JPS645923B2 - - Google Patents

Info

Publication number
JPS645923B2
JPS645923B2 JP57090515A JP9051582A JPS645923B2 JP S645923 B2 JPS645923 B2 JP S645923B2 JP 57090515 A JP57090515 A JP 57090515A JP 9051582 A JP9051582 A JP 9051582A JP S645923 B2 JPS645923 B2 JP S645923B2
Authority
JP
Japan
Prior art keywords
oils
fats
methylene chloride
oil
solvent
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
JP57090515A
Other languages
Japanese (ja)
Other versions
JPS58207902A (en
Inventor
Hiroyuki Kowada
Isao Yoshida
Eiji Kawai
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.)
Tokuyama Corp
Original Assignee
Tokuyama Corp
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 Tokuyama Corp filed Critical Tokuyama Corp
Priority to JP57090515A priority Critical patent/JPS58207902A/en
Publication of JPS58207902A publication Critical patent/JPS58207902A/en
Publication of JPS645923B2 publication Critical patent/JPS645923B2/ja
Granted legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working

Landscapes

  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Description

【発明の詳細な説明】 本発明は金属類の加工時に用いた油脂類のう
ち、金属類に付着たものを回収、再使用するため
の回収、再使用方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a recovery and reuse method for recovering and reusing oils and fats attached to metals from among oils and fats used during the processing of metals.

鉄板、鉄線、パイプその他の圧延や引き抜き、
金属の切削、研磨、焼入れ等金属の加工をスムー
ズに行うため油脂類が多く用いられる。これらの
油脂は、当然金属表面に付着するが、次工程以後
において不都合を生ずるため洗浄徐去されること
になる。
Rolling and drawing of iron plates, iron wire, pipes, etc.
Oils and fats are often used to smoothly perform metal processing such as cutting, polishing, and hardening metals. These oils and fats naturally adhere to the metal surface, but because they cause inconvenience in subsequent steps, they must be removed by washing.

従来最も一般的な油脂の除去方法は、所謂アル
カリ洗浄である。この場合油脂はアルカリで一部
分解され、残部は乳濁状態の廃液を生ずる。この
方法の欠点はまず、洗浄に要する時間が比較的長
いこと、油脂除去後の廃液の処理、即ちBOD,
CODの減少処理、PHの調整等厄介な問題がある。
Conventionally, the most common method for removing fats and oils is so-called alkaline cleaning. In this case, the fats and oils are partially decomposed by the alkali, and the remainder produces an emulsified waste liquid. The disadvantages of this method are the relatively long time required for cleaning, the treatment of waste liquid after oil and fat removal, i.e. BOD,
There are troublesome issues such as COD reduction processing and PH adjustment.

そこでパークロルエチレンやトリクロルエチレ
ン、1,1,1−トリクロルエタンなどの有機溶
剤を用いて洗浄する方法も提案された。これによ
り、金属に付着した油脂の除去速度は向上した
が、一般に有機溶剤、特に塩素化溶剤と機械、工
作油等の由脂との混合物は、両者の沸点に大きな
差があるにかかわらず完全分離は容易でない。例
えば、パークロルエチレンやトリクロルエチレン
等の溶剤と機械油との混合物を常圧下に単蒸溜に
よつて分離しようとすると、低沸点成分である溶
剤を約30%程度含有した状態で沸点の上昇を来た
し、これを更に加熱すると油の劣化温度である
130℃以上、場合によつては150℃を越えてしま
う。
Therefore, a method of cleaning using an organic solvent such as perchlorethylene, trichlorethylene, or 1,1,1-trichloroethane has also been proposed. This has improved the rate of removal of oils and fats adhering to metals, but in general, mixtures of organic solvents, especially chlorinated solvents, and oils such as machine and work oils are completely removed, despite the large difference in their boiling points. Separation is not easy. For example, if a mixture of a solvent such as perchlorethylene or trichlorethylene and machine oil is separated by simple distillation under normal pressure, the boiling point will rise when the solvent contains about 30% of the low boiling point component. If you heat this further, it will reach the deterioration temperature of the oil.
The temperature exceeds 130℃, and in some cases exceeds 150℃.

また溶剤を約30%も含有する機械油は一般に用
途がないため、廃油として焼却されることにな
る。即ち、従来金属類の加工時に使用される油の
うち、該金属類に付着して持ち去られる部分は最
早回収不能分と看做されていたのである。
Additionally, machine oil that contains approximately 30% solvent is generally of no use, so it is incinerated as waste oil. That is, of the oil used in the processing of metals, the portion that adheres to the metals and is carried away is considered to be irretrievable.

本発明者等は、金属加工、即ち金属の切削、穿
孔、圧延、引抜き、プレス、焼入れ、焼鈍、表面
保護等の加工工程において潤滑、冷却、防錆その
他の目的で該金属上に塗布され、又は付着する油
脂の量が意外と多いことに着目し、これらを回収
し、有効に利用する方法を検討した結果、前記溶
剤として塩化メチレンを用いた場合には、その固
有の特性により、特定の蒸溜によつて高純度で油
脂の回収ができ、該油脂を再使用し得ることを見
い出し、本発明に到達した。即ち、本発明は、金
属類の加工に際し付着した油脂類を塩化メチレン
を用いた洗浄により溶解除去し、該油脂を含有す
る塩化メチレンを、120℃以下の温度下に常圧蒸
溜及び減圧蒸溜に順次付して溶剤を分離回収する
ことにより蒸溜残分中に含まれる塩化メチレンを
5重量%以下とし、回収された塩化メチレンは、
これを上記洗浄に供すると共に、蒸溜残分は、こ
れに新たな油脂を補充した後、上記加工工程に再
使用することを特徴とする金属類の加工用油脂の
回収、再使用方法である。
The present inventors have discovered that in metal processing, that is, metal cutting, drilling, rolling, drawing, pressing, quenching, annealing, surface protection, etc., coatings on the metal for lubrication, cooling, rust prevention, and other purposes, Also, we focused on the surprisingly large amount of oils and fats that adhered, and as a result of investigating ways to recover and use them effectively, we found that when methylene chloride is used as the solvent, its unique characteristics make it difficult to carry out certain distillations. It has been discovered that oils and fats can be recovered with high purity and reused by this method, and the present invention has been achieved. That is, the present invention dissolves and removes fats and oils that adhere to metals during processing by washing with methylene chloride, and then subjects the methylene chloride containing the fats and oils to atmospheric distillation and vacuum distillation at a temperature of 120°C or lower. By sequentially separating and recovering the solvent, the methylene chloride contained in the distillation residue is reduced to 5% by weight or less, and the recovered methylene chloride is
This is a method for recovering and reusing oils and fats for processing metals, characterized in that the oils and fats for processing metals are subjected to the above-mentioned cleaning, and the distillation residue is reused in the above-mentioned processing step after being supplemented with new oils and fats.

本発明においては、まず、溶剤洗浄に供した後
の油脂を溶解している塩化メチレン(以下単に油
脂溶液ともいう)から蒸溜手段により塩化メチレ
ンを回収した後の蒸溜残分に新たな油脂類を加え
て、得られる混合油中の塩化メチレン含量が、金
属類の加工時に用いる油脂として使用可能な範囲
の量になるまで低下せしめた後、該加工に供する
ことにより無駄なく油脂類を使用することが可能
となる。
In the present invention, first, new oils and fats are added to the distillation residue after recovering methylene chloride by distillation means from methylene chloride in which oils and fats have been dissolved after being subjected to solvent cleaning (hereinafter also simply referred to as an oil and fat solution). In addition, after reducing the methylene chloride content in the resulting mixed oil to a level that can be used as an oil or fat used in the processing of metals, the oil or fat can be used without waste by subjecting it to the processing. becomes possible.

更に本発明を効率よく行うためには、油脂溶液
を蒸溜する方法を工夫し、蒸溜残分に含まれる溶
剤量を可及的に減少させることである。一般には
常圧下での単蒸溜によつては、油の劣化温度を加
味して、120℃以下では約30%もの溶剤を回収す
ることができない。この場合、例えば再使用可能
な溶剤残存量が6%であるとすれば、新たな油に
より5倍以上に稀釈する必要がある。一般に、回
収される油脂の量は、加工に使われる全油脂量に
比して少量であり、また加工時のこぼれ、その他
の損失分の補填も必要となり、この程度の油の追
加は油脂の収支をくずすものではないが、更に溶
剤を十分分離する手段を講ずるのが好ましい。そ
こで、本発明は、油脂の洗浄に用いる溶剤とし
て、沸点が低く、且つ蒸溜分離性が良好な塩化メ
チレンを使用することにより、上記洗浄によつて
得られる廃液を、油脂の劣化の少ない120℃以下
の温度下で常圧蒸溜及び減圧蒸溜を実用的な条件
で順次行い、蒸溜残渣中の塩化メチレンを5重量
%以下まで減少させ、塩化メチレンは洗浄に、蒸
溜残渣は、新たな樹脂を補充して加工工程に再使
用することよりなる工程を可能とした。
Furthermore, in order to carry out the present invention efficiently, it is necessary to devise a method for distilling the oil and fat solution and to reduce the amount of solvent contained in the distillation residue as much as possible. Generally, by simple distillation under normal pressure, approximately 30% of the solvent cannot be recovered at temperatures below 120°C, taking into account the deterioration temperature of the oil. In this case, for example, if the remaining amount of reusable solvent is 6%, it is necessary to dilute it five times or more with new oil. Generally, the amount of oil recovered is small compared to the total amount of oil used in processing, and it is also necessary to compensate for spills and other losses during processing, so adding this amount of oil is Although it does not break the balance, it is preferable to take measures to sufficiently separate the solvent. Therefore, the present invention uses methylene chloride, which has a low boiling point and good distillation separation properties, as a solvent for cleaning fats and oils, so that the waste liquid obtained by the above cleaning can be heated to 120°C, where there is less deterioration of fats and oils. Atmospheric pressure distillation and reduced pressure distillation are performed sequentially under practical conditions at the following temperatures to reduce the methylene chloride in the distillation residue to 5% by weight or less. The methylene chloride is used for cleaning, and the distillation residue is used to replenish new resin. This enables a process that consists of reusing the material in the processing process.

以下第1図により本発明を具体的に説明する。
図中1は金属類加工工程であり、油だめ2より加
工油が適宜供給されていることを概念的に示した
ものである。3は金属類に付着した油脂を溶剤洗
浄すると共に常圧下での単蒸溜を行うための装置
である。即ち、溶剤洗浄槽4の塩化メチレン中
に、油脂類の付着した金属加工品5を浸漬し油脂
類を溶解除去し、次いで、該金属加工品を溶剤液
面上空間部6に引き上げ塩化メチレン蒸気に曝し
て蒸気洗浄し、取り出される。塩化メチレンの蒸
気は、金属加工品上又は冷却管7によつて凝縮さ
れ溶剤槽4に落下する。このため溶剤槽4中の微
量の油脂分を含んだ塩化メチレンは増加しオーバ
ーフローによつて蒸発槽8に移行する。蒸発槽で
は適当な加熱手段9によつて、塩化メチレン溶液
を加熱し、所謂単蒸溜の原理によつて溶剤の蒸気
が発生し、空間部6に供給される。かくして、蒸
発槽8には高濃度の油脂類を含む塩化メチレンが
蓄積するので、これをパイプライン20によつて
減圧蒸溜装置の蒸発缶10に供給する蒸発缶はエ
ジエクターその他の手段11で減圧されており、
塩化メチレンの蒸発を助ける。蒸発された塩化メ
チレンは凝縮器12等により液化され、パイプラ
イン21よりタンク13に回収される。これはパ
イプライン22により洗浄工程に循環再使用され
る。他方蒸溜残分は、パイプライン23により適
宜金属加工工程の油溜め2へ戻される。ここでは
24より新しく油脂が供給されて油溜め2内の塩
化メチレン濃度は金属加工時における許容濃度範
囲内に保持される。尚図中25からは不足する溶
剤を補給することができる。また各パイプライン
の途中等において、脱水乾燥工程を経油させるこ
とも任意である。
The present invention will be specifically explained below with reference to FIG.
In the figure, reference numeral 1 indicates a metal processing process, and conceptually shows that processing oil is appropriately supplied from an oil sump 2. 3 is an apparatus for cleaning oils and fats adhering to metals with a solvent and carrying out simple distillation under normal pressure. That is, the metal workpiece 5 with oils and fats adhered to it is immersed in methylene chloride in the solvent cleaning tank 4 to dissolve and remove the oils, and then the metal workpiece is pulled up to the space 6 above the solvent surface and methylene chloride vapor is removed. exposed to steam for cleaning and then removed. The methylene chloride vapor is condensed on the metal workpiece or by the cooling pipe 7 and falls into the solvent bath 4. Therefore, methylene chloride containing a trace amount of oil and fat in the solvent tank 4 increases and moves to the evaporation tank 8 by overflow. In the evaporation tank, the methylene chloride solution is heated by a suitable heating means 9, and solvent vapor is generated and supplied to the space 6 according to the so-called simple distillation principle. In this way, methylene chloride containing highly concentrated oils and fats is accumulated in the evaporator tank 8, and the evaporator is supplied to the evaporator 10 of the vacuum distillation apparatus through the pipeline 20, and the pressure is reduced by an ejector or other means 11. and
Helps evaporate methylene chloride. The evaporated methylene chloride is liquefied by a condenser 12 or the like, and is recovered into a tank 13 via a pipeline 21. This is recycled by pipeline 22 for the cleaning process. On the other hand, the distillation residue is appropriately returned to the oil sump 2 of the metal processing process by a pipeline 23. Here, new oil is supplied from 24, and the methylene chloride concentration in the oil reservoir 2 is maintained within the permissible concentration range during metal processing. Incidentally, the insufficient solvent can be replenished from 25 in the figure. It is also optional to carry out a dehydration and drying process in the middle of each pipeline.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の工程の1例を示す図である。
図中1は金属類の加工工程を、2は金属加工時に
用いる油脂類の溜槽を示す。3は溶剤洗浄装置で
あり、4は洗浄槽、5は被洗浄物、8は蒸気槽、
10は蒸圧蒸発缶、13はタンクを夫々表す。
FIG. 1 is a diagram showing an example of the process of the present invention.
In the figure, 1 indicates a metal processing process, and 2 indicates a reservoir for oils and fats used during metal processing. 3 is a solvent cleaning device, 4 is a cleaning tank, 5 is an object to be cleaned, 8 is a steam tank,
10 represents a steam pressure evaporator, and 13 represents a tank.

Claims (1)

【特許請求の範囲】[Claims] 1 金属類の加工に際し付着した油脂類を塩化メ
チレンを用いた洗浄により溶解除去し、該油脂を
含有する塩化メチレンを、120℃以下の温度下に
常圧蒸溜及び減圧蒸溜に順次付して塩化メチレン
を分離回収することにより蒸溜残分中に含まれる
塩化メチレンを5重量%以下とし、回収された塩
化メチレンは、これを上記洗浄に供すると共に、
蒸溜残分は、これ新たな油脂を補充した後、上記
加工工程に再使用することを特徴とする金属類の
加工油脂類の回収、再使用方法。
1 The fats and oils that adhere to metals during processing are dissolved and removed by washing with methylene chloride, and the methylene chloride containing the fats and oils is chlorinated by sequentially applying atmospheric distillation and vacuum distillation at a temperature of 120°C or less. By separating and recovering methylene, the methylene chloride contained in the distillation residue is reduced to 5% by weight or less, and the recovered methylene chloride is subjected to the above-mentioned washing, and
A method for recovering and reusing metal processing oils and fats, characterized in that the distillation residue is reused in the above-mentioned processing step after being replenished with new oils and fats.
JP57090515A 1982-05-29 1982-05-29 Recovery of oil adhered to metal Granted JPS58207902A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57090515A JPS58207902A (en) 1982-05-29 1982-05-29 Recovery of oil adhered to metal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57090515A JPS58207902A (en) 1982-05-29 1982-05-29 Recovery of oil adhered to metal

Publications (2)

Publication Number Publication Date
JPS58207902A JPS58207902A (en) 1983-12-03
JPS645923B2 true JPS645923B2 (en) 1989-02-01

Family

ID=14000592

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57090515A Granted JPS58207902A (en) 1982-05-29 1982-05-29 Recovery of oil adhered to metal

Country Status (1)

Country Link
JP (1) JPS58207902A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5992115A (en) * 1982-11-17 1984-05-28 Tokuyama Soda Co Ltd Cold drawing method of metallic pipe

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5727522Y2 (en) * 1977-10-12 1982-06-16
JPS5853956B2 (en) * 1980-08-25 1983-12-02 日本化工機工業株式会社 Circulating refrigeration system for solvent degreasing cleaning machine

Also Published As

Publication number Publication date
JPS58207902A (en) 1983-12-03

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