WO2017051586A1 - Aluminum chip melting apparatus and melting method - Google Patents

Aluminum chip melting apparatus and melting method Download PDF

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Publication number
WO2017051586A1
WO2017051586A1 PCT/JP2016/069969 JP2016069969W WO2017051586A1 WO 2017051586 A1 WO2017051586 A1 WO 2017051586A1 JP 2016069969 W JP2016069969 W JP 2016069969W WO 2017051586 A1 WO2017051586 A1 WO 2017051586A1
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WO
WIPO (PCT)
Prior art keywords
aluminum
melting
oil
chips
melting furnace
Prior art date
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PCT/JP2016/069969
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French (fr)
Japanese (ja)
Inventor
秀昭 楢原
俊治 岩崎
洋二 青木
峻輔 蒔田
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株式会社広築
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Application filed by 株式会社広築 filed Critical 株式会社広築
Priority to JP2017541453A priority Critical patent/JP6452182B2/en
Publication of WO2017051586A1 publication Critical patent/WO2017051586A1/en

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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/027Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27BFURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B14/00Crucible or pot furnaces
    • F27B14/08Details peculiar to crucible or pot furnaces
    • F27B14/14Arrangements of heating devices
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/08Screw feeders; Screw dischargers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D7/00Forming, maintaining, or circulating atmospheres in heating chambers
    • F27D7/02Supplying steam, vapour, gases, or liquids
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D7/00Forming, maintaining, or circulating atmospheres in heating chambers
    • F27D7/06Forming or maintaining special atmospheres or vacuum within heating chambers
    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling
    • 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
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Definitions

  • the present invention relates to an aluminum chip melting apparatus and a melting method, and in particular, in obtaining a molten aluminum by melting chips that are cutting scraps of aluminum metal or alloy, pay attention to environmental protection, and provide safe and energy-saving operation.
  • the present invention relates to an aluminum chip melting apparatus and a melting method that can be achieved.
  • Aluminum metal requires a large amount of power for its production, so its production cost is high. Therefore, as long as scrap and scrap generated when processing into an aluminum product take the form of aluminum metal, the value is great in consideration of the manufacturing cost. Therefore, it is usual to recycle and melt aluminum scraps, cans and the like to obtain molten aluminum, and then to make aluminum products, and aluminum metal cutting scraps, so-called aluminum chips, are similarly treated.
  • This equipment is good in that aluminum chips can be reused, but the equipment requires a large variety of equipment, etc., and when it is dried and calcined, it is used in dust collectors and ducts with aluminum dust generated from the rotary kiln. There were problems such as the risk of ignition and explosion.
  • return materials, cans, and briquettes containing chips such as aluminum are indirectly heated in the preheating tower using the combustion exhaust gas from the melting and holding furnace to burn off the oil, etc.
  • Prior art for charging to obtain molten metal is disclosed.
  • the above prior art is excellent in that it is preheated so as not to oxidize the return material and briquette material containing chips by indirect heating, but the oil adhering to the material to be melted such as chips is heated and evaporated in the inner case. After that, it is said that it is possible to effectively suppress flue gas generation because it can be removed by entrapping and burning new air at the upper end of the preheating tower, but it is difficult to completely prevent flue gas generation, and oil etc. are retained There were problems such as not using latent heat energy.
  • An object of the present invention is to provide an aluminum chip melting apparatus and a melting method capable of saving energy and preventing air pollution by substituting fuel for gasification of oil in a melting furnace, inviting it to a heating burner of the melting furnace, and burning it. It is what.
  • an aluminum chip melting apparatus comprises a drying / preheating means for removing moisture in the cutting oil adhered to the aluminum chip, and the dried / preheated aluminum chip.
  • An oil gasification combustion means is provided.
  • the cutting oil used for producing aluminum products by cutting aluminum an emulsion obtained by diluting water-soluble cutting oil with water is often used. Therefore, since the aluminum chips that are cutting scraps are accompanied by 10 to 20 wt% of cutting oil with respect to the oil-containing chips, a mixture of oil and water is attached. The breakdown is 5 to 15 wt% of oil and 1 to 5 wt% of water.
  • moisture is removed by heating and evaporation from the cutting oil accompanying the aluminum swarf, and only the oil is left and then charged into a melting furnace to obtain a molten aluminum.
  • the oil can be gasified and combusted as a partial substitute fuel for the heating burner of the melting furnace. As a result, it is possible to recover aluminum as a fuel for the melting furnace without recovering resources from the aluminum chips and gasifying the accompanying cutting oil to cause pollution such as air pollution.
  • the aluminum chip melting apparatus according to claim 2 is the aluminum chip melting apparatus according to claim 1, wherein the drying / preheating means conveys the aluminum chip by a drying / preheating screw conveyor in which the aluminum chips are sealed, The aluminum chips are dried and preheated by heating the outer peripheral wall of the screw conveyor while adjusting the temperature of the combustion exhaust gas from the crucible melting furnace.
  • an aluminum chip melting apparatus is the aluminum chip melting apparatus according to claim 1 or 2, wherein the crucible melting furnace is provided with a refractory partition wall in the depth direction of the molten metal pool.
  • the molten metal part is divided into a molten part and a molten part, and further provided with a refractory filter over the entire horizontal cross section below the molten surface of the molten part, and the dried and preheated aluminum chips are It is charged into the molten metal at the lower part of the filter by charging means, and the aluminum chips are melted, and the oil component derived from the cutting oil accompanying the aluminum chips is gasified and the oil gas is taken out from the upper surface of the melting part.
  • the combustion burner is used for combustion.
  • the aluminum chips accompanying the oil are forcibly inserted into the lower part of the filter of the melting part, and the upward movement of the aluminum chips is suppressed by the filter. Then, the molten aluminum passes under the partition wall and moves to the molten metal part, and finally is discharged from the tapping tank.
  • the partition wall prevents the molten metal from short-circuiting and takes a long residence time.
  • the slag component which is an impurity, can be floated and separated, and the molten metal is sufficiently cleaned.
  • the oil is easily gasified because the oil-containing chips are sufficiently heated under the filter, floats through the filter, moves to the space above the melt, and then has a venturi effect on the combustion burner. Attracted and burned to replace the fuel, contributing to energy savings as well as saving fuel from melting aluminum.
  • An aluminum chip melting apparatus is the aluminum chip melting apparatus according to claim 3, wherein the melting part of the crucible melting furnace removes the dried and preheated aluminum chips in the lower part of the filter.
  • a stirrer that rotates in proximity to the charging means that is charged into the molten metal and a stirrer capable of injecting an inert gas of nitrogen or argon from the rotating shaft is provided, and the stirrer promotes dissolution of the aluminum chips. It is characterized by that.
  • the aluminum chips charged by the charging means are forcibly stirred and dispersed over a wide range with a stirring blade, and the aluminum chips are dissolved and oil content by finely diffusing the aluminum chips by inert gas injection. Gasification can be promoted.
  • An aluminum chip melting apparatus is the aluminum chip melting apparatus according to any one of claims 1 to 4, wherein the charging means is configured so that a discharge end of the drying / preheating screw conveyor is at an upper portion.
  • a connection opening is formed in the upper part of a closed charging hopper provided with a steam discharge valve, and a vertical or inclined charging screw conveyor is provided below the melting part filter of the crucible melting furnace from the lower part of the charging hopper. It is provided so that the lower end is immersed, and the dried and preheated aluminum chips are put into the molten metal by the charging screw conveyor and the inert gas of nitrogen or argon gas from the charging screw conveyor rotary shaft tube. It is characterized by charging in.
  • An aluminum chip melting apparatus is the aluminum chip melting apparatus according to any one of claims 1 to 4, wherein the charging means is configured such that the discharge end of the hermetic screw conveyor is steamed upward.
  • a connection opening is made in the upper part of the closed charging hopper provided with a discharge valve, and an inclined pusher is immersed from the lower part of the charging hopper below the melting part filter of the crucible melting furnace. The dried and preheated aluminum chips are charged into the molten metal by the pusher.
  • the aluminum chips can be forcibly charged into the melting furnace without being greatly affected by properties such as the particle size of the aluminum chips.
  • the charging amount is easily adjusted by the frequency of inserting the pusher, it is easy to control the dissolution amount of the chips.
  • An aluminum chip melting apparatus is the aluminum chip melting apparatus according to any one of claims 1 to 6, wherein the oil gasification combustion means includes a melting section and a molten metal of the crucible melting furnace.
  • the oil gasification combustion means includes a melting section and a molten metal of the crucible melting furnace.
  • a pipe connected to the combustion part of the combustion burner from the upper space of the part, and a venturi part connected to the combustion part at the end of the pipe, and the dried and preheated aluminum chips in the melting part of the melting furnace.
  • the oily gas generated during melting is collected and attracted to the combustion burner of the melting furnace for burning.
  • the oil content in the cutting oil accompanying the aluminum chips is gasified and recovered in the melting part of the melting furnace, and is sent to the combustion burner part via the venturi part by piping (duct). It burns with the flame of a combustion burner. This produces the effect of substituting the fuel for the combustion burner.
  • An aluminum chip melting apparatus is the aluminum chip melting apparatus according to any one of claims 1 to 7, wherein the drying / preheating means has a temperature at which the aluminum chip is dried / preheated.
  • the temperature range is from 125 ° C to 145 ° C, preferably 135 ° C.
  • the aluminum chips of the present invention are accompanied by an oil component derived from cutting oil.
  • this cutting oil is in an emulsion state of oil and water, and the amount thereof is in the range of 5 to 15 wt% for oil and 1 to 5 wt% for water with respect to the cutting oil containing cutting oil.
  • thermogravimetric-differential thermal analysis TG-DTA analysis
  • the oil content remains by setting the drying / preheating temperature of the aluminum chips accompanying the cutting oil in the range of 135 ⁇ 10 ° C., preferably 135 ° C. ,
  • the moisture can be evaporated, the melting of the aluminum chips in the melting furnace and the gasification of the oil can be carried out while maintaining the high temperature in the melting furnace, and the hydrogen content of the molten aluminum can be reduced. .
  • an aluminum chip melting apparatus is the aluminum chip melting apparatus according to any one of claims 1 to 8, wherein the drying / preheating means includes moisture in the aluminum chip after drying / preheating. Is 5% or less, preferably 1% or less.
  • the amount of water remaining in the charged aluminum chips is reduced, so the melting capacity is reduced without causing a temperature drop in the molten metal. It can be maintained and improved efficiently.
  • the amount of aluminum chips charged in the melting furnace and the gasification of oil can be more efficiently improved when the water content of the charged aluminum chips is 1% or less.
  • An aluminum chip dissolving apparatus is the aluminum chip dissolving apparatus according to any one of claims 1 to 9, wherein a centrifugal oil-water separator is provided upstream of the aluminum chip dissolving apparatus.
  • a pretreatment for reducing the amount of cutting oil adhering to the aluminum chips is performed by an oil / water separator.
  • the cutting oil can be physically separated by a centrifugal oil / water separator and its content can be easily reduced, and then there is a margin in the ability to heat and dehydrate with a screw conveyor that is a drying / preheating means.
  • a centrifugal oil / water separator it is possible to mainly reduce the moisture in the cutting oil adhering to the aluminum chips and efficiently preheat the chips. Therefore, by adding this centrifugal oil water separator to the aluminum chip dissolving device, the melting capacity of aluminum chips accompanied with cutting oil is improved, or the dissolution of aluminum chips accompanied by excess cutting oil Processing can be enabled.
  • the aluminum chip melting method according to claim 11 is a method of melting the aluminum chip to which cutting oil is adhered, and the aluminum chip is in the range of 125 ° C. to 145 ° C., preferably 135 ° C.
  • the crucible is dried and preheated by indirect heating using the exhaust gas of the crucible melting furnace to evaporate and remove moisture in the cutting oil, and then the dried and preheated aluminum chips are heated with a combustion burner.
  • the oil content in the cutting oil is gasified, and the gas is supplemented and used as fuel for indirect heating of the crucible melting furnace.
  • the molten aluminum is characterized in that only the molten metal is transferred from the melting part to the molten metal part of the crucible melting furnace to obtain a clean molten aluminum.
  • the method of the present invention is an aluminum chip melting method suitable for resource saving and energy saving.
  • the accompanying oil content of aluminum chips can be gasified in a high-temperature melting furnace and recovered as fuel in a closed circuit, so there is a risk of causing pollution such as air pollution compared to conventional methods in which oil is simply burned. It also contributes to the reduction of dissolved fuel.
  • the method for melting aluminum chips according to claim 12 is the method for melting aluminum chips according to claim 11, wherein the dried and preheated aluminum chips are charged into molten aluminum in the melting part of the crucible melting furnace. When dissolved, the mixture is stirred and mixed by a mechanical stirrer or inert gas injection to promote dissolution and oil gasification.
  • the aluminum chips charged in the melting part are forcibly stirred and dispersed over a wide range, and the aluminum chips are finely diffused by inert gas injection to dissolve the aluminum chips and gasify the oil. Can be promoted.
  • a high-quality aluminum melt can be obtained using aluminum chips accompanied by cutting oil as a raw material, and the cutting By efficiently gasifying the oil content of the oil in a closed circuit, a part of the fuel of the melting burner can be replaced. As a result, it is possible to replace dissolved fuel by recovering aluminum resources from the aluminum chips and recovering the energy stored in the associated oil, thereby contributing to resource utilization and energy saving.
  • this aluminum chip melting device is composed of equipment that has been used in a compact manner, has a smaller installation area than conventional ones, and does not require significant equipment costs. Also excellent equipment.
  • FIG. 1 is a schematic front sectional view of an aluminum chip melting apparatus according to an embodiment for carrying out the present invention.
  • FIG. 2 is a schematic side cross-sectional view in FIG.
  • FIG. 3 is a schematic cross-sectional view of a flue gas system connected to the drying / preheating device in FIG. 4 is a schematic cross-sectional view taken along the line AA in FIG.
  • FIG. 5 is a schematic front sectional view of an aluminum chip melting apparatus according to another embodiment for carrying out the present invention.
  • FIG. 6 is a schematic front sectional view of an aluminum chip melting apparatus according to another embodiment for carrying out the present invention.
  • FIG. 7 is a schematic cross-sectional view of a flue gas system connected to the drying / preheating device in FIG. 5 or FIG. FIG.
  • thermogravimetric-differential thermal analysis chart of the cutting oil for aluminum It is a figure which shows the effect of the nitrogen gas injection in aluminum chip melt
  • drying and preheating step (b) of the aluminum chips accompanied with cutting oil drying and preheating step (b) of the aluminum chips accompanied with cutting oil, charging step (c) of charging the dried and preheated aluminum chips into the melting furnace, and in the melting furnace holding the molten aluminum heated, It comprises a melting step (d) in which chips are charged and melted, and an oil gasification combustion step (e) in which oil gas obtained by gasifying oil in an aluminum melting furnace is burned in a melting furnace combustion burner.
  • An aluminum chip melting apparatus 1 will be described with reference to FIGS.
  • the aluminum chip melting apparatus 1 is equipped with a drying / preheating device 4 that removes moisture in the cutting oil adhered to the aluminum chip, and the dried / preheated aluminum chip is charged into the molten metal M of the crucible melting furnace 2.
  • a centrifugal oil / water separator (not shown) is provided in the preceding stage of the aluminum chip melting apparatus 1 to perform pretreatment to reduce the amount of cutting oil adhering to the aluminum chip, that is, the amount of excess oil moisture. .
  • this pretreatment means the excess oil and water content in the cutting oil adhered to the aluminum chips can be easily reduced without physical heating with a centrifugal oil / water separator, and then the aluminum chip melting apparatus 1 is dried and preheated. Since it can be further heated and dehydrated by the screw conveyor 4-2 as a means, the moisture in the cutting oil adhering to the aluminum chips can be efficiently reduced and preheated. Further, according to this apparatus, it is not necessary to use heat energy such as heating in the deoiled water, so there is no concern about air pollution associated therewith.
  • the aluminum swarf according to the present invention is mainly composed of cutting waste generated when an aluminum product is manufactured by cutting aluminum or an aluminum alloy. Therefore, the aluminum chips are accompanied by 10 to 20 wt% of the cutting oil with respect to the cutting oil containing chips 100, and normally, the cutting oil is an emulsion of oil and water, so that the amount of 5 to 15 wt% is used. A mixture of oil and 1-5 wt% water is adhered.
  • the aluminum chip melting apparatus 1 of the present invention removes moisture by heating and evaporating from the cutting oil associated with the aluminum chip, leaving only the oil content, and then charging it into the melting furnace 2 to melt the aluminum melt M.
  • the oil is gasified and combusted as a partial alternative fuel for the heating burner 6 of the melting furnace 2.
  • the oil is gasified and combusted as a partial alternative fuel for the heating burner 6 of the melting furnace 2.
  • the drying / preheating device 4 in the aluminum chip melting apparatus 1 is a drying / preheating screw conveyor 4-2 in which aluminum chips are rotated from a charging hopper 4-1 by a variable speed drive geared motor 4-2e.
  • the screw conveyor 4-2 is inserted into the drying / preheating chamber 4-3, and the screw conveyor outer cylinder 4-2b is passed through the combustion exhaust gas duct 8 from the crucible melting furnace 2.
  • the aluminum chips are dried and preheated by adjusting the temperature with the cold air from the dilution air inlet 8-1 and introducing it into the drying / preheating chamber 4-3 and heating.
  • the flow rate and temperature of the drying / preheating gas are determined by the values of the indoor pressure gauge 4-3d and the thermometer 4-3c provided in the drying / preheating chamber 4-3, and the damper and combustion exhaust gas at the dilution air inlet 8-1.
  • the degree of opening / closing of the damper 8-2 of the duct 8 can be adjusted.
  • the temperature for drying and preheating the aluminum chips is in the range of 125 ° C. to 145 ° C., preferably 135 ° C.
  • aluminum chips are accompanied by oil and moisture derived from cutting oil. Therefore, in the present invention, cutting oil used for the purpose of evaporating moisture by heating and leaving the oil (trade name: cedar cut) Thermogravimetric-differential thermal analysis (TG-DTA analysis) of CS-68DN-2) was performed. As a result, as shown in FIG. 9, it was found that moisture was removed by heating up to around 135 ° C., and the oil was oxidized and generated heat in the region of 200 to 500 ° C.
  • the drying / preheating temperature of the aluminum chips is in the range of 135 ⁇ 10 ° C., preferably 135 ° C.
  • the oil remains and the water can be removed in an evaporated state.
  • the melting furnace 2 can maintain a high temperature without lowering the melting temperature, and the hydrogen content of the molten aluminum M can be reduced. It leads to reduction.
  • the crucible type melting furnace 2 of the aluminum chip melting apparatus 1 has a melting furnace combustion chamber 7 surrounded by a furnace wall refractory 7-1 and a furnace lid refractory 7-2. It is installed on the furnace mounting table 2-5.
  • the melting furnace combustion burner 6 is provided at a corner near the bottom of the melting furnace combustion chamber 7, and the combustion exhaust gas outlet is located above the melting furnace combustion chamber 7 as shown in FIGS. Since the axis is shifted, the flame of the combustion burner 6 heats the crucible melting furnace 2 as a swirling flow licking the outer wall of the crucible melting furnace 2 from bottom to top.
  • the crucible melting furnace 2 is mainly formed of a carbonaceous refractory in a bowl shape, holds an aluminum melt M having a melting point of about 660 ° C. inside, and a swirl flow flame from the bottom to the top of the melting furnace combustion burner 6. Therefore, the melting furnace 2 is indirectly heated by the combustion burner 6. Since the melting furnace combustion chamber 7, the furnace upper space 2-4, and the inside of the melting furnace 2 are isolated by the refractory of the melting furnace 2, the atmosphere state is completely different. Usually, the combustion chamber temperature of the melting furnace is in the range of 700 ° C to 1000 ° C.
  • the size of the crucible melting furnace 2 is about 600 mm in diameter and about 500 mm in height when the melting amount of aluminum chips is 50 to 100 kg / hr.
  • the crucible melting furnace 2 of the aluminum chip melting apparatus 1 is connected to the molten metal pan 3 by a refractory partition wall 2-2 in the depth direction of the molten metal M pool. 1 is divided into a melted portion 2-b and a melted portion 2-a, and further below the surface of the melted portion 2-a as shown in FIGS. A refractory filter 2-3 is provided over the entire horizontal cross section.
  • the dried and preheated aluminum chips are accompanied by an inert gas such as nitrogen or argon by the vertical or inclined charging screw conveyor 5-2 of the charging device 5 or the inclined pusher.
  • a stirring blade rotating in the vicinity of the charging means 5 for charging the dried and preheated aluminum chips into the molten metal M below the filter 2-3 a stirring blade rotating in the vicinity of the charging means 5 for charging the dried and preheated aluminum chips into the molten metal M below the filter 2-3.
  • a stirrer 3 including a 3-1 and a rotating shaft 3-3 is provided. Further, the stirrer 3 can inject an inert gas of nitrogen from the rotating shaft 3-3, and the aluminum chips charged by the stirrer 3 are forcibly dispersed with a stirring blade 3-1 over a wide range. At the same time, by finely diffusing the aluminum chips by inert gas injection, dissolution of the aluminum chips and gasification of the oil can be promoted.
  • FIG. 10 shows the result of confirming the effect of nitrogen (N 2 ) injection on the dissolution of the above-described aluminum chips in the molten aluminum M in an experimental furnace.
  • the aluminum chips chips having a water content of 1% or less and an oil content of 1.5 to 2% after drying were used.
  • the elapsed time after charging aluminum chips was 10 to 20 minutes, and the dissolved ratio (dissolution efficiency) was 50 to 65%.
  • a dissolution rate (dissolution efficiency) of 65 to 85% was obtained in 3 to 10 minutes after the charging. From these, by performing nitrogen (N 2) injection in the aluminum melt M, the dissolution of aluminum chips was confirmed the possibility of achieving in a short time efficiently.
  • the chip charging device 5 of the aluminum chip melting apparatus 1 is opened by connecting the discharge end 4-2d of the drying / preheating screw conveyor 4-2 to the upper part of the hermetic charging hopper 5-1.
  • a steam discharge valve 5-3 is provided in the upper lid portion of the charging hopper 5-1.
  • a vertical or inclined charging screw conveyor 5-2 that is rotationally driven by a variable speed drive geared motor 5-2d from the lower portion of the charging hopper 5-1 is a melting part filter of the crucible melting furnace 2. 2-4 is provided so that its lower end is immersed, and dried and preheated aluminum chips are charged into the molten metal M by the charging screw conveyor 5-2, and nitrogen, which is an inert gas, is used at that time.
  • the vertical charging screw conveyor is more susceptible to changes in the charging speed depending on the degree of aluminum chip filling compared to the inclined charging screw conveyor. Adjustment is easy.
  • an inclined pusher 5-4 can be provided in place of the vertical or inclined charging screw conveyor 5-2.
  • the inclined type pusher 5-4 is used for melting the crucible melting furnace 2 from the lower part of the charging hopper 5-1 to which the hermetic screw conveyor 4-2 is connected to the upper part of the hermetic charging hopper 5-1.
  • the lower end of the partial filter 2-3 is provided so that its lower end is immersed, and dried and preheated aluminum chips can be charged into the molten metal M by the pusher 5-4.
  • it is intermittent by this inclined type pusher 5-4 it becomes possible to forcibly insert aluminum chips into the molten metal M of the melting part 2-a of the melting furnace 2.
  • the inclined pusher 5-4 it is possible to forcibly charge the aluminum chips into the melting furnace 2 without being greatly affected by the properties such as the particle size of the aluminum chips. Further, it is preferable that the inclined pusher 5-4 is driven by an air-driven rodless cylinder 5-4a. Also, the pusher tip 5-4b of the inclined pusher 5-4 is cut obliquely so that the aluminum chips can be easily pushed into the molten metal M. Further, since the charging amount can be easily adjusted by the charging frequency of the pusher 5-4, it is easy to control the dissolution amount of the chips.
  • the oil gas that has been gasified in the melting furnace 2 of the aluminum chip melting apparatus 1 and accumulated in the furnace upper space 2-4 is recovered from the gas from the furnace upper space 2-4 to the combustion part of the combustion burner 6. Since the duct 9 is provided and the venturi section 9-1 connected to the combustion section is provided at the end of the oil gas recovery duct 9, the oil gas generated from the melting furnace 2 is attracted and guided, and the melting furnace combustion burner 6 Can be burned in a flame. Thereby, a partial replacement of the fuel for the melting furnace combustion burner 6 becomes possible.
  • the cutting oil containing aluminum cutting powder can select the pre-processing of a centrifugal oil-water separator according to the amount of cutting oil contained. Then, the aluminum chips accompanied with the cutting oil are dried and preheated by indirect heating to a range of 125 ° C. to 145 ° C., preferably 135 ° C., to evaporate and remove moisture in the cutting oil, and then the drying -The preheated aluminum chips are charged into the melting part 2-a of the crucible melting furnace 2 heated by the combustion burner 6 and melted, whereby the oil in the cutting oil is gasified and the gas is melted into the crucible.
  • the molten aluminum is used as a fuel for the combustion burner 6 of the furnace 2, and the molten aluminum is transferred only from the melting part 2-a of the crucible melting furnace 2 to the molten metal part 2-b to obtain a clean molten aluminum M It is get those.
  • the outer cylinder 4-2b of the drying / preheating screw conveyor 4-2 is heated with melting furnace combustion exhaust gas at a predetermined temperature, so that the conveying aluminum cutting of the screw conveyor 4-2 is performed.
  • the powder is accompanied by evaporation of moisture, while the oil is not evaporated, and the aluminum chips are preheated and sent to the charging hopper 5-1 of the next-stage chip charging apparatus 5.
  • the water vapor is discharged into the hopper space and passes through the steam discharge port 5-3. To the atmosphere.
  • the preheated aluminum chips containing oil are deposited in the charging hopper 5-1 and then charged into the melting furnace 2.
  • Aluminum chips accompanied by oil are conveyed in a filled state from a charging hopper 5-1 by a vertical or inclined screw conveyor 5-2, and are moved to the lower area of the filter 2-3 of the melting part 2-a of the melting furnace 2. Then, it is charged together with an inert gas ejected through the screw rotating shaft 5-2c. Further, the aluminum chips are bubbling of the inert gas injection and the diffusion of the stirrer 3 by the stirring of the stirrer blade 3-1 of the stirrer 3 and the injection of the nitrogen gas outlet 3-3 of the rotating shaft 3-2. As a result, the oil melts more quickly to become the molten metal M, and the oil is gasified.
  • the molten aluminum M passes under the partition wall 2-2 and moves to the molten metal part 2-b, and finally is discharged from the hot water tank 2-1.
  • the molten metal M is prevented from flowing due to a short circuit by the partition wall 2-2, and by taking a long residence time, the molten metal M is sufficiently cleaned by levitating and separating impurities such as slag components.
  • the oil component is heated in the region under the filter 2-2 under the bubbling of the inert gas to be gasified without being oxidized, passes through the filter 2-2, floats up, and passes through the furnace upper space 2-4.
  • the fuel is replaced by the fuel by being attracted by the venturi section 9-1 in the combustion zone of the combustion burner 6 via the oil gas recovery duct 9 and burned, thereby contributing to energy saving and fuel saving.
  • the aluminum chips accompanied with oil are intermittently forced from the charging hopper 5-1 by the inclined charging pusher 5-3 to filter the aluminum chips in the melting part 2-a of the melting furnace 2.
  • 2-3 Can be charged into the molten metal M in the lower area.
  • the charged aluminum chips are rapidly melted by diffusion by the stirring of the stirring blade 3-1 of the adjacent stirrer 3 and the injection of the nitrogen gas outlet 3-3 of the rotating shaft 3-2. As it becomes M, the oil is gasified.
  • the molten aluminum M passes under the partition wall 2-2 and moves to the molten metal part 2-b, and finally is discharged from the hot water tank 2-1.
  • the molten metal M is prevented from flowing due to a short circuit by the partition wall 2-2, and by taking a long residence time, the molten metal M is sufficiently cleaned by levitating and separating impurities such as slag components.
  • the oil component is heated in the region under the filter 2-2 under the bubbling of the inert gas to be gasified without being oxidized, passes through the filter 2-2, floats up, and passes through the furnace upper space 2-4.
  • the fuel is replaced by the fuel by being attracted by the venturi section 9-1 in the combustion zone of the combustion burner 6 via the oil gas recovery duct 9 and burned, thereby contributing to energy saving and fuel saving.
  • the cutting oil contained in the aluminum chips includes cutting oil mainly composed of oil that does not contain water, apart from the oil composed of the oil and water targeted by the present invention.
  • the aluminum chip melting apparatus and the melting method of the present invention can be sufficiently applied to aluminum chips containing cutting fluid having no moisture. In this case, there is no need for energy to evaporate water as much as it does not contain water, the preheating temperature of the aluminum chips themselves is likely to rise, the processing capacity of the aluminum chips by this device is easy to improve, and the heat required for melting It becomes easy to save energy.
  • the molten aluminum M can be obtained with high thermal efficiency by using the aluminum chips accompanied with the cutting oil as a raw material, evaporating the accompanying moisture, and dissolving the preheated aluminum chips.
  • the oil component is gasified and recovered in the melting furnace 2 and can be used as a substitute for the fuel in the melting furnace 2, the present invention is an aluminum chip melting apparatus and method suitable for resource saving and energy saving.

Abstract

The present invention provides an aluminum chip melting apparatus that melts chips, which are aluminum metal or alloy cuttings, to obtain molten aluminum. This aluminum chip melting apparatus is characterized by being provided with: a centrifugal oil-water separating apparatus that reduces oily water in the cutting oil adhering to aluminum chips; a drying/preheating means for eliminating water in the cutting oil adhering to the aluminum chips; a charging means for charging the dried/preheated aluminum chips into the molten metal in a crucible melting furnace; an aluminum melting means for melting the dried/preheated aluminum chips using the crucible melting furnace, and producing molten aluminum; and an oil gasification combustion means for gasifying the oil remaining in the dried/preheated aluminum chips using the crucible melting furnace, and burning the result with a combustion burner.

Description

アルミニウム切粉溶解装置及び溶解方法Aluminum chip melting apparatus and melting method
 本発明は、アルミニウム切粉溶解装置及び溶解方法に関し、詳しくはアルミニウム金属又は合金の切削屑である切粉を溶解してアルミニウム溶湯を得るにあたり、環境保全に留意し、安全で、かつ省エネルギー操業を達成できるアルミニウム切粉溶解装置及び溶解方法に関するものである。 The present invention relates to an aluminum chip melting apparatus and a melting method, and in particular, in obtaining a molten aluminum by melting chips that are cutting scraps of aluminum metal or alloy, pay attention to environmental protection, and provide safe and energy-saving operation. The present invention relates to an aluminum chip melting apparatus and a melting method that can be achieved.
 アルミニウム金属は、その製造の際に多大の電力を必要とするために、その製造原価は高い。よって、アルミニウム製品に加工する際に発生する屑、スクラップもアルミニウム金属の形態をとる限り、製造コストを考慮すると、その価値は大きい。従って、アルミニウム屑、缶などもリサイクルして溶解しアルミニウム溶湯を得、次いでアルミニウム製品を作るのが常で、アルミニウム金属の切削屑、いわゆるアルミニウム切粉も同様に処理される。 Aluminum metal requires a large amount of power for its production, so its production cost is high. Therefore, as long as scrap and scrap generated when processing into an aluminum product take the form of aluminum metal, the value is great in consideration of the manufacturing cost. Therefore, it is usual to recycle and melt aluminum scraps, cans and the like to obtain molten aluminum, and then to make aluminum products, and aluminum metal cutting scraps, so-called aluminum chips, are similarly treated.
 アルミニウム切粉は、再溶解してアルミニウムとしてリサイクルされるのが、省資源、省エネルギの観点で望ましい。そのために切粉を溶解する前に、切粉に付着している切削油を加熱蒸発させて除去するのが、溶解アルミニウムの品質上及び製造する際の発煙防止などの環境保全の観点から望ましい。その一例として、図12のフロー図に示すように、切削油等が残存したアルミニウム切粉をロータリキルンでアルミニウムが酸化しないように仮焼して油分・水分を揮発させることにより除去した後、アルミニウム切粉をアルミニウム溶解炉に装入してアルミニウム溶湯を得るものがある。また、揮発した油分は再燃炉で燃焼し集塵機を経て大気に放散している。本設備は、アルミニウム切粉を再利用する点でよいが、設備が多種多様の装置を要する等、大掛かりになり、また乾燥、仮焼する時に、ロータリキルンから発生したアルミニウム粉じんによる集塵機やダクトにおいて着火、爆発の危険性がある等の問題があった。 It is desirable from the viewpoint of resource saving and energy saving that aluminum chips are remelted and recycled as aluminum. For this reason, it is desirable from the viewpoint of environmental conservation such as the quality of the molten aluminum and the prevention of smoke generation during production that the cutting oil adhering to the chips is removed by heating and evaporation before the chips are dissolved. As an example, as shown in the flow chart of FIG. 12, aluminum chips after remaining cutting oil and the like are calcined in a rotary kiln so that the aluminum is not oxidized and removed by volatilizing oil and moisture, and then aluminum. There is one that obtains molten aluminum by charging chips into an aluminum melting furnace. The volatilized oil is burned in a reburning furnace and diffused to the atmosphere through a dust collector. This equipment is good in that aluminum chips can be reused, but the equipment requires a large variety of equipment, etc., and when it is dried and calcined, it is used in dust collectors and ducts with aluminum dust generated from the rotary kiln. There were problems such as the risk of ignition and explosion.
 また、前述とは別に、アルミニウム等切粉を含むリターン材や缶材やブリケット材を溶解保持炉の燃焼排ガスを用いて予熱タワーで間接加熱して油分等を燃焼除去した後、溶解保持炉に装入して溶湯を得る先行技術が開示されている。 In addition to the above, return materials, cans, and briquettes containing chips such as aluminum are indirectly heated in the preheating tower using the combustion exhaust gas from the melting and holding furnace to burn off the oil, etc. Prior art for charging to obtain molten metal is disclosed.
特開2005-121289公報(〔0006~0007〕、〔0013〕、〔図1〕)Japanese Patent Laying-Open No. 2005-121289 ([0006-0007], [0013], [FIG. 1])
 前記先行技術は、切粉を含むリターン材、ブリケット材を間接加熱して酸化させないように予熱する点で優れているが、切粉等被溶解材に付着した油分等をインナケースで加熱蒸発させた後、予熱タワー上端で新しい空気を巻き込んで燃焼させて除去できるから排煙発生を効果的に抑制できるとしているが、排煙発生を完全に防止することが難しく、また、油分等が保有する潜在熱エネルギを活用していない等の課題があった。 The above prior art is excellent in that it is preheated so as not to oxidize the return material and briquette material containing chips by indirect heating, but the oil adhering to the material to be melted such as chips is heated and evaporated in the inner case. After that, it is said that it is possible to effectively suppress flue gas generation because it can be removed by entrapping and burning new air at the upper end of the preheating tower, but it is difficult to completely prevent flue gas generation, and oil etc. are retained There were problems such as not using latent heat energy.
 本発明は、これらの課題を解決したものであって、切削油分を随伴するアルミニウム切粉を予備処理により油分だけを残し、次いで、アルミニウム溶解炉で溶解して良質なアルミニウム溶湯を得ると共に、該油分を溶解炉でガス化して溶解炉の加熱バーナに誘引して燃焼させて、燃料を代替補助することにより省エネルギと大気汚染防止が図れるアルミニウム切粉溶解装置及び溶解方法を提供することを目的とするものである。 The present invention solves these problems, leaving only the oil by pretreatment of the aluminum chips accompanying the cutting oil, and then melting it in an aluminum melting furnace to obtain a high-quality molten aluminum, An object of the present invention is to provide an aluminum chip melting apparatus and a melting method capable of saving energy and preventing air pollution by substituting fuel for gasification of oil in a melting furnace, inviting it to a heating burner of the melting furnace, and burning it. It is what.
上記の目的を達成するために、本発明の請求項1に係るアルミニウム切粉溶解装置は、アルミニウム切粉の付着切削油中の水分を除去する乾燥・予熱手段と、該乾燥・予熱したアルミニウム切粉をルツボ型溶解炉の溶湯中に装入する装入手段と、燃焼バーナにより間接加熱した該ルツボ型溶解炉を用いて該乾燥・予熱したアルミニウム切粉を溶解してアルミニウム溶湯を製造するアルミニウム溶解手段と、を備え、該乾燥・予熱したアルミニウム切粉中に残留させた油分を該ルツボ型溶解炉で該アルミニウム切粉を溶解した際にガス化させて該燃焼バーナへ誘引して燃焼させる油分ガス化燃焼手段を設けたことを特徴とする。 In order to achieve the above object, an aluminum chip melting apparatus according to claim 1 of the present invention comprises a drying / preheating means for removing moisture in the cutting oil adhered to the aluminum chip, and the dried / preheated aluminum chip. Aluminum for producing molten aluminum by melting the dry and preheated aluminum chips using charging means for charging the powder into the molten metal of the crucible melting furnace and the crucible melting furnace indirectly heated by a combustion burner Melting means, and when the aluminum chips are melted in the crucible melting furnace, the oil remaining in the dried and preheated aluminum chips is gasified and attracted to the combustion burner to be burned. An oil gasification combustion means is provided.
 アルミニウムを切削加工してアルミニウム製品を製造する際に用いられる切削油は、水溶性切削油を水で希釈したエマルジョンが用いられることが多い。よって、切削屑であるアルミニウム切粉は、含油切粉に対して10~20wt%の切削油を随伴しているから油と水の混合物が付着していることになる。その内訳は、油の含有率が5~15wt%、水が1~5wt%である。この請求項1の構成をとることにより、アルミニウム切粉に随伴している切削油から水分を加熱蒸発して除去し、油分のみを残留させてから溶解炉に装入して、アルミニウム溶湯を得ると共に、油分をガス化して溶解炉の加熱バーナーの一部代替燃料として燃焼させることができる。これによりアルミニウム切粉からアルミニウムを資源回収すると共に、随伴している切削油をガス化させて大気汚染などの公害を惹起することなく溶解炉の燃料としてのエネルギ回収が可能となる。 As the cutting oil used for producing aluminum products by cutting aluminum, an emulsion obtained by diluting water-soluble cutting oil with water is often used. Therefore, since the aluminum chips that are cutting scraps are accompanied by 10 to 20 wt% of cutting oil with respect to the oil-containing chips, a mixture of oil and water is attached. The breakdown is 5 to 15 wt% of oil and 1 to 5 wt% of water. By adopting the structure of the first aspect, moisture is removed by heating and evaporation from the cutting oil accompanying the aluminum swarf, and only the oil is left and then charged into a melting furnace to obtain a molten aluminum. At the same time, the oil can be gasified and combusted as a partial substitute fuel for the heating burner of the melting furnace. As a result, it is possible to recover aluminum as a fuel for the melting furnace without recovering resources from the aluminum chips and gasifying the accompanying cutting oil to cause pollution such as air pollution.
 また、請求項2に係るアルミニウム切粉溶解装置は、請求項1に記載のアルミニウム切粉溶解装置において、前記乾燥・予熱手段が、アルミニウム切粉を密閉した乾燥・予熱スクリュコンベヤで運搬すると共に、該スクリュコンベヤの外周壁を前記ルツボ型溶解炉からの燃焼排ガスを温度調整して加熱することにより該アルミニウム切粉を乾燥・予熱することを特徴とする。 In addition, the aluminum chip melting apparatus according to claim 2 is the aluminum chip melting apparatus according to claim 1, wherein the drying / preheating means conveys the aluminum chip by a drying / preheating screw conveyor in which the aluminum chips are sealed, The aluminum chips are dried and preheated by heating the outer peripheral wall of the screw conveyor while adjusting the temperature of the combustion exhaust gas from the crucible melting furnace.
この構成により、乾燥・予熱スクリュコンベヤの外周を所定温度の溶解炉燃焼排ガスで加熱することにより、該スクリュコンベヤ内部の搬送アルミニウム切粉は随伴する切削油中の水分が蒸発し、一方油分は蒸発していない状態で、アルミニウム切粉が予熱されて次工程の装入装置に送ることができる。 With this configuration, when the outer periphery of the drying / preheating screw conveyor is heated with the melting furnace combustion exhaust gas at a predetermined temperature, the transported aluminum chips inside the screw conveyor evaporate the water in the accompanying cutting oil, while the oil component evaporates. In the state which is not carried out, the aluminum chip is preheated and can be sent to the charging apparatus of the next process.
また、請求項3にアルミニウム切粉溶解装置は、請求項1又は2に記載のアルミニウム切粉溶解装置において、前記ルツボ型溶解炉が、溶湯溜りの深さ方向に耐火物製の隔壁により出湯樋に連なる溶湯部と、溶解部と、に区分けし、さらに該溶解部の溶湯面より下で水平方向の断面全体に亘って耐火物製のフィルタを備え、前記乾燥・予熱したアルミニウム切粉が前記装入手段により該フィルタ下部の溶湯中に装入して、該アルミニウム切粉を溶解すると共に、該アルミニウム切粉に随伴する切削油由来の油分をガス化して該溶解部上面から油分ガスを取り出して前記燃焼バーナの燃焼に供することを特徴とする。 Further, an aluminum chip melting apparatus according to claim 3 is the aluminum chip melting apparatus according to claim 1 or 2, wherein the crucible melting furnace is provided with a refractory partition wall in the depth direction of the molten metal pool. The molten metal part is divided into a molten part and a molten part, and further provided with a refractory filter over the entire horizontal cross section below the molten surface of the molten part, and the dried and preheated aluminum chips are It is charged into the molten metal at the lower part of the filter by charging means, and the aluminum chips are melted, and the oil component derived from the cutting oil accompanying the aluminum chips is gasified and the oil gas is taken out from the upper surface of the melting part. The combustion burner is used for combustion.
この構成により、油分を随伴したアルミニウム切粉は、溶解部のフィルタ下部域に強制的に装入され、フィルタにより上部への移動が抑制されると共に、アルミニウム切粉は拡散・溶解して溶湯になり、次いで、アルミニウム溶湯が隔壁の下を通過して溶湯部へ移動し、最終的には出湯樋から出湯されるが、隔壁により溶湯が短絡して流れるのを防止し、滞留時間を長くとることで、不純物であるスラグ成分などを浮上・分離することができて、溶湯は十分清浄化される。また、油分は、油分を含んだ切粉がフィルタ下で十分加熱されるので容易にガス化し、フィルタを通過して浮上し、溶湯上部の空間部に移動し、次いで燃焼バーナにベンチュリ効果でもって誘引されて燃焼することで燃料代替を果たし、アルミニウム溶解の燃料の節減と共に省エネルギに貢献する。 With this configuration, the aluminum chips accompanying the oil are forcibly inserted into the lower part of the filter of the melting part, and the upward movement of the aluminum chips is suppressed by the filter. Then, the molten aluminum passes under the partition wall and moves to the molten metal part, and finally is discharged from the tapping tank. The partition wall prevents the molten metal from short-circuiting and takes a long residence time. Thus, the slag component, which is an impurity, can be floated and separated, and the molten metal is sufficiently cleaned. The oil is easily gasified because the oil-containing chips are sufficiently heated under the filter, floats through the filter, moves to the space above the melt, and then has a venturi effect on the combustion burner. Attracted and burned to replace the fuel, contributing to energy savings as well as saving fuel from melting aluminum.
また、請求項4に係るアルミニウム切粉溶解装置は、請求項3に記載のアルミニウム切粉溶解装置において、前記ルツボ型溶解炉の溶解部が、前記乾燥・予熱したアルミニウム切粉を前記フィルタ下部の溶湯中に装入する前記装入手段に近接して、回転する攪拌翼と、回転軸から窒素又はアルゴンの不活性ガスをインジェクションできるスターラを備え、該スターラにより該アルミニウム切粉の溶解を促進させることを特徴とする。 An aluminum chip melting apparatus according to claim 4 is the aluminum chip melting apparatus according to claim 3, wherein the melting part of the crucible melting furnace removes the dried and preheated aluminum chips in the lower part of the filter. A stirrer that rotates in proximity to the charging means that is charged into the molten metal and a stirrer capable of injecting an inert gas of nitrogen or argon from the rotating shaft is provided, and the stirrer promotes dissolution of the aluminum chips. It is characterized by that.
この構成により、装入手段で装入されたアルミニウム切粉を強制的に攪拌翼で広範囲に攪拌分散すると共に、不活性ガスインジェクションによりアルミニウム切粉を細かく拡散することによりアルミニウム切粉の溶解、油分のガス化を促進することができる。 With this configuration, the aluminum chips charged by the charging means are forcibly stirred and dispersed over a wide range with a stirring blade, and the aluminum chips are dissolved and oil content by finely diffusing the aluminum chips by inert gas injection. Gasification can be promoted.
また、請求項5に係るアルミニウム切粉溶解装置は、請求項1から4のいずれかに記載のアルミニウム切粉溶解装置において、前記装入手段が、前記乾燥・予熱スクリュコンベヤの排出端が上部に蒸気排出弁を設けた密閉式の装入ホッパー内の上部に接続開口されており、該装入ホッパー下部から竪型又は傾斜型の装入スクリュコンベヤが前記ルツボ型溶解炉の溶解部フィルタ下方にその下端を浸漬するように設けられ、前記乾燥・予熱したアルミニウム切粉を該装入スクリュコンベヤにより、また、窒素又はアルゴンガスの不活性ガスを該装入スクリュコンベヤ回転軸管から、共に溶湯中に装入することを特徴とする。 An aluminum chip melting apparatus according to claim 5 is the aluminum chip melting apparatus according to any one of claims 1 to 4, wherein the charging means is configured so that a discharge end of the drying / preheating screw conveyor is at an upper portion. A connection opening is formed in the upper part of a closed charging hopper provided with a steam discharge valve, and a vertical or inclined charging screw conveyor is provided below the melting part filter of the crucible melting furnace from the lower part of the charging hopper. It is provided so that the lower end is immersed, and the dried and preheated aluminum chips are put into the molten metal by the charging screw conveyor and the inert gas of nitrogen or argon gas from the charging screw conveyor rotary shaft tube. It is characterized by charging in.
この構成をとることにより、乾燥・予熱スクリュコンベヤで付着切削油の油分を随伴したアルミニウム切粉は予熱され、しかも水分は蒸発状態のまま搬送され、装入ホッパに排出された時点で、水蒸気がホッパ空間に放出され、蒸気排出弁を経由して大気に放散される。また、油分を含んだ予熱されたアルミニウム切粉は装入ホッパ下部に堆積し、次いで竪型又は傾斜型の装入スクリュコンベヤにより充填状態で搬送され、溶解部に不活性ガスと共に落下・装入させると共に、バブリングすることができる。また、竪型装入スクリュコンベヤは、傾斜型装入スクリュコンベヤに比し、アルミニウム切粉の充填度合いにより装入速度が変化し易いので、傾斜型スクリュコンベヤの方が装入量の調整が容易である。また、装入スクリュコンベヤ回転軸管に不活性ガスを導入して、アルミニウム切粉の拡散・溶解を強化することが可能となる。 By adopting this configuration, when the aluminum chips accompanied by the adhering cutting oil are preheated by the drying / preheating screw conveyor, the moisture is transported in an evaporated state, and when steam is discharged to the charging hopper, Released into the hopper space and dissipated to the atmosphere via a steam discharge valve. Also, preheated aluminum chips containing oil are deposited at the bottom of the charging hopper, and then transported in a filled state by a vertical or inclined charging screw conveyor, and dropped and charged together with an inert gas into the melting part. And bubbling. In addition, the vertical charging screw conveyor is easier to adjust the charging amount than the inclined charging screw conveyor because the charging speed is more likely to change depending on the degree of aluminum chip filling. It is. Further, it becomes possible to enhance the diffusion and melting of the aluminum chips by introducing an inert gas into the rotary screw tube of the charging screw conveyor.
また、請求項6に係るアルミニウム切粉溶解装置は、請求項1から4のいずれかに記載のアルミニウム切粉溶解装置において、前記装入手段が、前記密閉型スクリュコンベヤの排出端が上部に蒸気排出弁を設けた密閉式の装入ホッパー内の上部に接続開口されており、該装入ホッパー下部から傾斜型のプッシャーが前記ルツボ型溶解炉の溶解部フィルタ下方にその下端を浸漬するように設けられ、前記乾燥・予熱したアルミニウム切粉を該プッシャーにより溶湯中に装入することを特徴とする。 An aluminum chip melting apparatus according to claim 6 is the aluminum chip melting apparatus according to any one of claims 1 to 4, wherein the charging means is configured such that the discharge end of the hermetic screw conveyor is steamed upward. A connection opening is made in the upper part of the closed charging hopper provided with a discharge valve, and an inclined pusher is immersed from the lower part of the charging hopper below the melting part filter of the crucible melting furnace. The dried and preheated aluminum chips are charged into the molten metal by the pusher.
この構成により間歇的であるが、強制的にアルミニウム切粉を溶解炉の溶湯中に装入することが可能となる。また、このプッシャーによれば、アルミニウム切粉の粒度などの性状に大きく左右されずに、アルミニウム切粉を強制的に溶解炉に装入することが可能である。また、装入量もプッシャーの装入頻度で容易に調整し易いから切粉の溶解量を制御し易い。 Although it is intermittent by this structure, it becomes possible to forcibly insert the aluminum chips into the molten metal of the melting furnace. Further, according to this pusher, the aluminum chips can be forcibly charged into the melting furnace without being greatly affected by properties such as the particle size of the aluminum chips. In addition, since the charging amount is easily adjusted by the frequency of inserting the pusher, it is easy to control the dissolution amount of the chips.
また、請求項7に係るアルミニウム切粉溶解装置は、請求項1から6のいずれかに記載のアルミニウム切粉溶解装置において、前記油分ガス化燃焼手段が、前記ルツボ型溶解炉の溶解部及び溶湯部の上部空間から前記燃焼バーナの燃焼部につながる配管を備えると共に、該配管の末端に該燃焼部へとつながるベンチュリ部を備え、前記乾燥・予熱したアルミニウム切粉を前記溶解炉の溶解部で溶解する際に発生した油分ガスを回収して前記溶解炉の燃焼バーナへ誘引して燃焼させることを特徴とする。 An aluminum chip melting apparatus according to claim 7 is the aluminum chip melting apparatus according to any one of claims 1 to 6, wherein the oil gasification combustion means includes a melting section and a molten metal of the crucible melting furnace. A pipe connected to the combustion part of the combustion burner from the upper space of the part, and a venturi part connected to the combustion part at the end of the pipe, and the dried and preheated aluminum chips in the melting part of the melting furnace The oily gas generated during melting is collected and attracted to the combustion burner of the melting furnace for burning.
この構成により、アルミニウム切粉に随伴した切削油中の油分は溶解炉の溶解部でガス化して回収され、配管(ダクト)により燃焼バーナ部へベンチュリ部を経由して誘引されて送られ、そこで燃焼バーナの火炎により燃焼する。これにより燃焼バーナの燃料を代替する効果が生じる。 With this configuration, the oil content in the cutting oil accompanying the aluminum chips is gasified and recovered in the melting part of the melting furnace, and is sent to the combustion burner part via the venturi part by piping (duct). It burns with the flame of a combustion burner. This produces the effect of substituting the fuel for the combustion burner.
また、請求項8に係るアルミニウム切粉溶解装置は、請求項1から7のいずれかに記載のアルミニウム切粉溶解装置において、前記乾燥・予熱手段が、前記アルミニウム切粉の乾燥・予熱する温度が125℃から145℃の範囲であって、好ましくは135℃にすることを特徴とする。 An aluminum chip melting apparatus according to claim 8 is the aluminum chip melting apparatus according to any one of claims 1 to 7, wherein the drying / preheating means has a temperature at which the aluminum chip is dried / preheated. The temperature range is from 125 ° C to 145 ° C, preferably 135 ° C.
本発明のアルミニウム切粉は切削油由来の油分を随伴している。通常、この切削油は油と水のエマルジョン状態を呈しており、その量は含切削油切粉に対して油が5~15wt%、水が1~5wt%の範囲である。この切削油を加熱することにより、水分を蒸散し、油分を残留させることを目的として、処理対象の切削油の熱重量―示差熱分析(TG-DTA分析)を行った。その結果、135℃付近までの加熱で水分は除去され、200~500℃の領域で油分が酸化・発熱することが判明した(図9参照)。これに基づいて、請求項10の構成をとることにより、切削油を随伴するアルミニウム切粉の乾燥・予熱温度を135±10℃の範囲に、好ましくは135℃にすることにより、油分は残留し、水分を蒸発状態にすることができ、アルミニウム切粉の溶解炉での溶解及び油分のガス化を溶解炉で高温を維持して実施でき、また溶湯アルミニウムの水素含有を低減させることが達成できる。 The aluminum chips of the present invention are accompanied by an oil component derived from cutting oil. Normally, this cutting oil is in an emulsion state of oil and water, and the amount thereof is in the range of 5 to 15 wt% for oil and 1 to 5 wt% for water with respect to the cutting oil containing cutting oil. For the purpose of evaporating moisture and leaving the oil component by heating the cutting oil, thermogravimetric-differential thermal analysis (TG-DTA analysis) of the cutting oil to be treated was performed. As a result, it was found that the water was removed by heating up to around 135 ° C., and the oil component was oxidized and generated heat in the region of 200 to 500 ° C. (see FIG. 9). Based on this, by taking the constitution of claim 10, the oil content remains by setting the drying / preheating temperature of the aluminum chips accompanying the cutting oil in the range of 135 ± 10 ° C., preferably 135 ° C. , The moisture can be evaporated, the melting of the aluminum chips in the melting furnace and the gasification of the oil can be carried out while maintaining the high temperature in the melting furnace, and the hydrogen content of the molten aluminum can be reduced. .
また、請求項9に係るアルミニウム切粉溶解装置は、請求項1から8のいずれかに記載のアルミニウム切粉溶解装置において、前記乾燥・予熱手段が、乾燥・予熱処理後のアルミニウム切粉の水分を5%以下にすること、好ましくは1%以下にすることを特徴とする。 Further, an aluminum chip melting apparatus according to claim 9 is the aluminum chip melting apparatus according to any one of claims 1 to 8, wherein the drying / preheating means includes moisture in the aluminum chip after drying / preheating. Is 5% or less, preferably 1% or less.
 この構成を採ることにより、溶解炉でのアルミニウム切粉の溶解と油分のガス化において、装入アルミニウム切粉に残存する水分量がより少なくなるから溶湯に温度低下をもたらすことなく、溶解能力を効率良く維持、向上できる。また、装入アルミニウム切粉の水分を1%以下にする方が溶解炉でのアルミニウム切粉の溶解量と油分のガス化をさらに効率良く向上できる。 By adopting this configuration, in the melting of the aluminum chips and gasification of oil in the melting furnace, the amount of water remaining in the charged aluminum chips is reduced, so the melting capacity is reduced without causing a temperature drop in the molten metal. It can be maintained and improved efficiently. In addition, the amount of aluminum chips charged in the melting furnace and the gasification of oil can be more efficiently improved when the water content of the charged aluminum chips is 1% or less.
また、請求項10に係るアルミニウム切粉溶解装置は、請求項1から9のいずれかに記載のアルミニウム切粉溶解装置において、前記アルミニウム切粉溶解装置の前段に、遠心油水分離機を備え、遠心油水分離機によりアルミニウム切粉の付着切削油量を減少する前処理を行うことを特徴とする。 An aluminum chip dissolving apparatus according to claim 10 is the aluminum chip dissolving apparatus according to any one of claims 1 to 9, wherein a centrifugal oil-water separator is provided upstream of the aluminum chip dissolving apparatus. A pretreatment for reducing the amount of cutting oil adhering to the aluminum chips is performed by an oil / water separator.
この構成の前処理手段により、遠心油水分離機で物理的に切削油を分別して、その含有量を容易に減じることができ、次いで乾燥・予熱手段であるスクリュコンベヤで加熱脱水する能力に余裕が生じ、アルミニウム切粉の付着切削油中の水分を主として効率よく減じて、かつ、切粉を十分予熱することができる。したがって、アルミニウム切粉溶解装置に、本遠心油水分離機を付加することにより、切削油を随伴するアルミニウム切粉の溶解能力を向上すること、又は、過剰な切削油を随伴するアルミニウム切粉の溶解処理を可能にすることができる。また、本構成によると、脱油水において加熱などの熱エネルギを使用する必要がないから、脱水・予熱面で省エネルギに貢献し、かつ、大気汚染の心配がない。 With the pretreatment means of this configuration, the cutting oil can be physically separated by a centrifugal oil / water separator and its content can be easily reduced, and then there is a margin in the ability to heat and dehydrate with a screw conveyor that is a drying / preheating means. As a result, it is possible to mainly reduce the moisture in the cutting oil adhering to the aluminum chips and efficiently preheat the chips. Therefore, by adding this centrifugal oil water separator to the aluminum chip dissolving device, the melting capacity of aluminum chips accompanied with cutting oil is improved, or the dissolution of aluminum chips accompanied by excess cutting oil Processing can be enabled. Further, according to this configuration, it is not necessary to use heat energy such as heating in the deoiled water, which contributes to energy saving in terms of dehydration and preheating, and there is no concern about air pollution.
また、請求項11のアルミニウム切粉の溶解方法は、切削油が付着しているアルミニウム切粉を溶解する方法であって、該アルミニウム切粉を125℃から145℃の範囲に、好ましくは135℃にルツボ型溶解炉の排ガスを利用して間接加熱することにより乾燥・予熱して、切削油中の水分を蒸発除去し、次いで、該乾燥・予熱したアルミニウム切粉を燃焼バーナで加熱する該ルツボ型溶解炉の溶解部の溶湯アルミニウム中に装入して溶解することにより、切削油中の油分はガス化して、そのガスを該ルツボ型溶解炉の間接加熱用燃料として補填して使用すると共に、溶解したアルミニウムは、該ルツボ型溶解炉の溶解部から溶湯部へ溶湯のみを移行させて清浄なアルミニウム溶湯を得ることを特徴とする。 Further, the aluminum chip melting method according to claim 11 is a method of melting the aluminum chip to which cutting oil is adhered, and the aluminum chip is in the range of 125 ° C. to 145 ° C., preferably 135 ° C. The crucible is dried and preheated by indirect heating using the exhaust gas of the crucible melting furnace to evaporate and remove moisture in the cutting oil, and then the dried and preheated aluminum chips are heated with a combustion burner. By charging and melting in molten aluminum in the melting part of the mold melting furnace, the oil content in the cutting oil is gasified, and the gas is supplemented and used as fuel for indirect heating of the crucible melting furnace. The molten aluminum is characterized in that only the molten metal is transferred from the melting part to the molten metal part of the crucible melting furnace to obtain a clean molten aluminum.
この構成により、切削油を随伴しているアルミニウム切粉の随伴水分を蒸発させ、かつ予熱したアルミニウム切粉を溶解することにより、アルミニウム溶湯を熱効率よく得ることができる。また、油分は溶解炉でガス化して回収し、溶解炉燃料の代替として使用できるので、本発明方法は省資源、省エネルギに適したアルミニウム切粉溶解方法である。また、アルミニウム切粉の随伴油分は、高温の溶解炉でガス化して閉回路で燃料として回収できるので、従来のように油分を単に燃焼させる方式と比べて大気汚染などの公害を招来する恐れがなく、また、溶解燃料の軽減に貢献する。 With this configuration, it is possible to obtain a molten aluminum with high thermal efficiency by evaporating the accompanying moisture of the aluminum chips accompanied with the cutting oil and dissolving the preheated aluminum chips. In addition, since the oil can be recovered by gasification in a melting furnace and used as a substitute for melting furnace fuel, the method of the present invention is an aluminum chip melting method suitable for resource saving and energy saving. In addition, the accompanying oil content of aluminum chips can be gasified in a high-temperature melting furnace and recovered as fuel in a closed circuit, so there is a risk of causing pollution such as air pollution compared to conventional methods in which oil is simply burned. It also contributes to the reduction of dissolved fuel.
また、請求項12のアルミニウム切粉の溶解方法は、請求項11のアルミニウム切粉の溶解方法において、該乾燥・予熱したアルミニウム切粉を該ルツボ型溶解炉の溶解部の溶湯アルミニウム中に装入して溶解する際に、機械式スターラ又は不活性ガスインジェクションにより攪拌混合して溶解及び油分ガス化を促進することを特徴とする。 The method for melting aluminum chips according to claim 12 is the method for melting aluminum chips according to claim 11, wherein the dried and preheated aluminum chips are charged into molten aluminum in the melting part of the crucible melting furnace. When dissolved, the mixture is stirred and mixed by a mechanical stirrer or inert gas injection to promote dissolution and oil gasification.
この構成により、溶解部に装入されたアルミニウム切粉を強制的に広範囲に攪拌分散すると共に、不活性ガスインジェクションによりアルミニウム切粉を細かく拡散することによりアルミニウム切粉の溶解、油分のガス化を促進することができる。 With this configuration, the aluminum chips charged in the melting part are forcibly stirred and dispersed over a wide range, and the aluminum chips are finely diffused by inert gas injection to dissolve the aluminum chips and gasify the oil. Can be promoted.
本発明に係る請求項1から12に記載のアルミニウム切粉溶解装置及び溶解方法によれば、切削油を随伴したアルミニウム切粉を原料として、品質の良いアルミニウム溶湯を得ることができると共に、該切削油の油分を効率よく閉回路でガス化することにより溶解バーナの燃料の一部を代替することが可能となる。これらにより、アルミニウム切粉からアルミニウム資源の回収及び随伴油分の保有エネルギの回収により溶解燃料の代替が図られ、資源の活用、省エネルギ源に貢献する。また、本発明によれば、随伴切削油分の除去において、従来法と異なり大気汚染などの公害の恐れがないクリーンな処理ができる装置であり、方法である。また、本アルミニウム切粉溶解装置は、使用実績のある設備をコンパクトに集約して構成されており、従来よりも設置面積も小さく、設備費用も多大とならない、かつ、大気汚染もない環境的にも優れた設備である。 According to the aluminum chip melting apparatus and the melting method according to claims 1 to 12 of the present invention, a high-quality aluminum melt can be obtained using aluminum chips accompanied by cutting oil as a raw material, and the cutting By efficiently gasifying the oil content of the oil in a closed circuit, a part of the fuel of the melting burner can be replaced. As a result, it is possible to replace dissolved fuel by recovering aluminum resources from the aluminum chips and recovering the energy stored in the associated oil, thereby contributing to resource utilization and energy saving. Further, according to the present invention, in the removal of the accompanying cutting oil, unlike the conventional method, it is an apparatus and method that can perform a clean process without fear of pollution such as air pollution. In addition, this aluminum chip melting device is composed of equipment that has been used in a compact manner, has a smaller installation area than conventional ones, and does not require significant equipment costs. Also excellent equipment.
図1は、本発明を実施するための形態に係るアルミニウム切粉溶解装置の模式的正面断面図である。FIG. 1 is a schematic front sectional view of an aluminum chip melting apparatus according to an embodiment for carrying out the present invention. 図2は、図1における模式的側面断面図である。FIG. 2 is a schematic side cross-sectional view in FIG. 図3は、図2における乾燥・予熱装置に連なる燃焼排ガス系の模式的断面図である。FIG. 3 is a schematic cross-sectional view of a flue gas system connected to the drying / preheating device in FIG. 図4は、図2におけるA-A矢視の模式的断面図である。4 is a schematic cross-sectional view taken along the line AA in FIG. 図5は、本発明を実施するための別の形態に係るアルミニウム切粉溶解装置の模式的正面断面図である。FIG. 5 is a schematic front sectional view of an aluminum chip melting apparatus according to another embodiment for carrying out the present invention. 図6は、本発明を実施するための別の形態に係るアルミニウム切粉溶解装置の模式的正面断面図である。FIG. 6 is a schematic front sectional view of an aluminum chip melting apparatus according to another embodiment for carrying out the present invention. 図7は、図5又は図6における乾燥・予熱装置に連なる燃焼排ガス系の模式的断面図である。FIG. 7 is a schematic cross-sectional view of a flue gas system connected to the drying / preheating device in FIG. 5 or FIG. 図8は、図7におけるA-A矢視の模式的断面図である。FIG. 8 is a schematic cross-sectional view taken along the line AA in FIG. アルミニウム用切削油の熱重量―示差熱分析チャートの代表例である。It is a typical example of the thermogravimetric-differential thermal analysis chart of the cutting oil for aluminum. アルミニウム切粉溶解における窒素ガスインジェクションの効果を示す図である。It is a figure which shows the effect of the nitrogen gas injection in aluminum chip melt | dissolution. 本発明のアルミニウム切粉の溶解工程を示すフロー図である。It is a flowchart which shows the melt | dissolution process of the aluminum chip of this invention. 従来例であってアルミニウム切粉の前処理方法を示すフロー図である。It is a prior art example, and is a flowchart which shows the pre-processing method of aluminum chips.
本発明に係る切削油を随伴したアルミニウム切粉の溶解処理工程を図11のフロー図に基づいて説明すると、エマルジョン状態の油と水から成る切削油を随伴したアルミニウム切粉は、その含油水量に応じて、遠心油水分離機に掛けて油水量を減少する(a)。次いで、切削油随伴アルミニウム切粉の乾燥・予熱工程(b)、乾燥・予熱されたアルミニウム切粉を溶解炉に装入する装入工程(c)、アルミニウム溶湯を加熱保持した溶解炉において、アルミニウム切粉を装入して溶解する溶解工程(d)、アルミニウム溶解炉で油分をガス化した油分ガスを溶解炉燃焼バーナで燃焼する油分ガス化燃焼工程(e)から構成される。 Referring to the flow chart of FIG. 11, the aluminum chip accompanied by the cutting oil according to the present invention will be described based on the flow chart of FIG. 11. Accordingly, the amount of oil and water is reduced by applying to a centrifugal oil-water separator (a). Next, drying and preheating step (b) of the aluminum chips accompanied with cutting oil, charging step (c) of charging the dried and preheated aluminum chips into the melting furnace, and in the melting furnace holding the molten aluminum heated, It comprises a melting step (d) in which chips are charged and melted, and an oil gasification combustion step (e) in which oil gas obtained by gasifying oil in an aluminum melting furnace is burned in a melting furnace combustion burner.
本発明に係るアルミニウム切粉溶解装置1を図1,2,3,4を用いて説明する。アルミニウム切粉溶解装置1は、アルミニウム切粉の付着切削油中の水分を除去する乾燥・予熱装置4と、該乾燥・予熱したアルミニウム切粉をルツボ型溶解炉2の溶湯M中に装入する切粉装入装置5と、燃焼バーナ6により間接加熱したルツボ型溶解炉2を用いて乾燥・予熱したアルミニウム切粉を溶解してアルミニウム溶湯Mを製造するアルミニウム溶解装置と、乾燥・予熱したアルミニウム切粉中に残留させた油分をルツボ型溶解炉2でアルミニウム切粉を溶解した際にガス化させた後、燃焼バーナ6へ誘引して燃焼させる油分ガス化燃焼装置から成る。 An aluminum chip melting apparatus 1 according to the present invention will be described with reference to FIGS. The aluminum chip melting apparatus 1 is equipped with a drying / preheating device 4 that removes moisture in the cutting oil adhered to the aluminum chip, and the dried / preheated aluminum chip is charged into the molten metal M of the crucible melting furnace 2. An aluminum melting device for producing a molten aluminum M by melting dry and preheated aluminum chips using a chip charging device 5 and a crucible type melting furnace 2 indirectly heated by a combustion burner 6, and dried and preheated aluminum It comprises an oil gasification combustion apparatus in which the oil remaining in the chips is gasified when the aluminum chips are melted in the crucible melting furnace 2 and then attracted to the combustion burner 6 for combustion.
また、アルミニウム切粉溶解装置1の前段に、遠心油水分離機(図示しない)を設け、アルミニウム切粉の過剰な付着切削油量、即ち、過剰な油水分量を減少する前処理を行うことができる。この前処理手段により、遠心油水分離機でアルミニウム切粉の付着切削油中の過剰な油水分量を物理的に加熱することなく容易に減じることができ、次いでアルミニウム切粉溶解装置1の乾燥・予熱手段であるスクリュコンベヤ4-2でさらに加熱脱水できるので、アルミニウム切粉の付着切削油中の水分を効率よく減じ、予熱することができる。また、この装置によると、脱油水において加熱などの熱エネルギを使用する必要がないから、それに伴う大気汚染の心配もない。 In addition, a centrifugal oil / water separator (not shown) is provided in the preceding stage of the aluminum chip melting apparatus 1 to perform pretreatment to reduce the amount of cutting oil adhering to the aluminum chip, that is, the amount of excess oil moisture. . With this pretreatment means, the excess oil and water content in the cutting oil adhered to the aluminum chips can be easily reduced without physical heating with a centrifugal oil / water separator, and then the aluminum chip melting apparatus 1 is dried and preheated. Since it can be further heated and dehydrated by the screw conveyor 4-2 as a means, the moisture in the cutting oil adhering to the aluminum chips can be efficiently reduced and preheated. Further, according to this apparatus, it is not necessary to use heat energy such as heating in the deoiled water, so there is no concern about air pollution associated therewith.
 本発明に係るアルミニウム切粉は、アルミニウム又はアルミニウム合金を切削加工してアルミニウム製品を製造する際に発生する切削屑を主体とする。したがって、アルミニウム切粉は、含切削油切粉100に対して10~20wt%の切削油を随伴しており、通常、切削油は、油と水のエマルジョンが用いられるから、5~15wt%の油と1~5wt%の水との混合物が付着している。本発明のアルミニウム切粉溶解装置1は、アルミニウム切粉に随伴している切削油から水分を加熱蒸発して除去し、油分のみを残留させてから溶解炉2に装入して、アルミニウム溶湯Mを得ると共に、油分をガス化して溶解炉2の加熱バーナー6の一部代替燃料として燃焼させるものである。これによりアルミニウム切粉からアルミニウムを資源回収すると共に、随伴している切削油を大気汚染などの公害を惹起することなく燃料としてのエネルギ回収が可能となる。 The aluminum swarf according to the present invention is mainly composed of cutting waste generated when an aluminum product is manufactured by cutting aluminum or an aluminum alloy. Therefore, the aluminum chips are accompanied by 10 to 20 wt% of the cutting oil with respect to the cutting oil containing chips 100, and normally, the cutting oil is an emulsion of oil and water, so that the amount of 5 to 15 wt% is used. A mixture of oil and 1-5 wt% water is adhered. The aluminum chip melting apparatus 1 of the present invention removes moisture by heating and evaporating from the cutting oil associated with the aluminum chip, leaving only the oil content, and then charging it into the melting furnace 2 to melt the aluminum melt M. In addition, the oil is gasified and combusted as a partial alternative fuel for the heating burner 6 of the melting furnace 2. As a result, it is possible to recover aluminum from the aluminum chips and to recover energy as fuel without causing pollution such as air pollution with the accompanying cutting oil.
 また、アルミニウム切粉溶解装置1における乾燥・予熱装置4は、装入ホッパ4-1からアルミニウム切粉を、可変速の駆動ギヤードモータ4-2eで回転駆動される乾燥・予熱スクリュコンベヤ4-2で、切出して運搬すると共に、乾燥・予熱室4-3内に該スクリュコンベヤ4-2を挿通し、スクリュコンベヤ外筒4-2bをルツボ型溶解炉2からの燃焼排ガスを燃焼排ガスダクト8を経る途中で希釈エア入口8-1からの冷気により温度調整して乾燥・予熱室4-3内に導いて加熱することによりアルミニウム切粉を乾燥・予熱する。なお、この乾燥・予熱ガスの流量及び温度は、乾燥・予熱室4-3に設けている室内圧力計4-3dと温度計4-3cの値により希釈エア入口8-1のダンパと燃焼排ガスダクト8のダンパ8-2の開閉度で調整できる。 The drying / preheating device 4 in the aluminum chip melting apparatus 1 is a drying / preheating screw conveyor 4-2 in which aluminum chips are rotated from a charging hopper 4-1 by a variable speed drive geared motor 4-2e. The screw conveyor 4-2 is inserted into the drying / preheating chamber 4-3, and the screw conveyor outer cylinder 4-2b is passed through the combustion exhaust gas duct 8 from the crucible melting furnace 2. During the course, the aluminum chips are dried and preheated by adjusting the temperature with the cold air from the dilution air inlet 8-1 and introducing it into the drying / preheating chamber 4-3 and heating. The flow rate and temperature of the drying / preheating gas are determined by the values of the indoor pressure gauge 4-3d and the thermometer 4-3c provided in the drying / preheating chamber 4-3, and the damper and combustion exhaust gas at the dilution air inlet 8-1. The degree of opening / closing of the damper 8-2 of the duct 8 can be adjusted.
この際、アルミニウム切粉の乾燥・予熱する温度が125℃から145℃の範囲であって、好ましくは135℃にするのが好適である。通常、アルミニウム切粉は切削油由来の油分と水分を随伴しているので、本発明では、加熱により水分を蒸発させて、油分を残留させることを目的として、使用する切削油(商品名:スギカットCS-68DN-2)の熱重量―示差熱分析(TG-DTA分析)を行った。その結果、図9に示すように、135℃付近までの加熱で水分は除去され、200~500℃の領域で油分が酸化・発熱することが判明した。これに基づいて、アルミニウム切粉の乾燥・予熱温度を135±10℃の範囲に、好ましくは135℃にすることにより、油分は残留し、水分を蒸発状態で除去することができる。引き続いて、このアルミニウム切粉を用いて溶解炉2での溶解及び油分のガス化を行った場合、溶解炉2で溶解温度を下げることなく高温に維持でき、また溶湯アルミニウムMの水素含有量を低減させることに繋げる。 At this time, the temperature for drying and preheating the aluminum chips is in the range of 125 ° C. to 145 ° C., preferably 135 ° C. Normally, aluminum chips are accompanied by oil and moisture derived from cutting oil. Therefore, in the present invention, cutting oil used for the purpose of evaporating moisture by heating and leaving the oil (trade name: cedar cut) Thermogravimetric-differential thermal analysis (TG-DTA analysis) of CS-68DN-2) was performed. As a result, as shown in FIG. 9, it was found that moisture was removed by heating up to around 135 ° C., and the oil was oxidized and generated heat in the region of 200 to 500 ° C. Based on this, when the drying / preheating temperature of the aluminum chips is in the range of 135 ± 10 ° C., preferably 135 ° C., the oil remains and the water can be removed in an evaporated state. Subsequently, when the aluminum chips are used for melting in the melting furnace 2 and gasifying the oil, the melting furnace 2 can maintain a high temperature without lowering the melting temperature, and the hydrogen content of the molten aluminum M can be reduced. It leads to reduction.
また、図3に示すように、アルミニウム切粉溶解装置1のルツボ型溶解炉2は、炉壁耐火物7-1と炉蓋耐火物7-2によって取囲まれた溶解炉燃焼室7内の炉載置台2-5上に設置している。溶解炉燃焼バーナ6は、溶解炉燃焼室7の底部近くの隅部に設けられ、また燃焼排ガス出口は、図4、8にも示すように、溶解炉燃焼室7の上部で、燃焼バーナ6と、その軸線をずらして設けているので、燃焼バーナ6の火炎は下から上へのルツボ型溶解炉2の外壁を舐める旋回流となってルツボ型溶解炉2を加熱する。ルツボ型溶解炉2は、主として炭素質耐火物で壺状に形成され、内部に融点約660℃のアルミニウム溶湯Mを保持すると共に、外壁を溶解炉燃焼バーナ6の下から上への旋回流火炎で加熱されるから、溶解炉2は燃焼バーナ6により間接加熱される。なお、溶解炉燃焼室7と、炉上部空間2-4及び溶解炉2内部とは、溶解炉2の耐火物で隔離されているので、雰囲気状態は完全に相異なる。通常、溶解炉の燃焼室温度は、700℃~1000℃の範囲である。また、ルツボ型溶解炉2の大きさは、アルミニウム切粉の溶解量50~100kg/hrで、直径600mm、高さ500mm位となる。 Further, as shown in FIG. 3, the crucible type melting furnace 2 of the aluminum chip melting apparatus 1 has a melting furnace combustion chamber 7 surrounded by a furnace wall refractory 7-1 and a furnace lid refractory 7-2. It is installed on the furnace mounting table 2-5. The melting furnace combustion burner 6 is provided at a corner near the bottom of the melting furnace combustion chamber 7, and the combustion exhaust gas outlet is located above the melting furnace combustion chamber 7 as shown in FIGS. Since the axis is shifted, the flame of the combustion burner 6 heats the crucible melting furnace 2 as a swirling flow licking the outer wall of the crucible melting furnace 2 from bottom to top. The crucible melting furnace 2 is mainly formed of a carbonaceous refractory in a bowl shape, holds an aluminum melt M having a melting point of about 660 ° C. inside, and a swirl flow flame from the bottom to the top of the melting furnace combustion burner 6. Therefore, the melting furnace 2 is indirectly heated by the combustion burner 6. Since the melting furnace combustion chamber 7, the furnace upper space 2-4, and the inside of the melting furnace 2 are isolated by the refractory of the melting furnace 2, the atmosphere state is completely different. Usually, the combustion chamber temperature of the melting furnace is in the range of 700 ° C to 1000 ° C. The size of the crucible melting furnace 2 is about 600 mm in diameter and about 500 mm in height when the melting amount of aluminum chips is 50 to 100 kg / hr.
また、図4、8に示すように、アルミニウム切粉溶解装置1のルツボ型溶解炉2が、溶湯M溜りの深さ方向に耐火物製の隔壁2-2により溶湯鍋3に出湯樋2-1を経て連なる溶湯部2-bと、溶解部2-aと、に区分けして構成されており、さらに図1,2,3に示すように該溶解部2-aの溶湯面より下で水平方向の断面全体に亘って耐火物製のフィルタ2-3を備えている。アルミニウム切粉の溶解については、前記乾燥・予熱したアルミニウム切粉が装入装置5の竪型又は傾斜型装入スクリュコンベヤ5-2により窒素またはアルゴンの不活性ガスを随伴して又は傾斜型プッシャー5-4により溶解炉2のフィルタ2-3の下部の溶湯M中に装入して、アルミニウム切粉を溶解すると共に、アルミニウム切粉に随伴する切削油由来の油分をガス化して溶解部2-a上面から放出し、炉上部空間2-4を経て油分ガスを取り出して油分回収ダクト9を経て燃焼バーナ6の補助燃焼に供する。 As shown in FIGS. 4 and 8, the crucible melting furnace 2 of the aluminum chip melting apparatus 1 is connected to the molten metal pan 3 by a refractory partition wall 2-2 in the depth direction of the molten metal M pool. 1 is divided into a melted portion 2-b and a melted portion 2-a, and further below the surface of the melted portion 2-a as shown in FIGS. A refractory filter 2-3 is provided over the entire horizontal cross section. As for the melting of the aluminum chips, the dried and preheated aluminum chips are accompanied by an inert gas such as nitrogen or argon by the vertical or inclined charging screw conveyor 5-2 of the charging device 5 or the inclined pusher. 5-4 is charged into the molten metal M at the lower part of the filter 2-3 of the melting furnace 2 to melt the aluminum chips and gasifies the oil derived from the cutting oil accompanying the aluminum chips. -A is discharged from the upper surface, oil gas is taken out through the furnace upper space 2-4, and supplied to the auxiliary combustion of the combustion burner 6 through the oil recovery duct 9.
また、ルツボ型溶解炉2の溶解部2-aにおいて、乾燥・予熱したアルミニウム切粉をフィルタ2-3の下部の溶湯M中に装入する装入手段5に近接して、回転する攪拌翼3-1と、回転軸3-3からなるスターラ3を設けている。また、スターラ3は、回転軸3-3からの窒素の不活性ガスをインジェクションすることができ、スターラ3により装入されたアルミニウム切粉を強制的に攪拌翼3-1で広範囲に攪拌分散すると共に、不活性ガスインジェクションによりアルミニウム切粉を細かく拡散することによりアルミニウム切粉の溶解、油分のガス化を促進することができる。 Further, in the melting part 2-a of the crucible type melting furnace 2, a stirring blade rotating in the vicinity of the charging means 5 for charging the dried and preheated aluminum chips into the molten metal M below the filter 2-3. A stirrer 3 including a 3-1 and a rotating shaft 3-3 is provided. Further, the stirrer 3 can inject an inert gas of nitrogen from the rotating shaft 3-3, and the aluminum chips charged by the stirrer 3 are forcibly dispersed with a stirring blade 3-1 over a wide range. At the same time, by finely diffusing the aluminum chips by inert gas injection, dissolution of the aluminum chips and gasification of the oil can be promoted.
前述したアルミニウム切粉のアルミニウム溶湯M中への溶解に及ぼす窒素(N)インジェクションの効果を実験炉で確認した結果を図10に示す。アルミニウム切粉としては、乾燥後で水分量1%以下、油分量1.5~2%の切粉を用いた。結果として、窒素インジェクション無しの場合で、アルミニウム切粉の装入後経過時間10~20分で、溶解した比率(溶解効率)50~65%に対し、窒素インジェクション有りの場合が、アルミニウム切粉の装入後経過時間3~10分で、溶解した比率(溶解効率)65~85%を得た。これらから、アルミニウム溶湯M中で窒素(N)インジェクションを行えば、アルミニウム切粉の溶解が効率よく短時間で達成できる可能性を確認した。 FIG. 10 shows the result of confirming the effect of nitrogen (N 2 ) injection on the dissolution of the above-described aluminum chips in the molten aluminum M in an experimental furnace. As the aluminum chips, chips having a water content of 1% or less and an oil content of 1.5 to 2% after drying were used. As a result, in the case of no nitrogen injection, the elapsed time after charging aluminum chips was 10 to 20 minutes, and the dissolved ratio (dissolution efficiency) was 50 to 65%. A dissolution rate (dissolution efficiency) of 65 to 85% was obtained in 3 to 10 minutes after the charging. From these, by performing nitrogen (N 2) injection in the aluminum melt M, the dissolution of aluminum chips was confirmed the possibility of achieving in a short time efficiently.
また、アルミニウム切粉溶解装置1の切粉装入装置5は、乾燥・予熱スクリュコンベヤ4-2の排出端4-2dが密閉式の装入ホッパ5-1の上部に接続して開口されており、また、装入ホッパ5-1の上蓋部に蒸気排出弁5-3を設けている。また、装入ホッパ5-1の下部から、可変速の駆動ギヤードモータ5-2dで回転駆動される竪型又は傾斜型の装入スクリュコンベヤ5-2が、ルツボ型溶解炉2の溶解部フィルタ2-4の下方にその下端を浸漬するように設けられており、乾燥・予熱したアルミニウム切粉を装入スクリュコンベヤ5-2により溶湯M中に装入し、その際不活性ガスである窒素を吹込み窒素流入口5-2eから管状の装入スクリュコンベヤ回転軸5-2cを通って窒素吹き出し口5-2fから溶湯M中にインジェクトしてバブリングさせ、装入したアルミニウム切粉の溶解と随伴した油分のガス化を促進する。また、溶湯Mからの脱ガス作用ももたらす。また、装入スクリュコンベヤ5-2のコンベヤ外筒5-2bとスクリュ羽根5-2aはアルミニウム溶湯Mと接するので耐火性を必要とする。なお、竪型又は傾斜型の装入スクリュコンベヤ5-2を採用した場合には、アルミニウム切粉はスクリュ羽根5-2aの螺旋状の空間を埋め尽くしているから、マテリアルシールを形成し、装入ホッパ5-1と溶解炉2とは完全にシールされるから、装入ホッパ5-1の空気や水蒸気が溶解炉2に流入することはないので、溶湯Mの品質に悪影響を与えない。また、竪型装入スクリュコンベヤは、傾斜型装入スクリュコンベヤに比し、アルミニウム切粉の充填度合いにより装入速度が変化し易いので、その点で傾斜型スクリュコンベヤの方が装入量の調整が容易である。 Further, the chip charging device 5 of the aluminum chip melting apparatus 1 is opened by connecting the discharge end 4-2d of the drying / preheating screw conveyor 4-2 to the upper part of the hermetic charging hopper 5-1. In addition, a steam discharge valve 5-3 is provided in the upper lid portion of the charging hopper 5-1. Also, a vertical or inclined charging screw conveyor 5-2 that is rotationally driven by a variable speed drive geared motor 5-2d from the lower portion of the charging hopper 5-1 is a melting part filter of the crucible melting furnace 2. 2-4 is provided so that its lower end is immersed, and dried and preheated aluminum chips are charged into the molten metal M by the charging screw conveyor 5-2, and nitrogen, which is an inert gas, is used at that time. Is injected from the nitrogen inlet 5-2e through the tubular charging screw conveyor rotary shaft 5-2c and injected into the molten metal M from the nitrogen outlet 5-2f to dissolve the charged aluminum chips. And promote the gasification of oil. Moreover, the degassing action from the molten metal M is also brought about. Further, since the outer casing 5-2b and the screw blade 5-2a of the charging screw conveyor 5-2 are in contact with the molten aluminum M, fire resistance is required. When the vertical or inclined charging screw conveyor 5-2 is adopted, the aluminum chips fill up the spiral space of the screw blade 5-2a. Since the inlet hopper 5-1 and the melting furnace 2 are completely sealed, the air and water vapor of the charging hopper 5-1 do not flow into the melting furnace 2, so that the quality of the molten metal M is not adversely affected. In addition, the vertical charging screw conveyor is more susceptible to changes in the charging speed depending on the degree of aluminum chip filling compared to the inclined charging screw conveyor. Adjustment is easy.
また、図6に示すように、竪型又は傾斜型の装入スクリュコンベヤ5-2の代わりに、傾斜型のプッシャー5-4を設けることができる。傾斜型のプッシャー5-4は、密閉型スクリュコンベヤ4-2が密閉式の装入ホッパー5-1の上部に接続している該装入ホッパー5-1の下部からルツボ型溶解炉2の溶解部フィルタ2-3下方にその下端を浸漬するように設けられており、乾燥・予熱したアルミニウム切粉をプッシャー5-4により溶湯M中に装入することができる。この傾斜型プッシャー5-4により間歇的であるが、強制的にアルミニウム切粉を溶解炉2の溶解部2-aの溶湯M中に装入することが可能となる。また、傾斜型プッシャー5-4によれば、アルミニウム切粉の粒度などの性状に大きく左右されずに、アルミニウム切粉を強制的に溶解炉2に装入することが可能である。また、傾斜型プッシャー5-4の駆動は、空気駆動のロッドレスシリンダ5-4aで行うのが好ましい。また、傾斜型のプッシャー5-4のプッシャーの先端部5-4bは、斜めに裁断されており、アルミニウム切粉を溶湯M中に押し込み易くしている。また、装入量もプッシャー5-4の装入頻度で容易に調整し易いから切粉の溶解量を制御し易い。 In addition, as shown in FIG. 6, an inclined pusher 5-4 can be provided in place of the vertical or inclined charging screw conveyor 5-2. The inclined type pusher 5-4 is used for melting the crucible melting furnace 2 from the lower part of the charging hopper 5-1 to which the hermetic screw conveyor 4-2 is connected to the upper part of the hermetic charging hopper 5-1. The lower end of the partial filter 2-3 is provided so that its lower end is immersed, and dried and preheated aluminum chips can be charged into the molten metal M by the pusher 5-4. Although it is intermittent by this inclined type pusher 5-4, it becomes possible to forcibly insert aluminum chips into the molten metal M of the melting part 2-a of the melting furnace 2. Further, according to the inclined pusher 5-4, it is possible to forcibly charge the aluminum chips into the melting furnace 2 without being greatly affected by the properties such as the particle size of the aluminum chips. Further, it is preferable that the inclined pusher 5-4 is driven by an air-driven rodless cylinder 5-4a. Also, the pusher tip 5-4b of the inclined pusher 5-4 is cut obliquely so that the aluminum chips can be easily pushed into the molten metal M. Further, since the charging amount can be easily adjusted by the charging frequency of the pusher 5-4, it is easy to control the dissolution amount of the chips.
また、アルミニウム切粉溶解装置1の溶解炉2で切削油分がガス化して炉上部空間2-4に溜まった油分ガスは、炉上部空間2-4から燃焼バーナ6の燃焼部につながる油分ガス回収ダクト9を設けると共に、油分ガス回収ダクト9の末端に前記燃焼部へとつながるベンチュリ部9-1を設けているので、溶解炉2から発生した油分ガスを誘引して導き、溶解炉燃焼バーナ6の火炎中で燃焼させることができる。これにより溶解炉燃焼バーナ6の燃料の一部代替が可能になる。 Further, the oil gas that has been gasified in the melting furnace 2 of the aluminum chip melting apparatus 1 and accumulated in the furnace upper space 2-4 is recovered from the gas from the furnace upper space 2-4 to the combustion part of the combustion burner 6. Since the duct 9 is provided and the venturi section 9-1 connected to the combustion section is provided at the end of the oil gas recovery duct 9, the oil gas generated from the melting furnace 2 is attracted and guided, and the melting furnace combustion burner 6 Can be burned in a flame. Thereby, a partial replacement of the fuel for the melting furnace combustion burner 6 becomes possible.
また、本発明に係るアルミニウム切粉溶解装置1を用いた溶解作業について総括的に述べると、含切削油アルミニウム切粉は、含有切削油量に応じて、遠心油水分離機の前処理を選択でき、次いで、切削油を随伴しているアルミニウム切粉を125℃から145℃の範囲に、好ましくは135℃に間接加熱により乾燥・予熱して切削油中の水分を蒸発除去し、次いで、該乾燥・予熱したアルミニウム切粉を燃焼バーナ6で加熱するルツボ型溶解炉2の溶解部2-aに装入して溶解することにより、切削油中の油分はガス化して、そのガスをルツボ型溶解炉2の燃焼バーナ6の燃料として補填して使用すると共に、溶解したアルミニウムは、ルツボ型溶解炉2の溶解部2-aから溶湯部2-bへ溶湯のみを移行させて清浄なアルミニウム溶湯Mを得るものである。 Moreover, when the melting operation | work using the aluminum chip melting apparatus 1 which concerns on this invention is described generally, the cutting oil containing aluminum cutting powder can select the pre-processing of a centrifugal oil-water separator according to the amount of cutting oil contained. Then, the aluminum chips accompanied with the cutting oil are dried and preheated by indirect heating to a range of 125 ° C. to 145 ° C., preferably 135 ° C., to evaporate and remove moisture in the cutting oil, and then the drying -The preheated aluminum chips are charged into the melting part 2-a of the crucible melting furnace 2 heated by the combustion burner 6 and melted, whereby the oil in the cutting oil is gasified and the gas is melted into the crucible. The molten aluminum is used as a fuel for the combustion burner 6 of the furnace 2, and the molten aluminum is transferred only from the melting part 2-a of the crucible melting furnace 2 to the molten metal part 2-b to obtain a clean molten aluminum M It is get those.
原料であるアルミニウム切粉の乾燥・予熱工程は、乾燥・予熱スクリュコンベヤ4-2の外筒4-2bを所定温度の溶解炉燃焼排ガスで加熱することにより、スクリュコンベヤ4-2の搬送アルミニウム切粉は随伴する水分が蒸発し、一方油分は蒸発していない状態にして、アルミニウム切粉は予熱されて次工程の切粉装入装置5の装入ホッパ5-1に送る。乾燥・予熱スクリュコンベヤ4-2からの乾燥・予熱されたアルミニウム切粉は、装入ホッパ5-1に排出された時点で、水蒸気がホッパ空間に放出され、蒸気排出口5-3を経由して大気に放散される。また、油分を含んだ予熱されたアルミニウム切粉は装入ホッパ5-1に堆積してから溶解炉2に装入される。 In the drying / preheating process of the aluminum chips that are the raw material, the outer cylinder 4-2b of the drying / preheating screw conveyor 4-2 is heated with melting furnace combustion exhaust gas at a predetermined temperature, so that the conveying aluminum cutting of the screw conveyor 4-2 is performed. The powder is accompanied by evaporation of moisture, while the oil is not evaporated, and the aluminum chips are preheated and sent to the charging hopper 5-1 of the next-stage chip charging apparatus 5. When the dried and preheated aluminum chips from the drying / preheating screw conveyor 4-2 are discharged to the charging hopper 5-1, the water vapor is discharged into the hopper space and passes through the steam discharge port 5-3. To the atmosphere. The preheated aluminum chips containing oil are deposited in the charging hopper 5-1 and then charged into the melting furnace 2.
油分を随伴したアルミニウム切粉は、装入ホッパ5-1から竪型又は傾斜型スクリュコンベヤ5-2により充填状態で搬送され、溶解炉2の溶解部2-aのフィルタ2-3下部域に、スクリュ回転軸5-2cを経由して噴出される不活性ガスと共に装入される。また、近接したスターラ3の攪拌翼3-1の攪拌と、回転軸3-2の窒素ガス噴出し口3-3のインジェクションにより、アルミニウム切粉は不活性ガスのインジェクションのバブリングとスターラ3の拡散により迅速に溶解して溶湯Mになると共に、油分はガス化する。次いで、アルミニウム溶湯Mが隔壁2-2の下を通過して溶湯部2-bへ移動し、最終的には出湯樋2-1から出湯される。この際、隔壁2-2により溶湯Mが短絡して流れるのを防止し、滞留時間を長くとることで、不純物であるスラグ成分などを浮上・分離して、溶湯Mは十分清浄化される。また、油分は不活性ガスのバブリングのもと、フィルタ2-2下の領域で加熱されて酸化されることなくガス化して、フィルタ2-2を通過して浮上し、炉上部空間2-4に移動し、次いで油分ガス回収ダクト9を経由して燃焼バーナ6の燃焼域でベンチュリ部9-1により誘引されて燃焼することで燃料代替を果たし、燃料の節減と共に省エネルギに貢献する。 Aluminum chips accompanied by oil are conveyed in a filled state from a charging hopper 5-1 by a vertical or inclined screw conveyor 5-2, and are moved to the lower area of the filter 2-3 of the melting part 2-a of the melting furnace 2. Then, it is charged together with an inert gas ejected through the screw rotating shaft 5-2c. Further, the aluminum chips are bubbling of the inert gas injection and the diffusion of the stirrer 3 by the stirring of the stirrer blade 3-1 of the stirrer 3 and the injection of the nitrogen gas outlet 3-3 of the rotating shaft 3-2. As a result, the oil melts more quickly to become the molten metal M, and the oil is gasified. Next, the molten aluminum M passes under the partition wall 2-2 and moves to the molten metal part 2-b, and finally is discharged from the hot water tank 2-1. At this time, the molten metal M is prevented from flowing due to a short circuit by the partition wall 2-2, and by taking a long residence time, the molten metal M is sufficiently cleaned by levitating and separating impurities such as slag components. Further, the oil component is heated in the region under the filter 2-2 under the bubbling of the inert gas to be gasified without being oxidized, passes through the filter 2-2, floats up, and passes through the furnace upper space 2-4. Then, the fuel is replaced by the fuel by being attracted by the venturi section 9-1 in the combustion zone of the combustion burner 6 via the oil gas recovery duct 9 and burned, thereby contributing to energy saving and fuel saving.
また別に、油分を随伴したアルミニウム切粉は、装入ホッパ5-1から傾斜型装入プッシャー5-3により間歇的に、強制的にアルミニウム切粉を溶解炉2の溶解部2-aのフィルタ2-3下部域の溶湯M中に装入できる。また、近接したスターラ3の攪拌翼3-1の攪拌と、回転軸3-2の窒素ガス噴出し口3-3のインジェクションにより、装入アルミニウム切粉は拡散することにより迅速に溶解して溶湯Mになると共に、油分はガス化する。次いで、アルミニウム溶湯Mが隔壁2-2の下を通過して溶湯部2-bへ移動し、最終的には出湯樋2-1から出湯される。この際、隔壁2-2により溶湯Mが短絡して流れるのを防止し、滞留時間を長くとることで、不純物であるスラグ成分などを浮上・分離して、溶湯Mは十分清浄化される。また、油分は不活性ガスのバブリングのもと、フィルタ2-2下の領域で加熱されて酸化されることなくガス化して、フィルタ2-2を通過して浮上し、炉上部空間2-4に移動し、次いで油分ガス回収ダクト9を経由して燃焼バーナ6の燃焼域でベンチュリ部9-1により誘引されて燃焼することで燃料代替を果たし、燃料の節減と共に省エネルギに貢献する。 Separately, the aluminum chips accompanied with oil are intermittently forced from the charging hopper 5-1 by the inclined charging pusher 5-3 to filter the aluminum chips in the melting part 2-a of the melting furnace 2. 2-3 Can be charged into the molten metal M in the lower area. In addition, the charged aluminum chips are rapidly melted by diffusion by the stirring of the stirring blade 3-1 of the adjacent stirrer 3 and the injection of the nitrogen gas outlet 3-3 of the rotating shaft 3-2. As it becomes M, the oil is gasified. Next, the molten aluminum M passes under the partition wall 2-2 and moves to the molten metal part 2-b, and finally is discharged from the hot water tank 2-1. At this time, the molten metal M is prevented from flowing due to a short circuit by the partition wall 2-2, and by taking a long residence time, the molten metal M is sufficiently cleaned by levitating and separating impurities such as slag components. Further, the oil component is heated in the region under the filter 2-2 under the bubbling of the inert gas to be gasified without being oxidized, passes through the filter 2-2, floats up, and passes through the furnace upper space 2-4. Then, the fuel is replaced by the fuel by being attracted by the venturi section 9-1 in the combustion zone of the combustion burner 6 via the oil gas recovery duct 9 and burned, thereby contributing to energy saving and fuel saving.
なお、アルミニウム切粉に含まれる切削油は、本発明が対象とする油と水のエマルジョンで構成されるものとは別に、水を含まない、主として油で構成される切削油がある。このような水分の無い切削油を含んだアルミニウム切粉に対しても本発明のアルミニウム切粉溶解装置及び溶解方法の適用は十分可能である。この場合、水分が含まれない分だけ水分を蒸発させるエネルギが不要で、アルミニウム切粉自体の予熱温度も上昇しやすく、本装置によるアルミニウム切粉の処理能力が向上し易く、溶解に必要な熱エネルギも節約し易くなる。 The cutting oil contained in the aluminum chips includes cutting oil mainly composed of oil that does not contain water, apart from the oil composed of the oil and water targeted by the present invention. The aluminum chip melting apparatus and the melting method of the present invention can be sufficiently applied to aluminum chips containing cutting fluid having no moisture. In this case, there is no need for energy to evaporate water as much as it does not contain water, the preheating temperature of the aluminum chips themselves is likely to rise, the processing capacity of the aluminum chips by this device is easy to improve, and the heat required for melting It becomes easy to save energy.
前述したように、切削油を随伴しているアルミニウム切粉を原料として、その随伴水分を蒸発させ、かつ予熱したアルミニウム切粉を溶解することにより、アルミニウム溶湯Mを熱効率よく得ることができる。また、油分は溶解炉2でガス化して回収し、溶解炉2の燃料の代替として使用できるので、本発明は省資源、省エネルギに適したアルミニウム切粉溶解装置および方法である。 As described above, the molten aluminum M can be obtained with high thermal efficiency by using the aluminum chips accompanied with the cutting oil as a raw material, evaporating the accompanying moisture, and dissolving the preheated aluminum chips. In addition, since the oil component is gasified and recovered in the melting furnace 2 and can be used as a substitute for the fuel in the melting furnace 2, the present invention is an aluminum chip melting apparatus and method suitable for resource saving and energy saving.
アルミニウム切粉の処理分野で利用されるのみならず、亜鉛、マグネシウム金属及びそれらの合金切粉の処理分野で適用することができる。 Not only can it be used in the field of processing aluminum chips, but it can also be applied in the field of processing of zinc, magnesium metal and their alloy chips.
1:アルミニウム切粉溶解装置  
2:ルツボ型溶解炉  2-a:溶解部  2-b:溶湯部
2-1:出湯樋   2-1b:溶湯鍋
2-2:隔壁  2-3:フィルタ 2-4:炉上部空間  2-5:炉載置台3:スターラ 3-1:攪拌翼  3-2:回転軸 3-3:窒素ガス噴出し口
3-4;窒素ガス配管
4:乾燥・予熱装置  4-1:装入ホッパ  4-2:スクリュコンベヤ
4-2a:スクリュ羽根 4-2b:コンベヤ外筒 4-2c:装入部
4-2d:排出端 4-2e:駆動ギヤードモータ
4-3:乾燥・予熱室  4-3a:ガス入口  4-3b:ガス出口
4-3c:温度計  4-3d:室内圧力計
5:切粉装入装置  5-1装入ホッパ 5-2:装入スクリュコンベヤ
5-2a:スクリュ羽根 5-2b:コンベヤ外筒 5-2c:スクリュ回転軸
5-2d:駆動ギヤードモータ 5-2e:吹込み窒素流入口
5-2f:窒素噴出し口  5-3:蒸気排出弁 5-4:装入プッシャー
5-4a:駆動用ロッドレスシリンダ 5-4b:プッシャ先端部
6:溶解炉燃焼バーナ 
7:溶解炉燃焼室 7-1:炉壁耐火物  7-2:炉蓋耐火物
8:燃焼排ガスダクト  8-1:希釈エア入口  8-2:ダンパ
9:油分ガス回収ダクト 9-1:誘引ベンチュリ部
M:溶湯
1: Aluminum chip melting device
2: crucible melting furnace 2-a: melting part 2-b: molten metal part 2-1: tapping pot 2-1b: molten metal pan 2-2: partition wall 2-3: filter 2-4: furnace upper space 2-5 : Furnace mounting table 3: Stirrer 3-1: Stirring blade 3-2: Rotating shaft 3-3: Nitrogen gas outlet 3-4; Nitrogen gas pipe 4: Drying / preheating device 4-1: Charge hopper 4- 2: Screw conveyor 4-2a: Screw blade 4-2b: Conveyor cylinder 4-2c: Loading section 4-2d: Discharge end 4-2e: Drive geared motor 4-3: Drying / preheating chamber 4-3a: Gas Inlet 4-3b: Gas outlet 4-3c: Thermometer 4-3d: Indoor pressure gauge 5: Chip charging device 5-1, charging hopper 5-2: charging screw conveyor 5-2a: screw blade 5-2b : Conveyor outer cylinder 5-2c: Screw rotating shaft 5-2d: Drive geared motor 5-2e Blowing nitrogen inlet 5-2F: nitrogen blowing mouth 5-3: steam discharge valve 5-4: loading pusher 5-4A: driving rodless cylinder 5-4B: pusher tip 6: melting furnace combustion burner
7: Melting furnace combustion chamber 7-1: Furnace wall refractory 7-2: Furnace lid refractory 8: Combustion exhaust gas duct 8-1: Dilution air inlet 8-2: Damper 9: Oil gas recovery duct 9-1: Induction Venturi M: Molten metal

Claims (12)

  1. アルミニウム切粉の付着切削油中の水分を除去する乾燥・予熱手段と、該乾燥・予熱したアルミニウム切粉をルツボ型溶解炉の溶湯中に装入する装入手段と、燃焼バーナにより間接加熱した該ルツボ型溶解炉を用いて該乾燥・予熱したアルミニウム切粉を溶解してアルミニウム溶湯を製造するアルミニウム溶解手段と、を備え、該乾燥・予熱したアルミニウム切粉中に残留させた油分を該ルツボ型溶解炉で該アルミニウム切粉を溶解した際にガス化させて該燃焼バーナへ誘引して燃焼させる油分ガス化燃焼手段を設けたことを特徴とするアルミニウム切粉溶解装置。 Drying / preheating means for removing moisture in cutting oil, charging means for charging the dried / preheated aluminum chips into the molten metal of the crucible melting furnace, and indirect heating with a combustion burner An aluminum melting means for producing a molten aluminum by melting the dried and preheated aluminum chips using the crucible melting furnace, and the oil remaining in the dried and preheated aluminum chips is removed from the crucible. An aluminum chip melting apparatus comprising oil gasification combustion means that gasifies and melts the aluminum chips in a mold melting furnace and induces them into the combustion burner for combustion.
  2. 前記乾燥・予熱手段が、アルミニウム切粉を密閉した乾燥・予熱スクリュコンベヤで運搬すると共に、該スクリュコンベヤの外周壁を前記ルツボ型溶解炉からの燃焼排ガスを温度調整して加熱することにより該アルミニウム切粉を乾燥・予熱することを特徴とする請求項1記載のアルミニウム切粉溶解装置。 The drying / preheating means conveys the aluminum chips by a dry / preheating screw conveyor in which aluminum chips are sealed, and heats the outer peripheral wall of the screw conveyor by adjusting the temperature of the combustion exhaust gas from the crucible melting furnace. The aluminum chip melting apparatus according to claim 1, wherein the chip is dried and preheated.
  3. 前記ルツボ型溶解炉が、溶湯溜りの深さ方向に耐火物製の隔壁により出湯樋に連なる溶湯部と、溶解部と、に区分けし、さらに該溶解部の溶湯面より下で水平方向の断面全体に亘って耐火物製のフィルタを備え、前記乾燥・予熱したアルミニウム切粉が前記装入手段により該フィルタ下部の溶湯中に装入して、該アルミニウム切粉を溶解すると共に、該アルミニウム切粉に随伴する切削油由来の油分をガス化して該溶解部上面から油分ガスを取り出して前記燃焼バーナの燃焼に供することを特徴とする請求項1又は2に記載のアルミニウム切粉溶解装置。 The crucible type melting furnace is divided into a molten metal part connected to a tapping pot by a refractory partition in the depth direction of the molten metal pool, and a molten part, and a horizontal cross section below the molten metal surface of the molten part A filter made of refractory material is provided throughout, and the dried and preheated aluminum chips are charged into the molten metal under the filter by the charging means to dissolve the aluminum chips, and the aluminum chips. 3. The aluminum chip melting apparatus according to claim 1, wherein an oil component derived from a cutting oil accompanying the powder is gasified and the oil component gas is taken out from the upper surface of the melting portion and used for combustion of the combustion burner.
  4. 前記ルツボ型溶解炉の溶解部が、前記乾燥・予熱したアルミニウム切粉を前記フィルタ下部の溶湯中に装入する前記装入手段に近接して、回転する攪拌翼と、回転軸から窒素又はアルゴンの不活性ガスをインジェクションできるスターラを備え、該スターラにより該アルミニウム切粉の溶解を促進させることを特徴とする請求項3記載のアルミニウム切粉溶解装置。 The melting part of the crucible melting furnace is in close proximity to the charging means for charging the dried and preheated aluminum chips into the molten metal under the filter, and a rotating stirring blade and nitrogen or argon from the rotating shaft An aluminum chip melting apparatus according to claim 3, further comprising a stirrer capable of injecting said inert gas, wherein the stirrer promotes dissolution of the aluminum chip.
  5. 前記装入手段が、前記乾燥・予熱スクリュコンベヤの排出端が上部に蒸気排出弁を設けた密閉式の装入ホッパー内の上部に接続開口されており、該装入ホッパー下部から竪型又は傾斜型の装入スクリュコンベヤが前記ルツボ型溶解炉の溶解部フィルタ下方にその下端を浸漬するように設けられ、前記乾燥・予熱したアルミニウム切粉を該装入スクリュコンベヤにより、また、窒素又はアルゴンガスの不活性ガスを該装入スクリュコンベヤ回転軸管から、共に溶湯中に装入することを特徴とする請求項1から4のいずれかに記載のアルミニウム切粉溶解装置。 The charging means has a discharge opening of the drying / preheating screw conveyor connected to an upper portion of a closed charging hopper provided with a steam discharge valve at an upper portion, and is formed in a vertical or inclined manner from the lower portion of the charging hopper. A mold charging screw conveyor is provided so that its lower end is immersed below the melting part filter of the crucible melting furnace, and the dried and preheated aluminum chips are fed into the charging screw conveyor by nitrogen or argon gas. 5. The aluminum chip melting apparatus according to claim 1, wherein both of the inert gas are charged into the molten metal from the charging screw conveyor rotary shaft tube.
  6. 前記装入手段が、前記密閉型スクリュコンベヤの排出端が上部に蒸気排出弁を設けた密閉式の装入ホッパー内の上部に接続開口されており、該装入ホッパー下部から傾斜型のプッシャーが前記ルツボ型溶解炉の溶解部フィルタ下方にその下端を浸漬するように設けられ、前記乾燥・予熱したアルミニウム切粉を該プッシャーにより溶湯中に装入することを特徴とする請求項1から4のいずれかに記載のアルミニウム切粉溶解装置。 The charging means has a discharge opening of the closed screw conveyor connected to an upper portion of a closed charging hopper provided with a steam discharge valve at an upper portion, and an inclined pusher is provided from the lower portion of the charging hopper. 5. The crucible type melting furnace is provided so that a lower end thereof is immersed below a melting part filter, and the dried and preheated aluminum chips are charged into the molten metal by the pusher. The aluminum chip melting apparatus according to any one of the above.
  7. 前記油分ガス化燃焼手段が、前記ルツボ型溶解炉の溶解部及び溶湯部の上部空間から前記燃焼バーナの燃焼部につながる配管を備えると共に、該配管の末端に該燃焼部へとつながるベンチュリ部を備え、前記乾燥・予熱したアルミニウム切粉を前記溶解炉の溶解部で溶解する際に発生した油分ガスを回収して前記溶解炉の燃焼バーナへ誘引して燃焼させることを特徴とする請求項1から6のいずれかに記載のアルミニウム切粉溶解装置。 The oil gasification combustion means includes a pipe connected to the combustion part of the combustion burner from an upper space of the melting part and the molten metal part of the crucible melting furnace, and a venturi part connected to the combustion part at the end of the pipe The oil gas generated when the dried and preheated aluminum chips are melted in the melting section of the melting furnace is collected and attracted to the combustion burner of the melting furnace to be burned. To 6. The aluminum chip melting apparatus according to any one of 6 to 6.
  8. 前記乾燥・予熱手段が、前記アルミニウム切粉の乾燥・予熱する温度が125℃から145℃の範囲であって、好ましくは135℃にすることを特徴とする請求項1から7のいずれかに記載のアルミニウム切粉溶解装置。 8. The drying / preheating means for drying / preheating the aluminum chips in a range of 125 [deg.] C. to 145 [deg.] C., preferably 135 [deg.] C. Aluminum chip melting equipment.
  9. 前記乾燥・予熱手段が、乾燥・予熱処理後のアルミニウム切粉の水分を5%以下にすること、好ましくは1%以下にすることを特徴とする請求項1から8のいずれかに記載のアルミニウム切粉溶解装置。 The aluminum according to any one of claims 1 to 8, wherein the drying / preheating means makes the moisture of the aluminum chips after the drying / preheating treatment 5% or less, preferably 1% or less. Chip melting device.
  10. 前記アルミニウム切粉溶解装置の前段に、遠心油水分離機を備え、遠心油水分離機によりアルミニウム切粉の付着切削油量を減少する前処理を行うことを特徴とする請求項1から9のいずれかに記載のアルミニウム切粉溶解装置。 The centrifugal oil / water separator is provided in the preceding stage of the aluminum chip dissolving device, and the pretreatment for reducing the amount of cutting oil adhering to the aluminum chip is performed by the centrifugal oil / water separator. An aluminum chip melting apparatus according to claim 1.
  11. 切削油が付着しているアルミニウム切粉を溶解する方法であって、該アルミニウム切粉を125℃から145℃の範囲に、好ましくは135℃にルツボ型溶解炉の排ガスを利用して間接加熱することにより乾燥・予熱して、切削油中の水分を蒸発除去し、次いで、該乾燥・予熱したアルミニウム切粉を燃焼バーナで加熱する該ルツボ型溶解炉の溶解部の溶湯アルミニウム中に装入して溶解することにより、切削油中の油分はガス化して、そのガスを該ルツボ型溶解炉の間接加熱用燃料として補填して使用すると共に、溶解したアルミニウムは、該ルツボ型溶解炉の溶解部から溶湯部へ溶湯のみを移行させて清浄なアルミニウム溶湯を得ることを特徴とするアルミニウム切粉の溶解方法。 A method for melting aluminum chips to which cutting oil is adhered, wherein the aluminum chips are indirectly heated to 125 ° C. to 145 ° C., preferably 135 ° C., using the exhaust gas from a crucible melting furnace. Then, the moisture in the cutting oil is evaporated and removed, and then the dried and preheated aluminum chips are charged into the molten aluminum in the melting portion of the crucible melting furnace heated by a combustion burner. As a result, the oil in the cutting oil is gasified and used as a fuel for indirect heating of the crucible melting furnace, and the dissolved aluminum is used as a melting part of the crucible melting furnace. A method for melting aluminum chips, wherein only molten metal is transferred from a molten metal to a molten metal portion to obtain a clean molten aluminum.
  12. 該乾燥・予熱したアルミニウム切粉を該ルツボ型溶解炉の溶解部の溶湯アルミニウム中に装入して溶解する際に、機械式スターラ又は不活性ガスインジェクションにより攪拌混合して溶解及び油分ガス化を促進することを特徴とする請求項11記載のアルミニウム切粉の溶解方法。 When the dried and preheated aluminum chips are charged and melted in the molten aluminum in the melting part of the crucible melting furnace, they are stirred and mixed by a mechanical stirrer or inert gas injection to dissolve and gasify the oil. The method for melting aluminum chips according to claim 11, wherein the method is promoted.
PCT/JP2016/069969 2015-09-26 2016-07-06 Aluminum chip melting apparatus and melting method WO2017051586A1 (en)

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JP2019183275A (en) * 2018-03-30 2019-10-24 株式会社広築 Melting method and melting unit of aluminum chip
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JP2019183275A (en) * 2018-03-30 2019-10-24 株式会社広築 Melting method and melting unit of aluminum chip
CN109059540A (en) * 2018-08-21 2018-12-21 陈孝 A kind of waste aluminum smelting furnace
CN109883197A (en) * 2019-03-22 2019-06-14 陈孝 A kind of aluminum profile smelting furnace
CN114340816A (en) * 2019-11-15 2022-04-12 株式会社东热 Metal melting device, sieve plate for metal melting, and metal melting method
WO2021095731A1 (en) * 2019-11-15 2021-05-20 株式会社トウネツ Metal melting device, screen plate for melting metal, and method for melting metal
CN114340816B (en) * 2019-11-15 2024-04-05 株式会社东热 Metal melting device, screen plate for metal melting, and metal melting method
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CN111020218A (en) * 2019-12-27 2020-04-17 浙江铂大工贸有限公司 Aluminum skimmings waste liquid recovery processing device
CN111020218B (en) * 2019-12-27 2022-06-21 浙江铂大工贸有限公司 Aluminum skimmings waste liquid recovery processing device
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WO2021235008A1 (en) * 2020-05-22 2021-11-25 株式会社広築 Method and apparatus for melting aluminum cutting chips
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