JPH0892569A - Purification of regenerated oil for injecting into tuyere of blast furnace - Google Patents
Purification of regenerated oil for injecting into tuyere of blast furnaceInfo
- Publication number
- JPH0892569A JPH0892569A JP26924894A JP26924894A JPH0892569A JP H0892569 A JPH0892569 A JP H0892569A JP 26924894 A JP26924894 A JP 26924894A JP 26924894 A JP26924894 A JP 26924894A JP H0892569 A JPH0892569 A JP H0892569A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- viscosity
- tuyere
- value
- regenerated
- 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
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、鉱物質廃油を回収し、
蒸溜器による再生油精製工程を経て高炉羽口吹込可能な
燃料として再生油を提供する高炉羽口吹込用再生油精製
方法に関する。BACKGROUND OF THE INVENTION The present invention collects mineral waste oil,
The present invention relates to a method for refining regenerated oil for tuyere injection of blast furnace, which provides regenerated oil as a fuel that can be injected into tuyere of blast furnace through a regenerated oil refining process using a distiller.
【0002】[0002]
【従来の技術】従来、鉱物質廃油を高炉の羽口吹込み燃
料として供給するには、一般に重油等精製油の液体燃料
制御供給装置を利用して羽口吹込みが行われており、ポ
ンプは通常ギャポンプやカスケードポンプ等が用いら
れ、流量計は楕円歯車式等の流量計が使用されていたた
め、供給する油の粘度が高すぎるとと極度にポンプ効率
が低下し、供給不能となることがあり、流量計の計量精
度が悪くなり、また、夾雑物の粒度にも限界があり、3
0メッシュ目開き相当の粒度を超えるとポンプ及び流量
計のの可動部分に詰まり動作不能となることがあり、適
正粘度を超える重粘質油を高炉の羽口吹込用燃料として
従来の液体燃料制御供給装置によって供給することが困
難であった。2. Description of the Related Art Conventionally, in order to supply mineral waste oil as tuyere injection fuel for a blast furnace, tuyere injection is generally performed using a liquid fuel control supply device for refined oil such as heavy oil. Normally, a gear pump or cascade pump is used for the flowmeter, and an elliptical gear type flowmeter is used for the flowmeter, so if the viscosity of the oil to be supplied is too high, the pump efficiency will drop extremely and the supply will be impossible. However, the accuracy of the flow meter is poor, and the particle size of impurities is limited.
Exceeding the particle size corresponding to the 0 mesh opening may cause the pump and flowmeter to become clogged with the moving parts, making it inoperable. Heavy viscous oil exceeding the appropriate viscosity may be used as fuel for tuyere injection in a blast furnace by conventional liquid fuel control. It was difficult to supply by the supply device.
【0003】[0003]
【発明が解決しようとする課題】従来の液体燃料制御供
給装置によって鉱物質廃油を高炉の羽口吹込み燃料とし
て供給するには、適正動粘度値30cSt(以下動粘度
値は50°Cにおける値を示す)、夾雑物の粒度が30
メッシュ目開き相当付近のものが適用されるのが実態で
あって、適正動粘度値を超える重粘質油は適用し難い状
況であって、重粘質油の高炉吹込み技術と、高炉羽口吹
込用再生油精製方法との確立が課題となっている。In order to supply the waste mineral oil as the tuyere blowing fuel of the blast furnace by the conventional liquid fuel control supply device, an appropriate kinematic viscosity value of 30 cSt (hereinafter, the kinematic viscosity value is a value at 50 ° C.). Particle size of the contaminants is 30
It is the actual situation that a mesh with mesh opening equivalent is applied, and it is difficult to apply heavy viscous oil that exceeds the appropriate kinematic viscosity value.Therefore, blast furnace blowing technology for heavy viscous oil and blast furnace blades The challenge is to establish a method for refining reclaimed oil for mouth blowing.
【0004】本発明は、この課題に対し、鉱物質廃油を
回収し、1次蒸溜器にて高炉羽口吹込適正粘度を超える
重粘質油と、羽口吹き込み適正粘度以下の軽粘質油とに
分溜し、さらに重粘質油のうち高粘度油と低粘度油とに
区分してそれぞれ高粘度油蒸溜器と低粘度油蒸溜器との
2次蒸溜器においてそれぞれ再生油分と水分とに分溜
し、再生油分のpH値及び粘度値を調整し、凝集剤を含
む薬液を注入して汚泥を凝集沈澱処理し、再生油分は油
水分離機により、水分を分離除去し、分離した油分は羽
口吹込適正粒度を得る濾過機により濾過し、スラリーポ
ンプにより高炉羽口へ吹込み可能とした再生油製品を得
るための高炉羽口吹込用再生油精製方法を提供すること
を目的とする。To solve this problem, the present invention collects mineral waste oil, and in a primary distiller, a heavy viscous oil having a blast furnace tuyere blowing proper viscosity and a light viscous oil having a tuyere blowing proper viscosity or less. Further, the heavy oil is divided into high-viscosity oil and low-viscosity oil, and regenerated oil content and water content are respectively separated in the high-viscosity oil distiller and the low-viscosity oil distiller secondary distiller. The pH value and the viscosity value of the regenerated oil are adjusted, and the sludge is coagulated and precipitated by injecting a chemical solution containing a coagulant. The regenerated oil is separated and removed by an oil-water separator to separate the separated oil Aims to provide a regenerated oil refining method for blast furnace tuyere blowing to obtain a regenerated oil product that can be blown into a blast furnace tuyere by a slurry pump after filtering with a filter that obtains an appropriate particle size for tuyere blowing. .
【0005】[0005]
【課題を解決するための手段】上記目的を達成するため
に、本発明の方法においては、鉱物質廃油を回収し、水
分、引火点、比重、pH値及び粘度値の測定並びに成分
分析を含む受入品質検査を経て、1次蒸溜器にて高炉羽
口吹込適正粘度を超える重粘質油と、羽口吹き込み適正
粘度以下の軽粘質油とに分溜し、さらに重粘質油のうち
高粘度油と低粘度油とに区分してそれぞれ高粘度油蒸溜
器と低粘度油蒸溜器との2次蒸溜器においてそれぞれ再
生油分と水分とに分溜し、再生油分より試料を採取し、
水分、引火点、比重、pH値及び粘度値の測定並びに成
分分析を含む再生油品質検査を経て、pH値が6.0以
下のときはアミン(アンモニア系)pH調整剤を添加し
てpH値6.0ないし8.0に調整し、粘度値が羽口適
正動粘度値30cStを超えるときは上記軽粘質油を添
加して適正動粘度値に調整し、凝集剤を含む薬液を注入
して汚泥を凝集沈澱処理し、再生油分は油水分離機によ
り、水分を分離除去し、分離した油分は30メッシュ目
開き相当の羽口吹込適正粒度を得る濾過機により濾過
し、スラリーポンプにより高炉羽口へ吹込み可能として
いる。In order to achieve the above object, in the method of the present invention, the mineral waste oil is recovered, and water content, flash point, specific gravity, pH value and viscosity value measurement and component analysis are included. After receiving quality inspection, it was fractionated in the primary distiller into heavy viscous oil that exceeds the optimum viscosity of the blast furnace tuyere and light viscous oil that is less than the optimum viscosity of the tuyere injection. A high-viscosity oil and a low-viscosity oil are classified into two parts, a high-viscosity oil distiller and a low-viscosity oil distiller, and a secondary distiller of the low-viscosity oil distillate into a regenerated oil content and a water content, respectively, and a sample is taken from the regenerated oil content.
After the water quality, the flash point, the specific gravity, the measurement of the pH value and the viscosity value, and the recycled oil quality inspection including the component analysis, when the pH value is 6.0 or less, the amine (ammonia-based) pH adjusting agent is added to the pH value. Adjusted to 6.0 to 8.0, and when the viscosity value exceeds the tuyere proper kinematic viscosity value of 30 cSt, the above light viscous oil is added to adjust to the proper kinematic viscosity value, and a chemical solution containing a coagulant is injected. The sludge is coagulated and settled, the regenerated oil is separated and removed by an oil-water separator, and the separated oil is filtered by a filter to obtain a proper tuyere blowing particle size equivalent to 30 mesh openings. Can be blown into the mouth.
【0006】ここに、流量計を設けるときは楕円歯車等
の機械方式の代わりに超音波ドプラー方式や電磁流量計
等の非接触形流量計を設けることとする。When a flow meter is provided, a non-contact type flow meter such as an ultrasonic Doppler system or an electromagnetic flow meter is provided instead of a mechanical system such as an elliptical gear.
【0007】また、上記の2次蒸溜器及び油水分離機に
より分離した水を廃水処理し、薬液注入器により凝集剤
を含む薬液を注入して汚泥を凝集沈澱処理している。Further, the water separated by the secondary distiller and the oil / water separator is treated as waste water, and a chemical liquid containing a coagulant is injected by a chemical liquid injector to coagulate and settle sludge.
【0008】[0008]
【作用】上記の手段及び方法により、鉱物質廃油を回収
し、水分、引火点、比重、pH値及び粘度値の測定並び
に成分分析を含む受入品質検査を経て、1次蒸溜器にて
高炉羽口吹込適正動粘度値30cStを超える重粘質油
と、動粘度値30cSt以下の軽粘質油とに分溜し、さ
らに重粘質油のうち高粘度油と低粘度油とに区分してそ
れぞれ高粘度油蒸溜器と低粘度油蒸溜器との2次蒸溜器
においてそれぞれ再生油分と水分とに分溜し、再生油分
より試料を採取し、水分、引火点、比重、pH値及び粘
度値の測定並びに成分分析を含む再生油品質検査におけ
る検査の結果、pH値が6.0以下のときはアミン(ア
ンモニア系)pH調整剤を添加してpH値6.0ないし
8.0に調整し、粘度値が羽口吹込適正動粘度値30c
St超えるときは上記軽粘質油を添加して適正動粘度値
に調整し、薬液注入器により凝集剤を含む薬液を注入し
て汚泥を凝集沈澱処理し、再生油分は油水分離機によ
り、水分を分離除去し、分離した油分は夾雑物が介在し
ていても30メッシュ目開き相当の羽口吹込適正粒度を
得る濾過機により濾過してスラリーポンプにより高炉羽
口へ吹込むこととする。By the means and method described above, the mineral waste oil is recovered, and the quality of water, flash point, specific gravity, pH value and viscosity value are measured, and the quality of the received material is analyzed. It is divided into heavy viscous oil having a kinematic viscosity value of 30 cSt or more and light viscous oil having a kinematic viscosity value of 30 cSt or less, and further classified into high viscosity oil and low viscosity oil of the heavy viscosity oil. In the secondary distillers of the high-viscosity oil distiller and the low-viscosity oil distiller, respectively, the regenerated oil content and the water content are separately fractionated, and samples are taken from the regenerated oil content to obtain the water content, the flash point, the specific gravity, the pH value and the viscosity value. As a result of the inspection in the regenerated oil quality inspection including the measurement and the component analysis, when the pH value is 6.0 or less, an amine (ammonia type) pH adjusting agent is added to adjust the pH value to 6.0 to 8.0. , Viscosity value is 30c
When it exceeds St, the above-mentioned light viscous oil is added to adjust the kinematic viscosity to an appropriate value, and a chemical solution containing a coagulant is injected by a chemical solution injector to coagulate and settle sludge. The separated oil is separated and removed, and the separated oil is filtered by a filter to obtain an appropriate particle size of tuyere blowing corresponding to the opening of 30 meshes even if foreign matters are present, and then blown into the tuyere of the blast furnace by a slurry pump.
【0009】ここに、流量計として超音波ドプラー方式
や電磁流量計等の非接触形流量計を設けるときは、重粘
質油であっても、夾雑物を含んでいても、流量及び計量
精度に影響することなく計測される。When a non-contact type flow meter such as an ultrasonic Doppler system or an electromagnetic flow meter is installed as the flow meter, the flow rate and the measurement accuracy are high, even if the oil is heavy viscous oil or contains impurities. Is measured without affecting the.
【0010】また、上記の2次蒸溜器及び油水分離機に
より分離した水を廃水処理し、薬液注入器により凝集剤
を含む薬液を注入し、汚泥を凝集沈澱処理して廃油処理
が完結される。Further, the water separated by the secondary distiller and the oil / water separator is treated as waste water, and the chemical liquid containing the coagulant is injected by the chemical liquid injector, and the sludge is coagulated and sedimented to complete the waste oil treatment. .
【0011】[0011]
【実施例】実施例について図面を参照して説明すると、
図1において、鉱物質廃油1を回収し、水分、引火点、
比重、pH値及び粘度値の測定並びに成分分析を含む受
入品質検査2を経て、1次蒸溜器3にて高炉43の羽口
44吹込適正粘度を超える重粘質油(缶出液)9と、羽
口44吹き込み適正粘度以下の軽粘質油(溜出液)7と
に分溜し、さらに重粘質油9は高粘度油ライン12と低
粘度油ライン13とに区分してそれぞれ高粘度油蒸溜器
14と低粘度油蒸溜器15との2次蒸溜器において、そ
れぞれ高粘度再生油18,低粘度再生油19と水分2
0,20とに分溜し、高粘度再生油18,低粘度再生油
19を再生油槽21に受け、再生油より試料22を採取
し、水分、引火点、比重、pH測定器32によるpH値
及び粘度測定器30による粘度値測定並びに成分分析を
含む再生油品質検査29の結果により、pH値が6.0
以下のときはアミン(アンモニア系)pH調整剤33を
添加してpH値6.0ないし8.0に調整し、粘度値3
0が羽口44の吹込適正動粘度値30cStを超えると
きは上記軽粘質油7を同油ライン11より添加して適正
動粘度値30cStに調整し、薬液注入器34により凝
集剤を含む薬液35を注入して汚泥を凝集沈澱処理し、
同再生油槽21の水分を含む再生油23を油水分離機2
4により、油分25と水分26とに分離し、分離した油
分25は30メッシュ目開き相当の羽口吹込適正粒度を
得る濾過機27により濾過し、スラリーポンプ41によ
り高炉43の羽口44へ吹込み可能とした再生油製品4
0を得ることを特徴とする高炉羽口吹込用再生油精製方
法を提供する。EXAMPLES Examples will be described with reference to the drawings.
In FIG. 1, the waste mineral oil 1 is collected, and the water content, the flash point,
After the acceptance quality inspection 2 including the measurement of the specific gravity, pH value and viscosity value and the component analysis, the heavy distillate oil (canned liquid) 9 in the primary distiller 3 which exceeds the proper viscosity of the tuyere 44 of the blast furnace 43 is blown. , The tuyere 44 is sprayed into a light viscous oil (distillate) 7 having an appropriate viscosity or less, and the heavy viscous oil 9 is divided into a high viscosity oil line 12 and a low viscosity oil line 13, In a secondary distiller consisting of a viscous oil distiller 14 and a low viscosity oil distiller 15, a high viscosity reclaimed oil 18, a low viscosity reclaimed oil 19 and a water content 2 respectively.
0 and 20 are fractionated, high-viscosity reclaimed oil 18 and low-viscosity reclaimed oil 19 are received in a reclaimed oil tank 21, a sample 22 is collected from the reclaimed oil, and the water content, the flash point, the specific gravity, and the pH value measured by a pH measuring device 32. According to the results of the regenerated oil quality inspection 29 including the measurement of the viscosity value by the viscosity meter 30 and the component analysis, the pH value was 6.0.
In the following cases, an amine (ammonia-based) pH adjuster 33 is added to adjust the pH value to 6.0 to 8.0, and the viscosity value 3
When 0 exceeds the proper kinematic viscosity value of 30 cSt blown into the tuyere 44, the light viscous oil 7 is added from the oil line 11 to adjust the kinematic viscosity value to 30 cSt, and the chemical liquid injector 34 is used to adjust the chemical liquid containing the coagulant. 35 to inject sludge for coagulation and sedimentation,
The reclaimed oil 23 containing water in the reclaimed oil tank 21 is transferred to the oil / water separator 2
4, the oil content 25 and the water content 26 are separated, and the separated oil content 25 is filtered by a filter 27 which obtains an appropriate particle size of tuyere blowing corresponding to the opening of 30 mesh, and is blown to the tuyere 44 of the blast furnace 43 by the slurry pump 41. Recycled oil products that can be included 4
A refining oil refining method for blast furnace tuyere injection is provided which is characterized by obtaining 0.
【0012】[0012]
【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。Since the present invention is configured as described above, it has the following effects.
【0013】鉱物質廃油を高炉燃料の羽口吹込に供する
再利用可能な原料として、計画的に回収作業を行うの
で、産業廃棄物として廃油処理を行う必要がない。Since the waste material of mineral matter is systematically recovered as a reusable raw material for the tuyere injection of blast furnace fuel, it is not necessary to treat waste oil as industrial waste.
【0014】また、1次蒸溜器において重粘質油のほか
に軽粘質油が得られ、重粘質油は本発明の方法で処理
し、高炉羽口への吹込ができるが、軽粘質油は従来技術
による既設液体燃料制御供給装置により、高炉羽口への
吹込ができるほか、前記の再生油分の動粘度測定値が3
0cStを超過するときに再生油分に添加して粘度を低
下することができる。In addition to the heavy viscous oil, a light viscous oil is obtained in the primary distiller, and the heavy viscous oil can be treated by the method of the present invention and blown into the tuyere of the blast furnace, The quality oil can be blown into the tuyere of the blast furnace by the existing liquid fuel control and supply device according to the prior art, and the measured kinematic viscosity of the regenerated oil is 3
When it exceeds 0 cSt, it can be added to the regenerated oil to reduce the viscosity.
【0015】また、2次蒸溜器は、粘度を異にする種類
の油を高粘度油蒸溜器と低粘度油蒸溜器とに区別して処
理するので、それぞれ油種に応じて蒸溜温度及び制御目
標値を設定しておけば工程の制御が容易で効率よく作業
を行うことができる。Further, since the secondary distiller processes the oils of different kinds of viscosity into the high-viscosity oil distiller and the low-viscosity oil distiller separately, the distilling temperature and the control target are respectively set according to the oil type. If a value is set, the process can be controlled easily and work can be performed efficiently.
【0016】また、再生油分より試料を採取し、水分、
引火点、比重、pH値及び粘度値の測定並びに成分分析
を含む再生油品質検査の結果により、pH値が6.0以
下のときはアミン(アンモニア系)pH調整剤を添加し
てpH値6.0ないし8.0に調整し、粘度測定値が羽
口吹込適正動粘度値30cStを超えるときは上記軽粘
質油を添加して適正動粘度値30cStに調整し、凝集
剤を含む薬液を注入して汚泥を凝集沈澱処理するので、
所望の安定した再生油の品質が得られる。Further, a sample is taken from the regenerated oil, and water,
According to the results of regenerated oil quality inspection including measurement of flash point, specific gravity, pH value and viscosity value, and component analysis, when the pH value is 6.0 or less, an amine (ammonia-based) pH adjusting agent is added to adjust the pH value to 6 When adjusted to 0.0 to 8.0, and the measured viscosity value exceeds the tuyere blowing proper kinematic viscosity value of 30 cSt, the above light viscous oil is added to regulate the kinematic viscosity value of 30 cSt to prepare a chemical solution containing a coagulant. Since it is injected and sludge is coagulated and settled,
The desired stable regenerated oil quality is obtained.
【0017】さらに、水分を含む再生油分を油水分離機
により、水分を分離除去し、再生油分を濾過機により濾
過して羽口吹込適正粒度としてスラリーポンプにより高
炉羽口へ支障なく吹込むことができる。Further, the regenerated oil containing water is separated and removed by an oil-water separator, the regenerated oil is filtered by a filter, and the tuyere can be blown to the tuyere of the blast furnace by a slurry pump as a proper particle size. it can.
【0018】なお、本発明の方法により得られる再生油
は、上記のように、単独に高炉の燃料とするだけでな
く、ミルスケール、含油スケール、研削鉄粉等の産業廃
棄物を豊富な粉粒状鉄原料として、再生油と混和してス
ラリー状となし、高炉の羽口から吹込み給装するための
原料媒体に供することができる。The regenerated oil obtained by the method of the present invention is not only used as a fuel for the blast furnace alone as described above, but is also rich in industrial waste such as mill scale, oil impregnated scale, and ground iron powder. As a granular iron raw material, it can be mixed with regenerated oil to form a slurry, and can be used as a raw material medium for blowing and feeding from tuyere of a blast furnace.
【図1】図1は本発明の実施例を示すフロー図である。FIG. 1 is a flow chart showing an embodiment of the present invention.
1 鉱物質廃油 2 受入品質検査 3 1次蒸溜器 7 軽粘質油(溜出液) 8 スチル 9 重粘質油(缶出液) 11 軽粘質油ライン 12 高粘度油ライン 13 低粘度油ライン 14 高粘度油蒸溜器 15 低粘度油蒸溜器 18 高粘度油 19 低粘度油 20 水 21 再生油槽 22 再生油試料 23 水分を含む再生油 24 油水分離機 25 油分 26 水分 27 濾過器 29 再生油品質検査 30 粘度測定器 32 pH測定器 33 pH調整剤 34 薬液注入器 35 薬液 36 制御弁 40 再生油製品 41 スラリーポンプ 42 非接触形流量計 43 高炉 44 羽口 1 Mineral waste oil 2 Acceptance quality inspection 3 Primary distiller 7 Light viscous oil (distillate) 8 Still 9 Heavy viscous oil (canned liquid) 11 Light viscous oil line 12 High viscosity oil line 13 Low viscosity oil Line 14 High-viscosity oil distiller 15 Low-viscosity oil distiller 18 High-viscosity oil 19 Low-viscosity oil 20 Water 21 Reclaimed oil tank 22 Reclaimed oil sample 23 Reclaimed oil containing water 24 Oil-water separator 25 Oil content 26 Moisture 27 Filter 29 Reclaimed oil Quality inspection 30 Viscosity meter 32 pH meter 33 pH adjuster 34 Chemical solution injector 35 Chemical solution 36 Control valve 40 Recycled oil product 41 Slurry pump 42 Non-contact type flow meter 43 Blast furnace 44 Tuyer
Claims (1)
重、pH値及び粘度値の測定並びに成分分析を含む受入
品質検査を経て、1次蒸溜器にて高炉羽口吹込適正粘度
を超える重粘質油と、羽口吹き込み適正粘度以下の軽粘
質油とに分溜し、さらに重粘質油のうち高粘度油と低粘
度油とに区分してそれぞれ高粘度油蒸溜器と低粘度油蒸
溜器との2次蒸溜器においてそれぞれ再生油分と水分と
に分溜し、再生油分より試料を採取し、水分、引火点、
比重、pH値及び粘度値の測定並びに成分分析を含む再
生油品質検査により、pH値は、必要に応じ、pH調整
剤を添加して羽口吹込適正pH値に調整し、粘度値は羽
口吹込適正粘度を超えるときは上記軽粘質油を添加して
羽口吹込適正粘度値に調整し、凝集剤を含む薬液を注入
して汚泥を凝集沈澱処理し、再生油分は油水分離機によ
り水分を分離除去し、分離した油分は羽口吹込適正粒度
を得る濾過機により濾過し、スラリーポンプにより高炉
羽口へ吹込み可能とした再生油製品を得ることを特徴と
する高炉羽口吹込用再生油精製方法1. The waste mineral oil is recovered and subjected to an acceptance quality inspection including measurement of water content, flash point, specific gravity, pH value and viscosity value, and component analysis, and then subjected to a blast furnace tuyere proper viscosity in a primary distiller. Over viscous oil and light viscous oil with proper viscosity less than the tuyere blowing, fractionated and further divided into high viscosity oil and low viscosity oil among heavy viscous oils and high viscosity oil distillers, respectively. In the low-viscosity oil distiller and the secondary distiller, the regenerated oil content and the water content are respectively fractionated, and samples are taken from the regenerated oil content, the water content, the flash point,
By regenerated oil quality inspection including measurement of specific gravity, pH value and viscosity value, and component analysis, the pH value is adjusted to the proper tuyere blowing pH value by adding a pH adjusting agent as necessary, and the viscosity value is the tuyere. When it exceeds the appropriate blowing viscosity, the above-mentioned light viscous oil is added to adjust it to the appropriate value for the tuyere blowing, and a chemical solution containing a flocculant is injected to coagulate and settle the sludge. The separated oil component is separated and filtered, and the separated oil is filtered by a filter to obtain the proper particle size for tuyere blowing, and a reclaimed oil product that can be blown into the tuyere of the blast furnace by a slurry pump is obtained. Oil refining method
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26924894A JPH0892569A (en) | 1994-09-26 | 1994-09-26 | Purification of regenerated oil for injecting into tuyere of blast furnace |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP26924894A JPH0892569A (en) | 1994-09-26 | 1994-09-26 | Purification of regenerated oil for injecting into tuyere of blast furnace |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0892569A true JPH0892569A (en) | 1996-04-09 |
Family
ID=17469714
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP26924894A Pending JPH0892569A (en) | 1994-09-26 | 1994-09-26 | Purification of regenerated oil for injecting into tuyere of blast furnace |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0892569A (en) |
-
1994
- 1994-09-26 JP JP26924894A patent/JPH0892569A/en active Pending
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