JPS6051518B2 - How to regenerate organic pressure regulating oil - Google Patents

How to regenerate organic pressure regulating oil

Info

Publication number
JPS6051518B2
JPS6051518B2 JP12964481A JP12964481A JPS6051518B2 JP S6051518 B2 JPS6051518 B2 JP S6051518B2 JP 12964481 A JP12964481 A JP 12964481A JP 12964481 A JP12964481 A JP 12964481A JP S6051518 B2 JPS6051518 B2 JP S6051518B2
Authority
JP
Japan
Prior art keywords
oil
pressure regulating
passing
remove
sludge
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
JP12964481A
Other languages
Japanese (ja)
Other versions
JPS5832698A (en
Inventor
政明 森山
隆夫 西野
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.)
Nippon Steel Corp
Original Assignee
Sumitomo Metal Industries Ltd
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 Sumitomo Metal Industries Ltd filed Critical Sumitomo Metal Industries Ltd
Priority to JP12964481A priority Critical patent/JPS6051518B2/en
Publication of JPS5832698A publication Critical patent/JPS5832698A/en
Publication of JPS6051518B2 publication Critical patent/JPS6051518B2/en
Expired legal-status Critical Current

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  • Lubricants (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

【発明の詳細な説明】 本発明は、有機系調圧油の再生方法に関する。[Detailed description of the invention] The present invention relates to a method for regenerating organic pressure regulating oil.

有機系調圧油を使用している調質圧延機では、スプレ
方式の調圧油供給が実施されており、一度使用した油は
そのまま廃棄処理されている。これは一回の使用におい
て圧延油中に異物が混入し、Fe分や灰分が増加すると
共に油の性状変質による劣化が起こるため、これを再使
用すると、銅板の表面性状が悪化し、ロール疵を生じさ
せるなどの理由が主なものである。 そこで、本発明の
目的は、このように機能の低 ・ 、 −M、・・−4
A−−1−J−f:11、、 、ホ1f■− ー ル
↓せる方法を提供し、この再生油を循環再利用すること
によつて、原単位の向上を図つたことにある。
In temper rolling mills that use organic pressure regulating oil, pressure regulating oil is supplied by a spray method, and once used oil is disposed of as is. This is because when used once, foreign matter gets mixed into the rolling oil, which increases the Fe content and ash content and causes deterioration due to changes in the properties of the oil. If this is reused, the surface quality of the copper plate deteriorates and roll defects occur. The main reason is to cause Therefore, the purpose of the present invention is to solve the problem of low function ・ , -M,...-4
A--1-J-f: 11, , Hole 1f■- ↓ By providing a method for recycling and recycling this recycled oil, we have attempted to improve the basic unit.

未使用の新油と循環1日使用後の使用油とについて、
性状を比較すると、第1表に示すような結果になる。
Regarding unused new oil and used oil after one day of circulation,
Comparing the properties, the results are shown in Table 1.

これによると、物理的諸性状に大きな変化はなく、劣化
は認められないが汚れの要素が著しい。 さらに、本発
明者等は、調圧油の必要な性質が失なわれる限界を調査
したところ、油のPH度と大きな関係があることを見い
出した。
According to this, there are no major changes in the physical properties and no deterioration is observed, but there is a significant amount of dirt. Furthermore, the present inventors investigated the limit at which the necessary properties of pressure regulating oil are lost, and found that there is a significant relationship with the PH degree of the oil.

例えば、油の役割りの一つである防錆性とPH度の関係
ではpH9以下て防錆効果に劣化が見られる。しかし、
油の劣化を判定するPH値は油の種類により変わるため
、油種ごとに実験により事前に調べる必要がある。 第
1表したがつて、使用油からFe分、灰分を除去するこ
とによつて再生油とし、PH管理をすることにより再使
用が可能となることに着目し、第1図に示す再生過程を
構成した。
For example, regarding the relationship between rust prevention, which is one of the roles of oil, and pH level, the rust prevention effect deteriorates when the pH is below 9. but,
Since the PH value used to determine oil deterioration varies depending on the type of oil, it is necessary to investigate each type of oil in advance through experiments. Table 1 Therefore, we focused on the fact that by removing the Fe content and ash from the used oil, it becomes recycled oil, and that it can be reused by controlling the pH.The regeneration process shown in Figure 1 was Configured.

調質圧延機1の調圧工程で使用ずみの油a1をトレイ2
に回収し、マグネット・セパレータ3を通過させて油中
に含まれるFe分を除去しておく。次に、このFe除去
後の油A2をフィルタ4による一次濾過工程を通過させ
、油中に含まれる固形物を取除く。フィルタ4としては
100μmメッシュ以下のフィルタを使用するが、5〜
10μmメッシュのベーパ●フィルタが最も良い。一次
濾過油A3は、外塵を寄せつけない状態を保つて、その
まま沈澱槽5に送り込み、油中に含まれるスラッジを沈
澱させることによつて、スラッジと油分とを暫定的に分
離させる。
Oil a1 used in the pressure adjustment process of temper rolling mill 1 is transferred to tray 2.
The oil is collected and passed through a magnetic separator 3 to remove Fe contained in the oil. Next, the oil A2 after Fe removal is passed through a primary filtration step using a filter 4 to remove solids contained in the oil. As filter 4, a filter with a mesh size of 100 μm or less is used, but
A 10μm mesh vapor filter is best. The primary filtered oil A3 is kept in a state where external dust is kept away, and is sent as it is to the settling tank 5, and the sludge contained in the oil is precipitated, thereby temporarily separating the sludge and the oil.

次に沈澱槽を出た暫定分離油A4を遠心分離機6に送り
、5000〜6000r′Pmの二次濾過を施したスラ
ッジと油分とを完全分離させる。この二次濾過工程では
、スラッジ廃液と清澄液とに分離して二次濾過柑肖とす
る−ものであつて、二次濾過油はそのまま供給タンク7
へ送られる。供給タンク7に送られた二次濾過油は、そ
れ自体が既に再生油とて使用可能の状態になされている
が、調質圧延工程で回収された時点の使用済の,油は、
使用量全体の約60%であつて、残りの約40%の大半
は調圧時、銅板表面に付着し持出されるものであるので
、供給タンク7に対しては、新油タンク8から未回収油
分の約40%の補充量に相当する新油を供給し、攪拌装
置71によつて均一質!に攪拌して再生圧延油?を得る
Next, the temporarily separated oil A4 that has come out of the settling tank is sent to a centrifugal separator 6 to completely separate the oil from the sludge that has been subjected to secondary filtration at 5,000 to 6,000 r'Pm. In this secondary filtration process, the sludge waste liquid and the clarified liquid are separated into the secondary filtration liquid, and the secondary filtration oil is left as it is in the supply tank 7.
sent to. The secondary filtered oil sent to the supply tank 7 is already in a state where it can be used as recycled oil, but the used oil at the time it is recovered in the temper rolling process is
It accounts for approximately 60% of the total amount used, and most of the remaining approximately 40% adheres to the surface of the copper plate during pressure adjustment and is taken out. New oil equivalent to approximately 40% of the recovered oil is supplied, and the agitation device 71 ensures uniform quality! Play rolling oil by stirring? get.

この再生油A6は調質圧延工程のノズル11から圧延油
として噴射供給され、使用後は再び回収されて以下同様
の過程を経て循環再使用される。さらに、油の劣化度を
PH測定により判断する。 3本発
明によつて再生処理した再生油の性状を新油および未処
理の使用油と比較した結果を第2表に示す。Fe分、灰
分の除去率は良好であり、混入異物の量、大きさ共大幅
に減少して新油に近い状態になつていることがわかる。
一方、PHは循環の経時使用と共に低下の傾向があり、
第2図のように示されるが、通常8〜9程度までの使用
が可能であるので、ダンプアウト(全油更新)の時期は
再生油の循環使用後20日程度とみておけばよい。なお
、このダンプアウトの時期判定はPH測定結果により判
断する。油のPH測定は連続測定が望ましいが、定期的
なバッチ測定でも良い。本発明によれば、従来、廃棄処
分にしていた調圧油を再生して循環使用することが可能
となつたため、原単位の向上は著しいものとなり、鋼生
産1トン当りにおける従来の油消費量に対し、本発明法
実施後の油消費量は30%に減少した。
This recycled oil A6 is injected and supplied as rolling oil from the nozzle 11 of the temper rolling process, and after use, it is recovered again and thereafter circulated and reused through the same process. Furthermore, the degree of deterioration of the oil is determined by pH measurement. 3 Table 2 shows the results of comparing the properties of the recycled oil treated according to the present invention with new oil and untreated used oil. It can be seen that the removal rate of Fe content and ash content was good, and that the amount and size of the mixed foreign substances were significantly reduced, and the oil was in a state similar to that of new oil.
On the other hand, PH tends to decrease with circulation over time.
As shown in FIG. 2, since it is normally possible to use the oil for about 8 to 9 days, the dump-out (total oil renewal) period can be considered to be about 20 days after the recycled oil is used. Note that this dumpout timing is determined based on the PH measurement results. Continuous measurement is desirable for oil PH measurement, but periodic batch measurements may also be used. According to the present invention, it has become possible to regenerate and recycle the pressure regulating oil, which was conventionally disposed of as waste, resulting in a significant improvement in basic unit consumption, which is lower than the conventional oil consumption per ton of steel production. On the other hand, the oil consumption after implementing the method of the present invention was reduced to 30%.

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

第1図は本発明方法の全体構成を示す説明図。 第2図は本発明法による再生油のPHの経時変化を示す
線図。1:調質圧延機、2:トレイ、3:マグネット◆
セパレータ、4:フイルタ、5:沈澱槽、6:遠心分離
機、7:供給タンク、8:新油タンク。
FIG. 1 is an explanatory diagram showing the overall configuration of the method of the present invention. FIG. 2 is a diagram showing the change over time in the pH of recycled oil according to the method of the present invention. 1: Temper rolling mill, 2: Tray, 3: Magnet◆
Separator, 4: Filter, 5: Sedimentation tank, 6: Centrifugal separator, 7: Supply tank, 8: New oil tank.

Claims (1)

【特許請求の範囲】[Claims] 1 調質圧延時の圧延油をトレイに回収しマグネット・
セパレータを通過させてFe分を除去すること、Fe分
除去後の油をフィルタによる第1次濾過工程に通し固形
物を除去すること、前記一次濾過油を沈澱槽に通過させ
て油分とスラッジとを暫定的に分離させること、暫定分
離後の一次濾過油を遠心分離機による第二次濾過工程に
通しスラッジと油分を完全分離すること、濾過工程の完
了した油を供給タンクに導き新油を補充混合して再生油
を得ること、再生油をpH測定により油の劣化を管理す
ることからなる有機系調圧油の再生方法。
1 Collect rolling oil during temper rolling into a tray and place it in a magnet.
passing the oil through a separator to remove the Fe content; passing the Fe content removed oil through a primary filtration step using a filter to remove solids; and passing the primary filtered oil through a settling tank to remove oil and sludge. The primary filtered oil after the temporary separation is passed through a secondary filtration process using a centrifuge to completely separate the sludge and oil, and the oil that has undergone the filtration process is led to a supply tank to supply new oil. A method for regenerating organic pressure regulating oil, which comprises obtaining regenerated oil by replenishing and mixing, and controlling oil deterioration by measuring the pH of the regenerated oil.
JP12964481A 1981-08-19 1981-08-19 How to regenerate organic pressure regulating oil Expired JPS6051518B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12964481A JPS6051518B2 (en) 1981-08-19 1981-08-19 How to regenerate organic pressure regulating oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12964481A JPS6051518B2 (en) 1981-08-19 1981-08-19 How to regenerate organic pressure regulating oil

Publications (2)

Publication Number Publication Date
JPS5832698A JPS5832698A (en) 1983-02-25
JPS6051518B2 true JPS6051518B2 (en) 1985-11-14

Family

ID=15014605

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12964481A Expired JPS6051518B2 (en) 1981-08-19 1981-08-19 How to regenerate organic pressure regulating oil

Country Status (1)

Country Link
JP (1) JPS6051518B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9507094B2 (en) 2013-07-04 2016-11-29 Yazaki Corporation Optical connector

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60207155A (en) * 1984-03-30 1985-10-18 Mita Ind Co Ltd Copying machine
JPS61287984A (en) * 1985-06-14 1986-12-18 Mitsubishi Kakoki Kaisha Ltd Method and device for cleaning heavy oil containing catalyst
CN103133843B (en) * 2013-03-08 2015-05-20 中国地质大学(北京) Lubricating oil automatic purification and circulating feed system for double-roll tester
CN103865624B (en) * 2014-02-24 2016-05-18 东莞市循美环保科技有限公司 A kind of cutting fluid intelligent circulation reclaim equiment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9507094B2 (en) 2013-07-04 2016-11-29 Yazaki Corporation Optical connector

Also Published As

Publication number Publication date
JPS5832698A (en) 1983-02-25

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