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JP6879063B2 - Recovery sand cooling system and recovery sand cooling method - Google Patents
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JP6879063B2 - Recovery sand cooling system and recovery sand cooling method - Google Patents

Recovery sand cooling system and recovery sand cooling method Download PDF

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JP6879063B2
JP6879063B2 JP2017114143A JP2017114143A JP6879063B2 JP 6879063 B2 JP6879063 B2 JP 6879063B2 JP 2017114143 A JP2017114143 A JP 2017114143A JP 2017114143 A JP2017114143 A JP 2017114143A JP 6879063 B2 JP6879063 B2 JP 6879063B2
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sand
water
air
temperature
recovered
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JP2018202473A (en
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裕一 小倉
裕一 小倉
酒井 毅
酒井  毅
原田 久
久 原田
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Sintokogio Ltd
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Sintokogio Ltd
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Priority to EP17850794.3A priority patent/EP3513887A4/en
Priority to PCT/JP2017/032307 priority patent/WO2018051891A1/en
Priority to US16/327,052 priority patent/US20190193141A1/en
Priority to CN201780056706.1A priority patent/CN109715314B/en
Priority to MX2019002661A priority patent/MX2019002661A/en
Priority to KR1020197006889A priority patent/KR20190044632A/en
Priority to BR112019004825A priority patent/BR112019004825A2/en
Priority to TW106131255A priority patent/TW201811460A/en
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Description

本発明は、生型鋳型に好適な、回収砂冷却システム及び回収砂冷却方法に関するものである。 The present invention relates to a recovered sand cooling system and a recovered sand cooling method suitable for a green mold.

周知のように、生型砂を鋳型として使用した鋳造方法である生型鋳造が、広く行われている。生型鋳造においては、鋳型の中に鋳込まれた溶湯金属が凝固した後に、型ばらしがなされて、鋳物から、鋳型として使用された砂が分離される。分離された砂は、回収砂として回収され、異物除去や砂冷却が行われた後に混練調整されて、生型の造型に再度使用される。 As is well known, green casting, which is a casting method using green sand as a mold, is widely used. In green casting, after the molten metal cast in the mold solidifies, the mold is disassembled to separate the sand used as the mold from the casting. The separated sand is recovered as recovered sand, kneaded and adjusted after foreign matter is removed and sand is cooled, and is used again for green mold molding.

回収砂の砂温や水分は後の混練工程や造型工程に影響を及ぼす。特に回収砂の砂温が高い状態で混練工程や造型工程に生型砂が送られると、混練機前に設置される生型砂貯留用ホッパの内壁に水分の凝集が原因の砂付着が発生する。また、混練後の砂の乾燥が早まることにより砂同士の結合力が低下し、鋳型の型落ちや砂かみなどの造型不良の原因となる可能性もある。 The sand temperature and moisture of the recovered sand affect the subsequent kneading process and molding process. In particular, when the raw sand is sent to the kneading process or the molding process when the sand temperature of the recovered sand is high, sand adhesion due to the aggregation of water occurs on the inner wall of the raw sand storage hopper installed in front of the kneading machine. In addition, the accelerated drying of the sand after kneading reduces the binding force between the sands, which may cause mold loss, sand biting, and other molding defects.

回収砂の冷却は、回収砂に含まれる水分が空気中に蒸発する時の蒸発潜熱を利用して行われることが多い。このような、水分の蒸発潜熱を利用した回収砂の冷却においては、回収砂を目標とする温度に冷却し、なおかつ、冷却後の回収砂が一定の水分量を有するように、冷却前に水が回収砂に散水される。この散水量は、冷却前の回収砂の、量、温度及び水分量の測定値を基に決定される。特許文献1には、上記の各測定値に加え、冷却後の回収砂の温度を基に、散水量を決定することが開示されている。 Cooling of the recovered sand is often performed by utilizing the latent heat of vaporization when the moisture contained in the recovered sand evaporates into the air. In such cooling of the recovered sand using the latent heat of evaporation of water, water is cooled before cooling so that the recovered sand is cooled to a target temperature and the recovered sand after cooling has a certain amount of water. Is sprinkled on the recovered sand. The amount of water sprinkled is determined based on the measured values of the amount, temperature and water content of the recovered sand before cooling. Patent Document 1 discloses that the amount of water sprinkled is determined based on the temperature of the recovered sand after cooling in addition to the above-mentioned measured values.

特公昭62−40098号公報Special Publication No. 62-40998

水の蒸発量は、周囲の空気の状態に大きく依存する。しかし、特許文献1は、冷却装置中の空気の状態を考慮することに関して開示がなされていないため、特許文献1に開示されている方法においては、空気の状態によって、回収砂の冷却度合いや、冷却後の回収砂の水分量にばらつきが生じる可能性がある。したがって、安定した冷却、含水結果を得るのが容易ではなく、回収砂の冷却を常に確実に行うことが難しい。 The amount of water evaporation largely depends on the condition of the surrounding air. However, since Patent Document 1 does not disclose the consideration of the state of air in the cooling device, in the method disclosed in Patent Document 1, the degree of cooling of the recovered sand and the degree of cooling of the recovered sand depend on the state of air. The amount of water in the recovered sand after cooling may vary. Therefore, it is not easy to obtain stable cooling and water content results, and it is difficult to always reliably cool the recovered sand.

本発明が解決しようとする課題は、回収砂を確実に冷却することが可能な、回収砂冷却システム及び回収砂冷却方法を提供することである。 An object to be solved by the present invention is to provide a recovered sand cooling system and a recovered sand cooling method capable of reliably cooling the recovered sand.

本発明による回収砂冷却システムは、回収砂を冷却し、冷却回収砂の水分量を調整するものであって、前記回収砂の水分量と温度を測定する砂水分温度測定器と、前記回収砂に加える水の量である、適正加水量を決定する制御装置と、前記適正加水量の水を前記回収砂に加え、水の蒸発潜熱で冷却して前記冷却回収砂とする散水冷却装置と、該散水冷却装置に空気を導入する空気導入装置と、前記散水冷却装置に導入される導入空気の温度を測定する導入空気温度測定器と、を備え、前記制御装置は、前記回収砂の水分量と温度、及び、前記導入空気の温度を基に、前記適正加水量を決定する。 The recovered sand cooling system according to the present invention cools the recovered sand and adjusts the water content of the cooled recovered sand, and is a sand moisture temperature measuring device for measuring the water content and temperature of the recovered sand, and the recovered sand. A control device for determining an appropriate amount of water to be added to the water, and a sprinkling cooling device for adding the appropriate amount of water to the recovered sand and cooling it with the latent heat of evaporation of water to obtain the cooling recovered sand. The control device includes an air introduction device that introduces air into the sprinkler cooling device and an introduction air temperature measuring device that measures the temperature of the introduction air introduced into the sprinkler cooling device. The appropriate amount of water added is determined based on the temperature and the temperature of the introduced air.

また、本発明による回収砂冷却システムは、回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却システムであって、前記回収砂の水分量と温度を測定する砂水分温度測定器と、前記回収砂に加える水の量である、適正加水量を決定する制御装置と、前記適正加水量の水を前記回収砂に加え、水の蒸発潜熱で冷却して前記冷却回収砂とする散水冷却装置と、該散水冷却装置に空気を導入する空気導入装置と、前記冷却回収砂の水分量と温度を測定する冷却回収砂水分温度測定器と、を備え、前記制御装置は、前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を基に、前記適正加水量を決定する。 Further, the recovered sand cooling system according to the present invention is a recovered sand cooling system that cools the recovered sand and adjusts the water content of the cooled recovered sand, and is a sand moisture temperature measuring device that measures the water content and temperature of the recovered sand. A control device for determining an appropriate amount of water to be added to the recovered sand, and water having an appropriate amount of water added to the recovered sand and cooled by the latent heat of evaporation of water to obtain the cooled recovered sand. The sprinkling cooling device, an air introducing device for introducing air into the sprinkling cooling device, and a cooling recovery sand moisture temperature measuring device for measuring the water content and temperature of the cooling recovery sand are provided, and the control device comprises the recovery. The appropriate amount of water added is determined based on the amount of water and temperature of the sand and the amount of water and temperature of the cooled recovery sand.

また、本発明による回収砂冷却方法は、回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却方法であって、前記回収砂の水分量と温度を測定し、前記回収砂に加える水の量である、適正加水量を決定し、前記適正加水量の水を前記回収砂に加え、空気を導入しながら水の蒸発潜熱で冷却して、前記冷却回収砂とし、導入される導入空気の温度を測定することを含むものであり、前記回収砂の水分量と温度、及び、前記導入空気の温度を基に、前記適正加水量を決定する。 Further, the recovered sand cooling method according to the present invention is a recovered sand cooling method in which the recovered sand is cooled and the water content of the cooled recovered sand is adjusted, and the water content and temperature of the recovered sand are measured and the recovered sand is used. The appropriate amount of water to be added, which is the amount of water to be added, is determined, the amount of water to be added is added to the recovered sand, and the sand is cooled by the latent heat of evaporation of water while introducing air to obtain the cooled recovered sand. It includes measuring the temperature of the introduced air, and determines the appropriate amount of water added based on the water content and temperature of the recovered sand and the temperature of the introduced air.

また、本発明による回収砂冷却方法は、回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却方法であって、前記回収砂の水分量と温度を測定し、前記回収砂に加える水の量である、適正加水量を決定し、前記適正加水量の水を前記回収砂に加え、空気を導入しながら水の蒸発潜熱で冷却して、前記冷却回収砂とし、前記冷却回収砂の水分量と温度を測定することを含むものであり、前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を基に、前記適正加水量を決定する。 Further, the recovered sand cooling method according to the present invention is a recovered sand cooling method in which the recovered sand is cooled and the water content of the cooled recovered sand is adjusted, and the water content and temperature of the recovered sand are measured and the recovered sand is used. The appropriate amount of water to be added, which is the amount of water to be added, is determined, and the water of the appropriate amount of water is added to the recovered sand and cooled by the latent heat of evaporation of water while introducing air to obtain the cooled recovered sand, which is cooled and recovered. It includes measuring the water content and temperature of the sand, and determines the appropriate water content based on the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand.

本発明によれば、回収砂を確実に冷却することが可能な、回収砂冷却システム及び回収砂冷却方法を、提供することが可能となる。 According to the present invention, it is possible to provide a recovered sand cooling system and a recovered sand cooling method capable of reliably cooling the recovered sand.

本発明の第一の実施形態として示した回収砂冷却システムの概略構成図である。It is a schematic block diagram of the recovered sand cooling system shown as the 1st Embodiment of this invention. 本発明の第一の実施形態として示した回収砂冷却システムにおける制御装置のブロック図である。It is a block diagram of the control device in the recovered sand cooling system shown as the 1st Embodiment of this invention. 本発明の第二の実施形態として示した回収砂冷却システムの概略構成図である。It is a schematic block diagram of the recovered sand cooling system shown as the 2nd Embodiment of this invention. 本発明の第二の実施形態として示した回収砂冷却システムにおける制御装置のブロック図である。It is a block diagram of the control device in the recovered sand cooling system shown as the 2nd Embodiment of this invention.

以下、本発明の実施形態について図面を参照して詳細に説明する。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.

図1は、本発明の第一の実施形態として示した回収砂冷却システム1の概略構成図である。回収砂とは、生型鋳造において、鋳型の中に鋳込まれた溶湯金属が凝固した後に、鋳型として使用された砂が鋳物から分離されたものである。回収砂は、異物除去や砂冷却が行われた後に混練調整されて、生型の造型に再度使用される。回収砂冷却システム1は、特に生型鋳型における生型回収砂を冷却し、冷却回収砂の水分を調整するシステムである。 FIG. 1 is a schematic configuration diagram of the recovered sand cooling system 1 shown as the first embodiment of the present invention. The recovered sand is the sand used as a mold separated from the casting after the molten metal cast in the mold is solidified in the green casting. The recovered sand is kneaded and adjusted after foreign matter is removed and sand is cooled, and is used again for green mold molding. The recovered sand cooling system 1 is a system that cools the raw recovered sand, especially in the green mold, and adjusts the water content of the cooled recovered sand.

回収砂冷却システム1は、回収砂の水分量と温度を測定する砂水分温度測定器2と、回収砂に加える水の量である、適正加水量を決定する制御装置3と、適正加水量の水を回収砂に加え、水の蒸発潜熱で冷却して冷却回収砂とする散水冷却装置4、5と、砂冷却装置に空気を導入する空気導入装置6と、砂冷却装置に導入される導入空気の温度を測定する導入空気温度測定器7と、を備えている。 The recovered sand cooling system 1 includes a sand moisture temperature measuring device 2 that measures the water content and temperature of the recovered sand, a control device 3 that determines the appropriate amount of water added to the recovered sand, and an appropriate amount of water added. Sprinkler cooling devices 4 and 5 that add water to the recovered sand and cool it with the latent heat of evaporation of water to make it cooled and recovered sand, an air introduction device 6 that introduces air into the sand cooling device, and an introduction introduced into the sand cooling device. An introduction air temperature measuring device 7 for measuring the temperature of air is provided.

以下、回収砂冷却システム1を詳細に説明する。回収砂冷却システム1は、ホッパ8、及びベルトフィーダー9を備えている。ホッパ8には、鋳物から分離された回収砂が貯蔵されている。ベルトフィーダー9は、ホッパ8の下に設けられている。ホッパ8内に貯蔵されている回収砂は、ホッパ8に設けられた回収砂供給口(図示無し)から、ベルトフィーダー9に対して供給される。 Hereinafter, the recovered sand cooling system 1 will be described in detail. The recovered sand cooling system 1 includes a hopper 8 and a belt feeder 9. The hopper 8 stores the recovered sand separated from the casting. The belt feeder 9 is provided below the hopper 8. The recovered sand stored in the hopper 8 is supplied to the belt feeder 9 from a recovered sand supply port (not shown) provided in the hopper 8.

ベルトフィーダー9は、インバータモータ10を備えており、このインバータモータ10によって駆動されている。インバータモータ10には、後述する制御装置3が電気的に接続されており、制御装置3からの信号に従い、インバータモータ10の回転速度が変化するように構成されている。これにより、ベルトフィーダー9に供給された回収砂は、散水冷却装置4、5へと搬送される。 The belt feeder 9 includes an inverter motor 10 and is driven by the inverter motor 10. A control device 3 described later is electrically connected to the inverter motor 10, and the rotation speed of the inverter motor 10 is changed according to a signal from the control device 3. As a result, the recovered sand supplied to the belt feeder 9 is conveyed to the sprinkler cooling devices 4 and 5.

砂水分温度測定器2は、ベルトフィーダー9上に設けられている。ベルトフィーダー9上を搬送される回収砂は、砂水分温度測定器2によって、水分量と温度が測定される。砂水分温度測定器2には、後述する制御装置3が電気的に接続されており、砂水分温度測定器2によって測定された回収砂の水分量と温度は、制御装置3に送信される。 The sand moisture temperature measuring device 2 is provided on the belt feeder 9. The water content and temperature of the recovered sand transported on the belt feeder 9 are measured by the sand water content temperature measuring device 2. A control device 3 described later is electrically connected to the sand moisture temperature measuring device 2, and the moisture content and temperature of the recovered sand measured by the sand moisture temperature measuring device 2 are transmitted to the control device 3.

散水冷却装置4、5は、散水装置4と、砂冷却装置5を備えている。回収砂冷却システム1は、水源11、及び水量調整弁12を備えており、水源11は散水装置4に接続されて、散水装置4に水を供給する。散水装置4は、ベルトフィーダー9から投入された回収砂に対して水源11から供給される水を散水した後に、回収砂を撹拌して、回収砂中に水分を分散させる。この、散水されて水分が分散された回収砂を、加水回収砂と呼称する。 The watering cooling devices 4 and 5 include a watering device 4 and a sand cooling device 5. The recovered sand cooling system 1 includes a water source 11 and a water amount adjusting valve 12, and the water source 11 is connected to the watering device 4 to supply water to the watering device 4. The sprinkler 4 sprinkles the water supplied from the water source 11 on the recovered sand input from the belt feeder 9, and then stirs the recovered sand to disperse the water in the recovered sand. This recovered sand that has been sprinkled with water and dispersed with water is called water-recovered sand.

水量調整弁12は、水源11と散水装置4の間に介装されている。水量調整弁12には、後述する制御装置3が電気的に接続されている。水量調整弁12は、水源11から散水装置4に供給される水の量が、制御装置3の算出した、回収砂に加える適正な水の量である適正加水量の値となるように、制御装置3によって制御される。これにより、散水装置4は、適正加水量の水を回収砂に加えて加水回収砂としている。 The water amount adjusting valve 12 is interposed between the water source 11 and the watering device 4. A control device 3 described later is electrically connected to the water amount adjusting valve 12. The water amount adjusting valve 12 is controlled so that the amount of water supplied from the water source 11 to the watering device 4 becomes the value of the appropriate amount of water added, which is the appropriate amount of water to be added to the recovered sand calculated by the control device 3. It is controlled by the device 3. As a result, the watering device 4 adds an appropriate amount of water to the recovered sand to make the water recovered sand.

散水装置4により撹拌されて水分が分散された加水回収砂は、散水装置4から排出されて、砂冷却装置5に投入される。砂冷却装置5は、加水回収砂を砂冷却装置5内の空気に接触させることにより冷却する。冷却された回収砂を、冷却回収砂と呼称する。 The water-recovered sand that has been agitated by the watering device 4 and dispersed with water is discharged from the watering device 4 and put into the sand cooling device 5. The sand cooling device 5 cools the water recovery sand by bringing it into contact with the air in the sand cooling device 5. The cooled recovery sand is called a cooled recovery sand.

回収砂冷却システム1は、空気加熱装置13と、集塵装置14を備えている。空気加熱装置13、砂冷却装置5、集塵装置14、及び空気導入装置6によって、空気がこの順に流れるように、1本の空気流路が形成されている。この空気流路の末端に設けられた空気導入装置6は、空気を上流の空気加熱装置13の方向から吸引することで空気流路内に空気の流れを作り出し、砂冷却装置5に空気を導入する、吸引型の装置である。 The recovered sand cooling system 1 includes an air heating device 13 and a dust collector 14. An air flow path is formed by an air heating device 13, a sand cooling device 5, a dust collector 14, and an air introduction device 6 so that air flows in this order. The air introduction device 6 provided at the end of the air flow path creates an air flow in the air flow path by sucking air from the direction of the upstream air heating device 13, and introduces the air into the sand cooling device 5. It is a suction type device.

空気加熱装置13は、この空気流路の最上流に設けられている。空気加熱装置13は、空気導入装置6の吸引によって外気または室内雰囲気から取り込まれた空気を、必要に応じて加熱して、導入空気として砂冷却装置5へ空気を導入する。空気加熱装置13には、後述する制御装置3が電気的に接続されている。空気加熱装置13は、砂冷却装置5へ導入される導入空気の温度が、制御装置3の算出した適正な空気温度となるように、制御装置3によって制御されて、導入空気を加熱する。 The air heating device 13 is provided at the uppermost stream of this air flow path. The air heating device 13 heats the air taken in from the outside air or the indoor atmosphere by the suction of the air introduction device 6 as necessary, and introduces the air into the sand cooling device 5 as the introduction air. A control device 3 described later is electrically connected to the air heating device 13. The air heating device 13 is controlled by the control device 3 so that the temperature of the introduced air introduced into the sand cooling device 5 becomes an appropriate air temperature calculated by the control device 3 to heat the introduced air.

砂冷却装置5において、加水回収砂からの水の蒸発と砂からの伝熱により温度、湿度が高まった排出空気は、集塵装置14に導入される。集塵装置14は、集塵装置14に導入された砂冷却装置5内を含む空気流路内の粉塵を除去する。粉塵が除去された空気は、空気導入装置6を介して外気へ排出される。 In the sand cooling device 5, the exhaust air whose temperature and humidity have increased due to the evaporation of water from the water recovery sand and the heat transfer from the sand is introduced into the dust collector 14. The dust collector 14 removes dust in the air flow path including the inside of the sand cooling device 5 introduced into the dust collector 14. The air from which the dust has been removed is discharged to the outside air via the air introduction device 6.

空気導入装置6は、インバータモータ15を備えており、このインバータモータ15によって駆動される。インバータモータ15には、後述する制御装置3が電気的に接続されている。インバータモータ15は、空気導入装置6の空気吸引量が、制御装置3の算出した適正な風量となるように、制御装置3によって制御されている。 The air introduction device 6 includes an inverter motor 15 and is driven by the inverter motor 15. A control device 3 described later is electrically connected to the inverter motor 15. The inverter motor 15 is controlled by the control device 3 so that the air suction amount of the air introduction device 6 becomes an appropriate air volume calculated by the control device 3.

回収砂冷却システム1は、上記した空気流路における空気の状態を測定するために、導入空気温度測定器7、排出空気温度測定器16、及び、風量測定器17を備えている。導入空気温度測定器7は、空気加熱装置13と砂冷却装置5の間に設けられており、砂冷却装置5に導入される導入空気の温度を測定する。導入空気温度測定器7には、後述する制御装置3が電気的に接続されている。導入空気温度測定器7によって測定された導入空気の温度は、制御装置3に送信される。 The recovered sand cooling system 1 includes an introduced air temperature measuring device 7, an exhaust air temperature measuring device 16, and an air volume measuring device 17 in order to measure the state of air in the above-mentioned air flow path. The introduced air temperature measuring device 7 is provided between the air heating device 13 and the sand cooling device 5, and measures the temperature of the introduced air introduced into the sand cooling device 5. A control device 3 described later is electrically connected to the introduced air temperature measuring device 7. The temperature of the introduced air measured by the introduced air temperature measuring device 7 is transmitted to the control device 3.

排出空気温度測定器16は、砂冷却装置5と集塵装置14の間に設けられており、砂冷却装置5から排出される排出空気の温度を測定する。排出空気温度測定器16には、後述する制御装置3が電気的に接続されている。排出空気温度測定器16によって測定された排出空気の温度は、制御装置3に送信される。 The exhaust air temperature measuring device 16 is provided between the sand cooling device 5 and the dust collector 14 and measures the temperature of the exhaust air discharged from the sand cooling device 5. A control device 3 described later is electrically connected to the exhaust air temperature measuring device 16. The temperature of the exhaust air measured by the exhaust air temperature measuring device 16 is transmitted to the control device 3.

風量測定器17は、集塵装置14と空気導入装置6の間に設けられており、空気導入装置6によって吸入される空気の量、すなわち、砂冷却装置5へと導入される導入空気の風量を測定する。風量測定器17には、後述する制御装置3が電気的に接続されている。風量測定器17によって測定された導入空気の風量は、制御装置3に送信される。 The air volume measuring device 17 is provided between the dust collector 14 and the air introduction device 6, and the amount of air sucked by the air introduction device 6, that is, the air volume of the introduced air introduced into the sand cooling device 5. To measure. A control device 3 described later is electrically connected to the air volume measuring device 17. The air volume of the introduced air measured by the air volume measuring device 17 is transmitted to the control device 3.

回収砂冷却システム1は、砂冷却装置5の冷却回収砂排出口(図示無し)の下に、ベルトコンベア18を備えている。ベルトコンベア18は、モータ19を備えており、このモータ19によって駆動されている。ベルトコンベア18は、砂冷却装置5から排出された冷却回収砂を、混練装置(図示無し)等の、次の工程に搬送する。 The recovered sand cooling system 1 includes a belt conveyor 18 under the cooling recovered sand discharge port (not shown) of the sand cooling device 5. The belt conveyor 18 includes a motor 19 and is driven by the motor 19. The belt conveyor 18 conveys the cooled recovery sand discharged from the sand cooling device 5 to the next step such as a kneading device (not shown).

回収砂冷却システム1は、冷却回収砂水分温度測定器20を備えている。冷却回収砂水分温度測定器20は、ベルトコンベア18上を搬送される冷却回収砂の水分量と温度を測定する。冷却回収砂水分温度測定器20には、後述する制御装置3が電気的に接続されている。冷却回収砂水分温度測定器20によって測定された冷却回収砂の水分量と温度は、制御装置3に送信される。 The recovered sand cooling system 1 includes a cooling recovered sand moisture temperature measuring device 20. The cooling recovery sand moisture temperature measuring device 20 measures the moisture content and temperature of the cooling recovery sand conveyed on the belt conveyor 18. A control device 3 described later is electrically connected to the cooling recovery sand moisture temperature measuring device 20. The moisture content and temperature of the cooling recovery sand measured by the cooling recovery sand moisture temperature measuring device 20 are transmitted to the control device 3.

上記したように、砂水分温度測定器2によって測定された回収砂の水分量と温度、冷却回収砂水分温度測定器20によって測定された冷却回収砂の水分量と温度、導入空気温度測定器7によって測定された導入空気の温度、排出空気温度測定器16によって測定された排出空気の温度、及び、風量測定器17によって測定された導入空気の風量は、制御装置3に送信される。制御装置3は、これらの測定値を受信し、当該測定値に基づいて、ベルトフィーダー9のインバータモータ10、水量調整弁12、空気導入装置6のインバータモータ15、及び空気加熱装置13を制御する。 As described above, the water content and temperature of the recovered sand measured by the sand moisture temperature measuring device 2, the water content and temperature of the cooled recovered sand measured by the cooling recovered sand moisture temperature measuring device 20, and the introduced air temperature measuring device 7 The temperature of the introduced air measured by, the temperature of the exhaust air measured by the exhaust air temperature measuring device 16, and the air volume of the introduced air measured by the air volume measuring device 17 are transmitted to the control device 3. The control device 3 receives these measured values and controls the inverter motor 10 of the belt feeder 9, the water amount adjusting valve 12, the inverter motor 15 of the air introduction device 6, and the air heating device 13 based on the measured values. ..

この実施の形態において制御装置3は、前記回収砂の水分量と温度、及び前記導入空気の温度に基づいて適正加水量を決定し、散水指示を行う。
また制御装置3は、冷却回収砂の水分量と温度等に基づいてシステムの動作補正を行う。
In this embodiment, the control device 3 determines the appropriate amount of water to be added based on the water content and temperature of the recovered sand and the temperature of the introduced air, and gives a watering instruction.
Further, the control device 3 corrects the operation of the system based on the water content and temperature of the cooling recovery sand.

上記のように構成された回収砂冷却システム1は、回収砂の水分量と温度を測定する砂水分温度測定器2と、回収砂に加える水の量である、適正加水量を決定する制御装置3と、適正加水量の水を前記回収砂に加え、水の蒸発潜熱で冷却して前記冷却回収砂とする散水冷却装置4,5と、該散水冷却装置4、5に空気を導入する空気導入装置6と、散水冷却装置4、5に導入される導入空気の温度を測定する導入空気温度測定器7とを備え、制御装置3は、前記回収砂の水分量と温度、及び、前記導入空気の温度を基に、前記適正加水量を決定する。 The recovered sand cooling system 1 configured as described above includes a sand moisture temperature measuring device 2 that measures the water content and temperature of the recovered sand, and a control device that determines an appropriate amount of water added to the recovered sand. 3 and sprinkler cooling devices 4 and 5 in which water having an appropriate amount of water is added to the recovered sand and cooled by the latent heat of evaporation of the water to obtain the cooled recovered sand, and air for introducing air into the sprinkler cooling devices 4 and 5. The introduction device 6 and the introduction air temperature measuring device 7 for measuring the temperature of the introduction air introduced into the sprinkler cooling devices 4 and 5 are provided, and the control device 3 includes the water content and temperature of the recovered sand and the introduction. The appropriate amount of water added is determined based on the temperature of the air.

これにより、導入空気の温度を考慮した、回収砂冷却システム内の適切な環境が実現可能であるため、例えば季節により温度や湿度が変化するような状況であったとしても、安定した冷却、含水効果を奏することが可能となる。したがって、導入空気の状態によらず、回収砂を目標温度まで冷却することが可能となる。 As a result, an appropriate environment in the recovered sand cooling system can be realized in consideration of the temperature of the introduced air. Therefore, even if the temperature and humidity change depending on the season, stable cooling and water content can be realized. It becomes possible to play an effect. Therefore, the recovered sand can be cooled to the target temperature regardless of the state of the introduced air.

次に、本発明の第二の実施形態について説明する。
図3は、本発明の第二の実施形態として示した回収砂冷却システム1Aの概略構成図であり、図4は、回収砂冷却システム1Aにおける制御装置のブロック図である。
これらの図において、第一の実施形態で説明した図1、図2に示す構成要素と同一の要素については同一符号を付し、その説明を省略する。
この実施形態が前述した第一の実施形態と異なる点は、制御装置3による適正加水量の決定を、回収砂の水分量と温度、及び、冷却回収砂の水分量と温度を基に行うようにしたことである。
Next, a second embodiment of the present invention will be described.
FIG. 3 is a schematic configuration diagram of the recovered sand cooling system 1A shown as the second embodiment of the present invention, and FIG. 4 is a block diagram of a control device in the recovered sand cooling system 1A.
In these figures, the same components as the components shown in FIGS. 1 and 2 described in the first embodiment are designated by the same reference numerals, and the description thereof will be omitted.
The difference between this embodiment and the first embodiment described above is that the control device 3 determines the appropriate amount of water added based on the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand. That's what I did.

すなわち、この実施の形態においては、図3に示す、回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却システムにおいて、前記回収砂の水分量と温度を測定する砂水分温度測定器2と、前記回収砂に加える水の量である、適正加水量を決定する制御装置3と、前記適正加水量の水を前記回収砂に加え、水の蒸発潜熱で冷却して前記冷却回収砂とする散水冷却装置4、5と、該散水冷却装置4、5に空気を導入する空気導入装置6と、前記冷却回収砂の水分量と温度を測定する冷却回収砂水分温度測定器20とを備え、前記制御装置3は、前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を基に、前記適正加水量を決定する。 That is, in this embodiment, in the recovered sand cooling system for cooling the recovered sand and adjusting the water content of the cooled recovered sand shown in FIG. 3, sand water temperature measurement for measuring the water content and temperature of the recovered sand. The vessel 2, the control device 3 for determining the appropriate amount of water added to the recovered sand, and the water of the appropriate amount of water added to the recovered sand and cooled by the latent heat of evaporation of the water to cool and recover. A sprinkling cooling device 4 or 5 for sand, an air introducing device 6 for introducing air into the sprinkling cooling devices 4 and 5, and a cooling recovery sand moisture temperature measuring device 20 for measuring the water content and temperature of the cooling recovery sand. The control device 3 determines the appropriate water content based on the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand.

この実施の形態では、砂水分温度測定器2の出力と冷却回収砂水分温度測定器20の出力で適正加水量を決定するので、第一の実施形態の構成要素である図1に示す導入空気温度測定器7、及び排出空気温度測定器16を備えていない。 In this embodiment, the appropriate amount of water is determined by the output of the sand moisture temperature measuring device 2 and the output of the cooling recovery sand moisture temperature measuring device 20, so that the introduced air shown in FIG. 1, which is a component of the first embodiment, is determined. The temperature measuring device 7 and the exhaust air temperature measuring device 16 are not provided.

この実施の形態においても、前述した第一の実施の形態と同様の効果が得られ、回収砂を目標温度まで冷却することが可能となる。 Also in this embodiment, the same effect as that of the first embodiment described above can be obtained, and the recovered sand can be cooled to the target temperature.

なお、本発明の回収砂冷却システム及び回収砂冷却方法は、図面を参照して説明した上述の実施形態に限定されるものではなく、その技術的範囲において他の様々な変形例が考えられ、本発明の主旨を逸脱しない限り、上記実施の形態で挙げた構成を取捨選択したり、他の構成に適宜変更したりすることが可能である。 The recovered sand cooling system and the recovered sand cooling method of the present invention are not limited to the above-described embodiments described with reference to the drawings, and various other modifications can be considered within the technical scope thereof. As long as it does not deviate from the gist of the present invention, it is possible to select the configuration described in the above embodiment or change it to another configuration as appropriate.

1、1A 回収砂冷却システム
2 砂水分温度測定器
3 制御装置
4 散水装置(散水冷却装置)
5 砂冷却装置(散水冷却装置)
6 空気導入装置
7 導入空気温度測定器
8 ホッパ
9 ベルトフィーダー
10 インバータモータ
11 水源
12 水量調整弁
13 空気加熱装置
14 集塵装置
15 インバータモータ
16 排出空気温度測定器
17 風量測定器
18 ベルトコンベア
19 モータ
20 冷却回収砂水分温度測定器
1, 1A Recovery sand cooling system 2 Sand moisture temperature measuring device 3 Control device 4 Sprinkler (sprinkler cooling device)
5 Sand cooling device (sprinkling cooling device)
6 Air introduction device 7 Introduction air temperature measuring device 8 Hopper 9 Belt feeder 10 Inverter motor 11 Water source 12 Water volume control valve 13 Air heating device 14 Dust collector 15 Inverter motor 16 Exhaust air temperature measuring device 17 Air volume measuring device 18 Belt conveyor 19 Motor 20 Cooling recovery sand Moisture temperature measuring device

Claims (7)

回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却システムであって、
前記回収砂の水分量と温度を測定する砂水分温度測定器と、
前記回収砂に加える水の量である、適正加水量を決定する制御装置と、
前記適正加水量の水を前記回収砂に加え、攪拌して水分を分散させて加水回収砂とする散水装置と、
前記加水回収砂を空気に接触させることにより水の蒸発潜熱で冷却して前記冷却回収砂とする冷却装置と、
該冷却装置に空気を導入する空気導入装置と、
前記冷却装置に導入される導入空気の温度を測定する導入空気温度測定器と、
前記散水装置に回収砂を搬送するベルトフィーダーと、
を備え、
前記制御装置は、前記回収砂の水分量と温度、及び、前記導入空気の温度を基に、前記適正加水量を決定
前記回収砂の水分量と温度、及び、前記導入空気の温度を含む要素に基づいて、前記ベルトフィーダーを制御する、回収砂冷却システム。
A recovery sand cooling system that cools the recovery sand and adjusts the amount of water in the recovery sand.
A sand moisture temperature measuring device that measures the moisture content and temperature of the recovered sand,
A control device that determines the appropriate amount of water added, which is the amount of water added to the recovered sand.
A watering device in which the appropriate amount of water is added to the recovered sand and the sand is stirred to disperse the water to obtain the recovered sand.
A cooling device that cools the water recovery sand with the latent heat of vaporization of water by bringing it into contact with air to obtain the cooling recovery sand.
An air introduction device that introduces air into the cooling device,
An introductory air temperature measuring device that measures the temperature of the introductory air introduced into the cooling device,
A belt feeder that conveys the collected sand to the watering device,
With
Wherein the control device, water content and temperature of the recovered sand, and, based on the temperature of the introduced air, to determine the proper amount of water,
A recovered sand cooling system that controls the belt feeder based on factors including the water content and temperature of the recovered sand and the temperature of the introduced air.
前記導入空気の風量を測定する風量測定器と、
前記導入空気を加熱する空気加熱装置と、を備え、
前記制御装置は、前記風量を更に基にして前記適正加水量を決定し、
前記回収砂の水分量と温度、及び、前記導入空気の温度を含む要素に基づいて、前記空気加熱装置を制御する、請求項1に記載の回収砂冷却システム。
An air volume measuring device that measures the air volume of the introduced air ,
An air heating device for heating the introduced air is provided.
The control device further determines the appropriate amount of water to be added based on the air volume .
The recovered sand cooling system according to claim 1 , wherein the air heating device is controlled based on an element including the water content and temperature of the recovered sand and the temperature of the introduced air.
回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却システムであって、
前記回収砂の水分量と温度を測定する砂水分温度測定器と、
前記回収砂に加える水の量である、適正加水量を決定する制御装置と、
前記適正加水量の水を前記回収砂に加え、攪拌して水分を分散させて加水回収砂とする散水装置と、
前記加水回収砂を空気に接触させることにより水の蒸発潜熱で冷却して前記冷却回収砂とする冷却装置と、
該冷却装置に空気を導入する空気導入装置と、
前記冷却回収砂の水分量と温度を測定する冷却回収砂水分温度測定器と、
を備え、
前記制御装置は、前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を基に、前記適正加水量を決定し、
前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を含む要素に基づいて、前記空気導入装置を制御する、回収砂冷却システム。
A recovery sand cooling system that cools the recovery sand and adjusts the amount of water in the recovery sand.
A sand moisture temperature measuring device that measures the moisture content and temperature of the recovered sand,
A control device that determines the appropriate amount of water added, which is the amount of water added to the recovered sand.
A watering device in which the appropriate amount of water is added to the recovered sand and the sand is stirred to disperse the water to obtain the recovered sand.
A cooling device that cools the water recovery sand with the latent heat of vaporization of water by bringing it into contact with air to obtain the cooling recovery sand.
An air introduction device that introduces air into the cooling device,
A cooling recovery sand moisture temperature measuring device for measuring the moisture content and temperature of the cooling recovery sand,
With
The control device determines the appropriate amount of water added based on the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand .
A recovery sand cooling system that controls the air introduction device based on factors including the water content and temperature of the recovered sand and the water content and temperature of the cooling recovery sand.
前記冷却装置に導入される導入空気の風量を測定する風量測定器と、
前記散水装置に回収砂を搬送するベルトフィーダーと、
前記導入空気を加熱する空気加熱装置と、を備え、
前記制御装置は、前記風量を更に基にして前記適正加水量を決定し、
前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を含む要素に基づいて、前記ベルトフィーダーと前記空気加熱装置を制御する、請求項3に記載の回収砂冷却システム。
An air volume measuring device that measures the air volume of the introduced air introduced into the cooling device, and
A belt feeder that conveys the collected sand to the watering device,
An air heating device for heating the introduced air is provided.
The control device further determines the appropriate amount of water to be added based on the air volume .
The recovered sand cooling system according to claim 3 , wherein the belt feeder and the air heating device are controlled based on an element including the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand.
回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却方法であって、
前記回収砂の水分量と温度を測定し、
前記回収砂に加える水の量である、適正加水量を決定し、
前記適正加水量の水を前記回収砂に加え、攪拌して水分を分散させて加水回収砂とし、
空気導入装置により空気を導入しながら前記加水回収砂を空気に接触させることにより水の蒸発潜熱で冷却して、前記冷却回収砂とし、
前記空気導入装置により導入される導入空気の温度を測定すること
前記回収砂をベルトフィーダーにより前記適正加水量の水を加え加水回収砂とする位置に搬送すること、を含むものであり、
前記回収砂の水分量と温度、及び、前記導入空気の温度を基に、前記適正加水量を決定し、
前記回収砂の水分量と温度、及び、前記導入空気の温度を含む要素に基づいて、前記ベルトフィーダーを制御する、回収砂冷却方法。
A method of cooling recovered sand that cools the recovered sand and adjusts the amount of water in the recovered sand.
Measure the water content and temperature of the recovered sand,
Determine the appropriate amount of water to be added to the recovered sand,
The appropriate amount of water was added to the recovered sand, and the sand was stirred to disperse the water to obtain the recovered sand.
By bringing the water recovery sand into contact with air while introducing air by an air introduction device, the sand is cooled by the latent heat of vaporization of water to obtain the cooling recovery sand.
Measuring the temperature of the introduced air introduced by the air introducing device ,
It includes transporting the recovered sand to a position where the recovered sand is prepared by adding water having an appropriate amount of water by a belt feeder.
The appropriate amount of water added is determined based on the water content and temperature of the recovered sand and the temperature of the introduced air .
A method for cooling recovered sand, which controls the belt feeder based on factors including the water content and temperature of the recovered sand and the temperature of the introduced air.
回収砂を冷却し、冷却回収砂の水分量を調整する回収砂冷却方法であって、
前記回収砂の水分量と温度を測定し、
前記回収砂に加える水の量である、適正加水量を決定し、
前記適正加水量の水を前記回収砂に加え、攪拌して水分を分散させて加水回収砂とし、
空気導入装置により空気を導入しながら前記加水回収砂を空気に接触させることにより水の蒸発潜熱で冷却して、前記冷却回収砂とし、
前記冷却回収砂の水分量と温度を測定することを含むものであり、
前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を基に、前記適正加水量を決定し、
前記回収砂の水分量と温度、及び、前記冷却回収砂の水分量と温度を含む要素に基づいて、前記空気導入装置を制御する、回収砂冷却方法。
A method of cooling recovered sand that cools the recovered sand and adjusts the amount of water in the recovered sand.
Measure the water content and temperature of the recovered sand,
Determine the appropriate amount of water to be added to the recovered sand,
The appropriate amount of water was added to the recovered sand, and the sand was stirred to disperse the water to obtain the recovered sand.
By bringing the water recovery sand into contact with air while introducing air by an air introduction device, the sand is cooled by the latent heat of vaporization of water to obtain the cooling recovery sand.
It includes measuring the water content and temperature of the cooled recovery sand.
Based on the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand, the appropriate water content is determined .
A method for cooling recovered sand, which controls the air introduction device based on an element including the water content and temperature of the recovered sand and the water content and temperature of the cooled recovered sand.
前記空気導入装置により導入される導入空気の風量を測定すること
前記導入空気を空気加熱装置により加熱すること、
を更に含み、
前記風量を更に基にして前記適正加水量を決定し、
前記回収砂の水分量と温度を含む要素に基づいて、前記空気加熱装置を制御する、請求項5又は請求項6に記載の回収砂冷却方法。
Measuring the air volume of the introduced air introduced by the air introducing device ,
Heating the introduced air with an air heating device,
Including
The appropriate amount of water added is determined based on the air volume .
The recovered sand cooling method according to claim 5 or 6 , wherein the air heating device is controlled based on an element including the water content and temperature of the recovered sand.
JP2017114143A 2016-09-14 2017-06-09 Recovery sand cooling system and recovery sand cooling method Active JP6879063B2 (en)

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JP2017114143A JP6879063B2 (en) 2017-06-09 2017-06-09 Recovery sand cooling system and recovery sand cooling method
PCT/JP2017/032307 WO2018051891A1 (en) 2016-09-14 2017-09-07 Recovered-sand cooling system and recovered-sand cooling method
US16/327,052 US20190193141A1 (en) 2016-09-14 2017-09-07 Return sand cooling system and return sand cooling method
CN201780056706.1A CN109715314B (en) 2016-09-14 2017-09-07 Recycled sand cooling system and recycled sand cooling method
EP17850794.3A EP3513887A4 (en) 2016-09-14 2017-09-07 Recovered-sand cooling system and recovered-sand cooling method
MX2019002661A MX2019002661A (en) 2016-09-14 2017-09-07 Recovered-sand cooling system and recovered-sand cooling method.
KR1020197006889A KR20190044632A (en) 2016-09-14 2017-09-07 In-house cooling system and in-house cooling method
BR112019004825A BR112019004825A2 (en) 2016-09-14 2017-09-07 return sand cooling system and return sand cooling method
TW106131255A TW201811460A (en) 2016-09-14 2017-09-12 Recovered-sand cooling system and recovered-sand cooling method

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