JPS63245447A - Production of porous article - Google Patents
Production of porous articleInfo
- Publication number
- JPS63245447A JPS63245447A JP8069587A JP8069587A JPS63245447A JP S63245447 A JPS63245447 A JP S63245447A JP 8069587 A JP8069587 A JP 8069587A JP 8069587 A JP8069587 A JP 8069587A JP S63245447 A JPS63245447 A JP S63245447A
- Authority
- JP
- Japan
- Prior art keywords
- forming agent
- resin
- porous body
- reaction
- curing
- 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
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 26
- 229920005989 resin Polymers 0.000 claims abstract description 16
- 239000011347 resin Substances 0.000 claims abstract description 16
- 229920003002 synthetic resin Polymers 0.000 claims abstract description 10
- 239000000057 synthetic resin Substances 0.000 claims abstract description 10
- 239000003054 catalyst Substances 0.000 claims abstract description 9
- 239000011148 porous material Substances 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 13
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 abstract description 16
- 229920002472 Starch Polymers 0.000 abstract description 8
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 8
- 239000005011 phenolic resin Substances 0.000 abstract description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 229940100445 wheat starch Drugs 0.000 abstract description 3
- KXGFMDJXCMQABM-UHFFFAOYSA-N 2-methoxy-6-methylphenol Chemical compound [CH]OC1=CC=CC([CH])=C1O KXGFMDJXCMQABM-UHFFFAOYSA-N 0.000 abstract description 2
- 239000000203 mixture Substances 0.000 abstract description 2
- 229920001568 phenolic resin Polymers 0.000 abstract description 2
- 229920002554 vinyl polymer Polymers 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 description 23
- 230000000052 comparative effect Effects 0.000 description 12
- 239000000047 product Substances 0.000 description 10
- 239000011550 stock solution Substances 0.000 description 10
- 239000000463 material Substances 0.000 description 8
- 239000007795 chemical reaction product Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 239000008107 starch Substances 0.000 description 5
- 235000019698 starch Nutrition 0.000 description 5
- 239000004372 Polyvinyl alcohol Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- 239000000839 emulsion Substances 0.000 description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 239000006061 abrasive grain Substances 0.000 description 3
- 239000003431 cross linking reagent Substances 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000003825 pressing Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 229920001342 Bakelite® Polymers 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000007689 inspection Methods 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000005498 polishing Methods 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000003082 abrasive agent Substances 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- LNEPOXFFQSENCJ-UHFFFAOYSA-N haloperidol Chemical compound C1CC(O)(C=2C=CC(Cl)=CC=2)CCN1CCCC(=O)C1=CC=C(F)C=C1 LNEPOXFFQSENCJ-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 238000010907 mechanical stirring Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Filtering Materials (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は、気孔生成剤に起因する以外の気泡の発生を
抑え、均質な多孔質体を取得する多孔質体の製法に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for producing a porous body that suppresses the generation of bubbles other than those caused by a pore-forming agent and obtains a homogeneous porous body.
各種多孔質体製造工業において、気孔生成剤を用いる製
法は、他の発泡法等に比較して均質かつ微細な気孔が得
られ、しかも得られた気孔は連続気孔であるため、単な
るクッション材、緩衝材のみならず、濾過材、吸液材あ
るいは研暦材として幅広く応用されている。In various porous material manufacturing industries, manufacturing methods using pore-forming agents produce more homogeneous and finer pores than other foaming methods, and the resulting pores are continuous, so they can be used as mere cushioning materials, It is widely used not only as a buffer material, but also as a filter material, liquid absorbent material, and research material.
上記製法は、基材となる樹脂の種類等により各々異なる
が、基本となる反応形式は下記に示すようなものである
。Although the above production methods differ depending on the type of resin used as the base material, the basic reaction format is as shown below.
すなわち、架橋剤、触媒および気孔生成剤である微粉あ
るいはエマルジョンが均一分散された合成樹脂の樹脂液
(原液)を加温状態に置き反応を完結せしめた後、水洗
1機械洗浄等の手段をもって上記微粉、エマルジョン等
の気孔生成剤を除去するものである。That is, a resin solution (undiluted solution) of a synthetic resin in which fine powder or emulsion as a crosslinking agent, a catalyst, and a pore-forming agent are uniformly dispersed is heated to complete the reaction, and then the above-mentioned process is carried out by washing with water, mechanical washing, etc. This removes pore-forming agents such as fine powder and emulsions.
前記の従来の方法においては、原液と架橋剤。 In the conventional method described above, a stock solution and a crosslinking agent are used.
触媒あるいは気孔生成剤を混合する際、機械的攪拌方法
を用いるため空気を巻き込みやすく、これが反応系の液
中の気泡となり、反応後も製品中の気泡となって残留す
るも量率が高く、製品の品質。When mixing the catalyst or pore-forming agent, mechanical stirring is used, which tends to entrain air, which becomes air bubbles in the reaction system liquid and remains as air bubbles in the product even after the reaction, but the volume ratio is high. Product quality.
歩留りあるいは性能の低下をきたすという欠点があった
。特に、濾過用途、研磨用途に応用された場合には、製
品としての重大な欠点となりかねず、この検査工程に多
大な負担を与えていた。This method has the drawback of decreasing yield or performance. In particular, when applied to filtration or polishing applications, this could lead to serious defects as a product, placing a great burden on the inspection process.
上記のような弊害を防止するため、原液を型枠に注型す
る際、スリット状の注型孔を用いて気孔を消滅させる、
あるいは減圧という手段を用いて内部の気泡を浮上させ
消滅させる等の方法が講じられているが、溶液が高粘度
であったり、液槽が深かったりした場合は効果が少なく
極めて不充分である。さらに、径の大きな気孔は比較的
消滅しやすいが、径が小さい細径の気泡は消滅し難く、
例えば、l *m以下の気泡は消滅させることが極めて
困難である。In order to prevent the above-mentioned adverse effects, when pouring the stock solution into the mold, slit-shaped casting holes are used to eliminate the pores.
Alternatively, methods such as using a means of depressurization to float and eliminate internal air bubbles have been taken, but this method is less effective and extremely insufficient if the solution has a high viscosity or the liquid tank is deep. Furthermore, large-diameter pores are relatively easy to eliminate, but small-diameter bubbles are difficult to eliminate.
For example, bubbles smaller than l*m are extremely difficult to eliminate.
この発明は、このような事情に鑑みなされたもので、気
孔生成剤に起因する連続気孔以外の独立気泡、特に径が
小さい細径の気泡が残留しない多孔質体の製法の提供を
その目的とする。The present invention was made in view of the above circumstances, and its purpose is to provide a method for producing a porous body in which closed cells other than continuous pores caused by a pore-forming agent, especially small-diameter cells, do not remain. do.
上記の目的を達成するため、この発明は、硬化剤、触媒
および気孔生成剤が均一分散された合成樹脂の樹脂液を
準備し、この樹脂液を硬化させて硬化体をつくり、この
硬化体から気孔生成剤を除去してその除去跡を気孔化す
る多孔質体の製法であって、上記樹脂液の硬化を加圧下
で行うという構成をとる。In order to achieve the above object, the present invention prepares a resin liquid of a synthetic resin in which a curing agent, a catalyst, and a pore-forming agent are uniformly dispersed, and hardens this resin liquid to create a cured body. This is a method for producing a porous body in which a pore-forming agent is removed and the residue left behind is made into pores, and the resin liquid is cured under pressure.
すなわち、本発明者らは上記の目的を達成するため一連
の研究を重ねた結果、多孔質体を製造するにあたって、
準備した合成樹脂液を所定の型枠に注型し硬化反応させ
る過程で、オートクレーブ等の高圧反応容器に入れ加圧
することによって、気孔生成剤に起因する連続気孔以外
の独立気泡が残留しない多孔質体が得られることを見い
だしこの発明に到達した。In other words, as a result of a series of studies conducted by the present inventors to achieve the above object, in manufacturing a porous body,
During the process of pouring the prepared synthetic resin liquid into a predetermined mold and allowing it to undergo a curing reaction, it is placed in a high-pressure reaction vessel such as an autoclave and pressurized, creating a porous structure in which closed cells other than open pores caused by the pore-forming agent remain. This invention was achieved by discovering that the body can be improved.
つぎに、この発明について詳しく説明する。Next, this invention will be explained in detail.
この発明の対象とする多孔質体は、ポリビニルホルマー
ル系樹脂、フェノール系樹脂、エポキシ系樹脂、酢酸ビ
ニル系樹脂あるいはアセテート系樹脂等を原料とするも
のおよびそれらを組み合わせて得られる多孔質体を意味
する。すなわち、流動性を有する原料中に、微細粒子、
エマルジョン。The porous body to which this invention is applied refers to porous bodies made from polyvinyl formal resins, phenol resins, epoxy resins, vinyl acetate resins, acetate resins, etc., and porous bodies obtained by combining them. do. In other words, fine particles,
emulsion.
具体的には、澱粉およびその誘導体、ポリエチレングリ
コール2ポリプロピレングリコールおよびその誘導体の
エマルジョンを投入、均一に攪拌し、樹脂を硬化させた
後、洗浄等の手段をもって気孔生成剤を除去する方法、
つまり気孔生成剤抽出法によって製造される多孔質体を
意味する。この発明の多孔質体は、他の製法、すなわち
発泡法によって製造される多孔質体とは、その有する性
質において下記(a)〜(c)に示すような利点を有す
る。Specifically, a method of adding an emulsion of starch and its derivatives, polyethylene glycol 2 polypropylene glycol and its derivatives, stirring uniformly, curing the resin, and then removing the pore forming agent by means such as washing;
In other words, it means a porous body produced by a pore-forming agent extraction method. The porous body of the present invention has the following advantages (a) to (c) in terms of its properties compared to porous bodies manufactured by other manufacturing methods, that is, foaming methods.
(a)気孔径が均一であること。(a) The pore diameter is uniform.
(b)連続気孔であること。(b) Continuous pores.
(c)微細気孔を有する多孔質体が製造可能であること
。(c) Porous bodies having micropores can be manufactured.
上記利点を応用しての用途としては、濾過材。An example of an application that takes advantage of the above advantages is as a filtration material.
吸水材あるいは組織内に砥粒を分散させた研磨材等純粋
な工業用途が多い。しかし、このような工業用途におい
ては、多孔質体本来が有する連続気孔以外の独立気泡は
、その特性に影響を与えやすい。すなわら、連続気孔は
、多孔質体の表面まで気孔が連続しているのに対し、独
立気泡は多孔質体中に泡状に分布している。このような
独立気泡の存在は、濾過材用途においては濾過特性を狂
わせ、研磨材用途においてはその独立気泡部分が欠点と
なり研磨性能を変化させるのみならず、硬質のものにお
いてはその総合的強度を著しく低下させる。There are many pure industrial uses such as water-absorbing materials or abrasive materials with abrasive grains dispersed within the structure. However, in such industrial applications, closed cells other than the continuous pores inherent in the porous material tend to affect its properties. That is, in the case of continuous pores, the pores are continuous up to the surface of the porous body, whereas in the case of closed pores, the pores are distributed in the form of bubbles in the porous body. The presence of such closed cells disrupts the filtration characteristics in filter media applications, and in abrasive applications, the closed cell portion becomes a drawback and not only changes the polishing performance, but also impairs the overall strength of hard materials. Significantly lower.
この発明の方法によれば、原液系に混入された独立気泡
は加圧下において液中に吸収されるため完全に消滅する
。そして、原液が初1υ1の硬化時期を経過したのち、
適宜の段階で加圧を解除すると、加圧下で消滅していた
独立気泡が再び発生するが、その気泡中の空気は、すで
に形成した多孔体組織(初期硬化を経ており剛性を備え
ている)を破壊することはない。このように、反応開始
後、初期硬化に至るまでの短時間、反応系を加圧下にお
けば、かかる気泡の残留は完全に解消される。しかも、
型枠の深さが表面積に比較して深いものであっても、深
層部までその効果は及ぶ。According to the method of this invention, closed air bubbles mixed into the stock solution system are absorbed into the solution under pressure and are completely eliminated. Then, after the stock solution has passed the initial 1υ1 hardening period,
When the pressure is released at an appropriate stage, the closed cells that disappeared under the pressure will regenerate, but the air in these cells will be replaced by the already formed porous structure (which has undergone initial hardening and has rigidity). will not be destroyed. As described above, if the reaction system is kept under pressure for a short period of time after the start of the reaction until the initial curing, the residual air bubbles can be completely eliminated. Moreover,
Even if the depth of the formwork is greater than the surface area, the effect extends to the deeper layers.
上記加圧方法は、原液を型枠に注型し、オートクレーブ
等の高圧容器に入れ、圧縮空気の封入または加圧蒸気の
封入等の気体を利用した加圧により行われ、このような
加圧下で少なくとも初期硬化が生起するまで反応させる
ことがなされる。この場合、加圧条件は1.0kg/c
J以上であることが好ましく、特に効果の点から1.5
kg / ad〜15kg/ CIl+に設定するこ
とが好適である。圧力が1.0 kg/cIA未満の場
合、効果が小さく独立気泡を充分に液中に吸収し得ない
場合がある。なお、上記のような気体を利用した加圧に
代えて、例えばエクストル−クンプレス機等による機械
的加圧を行うと、気孔生成剤たる澱粉等の粒子が破壊さ
れ所期の物性と異なるものが得られる場合があり好まし
くない。The above pressurization method is performed by pouring the stock solution into a mold, placing it in a high-pressure container such as an autoclave, and pressurizing it using a gas such as enclosing compressed air or pressurized steam. The reaction is carried out at least until initial curing occurs. In this case, the pressurization condition is 1.0 kg/c
J or higher is preferable, especially 1.5 from the viewpoint of effectiveness.
It is preferable to set it between kg/ad and 15 kg/CIl+. If the pressure is less than 1.0 kg/cIA, the effect may be small and closed cells may not be sufficiently absorbed into the liquid. In addition, if mechanical pressure is applied, for example, using an extrusion press machine, instead of the above-mentioned pressure using gas, particles such as starch, which is a pore-forming agent, may be destroyed and the physical properties may differ from the intended ones. This is not preferable in some cases.
つぎに、実施例について比較例と併せて説明する。Next, examples will be described together with comparative examples.
〔実施例1〕
重合度1700完全けん化のポリビニルアルコール95
0gを温水に溶解して15重量%(以下「%」と略す)
の水溶液を調製し、これに、硬化剤としてのホルムアル
デヒド、触媒としての硫酸を加え、全量をIONとなし
反応原液を調製した。[Example 1] Completely saponified polyvinyl alcohol 95 with a degree of polymerization of 1700
Dissolve 0g in warm water to make 15% by weight (hereinafter abbreviated as "%")
An aqueous solution of was prepared, and formaldehyde as a curing agent and sulfuric acid as a catalyst were added thereto, and the entire amount was converted into ION to prepare a reaction stock solution.
これを55℃に保持し、内径3Qmmφ、深さ30Q
mmの円筒形型枠に注型した。This is maintained at 55℃, inner diameter 3Qmmφ, depth 30Q
It was cast into a cylindrical mold of mm.
つぎに、反応原液を入れた円筒形型枠を加圧釜に入れ、
7 kg / cnlの圧力下において60°Cで加温
2時間保持した後、さらに温度60℃、常圧の条件にお
いて18時間反応を続けた。反応終了後、型枠より反応
生成物を取り出し水洗により過剰のホルムアルデヒド、
硫酸および澱粉を抽出除去しスポンジ状多孔質弾性体を
得た。Next, place the cylindrical mold containing the reaction stock solution into a pressure cooker.
After heating and holding at 60°C for 2 hours under a pressure of 7 kg/cnl, the reaction was continued for 18 hours at a temperature of 60°C and normal pressure. After the reaction is complete, remove the reaction product from the mold and wash with water to remove excess formaldehyde.
Sulfuric acid and starch were extracted and removed to obtain a sponge-like porous elastic body.
〔実施例2〕
加圧条件を1.2 kg / ctAに代えた。それ以
外は実施例1と同様にしてスポンジ状多孔質弾性体を得
た。[Example 2] The pressurization conditions were changed to 1.2 kg/ctA. A spongy porous elastic body was obtained in the same manner as in Example 1 except for the above.
〔比較例1〕
加圧せずそのまま60℃の雰囲気下において200時間
反応行った。それ以外は実施例1と同様にしてスポンジ
状多孔質弾性体を得た。[Comparative Example 1] The reaction was carried out for 200 hours in an atmosphere of 60° C. without applying pressure. A spongy porous elastic body was obtained in the same manner as in Example 1 except for the above.
以上の実施例1,2および比較例1より得られたスポン
ジ状多孔質弾性体を中央部にて切断し、多孔質体本来の
連続気孔以外の独立気泡の数を測定した。その結果を第
1表に示す。The sponge-like porous elastic bodies obtained in Examples 1 and 2 and Comparative Example 1 were cut at the center, and the number of closed cells other than the continuous pores inherent in the porous bodies was measured. The results are shown in Table 1.
第1表から・加圧条件下において得られた実施例1の多
孔質体は、独立気泡が全くなく著しく優れている。しか
し、実施例2のように、1.2kg/cnl程度の低圧
条件ではその効果が不充分であるが、それでも加圧を全
く行わない比較例品よりも優れている。なお、実施例1
および実施例2で得られた多孔質体は、その他の特性は
比較例1のものと全く異なることなく同等であった。From Table 1: The porous material of Example 1 obtained under pressurized conditions has no closed cells and is extremely excellent. However, as in Example 2, the effect is insufficient under the low pressure condition of about 1.2 kg/cnl, but it is still superior to the comparative example product in which no pressurization is applied. In addition, Example 1
The porous body obtained in Example 2 was the same as that of Comparative Example 1 with no difference in other properties.
〔実施例3〕
水溶性フェノール樹脂水溶液(住友ベークライト社製、
PR−961A、)に対し、平均重合度1700の完全
けん化ポリビニルアルコール(以下rPVAJと略す)
を、その比率が1/10となるように添加して液状体を
調製した。ついで、これに、硬化剤としてのホルマリン
、触媒としての硫酸さらに気孔生成剤としての小麦澱粉
を加え均l拌し、実施例1で用いたのと同様の型枠に注
型した。[Example 3] Water-soluble phenol resin aqueous solution (manufactured by Sumitomo Bakelite Co., Ltd.,
PR-961A,), completely saponified polyvinyl alcohol (hereinafter abbreviated as rPVAJ) with an average degree of polymerization of 1700
were added at a ratio of 1/10 to prepare a liquid. Next, formalin as a hardening agent, sulfuric acid as a catalyst, and wheat starch as a pore-forming agent were added to this, and the mixture was mixed and poured into the same mold as used in Example 1.
つぎに、上記反応原液を入れた型枠を加圧釜に入れ、7
kg / cJの加圧下において50℃に保持しつつ
2時間反応を行い、さらに得られた反応生成物を加圧釜
より取り出し、温度50℃、常圧の条件において18時
間反応を続げた。反応終了後、反応生成物をシャワーに
より洗浄し、酸、ホルマリンおよび澱粉を除去した。つ
いで反応生成物を乾燥したのち、窒素気流下、150℃
においてキユアリングを行い合成樹脂多孔質体を得た。Next, put the mold containing the above reaction stock solution into a pressure cooker, and then
The reaction was carried out for 2 hours while maintaining the temperature at 50°C under a pressure of kg/cJ, and the obtained reaction product was taken out from the pressure cooker, and the reaction was continued for 18 hours at a temperature of 50°C and normal pressure. After the reaction was completed, the reaction product was washed with a shower to remove acid, formalin, and starch. After drying the reaction product, it was heated at 150°C under a nitrogen stream.
A synthetic resin porous body was obtained by curing.
〔比較例2〕 加圧せず50°Cにおいて20時間反応を行った。[Comparative example 2] The reaction was carried out at 50°C for 20 hours without applying pressure.
それ以外は実施例2と同様にして合成樹脂多孔質体を得
た。A synthetic resin porous body was obtained in the same manner as in Example 2 except for the above.
以上の実施例3および比較例2より得られた合成樹脂多
孔質体より、断面l cm角・長さlQcmの試料を各
20個採取し、長さlQcm当たりの気泡の数および曲
げ強度を測定した。その結果を第2表および第3表に示
す。From the synthetic resin porous bodies obtained in Example 3 and Comparative Example 2, 20 samples each with a cross section of 1 cm square and length of 1 Q cm were collected, and the number of bubbles per length of 1 Q cm and bending strength were measured. did. The results are shown in Tables 2 and 3.
(以下余白) *:(最高値−最低値)の値である。(Margin below) *: Value of (highest value - lowest value).
比較例2に比較し、実施例3より得られた合成樹脂多孔
質体は気泡の数が少なく、曲げ強度におぃてばらつきが
少ない。すなわち、比較例2より得られた合成樹脂多孔
質体は気泡が数多く存在するため、強度がかなり低下し
ていることが明らかである。Compared to Comparative Example 2, the synthetic resin porous body obtained in Example 3 has fewer bubbles and less variation in bending strength. That is, it is clear that the synthetic resin porous body obtained in Comparative Example 2 has a considerable decrease in strength because of the presence of many air bubbles.
〔実施例4〕
重合度1700の完全けん化PVAの10%水溶液に、
平均粒子径5μmの炭化けい素微粉末よりなる砥粒を均
一分散せしめ、気孔生成剤として小麦澱粉、架橋剤とし
て37%ホルムアルデヒド水溶液、触媒として塩酸を適
量加えた。つぎに、これに、フェノール樹脂初期縮合体
(住友ベークライト社製、PR−961A)を加え全体
を精鋼なスラリー状原液とし、これを攪拌機を用いて均
一に撹拌混合を行った。[Example 4] In a 10% aqueous solution of completely saponified PVA with a degree of polymerization of 1700,
Abrasive grains made of fine silicon carbide powder having an average particle diameter of 5 μm were uniformly dispersed, and wheat starch as a pore-forming agent, a 37% formaldehyde aqueous solution as a crosslinking agent, and an appropriate amount of hydrochloric acid as a catalyst were added. Next, a phenolic resin initial condensate (manufactured by Sumitomo Bakelite Co., Ltd., PR-961A) was added to this to form a refined steel slurry stock solution, which was uniformly stirred and mixed using a stirrer.
上記各成分の配合比率は、PVA30%、フェノール樹
脂20%、砥粒50%である。The blending ratio of each of the above components is 30% PVA, 20% phenol resin, and 50% abrasive grains.
このようにして、均一に攪拌混合された原液を実施例1
と同様の型枠に注型した後加圧釜に入れ、10kg/c
nlの加圧下において60℃に保持しつつ2時間反応を
続けた。さらに、常圧にもどし60℃において10時間
反応を行った。つぎに、反応生成物を型枠より取り出し
、流水により洗浄し、澱粉、過剰の酸およびホルムアル
デヒドを除去し、合成砥石の初期生成物を得た。この合
成砥石の初期生成物を130℃において5時間加熱キユ
アリングし、フェノール樹脂の硬化反応を促進せしめ合
成砥石を得た。Example 1 The stock solution uniformly stirred and mixed in this way was
After pouring into a mold similar to that of
The reaction was continued for 2 hours while maintaining the temperature at 60°C under a pressure of nl. Furthermore, the pressure was returned to normal and the reaction was carried out at 60°C for 10 hours. Next, the reaction product was taken out from the mold and washed with running water to remove starch, excess acid and formaldehyde, and an initial product of a synthetic grindstone was obtained. The initial product of this synthetic whetstone was heated and cured at 130° C. for 5 hours to accelerate the curing reaction of the phenol resin, and a synthetic whetstone was obtained.
〔比較例3〕
加圧せずに12時間反応させた。それ以外は実施例4と
同様にして合成砥石を得た。[Comparative Example 3] Reaction was carried out for 12 hours without applying pressure. A synthetic grindstone was obtained in the same manner as in Example 4 except for the above.
以上の実施例4および比較例3で得られた合成砥石の切
断面の独 立気泡の数を測定した結果、比較例3で得ら
れた合成砥石では12個/ 10 clrの割合で気泡
が混入していたが、実施例4で得られた合成砥石では全
く気泡の混入が認められなかった。As a result of measuring the number of closed air bubbles on the cut surface of the synthetic whetstones obtained in Example 4 and Comparative Example 3, it was found that the synthetic whetstone obtained in Comparative Example 3 had air bubbles mixed in at a rate of 12/10 clr. However, no bubbles were observed in the synthetic grindstone obtained in Example 4.
以上のように、この発明は、加圧下で樹脂液を硬化させ
て多孔質体を製造するため、得られる多孔質体に、独立
気泡が残存しなくなり均質な性質のものとなる。すなわ
ち、この発明によれば、残存独立気泡にもとづく不良品
が少なくなるため、多孔質体の製造歩留を向上させるこ
とができ、また、製品の全体的な品質向上をもたらすと
いう利点がある。このように、残存独立気泡のない製品
を得ることができる結果、従来まで気孔混入物を製品か
ら除外する目的のために設置された全数検査工程を省略
することが可能となる。As described above, in the present invention, a porous body is manufactured by curing a resin liquid under pressure, so that the resulting porous body has homogeneous properties without remaining closed cells. That is, according to the present invention, since the number of defective products due to residual closed cells is reduced, the production yield of porous bodies can be improved, and there is an advantage that the overall quality of the product is improved. As a result of being able to obtain a product free of residual closed cells in this way, it becomes possible to omit the 100% inspection process that was conventionally installed for the purpose of excluding pore contaminants from the product.
Claims (5)
合成樹脂の樹脂液を準備し、この樹脂液を硬化させて硬
化体をつくり、この硬化体から気孔生成剤を除去してそ
の除去跡を気孔化する多孔質体の製法であつて、上記樹
脂液の硬化を加圧下で行うことを特徴とする多孔質体の
製法。(1) Prepare a synthetic resin liquid in which a curing agent, a catalyst, and a pore-forming agent are uniformly dispersed, cure this resin liquid to create a cured body, and remove the pore-forming agent from this cured body. 1. A method for producing a porous body in which marks are made into pores, the method comprising curing the resin liquid under pressure.
1項記載の多孔質体の製法。(2) The method for producing a porous body according to claim 1, wherein the pressurization is performed using gas.
れる特許請求の範囲第2項記載の多孔質体の製法。(3) The method for producing a porous body according to claim 2, wherein the pressurization using gas is performed by enclosing compressed air.
許請求の範囲第2項記載の多孔質体の製法。(4) The method for producing a porous body according to claim 2, wherein the pressurization using gas is performed by steam pressurization.
われる特許請求の範囲第1項ないし第4項のいずれかに
記載の多孔質体の製法。(5) The method for producing a porous body according to any one of claims 1 to 4, wherein the pressurization is performed under a pressure condition of 1.0 kg/cm^2 or more.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8069587A JPS63245447A (en) | 1987-03-31 | 1987-03-31 | Production of porous article |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8069587A JPS63245447A (en) | 1987-03-31 | 1987-03-31 | Production of porous article |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63245447A true JPS63245447A (en) | 1988-10-12 |
Family
ID=13725463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8069587A Pending JPS63245447A (en) | 1987-03-31 | 1987-03-31 | Production of porous article |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63245447A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995001878A1 (en) * | 1993-07-09 | 1995-01-19 | Canon Kabushiki Kaisha | Resin ink jet filter and method of manufacturing the same |
JP2010253175A (en) * | 2009-04-28 | 2010-11-11 | Yukosyokai Co Ltd | Insole |
-
1987
- 1987-03-31 JP JP8069587A patent/JPS63245447A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995001878A1 (en) * | 1993-07-09 | 1995-01-19 | Canon Kabushiki Kaisha | Resin ink jet filter and method of manufacturing the same |
JP2010253175A (en) * | 2009-04-28 | 2010-11-11 | Yukosyokai Co Ltd | Insole |
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