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JPS6336808B2 - - Google Patents

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Publication number
JPS6336808B2
JPS6336808B2 JP59187225A JP18722584A JPS6336808B2 JP S6336808 B2 JPS6336808 B2 JP S6336808B2 JP 59187225 A JP59187225 A JP 59187225A JP 18722584 A JP18722584 A JP 18722584A JP S6336808 B2 JPS6336808 B2 JP S6336808B2
Authority
JP
Japan
Prior art keywords
sol
thickener
acid
pores
layer
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
Application number
JP59187225A
Other languages
Japanese (ja)
Other versions
JPS6071007A (en
Inventor
Andore Ararii Jan
Koto Rui
Guguriemotsuto Furanshisu
Rarebo Andore
Gizaru Kurisuchan
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.)
SERABEERU
Original Assignee
SERABEERU
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 SERABEERU filed Critical SERABEERU
Publication of JPS6071007A publication Critical patent/JPS6071007A/en
Publication of JPS6336808B2 publication Critical patent/JPS6336808B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】 本発明は、微細濾過(microfiltration)、限外
濾過または逆浸透用エレメントの製造方法に係
り、該方法においては、任意に無水有機溶媒に溶
解したアルコキシド、有機金属化合物または無機
もしくは有機の酸の金属塩を加水分解して対応す
る化学元素の酸化物または水酸化物粒子のゾルを
生成し、前記ゾルに増粘剤を添加し、得られたゾ
ルを濾過エレメントに望ましい細孔より荒目の細
孔をもつ支持層にコーテイングし、次に支持層に
堆積した薄膜を乾燥させ、次に熱処理によつて増
粘剤を除去して堆積薄膜の粒子の焼結を生起す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing elements for microfiltration, ultrafiltration or reverse osmosis, in which alkoxides, organometallic compounds or A metal salt of an inorganic or organic acid is hydrolyzed to produce a sol of oxide or hydroxide particles of the corresponding chemical element, a thickening agent is added to said sol, and the resulting sol is desirably used in a filtration element. A support layer with coarser pores is coated, the thin film deposited on the support layer is then dried, and the thickening agent is removed by heat treatment to cause sintering of the particles of the deposited thin film. do.

ヨルダ(B.E.Yoldas)により(Ceramic
Bulletin、54 No.3(1975)286―290)、アルミニ
ウムアルコキシドを熱水で加水分解してアルミナ
ゲルを調製し、形成された懸濁液を、アルミニウ
ムと錯体を形成しないアニオンを生じる強酸によ
つて解膠する方法がすでに提案されている。得ら
れたゾルを乾燥して微孔性ゲルを形成させ、この
ゲルを濾材として使用し得る。
(Ceramic by BEYoldas)
Bulletin, 54 No. 3 (1975) 286-290), an alumina gel is prepared by hydrolyzing an aluminum alkoxide with hot water, and the suspension formed is treated with a strong acid, which produces an anion that does not complex with aluminum. A method for deflocculating the material has already been proposed. The resulting sol is dried to form a microporous gel that can be used as a filter medium.

また、フランス特許公開第2150390号では、ゾ
ルに増粘剤を添加し濾過作用によつてコーテイン
グを行なう方法が提案されている。
Further, French Patent Publication No. 2150390 proposes a method in which a thickener is added to the sol and coating is performed by a filtration action.

しかしながら、微孔性支持体に堆積させること
によつて濾過層を形成し得るゾルの製造は難し
く、また、微細濾過、限外濾過及び逆浸透での使
用に適する十分に微細な粒子サイズを得ることも
難しい。
However, it is difficult to produce sols that can be deposited onto microporous supports to form filtration layers, and to obtain particle sizes fine enough to be suitable for use in microfiltration, ultrafiltration and reverse osmosis. It's also difficult.

さらに、支持層に堆積したゲル層の乾燥と焼成
との過程でゲルの亀裂発生と崩壊とを阻止するこ
とも難しい。
Furthermore, it is difficult to prevent the gel from cracking and collapsing during the drying and firing process of the gel layer deposited on the support layer.

本発明の目的は、支持層にコーテイングによつ
て容易に堆積させることができ、ゲルの乾燥と焼
成との過程で粒子の粗粒化とゲルの亀裂及び崩壊
の発生とを阻止し得るような前記の如き微細濾
過、限外濾過または逆浸透用エレメントの製造方
法を提供することである。本発明の目的はさら
に、細孔サイズが極めて小さくまた細孔サイズが
均一であること、透過率が高いこと、厚みが薄く
均等であること、機械的耐久性が良く逆圧による
洗浄及び高い濾過圧力の使用ができること、化学
的耐性が良く微生物及び酸素の作用に強いこと等
の如き特性を有する微細濾過、限外濾過または逆
浸透用エレメントの製造方法を提供することであ
る。
The object of the present invention is to provide a coating material that can be easily deposited on a support layer by coating and that can prevent coarsening of particles and generation of cracks and collapse of the gel during the drying and baking process of the gel. It is an object of the present invention to provide a method for manufacturing an element for microfiltration, ultrafiltration, or reverse osmosis as described above. Further objects of the present invention include extremely small and uniform pore size, high permeability, thin and uniform thickness, good mechanical durability, back pressure cleaning and high filtration. The object of the present invention is to provide a method for producing an element for microfiltration, ultrafiltration, or reverse osmosis, which has characteristics such as being able to use pressure, having good chemical resistance, and being resistant to the effects of microorganisms and oxygen.

本発明の製造方法においては、アルコキシド、
有機金属化合物または無機酸もしくは有機酸の金
属塩中に存在する化学元素の酸化物または水酸化
物の粒子のゾルを加水分解によつて生成し、粒子
のゾルに対して、これら酸化物または水酸化物の
金属イオンと共に錯体を形成しないアニオンを生
じる強酸を増粘剤と共に添加し、濾過によらずに
単なる接触によつてコーテイングを行なう。
In the production method of the present invention, alkoxide,
A sol of particles of oxides or hydroxides of chemical elements present in organometallic compounds or metal salts of inorganic acids or organic acids is produced by hydrolysis, and the sol of particles is A strong acid, which produces an anion that does not form a complex with the metal ion of the oxide, is added together with a thickener, and the coating is effected by mere contact without filtration.

上記のように、酸化物または水酸化物の金属と
共に錯体を形成しないアニオンを生じる強酸を使
用することによつて、酸化物または水酸化物の金
属はイオンとして遊離せず酸化物または水酸化物
は沈澱物の状態に維持される。
As mentioned above, by using a strong acid that produces an anion that does not form a complex with the metal of the oxide or hydroxide, the metal of the oxide or hydroxide is not liberated as an ion and forms the oxide or hydroxide. is maintained in a precipitate state.

また、強酸であるので低濃度で添加しても解膠
に必要なゾル粒子表面の表面帯電硬化が得られ
る。高い濃度の酸を使用すると焼成前のゾル中に
酸の占める容量が極めて大きく、その酸が焼成時
に揮発し最終的に得られるエレメントが固化して
多孔性が得られないことになる。
In addition, since it is a strong acid, even if it is added at a low concentration, the surface charge hardening of the sol particle surface necessary for peptization can be obtained. If a high concentration of acid is used, the capacity occupied by the acid in the sol before firing will be extremely large, and the acid will volatilize during firing, solidifying the final element and making it impossible to obtain porosity.

前記方法は以下の特徴を1つ以上有するのが好
ましい。
Preferably, the method has one or more of the following features.

―増粘剤がポリビニルアルコールである。-The thickener is polyvinyl alcohol.

―強酸が硝酸である。-A strong acid is nitric acid.

―水の沸点より低温で緩徐に乾燥させる。- Slow drying at a temperature below the boiling point of water.

―熱処理に於いて、増粘剤に由来する有機物質を
除去し、水酸化物粒子の少なくとも一部を酸化
物粒子に分解し、前記粒子を支持層に堆積する
微孔性の固体均質層として焼結するに充分な温
度レベルと持続時間とを用いる。
- as a microporous solid homogeneous layer in which during heat treatment the organic substances originating from the thickener are removed and at least a portion of the hydroxide particles are decomposed into oxide particles and the said particles are deposited on the support layer; Use a temperature level and duration sufficient to cause sintering.

―より荒目の細孔をもつ層を得るために熱処理の
最高温度をより高くする。
- Increasing the maximum temperature of heat treatment to obtain a layer with coarser pores.

解膠剤の機能を果す強酸としては硝酸以外に、
特に塩酸、過塩素酸、トリクロロ酢酸が適当であ
る。
In addition to nitric acid, other strong acids that function as deflocculants include:
Particularly suitable are hydrochloric acid, perchloric acid, and trichloroacetic acid.

前記の方法を用い、特に粒子がアルミニウム、
チタン、ジルコニウムまたはケイ素またはそれら
の混合物の水酸化物または酸化物から成るような
微細濾過、限外濾過または逆浸透用エレメントを
製造し得る。
Using the method described above, in particular if the particles are aluminum,
Such microfiltration, ultrafiltration or reverse osmosis elements can be produced from hydroxides or oxides of titanium, zirconium or silicon or mixtures thereof.

以下に実施例として、本発明による膜の製法を
示す。
As an example, a method for manufacturing a membrane according to the present invention will be shown below.

実施例 1 コンデ・シミ(Condea―Chimie)社より“ピ
ユーラルSB(Pural SB)”の商品名で市販されて
いる、アルミニウムアルコキシドの加水分解によ
つて得られるベーマイト(一水化アルミナ)のゾ
ルを使用する。
Example 1 A sol of boehmite (monohydrated alumina) obtained by hydrolysis of aluminum alkoxide, which is commercially available from Condea-Chimie under the trade name "Pural SB", was used. use.

“ピユーラルSB”ベーマイト18g、脱イオン
水30―40g、および水160gに対して硝酸10gの
濃度の硝酸溶液1.5gを混合して組成物Aをつく
る。
Composition A is made by mixing 18 g of "Pural SB" boehmite, 30-40 g of deionized water, and 1.5 g of a nitric acid solution at a concentration of 10 g of nitric acid to 160 g of water.

さらに次の組成の組成物Bをつくる。 Furthermore, a composition B having the following composition is prepared.

―ポリビニルアルコールのゲル30―35g (水100gに対してアルコール12.5gの濃度
(商標名ロドビオール〔Rhodoviol〕25/140)) ―硝酸溶液12―13g (水150gに対して酸20gの濃度) 以上の組成物に対して、良好な解膠及び膜を堆
積させる表面の良好な湿潤を得るため、場合によ
つては界面活性剤を加える。
- 30-35 g of polyvinyl alcohol gel (concentration of 12.5 g of alcohol to 100 g of water (trade name Rhodoviol 25/140)) - 12-13 g of nitric acid solution (concentration of 20 g of acid to 150 g of water) Surfactants are optionally added to the composition in order to obtain good peptization and good wetting of the surface on which the film is deposited.

次に組成物AおよびBを撹拌し、均質化して、
粘性液体を得る。
Compositions A and B are then stirred and homogenized;
Obtain a viscous liquid.

この混合物を、限外濾過エレメントに所望され
る細孔より荒目の細孔を有する多孔性の管につめ
る。1〜数分後に管を空ける。混合物の1部が管
の内壁上に膜上に堆積して残る。
This mixture is filled into a porous tube having pores coarser than desired for the ultrafiltration element. Empty the tube after 1 to several minutes. A portion of the mixture remains deposited in a film on the inner wall of the tube.

次に乾燥と焼成のための熱処理を次の要領でお
こなう: ―20℃で24時間乾燥 ―20℃から200℃へ1時間で温度上昇 ―200℃から300℃へ1.5時間で温度上昇 ―300℃から560℃へ1時間で温度上昇 560℃での焼成後、厚さ約5ミクロン、細孔直
径58オングストローム、20℃での透水性5リツト
ル/時・m2・barの濾過層を得る。
Next, heat treatment for drying and firing is performed as follows: - Drying at 20°C for 24 hours - Temperature rise from 20°C to 200°C in 1 hour - Temperature rise from 200°C to 300°C in 1.5 hours - 300°C After calcination at 560°C, a filtration layer with a thickness of approximately 5 microns, a pore diameter of 58 angstroms and a water permeability of 5 liters/hour·m 2 ·bar at 20°C is obtained.

実験条件に依り厚さ1〜数10ミクロンの薄膜が
得られ、また最高焼成温度に依り数オングストロ
ーム〜数1000オングストロームの細孔直径が得ら
れ、膜体積の5〜75%の細孔容積の開孔率が得ら
れる。この薄膜は多孔性支持層上に焼結によつて
接合される。
Depending on the experimental conditions, a thin film with a thickness of 1 to several tens of microns can be obtained, and depending on the maximum firing temperature, a pore diameter of several angstroms to several thousand angstroms can be obtained, with an opening of 5 to 75% of the pore volume of the film volume. Porosity is obtained. This thin film is bonded onto the porous support layer by sintering.

最終焼成温度は所望の平均細孔直径の関数とし
て変化させることができる。最終温度560℃では
平均細孔直径は58オングストローム、最終温度
1000℃では106オングストローム、最終温度1200
℃では1100オングストロームとなる。
The final firing temperature can be varied as a function of the desired average pore diameter. At a final temperature of 560°C, the average pore diameter is 58 angstroms;
106 angstroms at 1000℃, final temperature 1200
At ℃ it is 1100 angstroms.

いずれの場合においても、細孔直径はその平均
値にかなり近いものが殆どである。たとえば細孔
の平均直径の2分の1〜2倍の範囲に含まれる直
径をもつ細孔の総細孔容積は90%に達する。
In either case, the pore diameter is mostly close to its average value. For example, the total pore volume of pores with diameters in the range of 1/2 to 2 times the average pore diameter reaches 90%.

実施例 2 イソブトキシドアルミニウムAl(OC4H93を50
g脱イオン水350gに混合する。85℃で2時間撹
拌すると、次の反応が生じる: Al(OC4H93+(2+X)H2O→AlOOH・
XH2O+3C4H9OH 水酸化物(ベーマイト)が析出する。この析出
物をブフナー漏斗による水洗にかける。多量の水
分を含んだままの析出物が再び得られる。
Example 2 50% of isobutoxide aluminum Al(OC 4 H 9 ) 3
g Mix with 350 g of deionized water. After stirring for 2 hours at 85°C, the following reaction occurs: Al(OC 4 H 9 ) 3 + (2+X)H 2 O→AlOOH・
XH 2 O + 3C 4 H 9 OH hydroxide (boehmite) precipitates. The precipitate is washed with water in a Buchner funnel. A precipitate is again obtained which still contains a large amount of water.

この析出物によつて以下の組成物Aをつくる: ―非乾燥ベーマイトの析出物 23重量% ―脱イオン水 27重量% ―水320gに対して硝酸20gの溶液 15重量% さらに以下の組成物Bをつくる: ―水100gに対してアルコール12.5% 4重量% の割合のポリビニルアルコール (ロドビオール25/140) ― 脱イオン水 31重量% 組成物AおよびBを混合して均質化する。 This precipitate makes up the following composition A: -Non-dried boehmite precipitate 23% by weight -Deionized water 27% by weight - 15% by weight solution of 20g nitric acid in 320g water Furthermore, the following composition B is made: - Alcohol 12.5% 4% by weight per 100g of water proportion of polyvinyl alcohol (Rhodobiol 25/140) - Deionized water 31% by weight Mix and homogenize compositions A and B.

得られた粘性液体を多孔性の管につめる。1〜
数分後管を空ける。液体の1部が管の内壁上に膜
上に堆積する。
The resulting viscous liquid is filled into a porous tube. 1~
Empty the tube after a few minutes. A portion of the liquid is deposited on the inner wall of the tube onto a film.

次に実施例1と同様の熱処理をおこなう。厚さ
2〜3ミクロン、焼成温度750℃においては40オ
ングストローム、また焼成温度1050℃においては
120オングストロームの平均細孔直径をもつ層が
得られる。
Next, the same heat treatment as in Example 1 is performed. 2-3 microns thick, 40 angstroms at 750°C firing temperature, and 40 angstroms at 1050°C firing temperature.
A layer with an average pore diameter of 120 angstroms is obtained.

Claims (1)

【特許請求の範囲】 1 微細濾過、限外濾過または逆浸透用エレメン
トの製造方法であつて、任意に無水有機溶媒に溶
解したアルコキシド、有機金属化合物または無機
もしくは有機の酸の金属塩を加水分解して対応す
る化学元素の酸化物または水酸化物の粒子ゾルを
生成し、前記ゾルに増粘剤を添加し、得られたゾ
ルを濾過エレメントに所望される細孔より荒目の
細孔を有する支持層にコーテイングし、次に支持
層に堆積した薄膜を乾燥させ、次に熱処理によつ
て増粘剤を除去して堆積薄膜の粒子の焼結を達成
する方法であり、酸化物または水酸化物粒子のゾ
ルに対して、これらの酸化物または水酸化物の金
属のイオンと共に錯体を形成しないアニオンを生
じる強酸を増粘剤と共に添加すること、及び濾過
を伴わない単なる接触によつて前記コーテイング
を行なうことを特徴とする前記方法。 2 増粘剤がポリビニルアルコールであることを
特徴とする特許請求の範囲第1項に記載の方法。 3 強酸が硝酸であることを特徴とする特許請求
の範囲第1項または第2項に記載の方法。 4 水の沸点より低温で緩徐に乾燥させることを
特徴とする特許請求の範囲第1項〜第3項のいず
れかに記載の方法。 5 熱処理に於いて、増粘剤に由来する有機物質
を除去し、水酸化物粒子を少なくとも部分的に酸
化物粒子に分解し、前記粒子を支持層に付着する
微孔性の固体均質層として焼結するに充分な温度
レベルと持続時間とを用いることを特徴とする特
許請求の範囲第1項〜第4項のいずれかに記載の
方法。 6 より荒目の細孔をもつ層を得るために熱処理
の最高温度をより高くすることを特徴とする特許
請求の範囲第5項に記載の方法。
[Claims] 1. A method for producing an element for microfiltration, ultrafiltration or reverse osmosis, which comprises hydrolyzing an alkoxide, an organometallic compound, or a metal salt of an inorganic or organic acid, optionally dissolved in an anhydrous organic solvent. to produce a particle sol of the oxide or hydroxide of the corresponding chemical element, add a thickener to the sol, and apply the resulting sol to a filter element with pores coarser than the desired pores. The method involves coating a support layer with Adding to the sol of oxide particles, together with a thickening agent, a strong acid which forms an uncomplexed anion with the ions of the metals of these oxides or hydroxides, and by mere contact without filtration. The method described above, characterized in that coating is performed. 2. The method according to claim 1, wherein the thickener is polyvinyl alcohol. 3. The method according to claim 1 or 2, wherein the strong acid is nitric acid. 4. The method according to any one of claims 1 to 3, characterized in that the drying is performed slowly at a temperature lower than the boiling point of water. 5. In the heat treatment, the organic substances originating from the thickener are removed and the hydroxide particles are at least partially decomposed into oxide particles, which form a microporous solid homogeneous layer that adheres to the support layer. 5. A method according to any of claims 1 to 4, characterized in that temperature levels and durations sufficient to cause sintering are used. 6. The method according to claim 5, characterized in that the maximum temperature of the heat treatment is increased in order to obtain a layer with coarser pores.
JP18722584A 1983-09-06 1984-09-06 Production of fine filtration, ultrafiltration or reverse osmosis element Granted JPS6071007A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR8314212 1983-09-06
FR8314212 1983-09-06
FR8318648 1983-11-23

Publications (2)

Publication Number Publication Date
JPS6071007A JPS6071007A (en) 1985-04-22
JPS6336808B2 true JPS6336808B2 (en) 1988-07-21

Family

ID=9292012

Family Applications (2)

Application Number Title Priority Date Filing Date
JP18722584A Granted JPS6071007A (en) 1983-09-06 1984-09-06 Production of fine filtration, ultrafiltration or reverse osmosis element
JP25816887A Granted JPS63116709A (en) 1983-09-06 1987-10-13 Manufacture of element for fine filtration, ultrafiltration or reverse osmosis

Family Applications After (1)

Application Number Title Priority Date Filing Date
JP25816887A Granted JPS63116709A (en) 1983-09-06 1987-10-13 Manufacture of element for fine filtration, ultrafiltration or reverse osmosis

Country Status (1)

Country Link
JP (2) JPS6071007A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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JP4968990B2 (en) * 2001-06-29 2012-07-04 京セラ株式会社 Manufacturing method of inorganic separation membrane
JP5033670B2 (en) * 2008-02-14 2012-09-26 日本碍子株式会社 Manufacturing method of ceramic filter
JP4960286B2 (en) * 2008-03-21 2012-06-27 日本碍子株式会社 Method for producing nanofiltration membrane

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US3941719A (en) * 1972-08-17 1976-03-02 Owens-Illinois, Inc. Transparent activated nonparticulate alumina and method of preparing same
JPS5425520A (en) * 1977-07-27 1979-02-26 Kankyo Kaihatsu Kk Method of connecting sewer and so on
JPS5959224A (en) * 1982-09-28 1984-04-05 Mitsubishi Heavy Ind Ltd Preparation of porous diaphragm
JPS5992001A (en) * 1982-11-18 1984-05-28 Mitsubishi Heavy Ind Ltd Preparation of porous diaphragm
NL8303079A (en) * 1983-09-05 1985-04-01 Stichting Energie PROCESS FOR THE PREPARATION OF CRACK-FREE SEMI-PERMEABLE INORGANIC MEMBRANES.

Also Published As

Publication number Publication date
JPS63116709A (en) 1988-05-21
JPH0334970B2 (en) 1991-05-24
JPS6071007A (en) 1985-04-22

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