JPH08337799A - Purification of rinsing water - Google Patents
Purification of rinsing waterInfo
- Publication number
- JPH08337799A JPH08337799A JP17789295A JP17789295A JPH08337799A JP H08337799 A JPH08337799 A JP H08337799A JP 17789295 A JP17789295 A JP 17789295A JP 17789295 A JP17789295 A JP 17789295A JP H08337799 A JPH08337799 A JP H08337799A
- Authority
- JP
- Japan
- Prior art keywords
- water
- rinsing water
- oil
- hydrocarbon residue
- hlb
- 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
- 239000008237 rinsing water Substances 0.000 title claims abstract 10
- 238000000746 purification Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 95
- -1 polyoxyethylene Polymers 0.000 claims abstract description 27
- 229920003171 Poly (ethylene oxide) Polymers 0.000 claims abstract description 10
- 150000005215 alkyl ethers Chemical class 0.000 claims abstract description 9
- 150000002430 hydrocarbons Chemical group 0.000 claims abstract description 6
- 239000000203 mixture Substances 0.000 claims abstract description 4
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 3
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract 2
- 239000012459 cleaning agent Substances 0.000 claims description 16
- 239000007788 liquid Substances 0.000 claims description 9
- 238000000034 method Methods 0.000 claims description 8
- 125000004432 carbon atom Chemical group C* 0.000 claims description 7
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 239000003599 detergent Substances 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 3
- 150000001875 compounds Chemical class 0.000 abstract 2
- 239000011347 resin Substances 0.000 abstract 1
- 229920005989 resin Polymers 0.000 abstract 1
- 238000000926 separation method Methods 0.000 description 19
- 239000003921 oil Substances 0.000 description 16
- 235000019198 oils Nutrition 0.000 description 16
- 238000004140 cleaning Methods 0.000 description 8
- 235000014113 dietary fatty acids Nutrition 0.000 description 6
- 229930195729 fatty acid Natural products 0.000 description 6
- 239000000194 fatty acid Substances 0.000 description 6
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 5
- 238000001704 evaporation Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 230000004907 flux Effects 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 229920000259 polyoxyethylene lauryl ether Polymers 0.000 description 4
- 125000001183 hydrocarbyl group Chemical group 0.000 description 3
- WIBFFTLQMKKBLZ-SEYXRHQNSA-N n-butyl oleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCCCC WIBFFTLQMKKBLZ-SEYXRHQNSA-N 0.000 description 3
- MMXKVMNBHPAILY-UHFFFAOYSA-N ethyl laurate Chemical compound CCCCCCCCCCCC(=O)OCC MMXKVMNBHPAILY-UHFFFAOYSA-N 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 description 2
- UQDUPQYQJKYHQI-UHFFFAOYSA-N methyl laurate Chemical compound CCCCCCCCCCCC(=O)OC UQDUPQYQJKYHQI-UHFFFAOYSA-N 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- AJDIZQLSFPQPEY-UHFFFAOYSA-N 1,1,2-Trichlorotrifluoroethane Chemical compound FC(F)(Cl)C(F)(Cl)Cl AJDIZQLSFPQPEY-UHFFFAOYSA-N 0.000 description 1
- FOKDITTZHHDEHD-PFONDFGASA-N 2-ethylhexyl (z)-octadec-9-enoate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC(CC)CCCC FOKDITTZHHDEHD-PFONDFGASA-N 0.000 description 1
- LWLRMRFJCCMNML-UHFFFAOYSA-N 2-ethylhexyl dodecanoate Chemical compound CCCCCCCCCCCC(=O)OCC(CC)CCCC LWLRMRFJCCMNML-UHFFFAOYSA-N 0.000 description 1
- NDKYEUQMPZIGFN-UHFFFAOYSA-N Butyl dodecanoate Chemical compound CCCCCCCCCCCC(=O)OCCCC NDKYEUQMPZIGFN-UHFFFAOYSA-N 0.000 description 1
- LVGKNOAMLMIIKO-UHFFFAOYSA-N Elaidinsaeure-aethylester Natural products CCCCCCCCC=CCCCCCCCC(=O)OCC LVGKNOAMLMIIKO-UHFFFAOYSA-N 0.000 description 1
- 229920006197 POE laurate Polymers 0.000 description 1
- 235000021314 Palmitic acid Nutrition 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical group CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical group C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 235000019864 coconut oil Nutrition 0.000 description 1
- 239000003240 coconut oil Substances 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- QYDYPVFESGNLHU-UHFFFAOYSA-N elaidic acid methyl ester Natural products CCCCCCCCC=CCCCCCCCC(=O)OC QYDYPVFESGNLHU-UHFFFAOYSA-N 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- LVGKNOAMLMIIKO-QXMHVHEDSA-N ethyl oleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OCC LVGKNOAMLMIIKO-QXMHVHEDSA-N 0.000 description 1
- 229940093471 ethyl oleate Drugs 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 150000008282 halocarbons Chemical class 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- XUGNVMKQXJXZCD-UHFFFAOYSA-N isopropyl palmitate Chemical compound CCCCCCCCCCCCCCCC(=O)OC(C)C XUGNVMKQXJXZCD-UHFFFAOYSA-N 0.000 description 1
- 239000010721 machine oil Substances 0.000 description 1
- 239000002075 main ingredient Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000005555 metalworking Methods 0.000 description 1
- QYDYPVFESGNLHU-KHPPLWFESA-N methyl oleate Chemical compound CCCCCCCC\C=C/CCCCCCCC(=O)OC QYDYPVFESGNLHU-KHPPLWFESA-N 0.000 description 1
- 229940073769 methyl oleate Drugs 0.000 description 1
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910000679 solder Inorganic materials 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 150000005846 sugar alcohols Polymers 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- INJZMNQWJIWOEA-UHFFFAOYSA-N tridecyl dodecanoate Chemical compound CCCCCCCCCCCCCOC(=O)CCCCCCCCCCC INJZMNQWJIWOEA-UHFFFAOYSA-N 0.000 description 1
- CTWLAMKOJQOQLN-UHFFFAOYSA-N tridecyl tetradecanoate Chemical compound CCCCCCCCCCCCCOC(=O)CCCCCCCCCCCCC CTWLAMKOJQOQLN-UHFFFAOYSA-N 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Landscapes
- Removal Of Specific Substances (AREA)
- Detergent Compositions (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は電子・電気分野で使用さ
れるプリント基板をはじめとする精密部品、あるいは機
械分野で用いられる各種部品等硬質表面をもつ金属、ガ
ラス、プラスチック製部品の洗浄の際に発生する使用済
リンス水を精製する方法を提供するものである。BACKGROUND OF THE INVENTION The present invention is for cleaning precision parts such as printed circuit boards used in the electronic and electrical fields, or metal, glass and plastic parts having hard surfaces such as various parts used in the mechanical field. The present invention provides a method for purifying used rinse water generated at the time.
【0002】[0002]
【従来の技術】電子・電気分野や機械分野で使用される
部品類は、その製造工程でこれらの表面に付着している
ハンダフラックスや金属加工油等を除去するためにフロ
ン113やトリクロロエタンのようなハロゲン化炭化水
素を用いて洗浄されている。しかし、これらはオゾン層
破壊物質として、あるいは人体に対する毒性からいずれ
も1995年12月末で使用禁止される。これらの洗浄
剤にかわるものとして各種の洗浄剤が開発され、一部実
用化の段階に入っている。これらを大別すれば、活性剤
を主体とする水系あるいは準水系洗浄剤と炭化水素や低
級アルコールなどの溶剤系洗浄剤である。この内水系あ
るいは準水系洗浄剤を用いた場合、洗浄により被洗浄物
表面に付着した洗浄液を水でリンスする必要があり、こ
れによって洗浄剤を含む大量の廃水が発生する。通常こ
の廃水は産業廃棄物として廃棄するか、水を加熱蒸発さ
せ濃縮後廃棄するか、燃焼するか、あるいは水と洗浄剤
が比較的分離しやすい場合は油水分離装置を通して油水
分離後水部分をリンス水として再利用する方法がとられ
ている。しかしいずれの場合も非常にコストがかかる。
すなわち廃棄の場合は廃棄コスト、処理する場合は処理
のための設備コストに多大のコストがかかる。またかな
りの広さの場所を必要とする。さらに、油水分離で水部
分をリンス水として再利用するとしても油水分離の程度
が不十分で水中の有機物含量が高くリンス水として不適
な場合が多い。2. Description of the Related Art Parts used in the fields of electronics and electricity and machinery are manufactured using CFCs such as CFC 113 or trichloroethane in order to remove the solder flux and metal working oil adhering to their surfaces during the manufacturing process. Washed with different halogenated hydrocarbons. However, these are prohibited from use as ozone-depleting substances or due to their toxicity to the human body at the end of December 1995. Various cleaning agents have been developed as alternatives to these cleaning agents, and are partially in the stage of practical application. These are roughly classified into water-based or semi-water-based detergents containing an activator as a main ingredient and solvent-based detergents such as hydrocarbons and lower alcohols. When this internal water-based or semi-aqueous cleaning agent is used, it is necessary to rinse the cleaning liquid adhering to the surface of the object to be cleaned with water, which causes a large amount of waste water containing the cleaning agent. Usually, this waste water is either discarded as industrial waste, or is heated and evaporated to be concentrated and then discarded, or burned, or if the water and the cleaning agent are relatively easy to separate, pass the oil and water separation device to separate the water portion after the oil and water separation device. The method of reuse as rinse water is adopted. However, both cases are very costly.
That is, in the case of disposal, a great deal of cost is required for disposal, and for processing, a large amount of equipment cost is required for processing. It also requires a lot of space. Further, even if the water portion is reused as rinse water in oil-water separation, the degree of oil-water separation is insufficient, the organic matter content in water is high, and it is often unsuitable as rinse water.
【0003】[0003]
【発明が解決しようとする課題】したがって、本発明に
おいては水系あるいは準水系洗浄システムのもつ最大の
問題点である洗浄後水でリンスする際、発生する洗浄剤
含有リンス水の精製再利用を低コストで行う方法を提供
するものである。Therefore, in the present invention, the biggest problem of the water-based or semi-water-based cleaning system is to reduce the purification reuse of the rinse water containing the cleaning agent, which occurs when rinsing with water after cleaning. It provides a cost-effective way.
【0004】[0004]
【課題を解決するための手段】本発明者らは、上記課題
を解決すべく鋭意研究を重ねた結果,洗浄に使用する洗
浄剤に特定組成のものを使用し,これと,特定の油水分
離方法との組合せにより課題を解決し本発明に至った。
すなわち,HLBが13以下のポリオキシエチレンアル
キルエーテルを必須成分とする洗浄剤を含有するリンス
水を,該リンス水の曇点より10℃以上高温に保った水
の表面もしくは表面近くの水中に連続的に細かい液滴に
して滴下もしくは注入して両液を接触させ,浮上する洗
浄剤等の油分を分離することを特長とするリンス水の精
製方法である。この精製方法においては,リンス水中に
含まれる洗浄剤としてHLBが13以下のポリオキシエ
チレンアルキルエーテルを含有することを必須とする
が,とりわけ以下の洗浄剤が優れている。 すなわち一
般式(1) R1COOR2 (1) (式中R1は炭素数11〜17の炭化水素残基、R2は
炭素数1〜13の炭化水素残基)で表される脂肪酸エス
テルおよび一般式(2) R3(CH2CH2O)nH (2) (式中R3は炭素数8〜12の炭化水素残基、nは3〜
8)で表されるHLBが13以下のポリオキシアルキル
エーテルとの配合物である。As a result of intensive studies to solve the above problems, the present inventors have used a cleaning agent having a specific composition as a cleaning agent for cleaning, and separating it from a specific oil-water separation. The problem was solved by the combination with the method, and the present invention was achieved.
That is, rinse water containing a cleaning agent containing a polyoxyethylene alkyl ether having an HLB of 13 or less as an essential component is continuously added to the surface of water kept at a temperature of 10 ° C. or higher from the cloud point of the rinse water or water near the surface. This is a method for purifying rinse water, which is characterized in that the two liquids are brought into contact with each other by making them into fine liquid droplets and injecting them to separate the oil such as the floating detergent. In this purification method, it is essential that HLB contains a polyoxyethylene alkyl ether having an HLB of 13 or less as a detergent contained in the rinse water, but the following detergents are particularly excellent. That is, a fatty acid ester represented by the general formula (1) R 1 COOR 2 (1) (wherein R 1 is a hydrocarbon residue having 11 to 17 carbon atoms, and R 2 is a hydrocarbon residue having 1 to 13 carbon atoms). And R 3 (CH 2 CH 2 O) nH (2) (wherein R 3 is a hydrocarbon residue having 8 to 12 carbon atoms, and n is 3 to
A blend with a polyoxyalkyl ether having an HLB of 13 or less represented by 8).
【0005】本発明を実施するにあたっては特別な高価
な油水分離装置は必要ない。すなわちリンス水の曇点よ
り10℃以上高温に保った水が入り,連続的または間欠
的に使用済リンス水が導入できる入口と,連続的または
間欠的に油分分離後の水層が取り出せる出口をそなえた
縦長の容器であればよく,きわめて低コストで製作でき
る。また容器の大きさも大きいものは必要ない。何故な
らリンス水を容器中の水に接触させた瞬間に油分と水層
が分離し,しかもリンス水の滴下もしくは注入場所がい
ずれも水面近くであり,分離した油分の浮上に時間を要
しないためである。No special expensive oil-water separator is required to practice the present invention. That is, there is an inlet into which the water kept at a temperature 10 ° C or more higher than the cloud point of the rinse water can be introduced to continuously and intermittently introduce the used rinse water, and an outlet from which the water layer after oil separation can be continuously or intermittently taken out. Any vertically long container provided can be used, and it can be manufactured at extremely low cost. In addition, the size of the container does not need to be large. Because the oil and the water layer are separated at the moment when the rinse water is brought into contact with the water in the container, and the dripping or pouring place of the rinse water is near the water surface, and it does not take time to float the separated oil. Is.
【0006】本発明において油水分離のための容器中の
水の温度はリンス水の曇点より,高温であればよいが,
油層と水層が明瞭に分離するためには最低10℃以上高
温である必要がある。一方高温になりすぎると,容器中
の水の対流がおこり,水層中の油分が多くなり好ましく
ない。通常常圧で操作する場合90℃以上は好ましくな
い。In the present invention, the temperature of the water in the container for oil-water separation may be higher than the cloud point of the rinse water,
In order for the oil layer and the water layer to be clearly separated, the temperature must be at least 10 ° C. or higher. On the other hand, if the temperature becomes too high, convection of water in the container occurs and the amount of oil in the water layer increases, which is not preferable. When operating under normal pressure, 90 ° C or higher is not preferable.
【0007】本発明の必須要件としては,被処理リンス
水の中にHLB13以下のポリオキシエチレンアルキル
エーテル成分が含有されていることである。この成分は
洗浄工程で使用する洗浄液に由来するものである。ポリ
オキシエチレンアルキルエーテルの具体例としては、ポ
リオキシエチレンオクチルエーテル、ポリオキシエチレ
ンデシルエーテル、ポリオキシエチレンドデシルエーテ
ル、ポリオキシエチレンラウリルエーテル、ポリオキシ
エチレンセチルエーテル、ポリオキシエチレンステアリ
ルエーテル、ポリオキシエチレンオレイルエーテルなど
のうちHLB13以下の範囲にエチレンオキサイド付加
モル数を調整したものである。An essential requirement of the present invention is that the rinse water to be treated contains a polyoxyethylene alkyl ether component having an HLB of 13 or less. This component is derived from the cleaning liquid used in the cleaning process. Specific examples of polyoxyethylene alkyl ethers include polyoxyethylene octyl ether, polyoxyethylene decyl ether, polyoxyethylene dodecyl ether, polyoxyethylene lauryl ether, polyoxyethylene cetyl ether, polyoxyethylene stearyl ether, polyoxyethylene. Among oleyl ethers and the like, the number of moles of ethylene oxide added is adjusted in the range of HLB 13 or less.
【0008】ポリオキシエチレンアルキルエーテルは1
価アルコールにエチレンオキサイドを付加して製造され
るが,この場合エチレンオキサイドの一部をプロピレン
オキサイドやブチレンオキサイドで代替したものも含ま
れる。Polyoxyethylene alkyl ether is 1
It is produced by adding ethylene oxide to a polyhydric alcohol. In this case, ethylene oxide partly replaced with propylene oxide or butylene oxide is also included.
【0009】またこれらのエーテル類は単品でも,また
何種かの組合せでも使用できる。また他のエチレンオキ
サイド付加物たとえば脂肪酸やアルキルフェノールにエ
チレンオキサイドを付加したようなものもごく少量なら
配合してもかまわないが,配合量が増えると,使用済リ
ンス水の油水分離を悪化して好ましくない。These ethers can be used alone or in combination of several kinds. Other ethylene oxide adducts such as fatty acids and alkylphenols with ethylene oxide added may be added in a very small amount, but if the amount is increased, oil-water separation of used rinse water is deteriorated, which is preferable. Absent.
【0010】ポリオキシエチレンアルキルエーテルのH
LBは使用済リンス水の油水分離による再利用の面で重
要である。HLBが13を越えると使用済リンスの油水
分離操作に高温を要し,油水分離機中の水の対流がはげ
しくなり好ましくない。また油水分離後の水のなかの有
機物含量が高くなりリンス水として再利用するに好まし
くない。H of polyoxyethylene alkyl ether
LB is important in terms of reuse of used rinse water by separating oil and water. If the HLB exceeds 13, a high temperature is required for the oil / water separation operation of the used rinse, and the convection of water in the oil / water separator becomes harsh, which is not preferable. In addition, the content of organic matter in the water after oil-water separation becomes high, which is not preferable for reuse as rinse water.
【0011】被処理リンス中にはHLB13以下のポリ
オキシエチレンアルキルエーテルと同時に脂肪酸エステ
ルを含有すると油水分離によるリンス水の再生をより容
易にする。この成分も洗浄工程で使用する洗浄剤に由来
するものである。If the fatty acid ester is contained in the rinse to be treated at the same time as the polyoxyethylene alkyl ether having an HLB of 13 or less, regeneration of the rinse water by oil-water separation becomes easier. This component is also derived from the detergent used in the washing step.
【0012】本発明における脂肪酸エステルの具体例と
してはラウリン酸メチル、ラウリン酸エチル、ラウリン
酸ブチル、ラウリン酸2−エチルヘキシル、ラウリン酸
トリデシル、ミリスチン酸トリデシル、パルミチン酸2
−エチルヘキシル、オレイン酸メチル、オレイン酸エチ
ル、オレイン酸ブチル、オレイン酸2−エチルヘキシ
ル、その他ヤシ油脂肪酸ブチルのような混合脂肪酸エス
テルも同様に用いられるし、またいくつかのエステルを
配合してもかまわない。Specific examples of the fatty acid ester in the present invention include methyl laurate, ethyl laurate, butyl laurate, 2-ethylhexyl laurate, tridecyl laurate, tridecyl myristate, palmitic acid 2
-Mixed fatty acid esters such as ethylhexyl, methyl oleate, ethyl oleate, butyl oleate, 2-ethylhexyl oleate, and butyl coconut oil fatty acid may be used in the same manner, or some esters may be blended. Absent.
【0013】[0013]
【実施例】以下実施例をあげ説明するが,本発明はこれ
に限定されるものではない。EXAMPLES Examples will be described below, but the present invention is not limited thereto.
【0014】[0014]
【実施例1】オレイン酸ブチル55部,ポリオキシエチ
レンラウリルエーテル(HLB12.1)45部からな
る洗浄剤90部とフラックス10部からなる不純物を2
%含有する使用済リンス水(40℃)1.1lを20m
l/分の速度で底面積120cm2,高さ25cmのビ
ーカーの水面上から液の粒径約1〜2mmにして滴下す
る。ビーカー内にはあらかじめ同一の使用済リンス水
1.5lを70℃に加温して入れてある。滴下中液温は
70℃に維持される。滴下終了後,ビーカーの底の方か
ら水層1.2lを抜きとる。この液の一部をサンプリン
グして蒸発残査量を求める。抜きとった液の残り1.1
lに上記の洗浄剤90部とフラックス10部からなる不
純物を2%加え,上記と同一操作で油水分離,水層の採
取を行う。以上の操作をさらに8回繰り返す。合計10
回の操作で採取した水層の蒸発残査量は0.3±0.1
%の範囲にあり,いずれもリンス水の水質として使用可
能なレベルにある。Example 1 90 parts of a cleaning agent composed of 55 parts of butyl oleate and 45 parts of polyoxyethylene lauryl ether (HLB 12.1) and 2 parts of impurities composed of 10 parts of flux.
% Of used rinse water (40 ° C) containing 1.1% of 20m
A beaker having a bottom area of 120 cm 2 and a height of 25 cm is dripped at a rate of 1 / min from the water surface to a particle size of the liquid of about 1 to 2 mm. Into the beaker, 1.5 liters of the same used rinse water was preheated to 70 ° C and placed. During the dropping, the liquid temperature is maintained at 70 ° C. After the dropping is completed, 1.2 l of the aqueous layer is drawn from the bottom of the beaker. A part of this liquid is sampled to obtain the evaporation residue amount. Remaining liquid 1.1
2% of the impurities consisting of 90 parts of the cleaning agent and 10 parts of the flux described above are added to 1 l, and oil and water are separated and the water layer is collected by the same operation as described above. The above operation is repeated eight more times. 10 in total
The amount of evaporation residue of the water layer collected by one operation is 0.3 ± 0.1
%, Both of which are at levels that can be used as the quality of rinse water.
【0015】[0015]
【実施例2】パルミリン酸2−エチルヘキシル40部,
ポリオキシエチレンラウリルエーテル(LB12.1)
60部からなる洗浄剤90部にフラックス10部からな
る不純物を2%含有する使用済のリンス水(40℃)を
使用した以外は実施例1と同一方法で油水分離を行っ
た。油水分離後の水層の蒸発残査量は0.2±0.1%
の範囲にあり,いずれもリンス層の水質としては十分で
あった。Example 2 40 parts of 2-ethylhexyl palmylate,
Polyoxyethylene lauryl ether (LB12.1)
Oil-water separation was performed in the same manner as in Example 1 except that used rinse water (40 ° C.) containing 2% of impurities of 10 parts of flux in 90 parts of 60 parts of detergent. The amount of evaporation residue of the water layer after oil-water separation is 0.2 ± 0.1%
The water quality of the rinse layer was sufficient.
【0016】[0016]
【実施例3】オレイン酸ブチル45部,ポリオキシエチ
レンラウリルエーテル(HLB10.8)55部からな
る洗浄剤90部にマシン油10部からなる不純物を2%
含有する使用済のリンス水(40℃)を用い,油水分離
を60℃で行う以外,実施例1と同一の方法で油水分離
を行った。油水分離後の水層の蒸発残査量は0.1±
0.1%の範囲にあり,いずれもリンス層の水質として
は十分であった。Example 3 90% of a cleaning agent composed of 45 parts of butyl oleate and 55 parts of polyoxyethylene lauryl ether (HLB10.8) and 2% of an impurity composed of 10 parts of machine oil.
Oil-water separation was performed in the same manner as in Example 1 except that used rinse water (40 ° C.) contained therein was used to separate oil-water at 60 ° C. The amount of evaporation residue in the water layer after oil-water separation is 0.1 ±
It was in the range of 0.1%, and both were sufficient as water quality for the rinse layer.
【0017】[0017]
【比較例】パルミチン酸イソプロピル60部,ポリオキ
シエチレンラウレート(HLB14.3)40部からな
る洗浄剤90部にフラックス10部からなる不純物を2
%含有する使用済リンス水(40℃)を使用した以外は
実施例1と同一方法で油水分離を行った。油水分離後の
油層と水層との界面は不明瞭であり,また水層の白濁程
度は烈しく,油層中の水含量も高かった。油水分離後の
水層の蒸発残査量は1.1±0.2%の範囲で油水分離
の効果は不良であった。[Comparative Example] 90 parts of a cleaning agent composed of 60 parts of isopropyl palmitate and 40 parts of polyoxyethylene laurate (HLB14.3) and 2 parts of an impurity composed of 10 parts of flux.
Oil water separation was carried out in the same manner as in Example 1 except that the used rinse water (40 ° C.) contained was used. The interface between the oil layers after the oil-water separation was unclear, the degree of cloudiness of the water layer was severe, and the water content in the oil layer was high. The evaporation residue amount of the water layer after oil-water separation was in the range of 1.1 ± 0.2%, and the effect of oil-water separation was poor.
【0018】[0018]
【発明の効果】以上のごとく本発明は従来の水系もしく
は準水系洗浄システムの最大のネックであった使用済リ
ンス水の処理をきわめて簡単な操作でリンス水として再
利用可能レベルの水質まで精製を可能にする。As described above, according to the present invention, the treatment of used rinse water, which has been the biggest bottleneck of the conventional water-based or semi-water-based cleaning system, can be purified to a reusable level as rinse water by an extremely simple operation. enable.
Claims (2)
ルキルエーテルを必須成分とする洗浄剤を含有するリン
ス水を、該リンス水の曇点より10℃以上高温に保った
水の表面もしくは表面近くの水中に連続的もしくは間欠
的に細かい液滴にして滴下もしくは注入して両液を接触
させ,浮上した洗浄剤等の油分を分離することを特長と
するリンス水の精製方法。1. Rinsing water containing a cleaning agent containing a polyoxyethylene alkyl ether having an HLB of 13 or less as an essential component is kept at a temperature of 10 ° C. or more above the cloud point of the rinsing water, or near the surface of the water. A method for purifying rinse water, which comprises continuously or intermittently forming fine droplets into water to drop or inject them into contact with the two liquids to separate the oil such as the floating cleaning agent.
(1) R1COOR2 (1) (式中R1は炭素数11〜17の炭化水素残基、R2は
炭素数1〜13の炭化水素残基)で表される脂肪酸エス
テル及び一般式(2) R3O(CH2CH2O)nH (2) (式中R3は炭素数8〜12の炭化水素残基、nは炭素
数3〜8)で表されるHLBが13以下のポリオキシア
ルキルエーテルとの混合物である請求項1記載のリンス
水精製方法。2. The cleaning agent contained in the rinse water is represented by the general formula (1) R 1 COOR 2 (1) (wherein R 1 is a hydrocarbon residue having 11 to 17 carbon atoms, and R 2 is 1 to 13 carbon atoms). A hydrocarbon residue) and a general formula (2) R 3 O (CH 2 CH 2 O) n H (2) (wherein R 3 is a hydrocarbon residue having 8 to 12 carbon atoms, The method for purifying rinse water according to claim 1, wherein n is a mixture with a polyoxyalkyl ether having an HLB represented by 3 to 8 carbon atoms and having an HLB of 13 or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17789295A JPH08337799A (en) | 1995-06-09 | 1995-06-09 | Purification of rinsing water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17789295A JPH08337799A (en) | 1995-06-09 | 1995-06-09 | Purification of rinsing water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08337799A true JPH08337799A (en) | 1996-12-24 |
Family
ID=16038893
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17789295A Pending JPH08337799A (en) | 1995-06-09 | 1995-06-09 | Purification of rinsing water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08337799A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013185120A (en) * | 2012-03-09 | 2013-09-19 | Yuken Industry Co Ltd | Method for producing reproduced cleaning solution and reuse agent |
-
1995
- 1995-06-09 JP JP17789295A patent/JPH08337799A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2013185120A (en) * | 2012-03-09 | 2013-09-19 | Yuken Industry Co Ltd | Method for producing reproduced cleaning solution and reuse agent |
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