JPS6158205B2 - - Google Patents
Info
- Publication number
- JPS6158205B2 JPS6158205B2 JP11230176A JP11230176A JPS6158205B2 JP S6158205 B2 JPS6158205 B2 JP S6158205B2 JP 11230176 A JP11230176 A JP 11230176A JP 11230176 A JP11230176 A JP 11230176A JP S6158205 B2 JPS6158205 B2 JP S6158205B2
- Authority
- JP
- Japan
- Prior art keywords
- fermentation
- penicillium
- bacterial cells
- separated
- acid
- 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
- 238000000855 fermentation Methods 0.000 claims description 18
- 230000004151 fermentation Effects 0.000 claims description 18
- 150000007524 organic acids Chemical class 0.000 claims description 15
- 230000001580 bacterial effect Effects 0.000 claims description 13
- 239000007788 liquid Substances 0.000 claims description 12
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 241000228143 Penicillium Species 0.000 claims description 7
- 235000005985 organic acids Nutrition 0.000 claims description 7
- 230000002378 acidificating effect Effects 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 241000233866 Fungi Species 0.000 claims description 3
- 150000004676 glycans Chemical class 0.000 claims description 3
- 150000002772 monosaccharides Chemical class 0.000 claims description 3
- 229920001282 polysaccharide Polymers 0.000 claims description 3
- 239000005017 polysaccharide Substances 0.000 claims description 3
- 239000010802 sludge Substances 0.000 description 8
- 239000007787 solid Substances 0.000 description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 description 2
- XUMBMVFBXHLACL-UHFFFAOYSA-N Melanin Chemical compound O=C1C(=O)C(C2=CNC3=C(C(C(=O)C4=C32)=O)C)=C2C4=CNC2=C1C XUMBMVFBXHLACL-UHFFFAOYSA-N 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000005273 aeration Methods 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 239000008394 flocculating agent Substances 0.000 description 2
- 230000003311 flocculating effect Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000001963 growth medium Substances 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000003449 preventive effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 159000000000 sodium salts Chemical class 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- USFZMSVCRYTOJT-UHFFFAOYSA-N Ammonium acetate Chemical compound N.CC(O)=O USFZMSVCRYTOJT-UHFFFAOYSA-N 0.000 description 1
- 239000005695 Ammonium acetate Substances 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229920002101 Chitin Polymers 0.000 description 1
- 229920001661 Chitosan Polymers 0.000 description 1
- 229920002261 Corn starch Polymers 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 150000001412 amines Chemical group 0.000 description 1
- 229940043376 ammonium acetate Drugs 0.000 description 1
- 235000019257 ammonium acetate Nutrition 0.000 description 1
- 235000019270 ammonium chloride Nutrition 0.000 description 1
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical compound N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 description 1
- 229910052921 ammonium sulfate Inorganic materials 0.000 description 1
- 235000011130 ammonium sulphate Nutrition 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- QLULGSLAHXLKSR-UHFFFAOYSA-N azane;phosphane Chemical compound N.P QLULGSLAHXLKSR-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 125000002091 cationic group Chemical group 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 239000008120 corn starch Substances 0.000 description 1
- 229940099112 cornstarch Drugs 0.000 description 1
- 239000008278 cosmetic cream Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000012024 dehydrating agents Substances 0.000 description 1
- 230000018044 dehydration Effects 0.000 description 1
- 238000006297 dehydration reaction Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910017053 inorganic salt Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002609 medium Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000000344 soap Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 235000015961 tonic Nutrition 0.000 description 1
- 230000001256 tonic effect Effects 0.000 description 1
- 229960000716 tonics Drugs 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Preparation Of Compounds By Using Micro-Organisms (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
Description
本発明は、例えば活性汚泥やスラツジ等の水中
浮遊性物質を濾過分離する際、添加混合すること
により該水中浮遊性物質のフロツク化を促進させ
る凝集剤に係る。
従来から前記凝集剤としては、キトザン、クル
クロル酸、燐酸、キチン、メラニン、アンノース
等が用いられているが、本発明は、単糖又は多糖
類を原料とし、これに酸性窒素源を加えてPH4以
下とした培地に、ペニシリウム・スポクリスポリ
ウム等のペニシリウムに属する糸状菌を用いて好
気条件下で有機酸を発酵させ、該発酵液から分離
した菌体を凝集剤として用いることを特徴とする
ものである。
前記有機酸の発酵生成は、次のようにして行な
われる。
使用されるペニシリウム・スピクリスポリウム
等のペニシリウムに属する糸状菌は、土壌等から
分離されたもので、本菌株は工業技術院微生物工
業研究所に寄託番号微工研菌寄第8727号(旧寄託
番号、通商産業省発酵研究所、寄託番号No.65)と
して寄託されているものである。
単糖、多糖類を原料料とする培地のPH制御は、
塩安、硫安、燐安、酢酸アンモン等の酸性窒素源
を加えることにより行なう。各種窒素源を用いて
PH値を制御した場合の、PH値と生酸量との関係は
下表の通りで、PH4以下の酸性、強酸性条件範囲
で生酸量の最大値が存在する。
The present invention relates to a flocculant that promotes flocculation of water-floating substances, such as activated sludge and sludge, by adding and mixing them when the water-floating substances are separated by filtration. Conventionally, chitosan, curchloric acid, phosphoric acid, chitin, melanin, annose, etc. have been used as the flocculant, but in the present invention, monosaccharides or polysaccharides are used as raw materials, and an acidic nitrogen source is added thereto to achieve pH4. It is characterized by fermenting an organic acid under aerobic conditions using filamentous fungi belonging to Penicillium such as Penicillium spocrisporium in the following culture medium, and using the bacterial bodies separated from the fermentation liquid as a flocculant. It is something. The fermentation production of the organic acid is carried out as follows. The filamentous fungi belonging to Penicillium, such as Penicillium and Spicrisporium, that are used are isolated from soil, etc., and this strain has been deposited at the Institute of Microbiology, Agency of Industrial Science and Technology, with deposit number No. 8727 (formerly deposited). No. 65), Ministry of International Trade and Industry Fermentation Research Institute, Deposit No. 65). PH control of media using monosaccharides and polysaccharides as raw materials is
This is done by adding an acidic nitrogen source such as ammonium chloride, ammonium sulfate, ammonium phosphorus, or ammonium acetate. using various nitrogen sources
The relationship between the PH value and the amount of bioacid when the PH value is controlled is shown in the table below, and the maximum amount of bioacid exists in the range of acidic and strongly acidic conditions below PH4.
【表】
又、PH制御に無機塩を用いることができ、
KH2PO4、MgSO4・7H2Oを添加する。窒素源と
してコーンステイープリカーを0.2%程度用いれ
ば無機塩の添加を減ずるか全く添加しなくても良
い。又、コーンステイープリカーを加えずに糖と
無機塩だけでも生酸可能であるが、0.05%程度加
えると発酵速度が向上する。その他重金属として
FeSO4を0.005%程度添加することも発酵速度に
好影響を及ぼす。
次に、培地の糖濃度と好気条件に関しては、培
養は好気的な条件ほど生酸が良く、糖濃度は10%
程度以下が良い。通気量が少ないか糖濃度が高す
ぎるときは、生酸の収率が落ちて代りにエタノー
ルの生成が起る。通気量を多くすれば糖濃度は10
%以上でも良い。このような点から培養中補糖し
ながら発酵させることもでき、酸の収率を落さず
に糖の高濃度(累積値)仕込みが可能となる。
次に発酵培養の実施例を記す。
グリコース10%、MgSO4+KH2PO4+NH4Clを
約0.05〜0.5%、残部水道水からなる溶液に、ペ
ニシリウム・スポクリスポリウム・レーマンNo.10
―1を培養したものを約0.01〜0.05%加え、この
溶液100を30℃、120rpmの回転振動状態で発酵
培養した。培養日数10日で有機酵が生成され、有
機酸は加水分解型として培地中に菌体と共に析出
した。
このようにして生成された有機酸は、長鎖のア
ルキル基、カルボキシル基、水酸基等を有し、親
水性、親油性を共に備え、界面、表面に対する強
い吸着作用を有し、又、この吸着作用によつて粒
子表面の濡れ性を高める等、優れた界面活性作用
を有するため、従来から各種の界面活性剤として
有用であることが知られており、例えば、機械加
工や電気加工の加工液に添加混合する防錆剤とし
て、各種粒子を研削ペースト、洗剤ペースト或い
は接着剤に混合分散させる際の分散剤として、焼
入部分等の表面の傷の有無を検査する際の探傷液
として、その他塗料、各種の充填材、潤滑剤、表
面保護剤、表面浄化剤、洗剤、石鹸、洗髪剤、ポ
マード、養毛剤、化粧用クリーム、塗布薬料等の
添加剤として利用し得るものである。
発酵液から有機酸を分離する方法としては、例
えば、発酵液を遠心分離により固液分離し、分離
された有機酸と菌体からなる固形物を乾燥後、有
機酸をアルコール等により溶媒抽出して菌体と分
離して得る方法がとられる。この方法により前記
実施例に於て、発酵培養液を回転数3600rpmで遠
心分離することにより、発酵液は約90の分離液
と、有機酸と菌体からなる固形物とに分離され、
この固形物を充分乾燥した後、アルコール抽出し
て菌体と分離と、再び乾燥させたところ、約3Kg
の有機酸と約0.9Kgの菌体固形物とが得られた。
このようにして得られた酸は、常温では水に不溶
であるから、メタノール等のアルコールに溶解し
アルコール溶液としてエステル化して利用し、又
或いはナトリウムに溶解してナトリウム塩とした
カリウム、カルシウム、マグネシウム等の金属塩
として利用される。
又、前記実施例に於て発酵培養液から固液分離
された分離液は、その液中に酸成分を約0.7〜1
%(定量値)程度含有しており、これは水溶液で
あるからそのまま加工液に添加する防錆剤等とし
て利用することができる。
このように、発酵培養により生成された有機酸
は各種界面活性剤として有用なものであるが、本
発明は発酵液から分離除去された菌体固形物を利
用しようとするものであり、研究の結果、分離さ
れた菌体が、活性汚泥やスラツジ等に於ける水中
浮遊性物質のフロツク化を促進させる凝集剤、凝
集脱水剤として有用であることが認められた。凝
集効果は、アニオン系に限らず、アミン系変性し
てカチオン系凝集剤としても有効である。又、前
記発酵により生成した有機酸も凝集作用を有して
おり、前記菌体固形物と有機酸とを混合して利用
することも有効である。例えば、活性汚泥に於
て、菌体固形物50%と有機酸のナトリウム塩50%
からなる混合凝集脱水剤を活性汚泥液に60ppm
混合し、Pt陽極とグラフアイト陰極間に30Vの電
圧を印加して電解したとき、1〜2秒間で陽極表
面に0.5mm厚の汚泥の凝集層が形成された。この
層の水分は約32%であつた。又、この処理前の汚
水のSS濃度は1300ppmであつたが処理後のSS濃
度は約3.4ppmとなり、優れた浄化作用が認めら
れた。
このように活性汚泥の浄化処理に於て、極めて
能率良く急速に且つ高い脱水率で水中不純物を凝
集脱水して分離除去することができる。
以上の通り、本発明は、発酵培養液から有機酸
を分離収集する際、分離除去されてさしたる利用
価値のなかつた菌体固形物を凝集剤として利用す
るものであるから、経済的に有利であり実用上効
果が大である。[Table] Inorganic salts can also be used to control pH,
Add KH 2 PO 4 and MgSO 4 .7H 2 O. If about 0.2% of cornstarch liquor is used as a nitrogen source, the addition of inorganic salts can be reduced or not added at all. In addition, although it is possible to produce a raw acid using only sugar and inorganic salt without adding cornstap liquor, the fermentation speed is improved by adding about 0.05%. Other heavy metals
Addition of about 0.005% FeSO 4 also has a positive effect on the fermentation rate. Next, regarding the sugar concentration and aerobic conditions of the culture medium, the more aerobic the culture, the better the bioacid, and the sugar concentration is 10%.
It is better if it is below that level. When the aeration rate is low or the sugar concentration is too high, the yield of bioacid decreases and ethanol formation occurs instead. If the aeration rate is increased, the sugar concentration will be 10
It may be more than %. From this point of view, fermentation can be carried out while supplementing sugar during culture, making it possible to charge a high concentration (cumulative value) of sugar without reducing the acid yield. Next, examples of fermentation culture will be described. Penicillium spocrisporium Lehmann No. 10 was added to a solution consisting of 10% glycose, about 0.05-0.5% MgSO 4 +KH 2 PO 4 +NH 4 Cl, and the balance tap water.
Approximately 0.01 to 0.05% of the cultured 1-1 was added, and this solution 100 was fermented and cultured at 30° C. and under rotational vibration at 120 rpm. Organic fermentation was produced after 10 days of culture, and the organic acid was precipitated in the medium together with the bacterial cells in the form of hydrolysis. The organic acids produced in this way have long-chain alkyl groups, carboxyl groups, hydroxyl groups, etc., have both hydrophilicity and lipophilicity, and have a strong adsorption effect on interfaces and surfaces. It has long been known to be useful as a variety of surfactants because it has excellent surfactant effects, such as increasing the wettability of particle surfaces.For example, it is used as a processing fluid for mechanical processing and electrical processing. As a rust preventive agent to be added and mixed in, as a dispersant when mixing and dispersing various particles into grinding paste, detergent paste, or adhesive, as a flaw detection liquid when inspecting the presence or absence of scratches on the surface of hardened parts, etc. It can be used as an additive for paints, various fillers, lubricants, surface protectants, surface purifiers, detergents, soaps, hair washes, pomades, hair tonics, cosmetic creams, coating agents, and the like. As a method for separating organic acids from fermentation liquid, for example, the fermentation liquid is subjected to solid-liquid separation by centrifugation, the solid material consisting of the separated organic acids and bacterial cells is dried, and then the organic acids are extracted with a solvent such as alcohol. A method is used to obtain it by separating it from the bacterial cells. According to this method, in the above example, by centrifuging the fermentation culture solution at a rotation speed of 3600 rpm, the fermentation solution is separated into about 90 separated liquids and a solid substance consisting of organic acid and bacterial cells,
After thoroughly drying this solid matter, we extracted it with alcohol to separate it from the bacterial cells and dried it again, which resulted in approximately 3 kg.
of organic acid and about 0.9 kg of solid bacterial cells were obtained.
The acid obtained in this way is insoluble in water at room temperature, so it can be dissolved in alcohol such as methanol and esterified as an alcohol solution, or dissolved in sodium to make sodium salts such as potassium, calcium, Used as a metal salt such as magnesium. In addition, the separated liquid obtained by solid-liquid separation from the fermentation culture liquid in the above example contains an acid component of about 0.7 to 1
% (quantitative value), and since it is an aqueous solution, it can be used as a rust preventive agent added to the processing fluid as it is. As described above, organic acids produced by fermentation culture are useful as various surfactants, but the present invention aims to utilize the bacterial solids separated and removed from the fermentation liquid, and is useful for research. As a result, the isolated bacterial cells were found to be useful as a flocculant and coagulation-dehydrating agent that promotes flocculation of water-suspended substances in activated sludge, sludge, etc. The flocculating effect is effective not only for anionic flocculants but also for cationic flocculants modified with amines. Furthermore, the organic acid produced by the fermentation also has a flocculating effect, and it is also effective to mix and use the solid bacterial cells and the organic acid. For example, in activated sludge, 50% bacterial solids and 50% sodium salt of organic acid
60ppm of mixed coagulation and dehydration agent to activated sludge liquid.
When mixed and electrolyzed by applying a voltage of 30 V between the Pt anode and graphite cathode, a 0.5 mm thick sludge agglomeration layer was formed on the anode surface in 1 to 2 seconds. The moisture content of this layer was approximately 32%. Furthermore, the SS concentration in the wastewater before this treatment was 1300 ppm, but after the treatment, the SS concentration was approximately 3.4 ppm, indicating an excellent purifying effect. In this manner, in the purification treatment of activated sludge, impurities in water can be coagulated and dehydrated and separated and removed very efficiently, rapidly, and at a high dewatering rate. As described above, the present invention is economically advantageous because, when separating and collecting organic acids from a fermentation culture solution, the bacterial solids that have been separated and removed and have no significant utility value are used as a flocculant. Yes, it has a great practical effect.
Claims (1)
源を加えてPH4以下とした培地に、ペニシリウ
ム・スピクリスポリウム等のペニシリウムに属す
る糸状菌を用いて好気条件下で有機酸を発酵さ
せ、該発酵液から分離した菌体から成る凝集剤。1. Organic acids are fermented under aerobic conditions using filamentous fungi belonging to Penicillium, such as Penicillium and Spicrisporium, in a medium made from monosaccharides or polysaccharides and adjusted to pH 4 or less by adding an acidic nitrogen source. , a flocculant consisting of bacterial cells separated from the fermentation liquid.
Priority Applications (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11230176A JPS5337189A (en) | 1976-09-17 | 1976-09-17 | Production of surfactant |
US05/816,966 US4130493A (en) | 1976-07-20 | 1977-07-19 | Machining fluid |
FR7722281A FR2359201A1 (en) | 1976-07-20 | 1977-07-20 | MACHINING FLUID |
DE19772732818 DE2732818A1 (en) | 1976-07-20 | 1977-07-20 | WORKING LIQUID |
IT50370/77A IT1079797B (en) | 1976-07-20 | 1977-07-20 | WORKING LIQUID |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11230176A JPS5337189A (en) | 1976-09-17 | 1976-09-17 | Production of surfactant |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5337189A JPS5337189A (en) | 1978-04-06 |
JPS6158205B2 true JPS6158205B2 (en) | 1986-12-10 |
Family
ID=14583246
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP11230176A Granted JPS5337189A (en) | 1976-07-20 | 1976-09-17 | Production of surfactant |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5337189A (en) |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS55133054U (en) * | 1979-03-13 | 1980-09-20 | ||
JPS55124232A (en) * | 1979-03-20 | 1980-09-25 | Matsushita Electric Ind Co Ltd | Application method of substrate treatment solution and the device therefor |
JPS57197068A (en) * | 1981-05-28 | 1982-12-03 | Oki Electric Ind Co Ltd | Apparatus for coating resist |
JPS592134U (en) * | 1982-06-28 | 1984-01-09 | 株式会社東芝 | Rotary coating device |
JPS6071008A (en) * | 1983-09-26 | 1985-04-22 | Sanyo Chem Ind Ltd | Preparation of substance having flocculation activity |
JPS60189937A (en) * | 1984-03-12 | 1985-09-27 | Fujitsu Ltd | Applicator of resist |
KR970006206B1 (en) * | 1988-02-10 | 1997-04-24 | 도오교오 에레구토론 가부시끼가이샤 | Automatic coating system |
JPH05109612A (en) * | 1991-10-18 | 1993-04-30 | Fujitsu Ltd | Resist coating apparatus |
JPH0593569U (en) * | 1992-05-15 | 1993-12-21 | 関東自動車工業株式会社 | Coating equipment |
-
1976
- 1976-09-17 JP JP11230176A patent/JPS5337189A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5337189A (en) | 1978-04-06 |
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