantageously used, such as carbon such as graphite, porous carbon such as charcoal, activated carbon, organic substances such as cellulose and crystalline cellulose, and preferably carbon and porous carbon. It is. The combined ratio of the base material and the carbonaceous material varies depending on the type of base material and carbonaceous material used, and it depends on the size and shape of the pores in the porous sintered body obtained by the present invention and the proportion of the total volume of the sintered body. It controls the volume ratio of pores (porosity), but usually when solid glass powder is used as the base material, 1 to 2500 parts of carbonaceous material per 50 parts by weight of the base material.
For example, in the case of manufacturing a porous sintered body used as a bacterial carrier, 5 parts by weight of carbonaceous material per 100 parts by weight of the base material.
~200 parts by weight. Further, when the base material is a glass raw material for sol-gel method, the weight ratio of the weight after removing water to the carbonaceous material is in the range of 100 to 1 and 1 to 100. Note that even when ceramic powder is used as the base material, the amount of carbonaceous material is 5 to 200 parts by weight per 100 parts by weight of the base material.
母材の粒径は、得られる多孔質焼結体の気孔の径によっ
て支配されるが、通常、炭素質材料の3倍以下、好まし
くは1/3以下である。The particle size of the base material is controlled by the pore size of the resulting porous sintered body, but is usually 3 times or less, preferably 1/3 or less, of the carbonaceous material.
一方、炭素質材料の粒径は通常1μ〜10n+sであっ
て得られる多孔質焼結体の気孔径と同一であり、この気
孔径の大きさに従って通常選択される。On the other hand, the particle size of the carbonaceous material is usually 1 μ to 10 n+s, which is the same as the pore size of the resulting porous sintered body, and is usually selected according to the pore size.
この炭素質材の形状は、粉末状、球状、円筒体状、三角
錐状、表面に多数の突起を有する球体状等のいずれでも
良い.
原料混合物には、水等の湿潤剤を添加しても良く、また
、原料混合物の戒形時の形くずれを防止するための助材
、例えばカルボキシメチルセルロース、澱粉のり等を加
えたり、戒形時の粘度を増加させるための各種の増粘材
を添加することもできる.
また、原料混合物は適宜目的とする形状に或形されるが
、戒形にはプレス、遠心、鋳込み、押し出し等の方法が
採用される。The shape of this carbonaceous material may be powder, spherical, cylindrical, triangular pyramid, spherical with many protrusions on the surface, etc. A wetting agent such as water may be added to the raw material mixture, and auxiliary materials such as carboxymethyl cellulose, starch paste, etc. may be added to prevent the raw material mixture from deforming during shaping. Various thickening agents can also be added to increase the viscosity of the product. Further, the raw material mixture is appropriately shaped into a desired shape, and methods such as pressing, centrifugation, casting, extrusion, etc. are employed for shaping.
本発明においては、得られた原料混合物を適宜戒形の後
に還元性条件下で加熱、焼結、または加圧下に加熱、焼
結して、炭素質材料が未変化のままで焼結された母材中
に混入されている状態の焼結混合物を製造する。In the present invention, the obtained raw material mixture is appropriately shaped and then heated and sintered under reducing conditions or heated and sintered under pressure, so that the carbonaceous material is sintered while remaining unchanged. A sintered mixture mixed in a base material is produced.
ここで、還元性条件下とは、炭素質材料を燃焼させずに
母材を焼結することができる状態を意味し、例えば窒素
、炭酸ガス等の非酸化性ガス雰囲気、ヘリウム、ネオン
等の不活性ガス雰囲気下、炭素、有機物等の還元性物質
で上記混合物を覆った状態、あるいは非酸化性ガスや不
活性ガスの雰囲気下で、かつ上記混合物を炭素等の還元
性物質で覆った状態が含まれる.焼結温度は使用する母
材材質によって大きく異なる。例えば母材としてソーダ
石灰ガラスを単独使用した場合には、500〜800℃
、セラ主ックス材料を使用した場合にはセラミックス材
料に通した温度を採用することが好ましい。Here, the term "reducing conditions" refers to a state in which the base material can be sintered without burning the carbonaceous material, such as a non-oxidizing gas atmosphere such as nitrogen or carbon dioxide, or a non-oxidizing gas atmosphere such as helium or neon. A state where the above mixture is covered with a reducing substance such as carbon or an organic substance under an inert gas atmosphere, or a state where the above mixture is covered with a reducing substance such as carbon under an atmosphere of a non-oxidizing gas or an inert gas. is included. The sintering temperature varies greatly depending on the base material used. For example, when soda lime glass is used alone as the base material, the temperature is 500 to 800℃.
When a ceramic material is used, it is preferable to use the temperature that is passed through the ceramic material.
この焼結によって、炭素質材料は燃焼消滅することなく
、母材中に混入された状態になる.次いで本発明におい
ては、得られた焼結混合物を、この焼結混合物の形状を
保持しながら酸化性雰囲気下に加熱し、炭素質材料を酸
化燃焼させ、開放気孔を形威させる.
換言すれば、酸化性雰囲気下に炭素質材料を十分燃焼さ
せることができるが焼結混合物を溶融変形させることの
ない温度に保持する.酸化性雰囲気とは、空気、酸素ま
たは酸素富化空気の雰囲気を意味する.
また、この温度は通常では400℃以上が望ましい.
炭素質材料の燃焼によって開放性気孔を有する多孔質焼
結体が得られる。Due to this sintering, the carbonaceous material is mixed into the base material without being burned away. Next, in the present invention, the obtained sintered mixture is heated in an oxidizing atmosphere while maintaining the shape of the sintered mixture, thereby oxidizing and burning the carbonaceous material to form open pores. In other words, the carbonaceous material is maintained at a temperature that is sufficient to combust the carbonaceous material in an oxidizing atmosphere but does not cause the sintered mixture to melt and deform. Oxidizing atmosphere means an atmosphere of air, oxygen or oxygen-enriched air. In addition, this temperature is normally preferably 400°C or higher. A porous sintered body with open pores is obtained by combustion of the carbonaceous material.
得られた焼結体は、そのまま、または洗浄の後に製品と
なり、化学反応における触媒担持用または菌体付着用等
の用途がある。The obtained sintered body is used as a product as it is or after cleaning, and has uses such as supporting catalysts in chemical reactions or attaching bacterial cells.
以下、本願発明の実施例を述べる.
〔実施例〕
実施例1〜3
下記第1表に示す配合割合でソーダ石灰ガラスと活性炭
を乾燥状態で攪拌混合した後に助材としてのCMC
(カルボキシメチルセルロース)および湿潤材としての
蒸溜水を加えて混練し、直径1 〜1.5+eo+ ,
長さ2 〜5 nowの円筒状に威形した。この戒形体
を粒径250μm未満の活性炭中に埋め、密封した後に
650℃で2時間焼威した.得られた焼威混合物を活性
炭から取り出して大気中で550℃で12時間保持して
多孔性焼結体を製造した。Examples of the present invention will be described below. [Example] Examples 1 to 3 After stirring and mixing soda-lime glass and activated carbon in a dry state at the mixing ratio shown in Table 1 below, CMC was added as an auxiliary material.
(carboxymethylcellulose) and distilled water as a wetting agent and knead to obtain a diameter of 1 to 1.5+eo+,
It has a cylindrical shape with a length of 2 to 5 now. This precept was buried in activated carbon with a particle size of less than 250 μm, sealed, and then incinerated at 650°C for 2 hours. The obtained firing mixture was taken out from the activated carbon and held at 550° C. for 12 hours in the atmosphere to produce a porous sintered body.
第1表
この焼結体中、
実施例3のものについて物性
を測定したところ下記の結果を得た.
真比重 2.5
見掛け比重 0.675
気孔率 73%
なお、水鎮圧人法により測定したところ、細孔径100
μ一以下の気孔率は33%であった.よって、径100
μ一以上の気孔の気孔率は40%と推定されれる。Table 1 Among these sintered bodies, the physical properties of Example 3 were measured and the following results were obtained. True specific gravity: 2.5 Apparent specific gravity: 0.675 Porosity: 73% Pore diameter: 100% when measured using the water suppression method
The porosity below μ1 was 33%. Therefore, the diameter is 100
The porosity of pores with a diameter of μ1 or more is estimated to be 40%.
実施例4
実施例3で得られた焼結体を用い、中温消化法によって
菌付着試験を行った。Example 4 Using the sintered body obtained in Example 3, a bacterial adhesion test was conducted by a mesotemperature digestion method.
すなわち、37℃に保持したvSS濃度6 g/l,容
積負荷3 gTOc / 1・日の嫌気性消化槽中に焼
結体を投入し、下記日数の経過後に取り出し、洗浄して
菌付着量(重量増加量)を測定した。That is, the sintered body was placed in an anaerobic digestion tank maintained at 37°C with a vSS concentration of 6 g/l and a volume load of 3 gTOc/1 day, and after the following number of days had elapsed, it was taken out, washed, and the amount of bacteria attached ( weight increase) was measured.
結果を下記に示す。The results are shown below.
10日後 35.9mg/g
20日後 37.8mg/g
35日後 40.9mg/g
50日後 44.6mg/g
上記方法で付着させた固定化菌を用いた嫌気性消化槽に
原水濃度500mgTOC/ 1 (グルコース、ペプ
トン系人工下水)を供給し、消化を行ったところ、第l
相消化(酸生t&)の}IRTは2時間〜3時間である
ことがわかった.これらの結果は浮遊菌完全混合型消化
槽に比べてHRTが1/2〜173程度で、優れた特性
を示した.〔発明の効果〕
以上述べたように本発明によれば、原料混合物が還元性
条件下で焼結されるので、炭素質材料を燃焼によって損
なうことなく、母材中に混入させることができる.
一般に炭素質材料は還元性条件下、高温での反応性が低
いので、母材の焼結温度がかなり高温の場合でも母材と
炭素質材料との反応を回避することができる.
また、母材中に混入する可能性のある物質を炭素質材料
に限定することができるので、焼結後の母材の性質を殆
ど変えることがない.増粘材や助材が原料混合物中に混
入されていても、焼成中に炭化するので母材の性質に影
響を与えることが少ない。After 10 days: 35.9 mg/g After 20 days: 37.8 mg/g After 35 days: 40.9 mg/g After 50 days: 44.6 mg/g The raw water concentration was 500 mg TOC/1 in an anaerobic digestion tank using the immobilized bacteria attached using the above method. (glucose, peptone-based artificial sewage) was supplied, and digestion was performed.
The IRT for phase digestion (acidic t&) was found to be 2 to 3 hours. These results showed that the HRT was about 1/2 to 173 compared to the suspended bacteria complete mixing type digester, indicating excellent characteristics. [Effects of the Invention] As described above, according to the present invention, since the raw material mixture is sintered under reducing conditions, the carbonaceous material can be mixed into the base material without being damaged by combustion. In general, carbonaceous materials have low reactivity under reducing conditions and at high temperatures, so it is possible to avoid reaction between the base material and the carbonaceous material even if the sintering temperature of the base material is quite high. Furthermore, since the substances that may be mixed into the base material can be limited to carbonaceous materials, the properties of the base material after sintering are hardly changed. Even if thickeners or auxiliary materials are mixed into the raw material mixture, they will carbonize during firing, so they will have little effect on the properties of the base material.
更にまた本発明においては、母材中に還元性雰囲気下で
炭素質材料が混入された後に焼結混合物の形状を保持し
ながら炭素質材料が酸化性雰囲気下で燃焼されるので、
開放気孔の形威による焼結混合物の収縮を伴う形状変化
を極力回避することができる.
しかも気孔の形状や大きさは、炭素質材料の種類や添加
量によって基本的に支配されるが、炭素質材料は加工性
が良好であり、かつ種類も多いので選択の自由度が高く
、従って気孔の形状や大きさを広範囲かつ精密に制御す
ることができる.
また、従来の方法のように焼結後に可溶性物質の溶出の
ような後処理を必要としないので、製造コストを容易に
低下させることができる。Furthermore, in the present invention, after the carbonaceous material is mixed into the base material under a reducing atmosphere, the carbonaceous material is burned under an oxidizing atmosphere while maintaining the shape of the sintered mixture.
Changes in shape due to shrinkage of the sintered mixture due to the shape of open pores can be avoided as much as possible. Moreover, the shape and size of pores are basically controlled by the type and amount of carbonaceous material added, but carbonaceous materials have good workability and are available in many types, so there is a high degree of freedom in selection. Pore shape and size can be controlled over a wide range and precisely. Further, unlike conventional methods, post-processing such as elution of soluble substances is not required after sintering, so manufacturing costs can be easily reduced.
更に得られる多孔質焼結体を外径11〜数10−、内径
0.5〜数lOIIII、厚さ0.5〜数10III1
のリング状とすれば、触媒担体として使用するに際し、
カラムへの充填およびかさ密度のコントロールが容易と
なり、かつカラム内において十分な強度と均一性とを確
保することができる.工業技術院長の復代理人
岡本特殊硝子株式会社及び
互栄商事株式会社の代理人Furthermore, the obtained porous sintered body has an outer diameter of 11 to several 10 mm, an inner diameter of 0.5 to several 10 mm, and a thickness of 0.5 to several 10 mm.
If it is ring-shaped, when used as a catalyst carrier,
It becomes easy to control column packing and bulk density, and it is possible to ensure sufficient strength and uniformity within the column. Agent for Okamoto Special Glass Co., Ltd. and Kōei Shoji Co., Ltd., sub-agents of the Director of the Agency of Industrial Science and Technology
Claims (1)
なる群から選ばれた少なくとも1種の母材と炭素質材料
とからなる原料混合物を、還元性条件下で焼結して焼結
混合物を製造し、ついで該焼結混合物の形状を保持しな
がら該焼結混合物を酸化性雰囲気内で加熱して前記炭素
質材料を燃焼させることを特徴とする開放気孔を有する
多孔質焼結体の製造方法A raw material mixture consisting of at least one base material selected from the group consisting of solid glass powder and glass raw materials for sol-gel method and a carbonaceous material is sintered under reducing conditions to produce a sintered mixture. , and then heating the sintered mixture in an oxidizing atmosphere to burn the carbonaceous material while maintaining the shape of the sintered mixture.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1224495A JPH0623060B2 (en) | 1989-09-01 | 1989-09-01 | Method for producing porous sintered body having open pores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1224495A JPH0623060B2 (en) | 1989-09-01 | 1989-09-01 | Method for producing porous sintered body having open pores |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0393634A true JPH0393634A (en) | 1991-04-18 |
JPH0623060B2 JPH0623060B2 (en) | 1994-03-30 |
Family
ID=16814692
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1224495A Expired - Fee Related JPH0623060B2 (en) | 1989-09-01 | 1989-09-01 | Method for producing porous sintered body having open pores |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0623060B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05172100A (en) * | 1991-10-09 | 1993-07-09 | Hitachi Ltd | Centrifugal fan, fan of car air conditioner and car air conditioner equipped with centrifugal fan |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5321211A (en) * | 1976-08-11 | 1978-02-27 | Tokushiyu Muki Zairiyou Kenkiy | Complex of electrooconductive inorganic glass and method of manufacturing thereof |
JPH01294545A (en) * | 1988-05-20 | 1989-11-28 | Nippon Telegr & Teleph Corp <Ntt> | Method for forming glass |
-
1989
- 1989-09-01 JP JP1224495A patent/JPH0623060B2/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5321211A (en) * | 1976-08-11 | 1978-02-27 | Tokushiyu Muki Zairiyou Kenkiy | Complex of electrooconductive inorganic glass and method of manufacturing thereof |
JPH01294545A (en) * | 1988-05-20 | 1989-11-28 | Nippon Telegr & Teleph Corp <Ntt> | Method for forming glass |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH05172100A (en) * | 1991-10-09 | 1993-07-09 | Hitachi Ltd | Centrifugal fan, fan of car air conditioner and car air conditioner equipped with centrifugal fan |
Also Published As
Publication number | Publication date |
---|---|
JPH0623060B2 (en) | 1994-03-30 |
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