JPH0649459A - Regeneration of industrial waste oil - Google Patents

Regeneration of industrial waste oil

Info

Publication number
JPH0649459A
JPH0649459A JP22495992A JP22495992A JPH0649459A JP H0649459 A JPH0649459 A JP H0649459A JP 22495992 A JP22495992 A JP 22495992A JP 22495992 A JP22495992 A JP 22495992A JP H0649459 A JPH0649459 A JP H0649459A
Authority
JP
Japan
Prior art keywords
waste oil
oil
industrial waste
chlorine
aniline
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.)
Withdrawn
Application number
JP22495992A
Other languages
Japanese (ja)
Inventor
Kiyoshi Matsuura
清 松浦
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.)
AKAGI KOUYU KK
Original Assignee
AKAGI KOUYU KK
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 AKAGI KOUYU KK filed Critical AKAGI KOUYU KK
Priority to JP22495992A priority Critical patent/JPH0649459A/en
Publication of JPH0649459A publication Critical patent/JPH0649459A/en
Withdrawn legal-status Critical Current

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

Abstract

PURPOSE:To enable the regeneration of an industrial waste oil to a fuel oil (heavy oil) generating little chlorine gas which causes the corrosion of a burner and the lowering of the combustion calorie. CONSTITUTION:Chlorine compounds in a recovered industrial waste oil are removed by adding benzene and/or aniline to the industrial waste oil and irradiating the oil with ultraviolet ray during the regeneration of the waste oil.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、回収した各種の工業用
廃油を燃焼用油として再生する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for recycling various industrial waste oils recovered as combustion oils.

【0002】[0002]

【従来の技術】貯蔵用タンクに集められた工業用廃油
は、熱交換器にて低沸点化合物を除去し、さらに遠心分
離機によって水と固形物とを取り除くことにより燃焼用
油(重油)として再生されている。
BACKGROUND OF THE INVENTION Industrial waste oil collected in a storage tank is used as a combustion oil (heavy oil) by removing low boiling point compounds in a heat exchanger and further removing water and solids by a centrifuge. Is being played.

【0003】[0003]

【発明が解決しようとする課題】ところで、前記貯蔵用
タンクに集められた工業用廃油の中には、切削オイルや
金属成形体の焼き入れの際の浸漬用オイル等が混入して
おり、切削物に付着した切削オイルや金属成形体に付着
した浸漬用オイルの除去に使用したトリクロロエチレン
やテトラクロロエチレン等による塩素系溶剤等が混入し
ている。
By the way, the industrial waste oil collected in the storage tank contains cutting oil, dipping oil during quenching of the metal formed body, and the like. Chlorine-based solvent such as trichlorethylene or tetrachlorethylene used for removing cutting oil adhering to objects and dipping oil adhering to metal moldings is mixed.

【0004】塩素化合物が混入している廃油を前記した
従来の方法にて再生した燃焼用油には、依然として塩素
化合物が混入しており、これを燃焼させると塩素ガスが
生成する。このため、再生した燃焼用油の燃焼の際に
は、生成塩素ガスが燃焼装置を腐食させる原因となるだ
けでなく燃焼カロリーを低下させる要因ともなる。
[0004] The combustion oil regenerated from waste oil containing chlorine compounds by the above-mentioned conventional method still contains chlorine compounds, and when this is burned, chlorine gas is produced. Therefore, when the regenerated combustion oil is burned, the generated chlorine gas not only causes the combustion device to corrode but also reduces the calories burned.

【0005】これに対して本発明は、工業用廃油から燃
焼用油を再生する工程中に塩素化合物の除去工程を設け
ることにより、塩素化合物の含有量の少ない再生油から
なる燃焼用油を得るものである。
On the other hand, according to the present invention, by providing a chlorine compound removing step in the step of regenerating a combustion oil from industrial waste oil, a combustion oil composed of a regenerated oil having a low chlorine compound content is obtained. It is a thing.

【0006】[0006]

【発明が解決しようとする課題】本発明の工業用廃油の
再生方法は、回収した工業用廃油を燃焼用油として再生
する工程中に、工業用廃油にベンゼン及び/又はアニリ
ンを添加して紫外線照射を行なうことからなる塩素化合
物の除去工程を有する。
DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention The method for recycling industrial waste oil of the present invention is to add ultraviolet light by adding benzene and / or aniline to the industrial waste oil during the step of recycling the recovered industrial waste oil as combustion oil. There is a chlorine compound removal step consisting of performing irradiation.

【0007】工業用廃油は、紫外線照射によって工業用
廃油中に含まれている塩素化合物が分解して塩素ガスと
なって大気中に放散される。しかしながら、紫外線照射
のみによる塩素化合物の分解反応は極めて緩慢であり、
例えば、100時間もの紫外線照射を行なっても塩素化
合物の除去率は30%程度であることが本発明者らの実
験によって確認されており、紫外線照射のみによる塩素
化合物の除去方法は実用的ではない。
[0007] Industrial waste oil is decomposed into chlorine gas contained in the industrial waste oil by irradiation with ultraviolet rays to become chlorine gas, which is then released into the atmosphere. However, the decomposition reaction of chlorine compounds only by ultraviolet irradiation is extremely slow,
For example, it has been confirmed by experiments by the present inventors that the removal rate of chlorine compounds is about 30% even after 100 hours of UV irradiation, and the method of removing chlorine compounds by only UV irradiation is not practical. .

【0008】本発明方法においては、工業用廃油中に含
まれている塩素化合物を紫外線照射によって分解して大
気中に放散させる際に、燃焼油としての性能に悪影響を
及ぼすことのないベンゼン及び/又はアニリンを触媒と
して用いることにより、紫外線照射のみによる場合に比
較して遥かに短時間の紫外線照射にて塩素化合物を効率
良く分解し除去するものである。
In the method of the present invention, when chlorine compounds contained in industrial waste oil are decomposed by ultraviolet irradiation and released into the atmosphere, benzene and // Alternatively, by using aniline as a catalyst, chlorine compounds can be efficiently decomposed and removed by ultraviolet irradiation for a far shorter time than in the case of only ultraviolet irradiation.

【0009】廃油中に添加する触媒としてのベンゼン及
び/又はアニリンの量は、一定の範囲迄はその量が多く
なる程得られる効果が高くなるが、10.0重量%を超
えるとベンゼン及び/又はアニリンの添加量を高めたこ
とに対する相応の効果は得られなくなり不経済になる。
したがって、触媒としてのベンゼン及び/又はアニリン
の添加量は、工業用廃油の2.0〜10.0重量%程度
で十分である。
The amount of benzene and / or aniline as a catalyst to be added to waste oil increases as the amount increases up to a certain range. However, when the amount exceeds 10.0% by weight, benzene and / or aniline are added. Alternatively, it becomes uneconomical because the corresponding effect for increasing the addition amount of aniline cannot be obtained.
Therefore, the addition amount of benzene and / or aniline as a catalyst is sufficient to be about 2.0 to 10.0% by weight of industrial waste oil.

【0010】本発明の工業用廃油の再生方法において
は、各種の所定箇所から集めた工業用廃油を貯蔵タンク
に貯留した後、これを熱交換器に通して低沸点化合物を
除去し、さらに、遠心分離機で水と固形物とを分離した
後に得られたものを燃焼用の再生油とする工程中にて、
前述のベンゼン及び/又はアニリンの添加の下での紫外
線照射処理を、廃油の処理工程中の遠心分離機での処理
の前あるいは遠心分離機での処理の後のいずれかで行な
うのが良い。
In the industrial waste oil recycling method of the present invention, the industrial waste oil collected from various predetermined locations is stored in a storage tank and then passed through a heat exchanger to remove low boiling point compounds. In the process of making the regenerated oil for combustion what was obtained after separating water and solid matter with a centrifuge,
The UV irradiation treatment with the addition of benzene and / or aniline as described above may be carried out either before the treatment with the centrifuge or after the treatment with the centrifuge during the treatment step of the waste oil.

【0011】[0011]

【実施例】以下、本発明の工業用廃油の再生方法の具体
的な構成を実施例に基づいて説明する。
EXAMPLES The concrete constitution of the method for recycling industrial waste oil of the present invention will be described below based on examples.

【0012】[実施例1]高塩素系廃油「塩素濃度=1
0638ppm」を直径60m/mのシャーレに20m
l秤量した後、これに5重量%のベンゼン「和光純薬1
級」を添加し、波長254nmの紫外線ランプ「 (株)
:ラボスコ製,15W×2灯」による紫外線の照射を
行なった。
[Example 1] High chlorine waste oil "chlorine concentration = 1"
0638ppm "in a petri dish with a diameter of 60m / m for 20m
l Weighed, and then 5% by weight of benzene “Wako Pure Chemical 1
UV lamp with a wavelength of 254 nm is added.
: 15 W x 2 lamps manufactured by Labosco ".

【0013】廃油中の塩素の含有量の分析を所定時間毎
に行なうことにより、紫外線の照射時間に対する塩素の
除去率を測定した。結果を[表1]に示す。
By analyzing the chlorine content in the waste oil every predetermined time, the chlorine removal rate with respect to the ultraviolet irradiation time was measured. The results are shown in [Table 1].

【0014】[0014]

【表1】 [Table 1]

【0015】[実施例2]高塩素系廃油「塩素濃度=1
0638ppm」を直径60m/mのシャーレに20m
l秤量した後、これに5重量%のアニリン「和光純薬1
級」を添加し、波長254nmの紫外線ランプ「 (株)
:ラボスコ製,15W×2灯」による紫外線の照射を
行なった。
[Example 2] High chlorine waste oil "chlorine concentration = 1"
0638ppm "in a petri dish with a diameter of 60m / m for 20m
l Weighed, then 5% by weight of aniline “Wako Pure Chemical 1
UV lamp with a wavelength of 254 nm is added.
: 15 W x 2 lamps manufactured by Labosco ".

【0016】廃油中の塩素の含有量の分析を所定時間毎
に行なうことにより、紫外線の照射時間に対する塩素の
除去率を測定した。結果を[表2]に示す。
By analyzing the content of chlorine in the waste oil every predetermined time, the chlorine removal rate with respect to the irradiation time of ultraviolet rays was measured. The results are shown in [Table 2].

【0017】[0017]

【表2】 [Table 2]

【0018】[実施例3]高塩素系廃油「塩素濃度=1
0638ppm」を直径60m/mのシャーレに20m
l秤量した後、これに2.5重量%,5.0重量%,及
び7.5重量%のアニリン「和光純薬1級」を添加し、
波長254nmの紫外線ランプ「 (株) :ラボスコ製,
15W×2灯」による紫外線の照射を行なった。
[Example 3] High chlorine waste oil "chlorine concentration = 1"
0638ppm "in a petri dish with a diameter of 60m / m for 20m
After weighing 1, 2.5% by weight, 5.0% by weight, and 7.5% by weight of aniline “Wako Pure Chemical Grade 1” were added to the mixture,
UV lamp with a wavelength of 254 nm "(Ltd.): Labosco,
Irradiation with ultraviolet rays was performed by "15 W x 2 lamps".

【0019】廃油中の塩素の含有量の分析を所定時間毎
に行なうことにより、紫外線の照射時間に対する塩素の
除去率を測定した。2.5重量%のアニリンを添加した
場合を[表3]に、5.0重量%のアニリンを添加した
場合を[表4]に、7.5重量%のアニリンを添加した
場合を[表5]にそれぞれ示す。
By analyzing the chlorine content in the waste oil every predetermined time, the chlorine removal rate with respect to the ultraviolet irradiation time was measured. [Table 3] when 2.5 wt% of aniline was added, [Table 4] when 5.0 wt% of aniline was added, and [Table 4] when 7.5 wt% of aniline was added. 5] respectively.

【0020】[0020]

【表3】 [Table 3]

【0021】[0021]

【表4】 [Table 4]

【0022】[0022]

【表5】 [Table 5]

【0023】[比較例1]高塩素系廃油「塩素濃度=1
0638ppm」を直径60m/mのシャーレに20m
l秤量した後、波長254nmの紫外線ランプ「 (株)
:ラボスコ製,15W×2灯」による紫外線の照射を
行なった。
[Comparative Example 1] High chlorine waste oil "chlorine concentration = 1"
0638ppm "in a petri dish with a diameter of 60m / m for 20m
l After weighing, UV lamp with wavelength of 254 nm
: 15 W x 2 lamps manufactured by Labosco ".

【0024】廃油中の塩素の含有量の分析を所定時間毎
に行なうことにより、紫外線の照射時間に対する塩素の
除去率を測定した。結果を[表6]及び[表7]に示
す。
By analyzing the content of chlorine in the waste oil every predetermined time, the chlorine removal rate with respect to the irradiation time of ultraviolet rays was measured. The results are shown in [Table 6] and [Table 7].

【0025】[0025]

【表6】 [Table 6]

【0026】[0026]

【表7】 [Table 7]

【0027】[0027]

【発明の作用,効果】本発明は、回収した工業用廃油を
燃焼用油として再生する工程中に、工業用廃油にベンゼ
ン及び/又はアニリンを添加して紫外線照射を行なう工
程を設けることにより、廃油中の塩素化合物を除去する
ことからなるもので、燃焼用油として使用する再生油中
の塩素化合物の含有量を低下させることにより、燃焼工
程での塩素ガスの発生量を抑えるようにするものであ
る。
INDUSTRIAL APPLICABILITY According to the present invention, by providing a step of adding benzene and / or aniline to industrial waste oil and performing ultraviolet irradiation during the step of regenerating the recovered industrial waste oil as combustion oil, It consists of removing chlorine compounds from waste oil. By reducing the content of chlorine compounds in recycled oil used as combustion oil, the amount of chlorine gas generated in the combustion process is suppressed. Is.

【0028】したがって、本発明の工業用廃油の再生方
法によって得られた燃焼用油の燃焼の際には、塩素ガス
の発生による燃焼装置の腐食や、燃焼カロリーの低下等
が無く、本発明の工業用廃油の再生方法によれば、実用
面で高度の利用価値を有する燃焼用再生油が得られる。
Therefore, when the combustion oil obtained by the industrial waste oil regeneration method of the present invention is burned, there is no corrosion of the combustion apparatus due to generation of chlorine gas, reduction of combustion calories, and the like. According to the industrial waste oil reclaiming method, a reclaimed oil for combustion having a high utility value in practical use can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 回収した工業用廃油を燃焼用油として再
生する工程中に、工業用廃油にベンゼン及び/又はアニ
リンを添加して紫外線照射を行なう工程を設けることに
より、廃油中の塩素化合物を除去することを特徴とする
工業用廃油の再生方法。
1. A chlorine compound in the waste oil is removed by providing a step of adding benzene and / or aniline to the industrial waste oil and irradiating with ultraviolet rays in the step of regenerating the recovered industrial waste oil as combustion oil. A method for reclaiming industrial waste oil, which comprises removing the waste oil.
JP22495992A 1992-07-31 1992-07-31 Regeneration of industrial waste oil Withdrawn JPH0649459A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP22495992A JPH0649459A (en) 1992-07-31 1992-07-31 Regeneration of industrial waste oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP22495992A JPH0649459A (en) 1992-07-31 1992-07-31 Regeneration of industrial waste oil

Publications (1)

Publication Number Publication Date
JPH0649459A true JPH0649459A (en) 1994-02-22

Family

ID=16821884

Family Applications (1)

Application Number Title Priority Date Filing Date
JP22495992A Withdrawn JPH0649459A (en) 1992-07-31 1992-07-31 Regeneration of industrial waste oil

Country Status (1)

Country Link
JP (1) JPH0649459A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100600940B1 (en) * 2002-04-13 2006-07-13 현대중공업 주식회사 Apparatus for the regeneration of industrial fluids with UV and nozzle type spray
KR100877671B1 (en) * 2007-08-31 2009-01-08 경북대학교 산학협력단 A device for recycling cutting oil using ultraviolet(uv) rays
JP2016160800A (en) * 2015-02-27 2016-09-05 株式会社セラフィム Fuel supply control method and its device for diesel engine

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100600940B1 (en) * 2002-04-13 2006-07-13 현대중공업 주식회사 Apparatus for the regeneration of industrial fluids with UV and nozzle type spray
KR100877671B1 (en) * 2007-08-31 2009-01-08 경북대학교 산학협력단 A device for recycling cutting oil using ultraviolet(uv) rays
JP2016160800A (en) * 2015-02-27 2016-09-05 株式会社セラフィム Fuel supply control method and its device for diesel engine

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Date Code Title Description
A300 Withdrawal of application because of no request for examination

Free format text: JAPANESE INTERMEDIATE CODE: A300

Effective date: 19991005