JP6133485B1 - Metal scrap processing equipment - Google Patents

Metal scrap processing equipment Download PDF

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JP6133485B1
JP6133485B1 JP2016227292A JP2016227292A JP6133485B1 JP 6133485 B1 JP6133485 B1 JP 6133485B1 JP 2016227292 A JP2016227292 A JP 2016227292A JP 2016227292 A JP2016227292 A JP 2016227292A JP 6133485 B1 JP6133485 B1 JP 6133485B1
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野田修嗣
竹之内秀樹
中山正則
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ENVIRONMENT ENERGY CO., LTD.
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Abstract

【課題】金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を短時間で確実かつ効率的に加熱分解して取り除くことができ、酸化を防ぎ、高歩留まりで処理能力が高く、省資源性、省エネルギー性に優れると共に、コンパクトで安全性、取扱い性、省スペース性に優れた金属屑処理装置の提供。【解決手段】金属屑搬送部と、金属屑搬送部の上流側に連設された金属屑供給部と、金属屑搬送部の下流側に連設された金属屑排出部と、金属屑搬送部に飽和蒸気及び/又は過熱蒸気を供給する蒸気供給部と、を有し、金属屑搬送部が、筒状の搬送路と、搬送路に内挿された撹拌部と、搬送路の周壁の上面側に形成された1以上のガス排出口と、搬送路の周壁の外側でガス排出口と連通し金属屑の付着物が加熱分解されて発生する分解ガスを金属屑搬送部から排出するガス導通路と、を備えている。【選択図】図2[PROBLEMS] To remove various deposits such as cutting fluid, paint, and rust preventives adhering to metal scraps by heat and decomposition in a short time and efficiently, prevent oxidation, and have high yield and high throughput. Providing a metal scrap disposal device that excels in resource and energy savings, and is compact, safe, easy to handle, and saves space. A metal scrap conveying section, a metal scrap supplying section connected to the upstream side of the metal scrap transport section, a metal scrap discharging section connected to the downstream side of the metal scrap transport section, and a metal scrap transport section. A steam supply section for supplying saturated steam and / or superheated steam to the metal scrap conveying section, a cylindrical conveying path, an agitating section inserted in the conveying path, and an upper surface of the peripheral wall of the conveying path One or more gas discharge ports formed on the side and a gas guide that communicates with the gas discharge ports on the outside of the peripheral wall of the transfer path and discharges the decomposition gas generated by the thermal decomposition of the metal scrap deposits from the metal scrap transfer unit And a passage. [Selection] Figure 2

Description

本発明は、アルミニウム、亜鉛、銅、鉄等の金属や真鍮、アルミニウム、ステンレス等の合金の加工時或いはこれらの金属製品の廃棄時に発生する金属屑に付着した切削油や研削油等の切削油剤、塗料、防錆剤等の各種付着物を飽和蒸気及び/又は過熱蒸気で加熱分解する金属屑処理装置に関する。   The present invention relates to a cutting fluid such as a cutting oil or a grinding oil adhered to metal scrap generated when processing a metal such as aluminum, zinc, copper, or iron, or an alloy such as brass, aluminum, or stainless steel, or disposal of these metal products. Further, the present invention relates to a metal scrap treatment apparatus that thermally decomposes various deposits such as paints and rust inhibitors with saturated steam and / or superheated steam.

従来、金属加工で発生する金属切粉は、溶融炉で溶融再生され各金属資源として再利用されている。しかし、切削加工や研削加工等の金属加工時に発生する金属切粉の表面には、切削油剤や金属加工の際に発生した金属の微粉、バイト屑等が付着している。このため、このような金属切粉を地金として再生する場合には、その前工程として、金属切粉に付着した切削油剤を乾燥させて取り除く必要がある。その乾燥方法として400℃〜600℃の熱風により切削油剤を蒸発させる単純な乾燥方法が主に用いられている。
しかし、このような単純な乾燥方法では切削油剤の油分は完全に乾燥せず、切削油剤由来の油分や炭素成分(コーク等)が金属切粉表面に残留し、金属切粉を溶解炉へ投入した際に、黒煙や発火が発生し易いという問題があった。
また、乾燥中に金属切粉を撹拌することにより発生する粉塵や金属切粉の表面に付着している金属の微粉やバイト屑が原因で粉塵爆発をおこす危険性もあった。
そこで、これらの金属切粉を高効率で再利用できる環境負荷の少ない乾燥方法及び乾燥装置が求められていた。
本願出願人が鋭意研究を行い出願した(特許文献1)には、切削油、金属屑、バイト屑が付着した金属切粉を乾燥炉内で多孔質材や、固体酸触媒、固体塩基触媒の内いずれか1以上を含有する乾燥処理材と混合し、乾燥処理材で切削油剤に由来する油分を乾燥させる金属切粉の乾燥方法が開示されている。
Conventionally, metal chips generated by metal processing are melted and regenerated in a melting furnace and reused as each metal resource. However, cutting oil, metal fine powder generated during metal processing, bite scraps, and the like adhere to the surface of the metal chips generated during metal processing such as cutting and grinding. For this reason, when reclaiming such metal chips as a bare metal, it is necessary to dry and remove the cutting oil adhering to the metal chips as a preceding process. As the drying method, a simple drying method in which cutting oil is evaporated by hot air of 400 ° C. to 600 ° C. is mainly used.
However, with such a simple drying method, the oil content of the cutting fluid is not completely dried. Oil and carbon components (such as coke) derived from the cutting fluid remain on the surface of the metal chips, and the metal chips are put into the melting furnace. When doing so, there was a problem that black smoke and ignition were likely to occur.
There is also a risk of dust explosion due to dust generated by stirring the metal chips during drying, metal dust or bite scraps adhering to the surface of the metal chips.
Therefore, there has been a demand for a drying method and a drying apparatus with low environmental load that can recycle these metal chips with high efficiency.
The applicant of the present application made an extensive research and applied (Patent Document 1), and the metal chips with cutting oil, metal scrap, and bite scrap adhered to a porous material, solid acid catalyst, solid base catalyst in a drying furnace. A method for drying metal chips is disclosed in which any one or more of them is mixed with a drying treatment material and the oil component derived from the cutting fluid is dried with the drying treatment material.

特開2015−42936号公報JP2015-42936A

(1)(特許文献1)の金属切粉の乾燥方法は、切削油剤が付着した金属切粉と、乾燥処理材とを乾燥炉内で混合し、金属切粉に付着した切削油剤を乾燥、接触分解することにより、乾燥後の金属切粉における残留炭素が著しく少なく、金属切粉を溶融炉へ投入した際の黒煙や発火の発生を防ぐことができ、安全性に優れると共に、乾燥後の金属切粉の酸化度が低く、金属の再生歩留まりに優れるものであった。
(2)しかし、乾燥処理材の供給量を管理しなければならず、また、乾燥済みの金属切粉と乾燥処理材を完全に分離することが困難であるため、乾燥処理材を使用することなく、簡単な制御で各種金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を短時間で確実かつ効率的に加熱分解して取り除くことができ、高歩留まりで省資源性、省エネルギー性に優れると共に、コンパクトで安全性、取扱い性、省スペース性に優れた金属屑処理装置の開発が強く望まれていた。
(1) The method for drying metal chips of (Patent Document 1) is to mix the metal chips to which the cutting fluid is adhered and the drying treatment material in a drying furnace, and dry the cutting fluid adhered to the metal chips. By catalytic cracking, the residual carbon in the metal chips after drying is remarkably low, and it is possible to prevent the occurrence of black smoke and ignition when the metal chips are put into the melting furnace. The degree of oxidation of the metal chips was low, and the metal regeneration yield was excellent.
(2) However, it is necessary to control the supply amount of the dry treatment material, and it is difficult to completely separate the dried metal chips from the dry treatment material. In addition, it is possible to remove various deposits such as cutting fluid, paint, and rust preventives that have adhered to various types of metal scraps with simple control by heat and decomposition in a short time, resulting in high yield and resource saving. There has been a strong demand for the development of a metal waste disposal apparatus that is excellent in energy saving and compact and excellent in safety, handling, and space saving.

本発明は上記要望に応えるものであり、金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を短時間で確実かつ効率的に加熱分解して取り除くことができ、酸化を防ぎ、高歩留まりで処理能力が高く、省資源性、省エネルギー性に優れると共に、コンパクトで安全性、取扱い性、省スペース性に優れた金属屑処理装置の提供を目的とする。   The present invention responds to the above-mentioned demand, and it can remove various deposits such as cutting fluid, paint, and rust preventives adhering to metal scraps by heat and decomposition reliably and efficiently in a short time to prevent oxidation. The purpose of the present invention is to provide a metal scrap disposal apparatus that is high in yield, has high processing capacity, is excellent in resource saving and energy saving, and is compact and excellent in safety, handling, and space saving.

課題を解決するための手段及びそれによって得られる作用、効果Means for solving the problems, and actions and effects obtained thereby

上記目的を達成するために本発明の金属屑処理装置は、以下の構成を有する。
本発明の請求項1に記載の金属屑処理装置は、金属屑の付着物を飽和蒸気及び/又は過熱蒸気で加熱分解する金属屑処理装置であって、
金属屑搬送部と、前記金属屑搬送部の上流側に連設された金属屑供給部と、前記金属屑搬送部の下流側に連設された金属屑排出部と、前記金属屑搬送部の搬送路の一側部に配設され前記飽和蒸気及び/又は前記過熱蒸気を供給する蒸気供給部と接続された蒸気供給管と、前記蒸気供給管と連通し前記搬送路の側壁に孔をあけて形成された複数の蒸気噴射口と、を有し、前記金属屑搬送部が、筒状の搬送路と、前記搬送路に内挿された撹拌部と、前記搬送路の周壁の上面側に形成された1以上のガス排出口と、前記搬送路の前記周壁の外側で前記ガス排出口と連通し前記金属屑の付着物が加熱分解されて発生する分解ガスを前記金属屑搬送部から排出するガス導通路と、を備えた構成を有している。
この構成により、以下のような作用、効果を有する。
(1)金属屑搬送部の上流側に連設された金属屑供給部と、金属屑搬送部の下流側に連設された金属屑排出部と、金属屑搬送部に飽和蒸気及び/又は過熱蒸気を供給する蒸気供給部を有することにより、金属屑供給部から供給された金属屑が金属屑搬送部で搬送されて金属屑排出部から排出されるまでの間に、金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を、蒸気供給部から供給される飽和蒸気及び/又は過熱蒸気によって短時間で加熱分解して取り除くことができ、省エネルギー性に優れる。
(2)金属屑搬送部が、筒状の搬送路と、搬送路に内挿された撹拌部を有することにより、撹拌部で金属屑を搬送しながら、蒸気供給部から供給される飽和蒸気及び/又は過熱蒸気と金属屑を確実に接触させて、金属屑の表面に付着した付着物を効率的に加熱分解することができ、付着物除去の効率性、確実性に優れる。
(3)金属屑搬送部が、搬送路の周壁の上面側に形成された1以上のガス排出口と、搬送路の周壁の外側でガス排出口と連通し金属屑の付着物が加熱分解されて発生する分解ガスを金属屑搬送部から排出するガス導通路を有することにより、金属屑の付着物が加熱分解されて発生する分解ガスをガス排出口から確実かつ効率的に排出させ、ガス導通路に沿ってスムーズに移動させて金属屑搬送部から系外に排出することができ、分解ガスの排出性に優れる。
(4)筒状の搬送路に撹拌部が内挿されることにより、ロータリーキルン等に比べて無駄な空間が少なく、装置をコンパクト化することができ、省スペース性に優れると共に、放熱ロスも少なく、加熱の効率性に優れる。
(5)乾燥処理材等を使用することなく飽和蒸気及び/又は過熱蒸気のみで金属屑の付着物を加熱分解して除去することができ、省資源性に優れると共に、金属屑に乾燥処理材等が付着することがなく、乾燥処理材等を分離する機構や工程が不要で、付着物のない金属屑を得ることができ、また酸化による劣化も防ぐことができるため、高歩留まりで金属屑のリサイクル性に優れる。
(6)撹拌部の回転数を制御するだけで搬送路内の金属屑の滞留時間をコントロールすることができるので、金属屑の大きさ、形状、嵩比重或いは付着物の種類等に応じて、必要な滞留時間を設定することにより、金属屑の付着物を確実に加熱分解することができ、操作性、汎用性、処理効率性に優れる。
(7)金属屑搬送部が、蒸気供給部と連結され金属屑搬送部の搬送路の周壁に形設された蒸気噴射口を有するので、蒸気噴射口から搬送路の内部に確実に飽和蒸気及び/又は過熱蒸気を噴射して金属屑の付着物を効率的に加熱分解することができ、加熱分解の効率性、安定性に優れる。
(8)搬送路の長手方向に沿って複数の蒸気噴射口を配置した場合、搬送路の全長にわたって効率的に飽和蒸気及び/又は過熱蒸気を行き渡らせることができ、金属屑との接触効率を高めることができるので、飽和蒸気及び/又は過熱蒸気の供給量を低減することが可能で、省エネルギー性に優れる。また、蒸気噴射口を搬送路の下流端側に配置した場合、搬送路に沿って搬送される金属屑に対して飽和蒸気及び/又は過熱蒸気の流れが向流になるため、金属屑の付着物と飽和蒸気及び/又は過熱蒸気を確実に接触させて加熱分解することができ、加熱分解処理の効率性に優れる。
In order to achieve the above object, the metal scrap disposal apparatus of the present invention has the following configuration.
The metal scrap processing apparatus according to claim 1 of the present invention is a metal scrap processing apparatus that thermally decomposes deposits of metal scrap with saturated steam and / or superheated steam,
A metal scrap conveying section, a metal scrap supplying section connected to the upstream side of the metal scrap transport section, a metal scrap discharging section connected to the downstream side of the metal scrap transport section, and the metal scrap transport section. A steam supply pipe disposed on one side of the transport path and connected to the steam supply section for supplying the saturated steam and / or the superheated steam, and a hole is formed in the side wall of the transport path in communication with the steam supply pipe. A plurality of vapor injection ports formed on the upper surface side of the peripheral wall of the conveyance path, the metal scrap conveyance unit, the cylindrical conveyance path, the stirring unit inserted in the conveyance path One or more formed gas discharge ports and the gas discharge port communicated with the gas discharge port outside the peripheral wall of the transfer path, and the decomposition gas generated by the thermal decomposition of the deposits of the metal scrap is discharged from the metal scrap transfer unit. And a gas conduction path.
This configuration has the following operations and effects.
(1) Scrap supply and / or superheated metal scrap supply section connected to the upstream side of the metal scrap transport section, metal scrap discharge section connected to the downstream side of the metal scrap transport section, and metal scrap transport section By having the steam supply part that supplies steam, the metal scrap supplied from the metal scrap supply part is transported by the metal scrap transport part and discharged from the metal scrap discharge part. Various deposits such as oil, paint, and rust preventive agent can be removed by thermal decomposition in a short time with saturated steam and / or superheated steam supplied from the steam supply unit, which is excellent in energy saving.
(2) Since the metal scrap conveyance unit has a cylindrical conveyance path and an agitation unit inserted in the conveyance path, saturated vapor supplied from the steam supply unit while conveying the metal scrap in the agitation unit and It is possible to reliably contact the superheated steam and the metal scrap, and to efficiently decompose the deposit attached to the surface of the metal scrap, thereby improving the efficiency and certainty of removing the deposit.
(3) One or more gas exhaust ports formed on the upper surface side of the peripheral wall of the transport path are connected to the gas exhaust port on the outer side of the peripheral wall of the transport path, and the metal scrap deposit is thermally decomposed. By providing a gas conduction path that discharges the cracked gas generated from the metal scrap conveying section, the cracked gas generated by the thermal decomposition of the metal scrap deposits is reliably and efficiently discharged from the gas discharge port. It can be smoothly moved along the passage and discharged out of the system from the metal scrap conveying section, and the decomposition gas discharge is excellent.
(4) The stirrer is inserted into the cylindrical conveyance path, so that there is less wasted space than a rotary kiln, etc., the device can be made compact, it is excellent in space saving, and there is little heat loss. Excellent heating efficiency.
(5) It is possible to remove metal waste deposits by thermal decomposition only with saturated steam and / or superheated steam without using a drying treatment material, etc. Is not attached, and there is no need for a mechanism or process for separating the dry processing material, etc., and it is possible to obtain metal scrap without deposits and to prevent deterioration due to oxidation. Excellent recyclability.
(6) Since it is possible to control the residence time of the metal scraps in the transport path only by controlling the number of revolutions of the stirring unit, according to the size, shape, bulk specific gravity or the kind of deposits of the metal scraps, By setting the necessary residence time, the deposits of metal scrap can be surely thermally decomposed, and the operability, versatility, and processing efficiency are excellent.
(7) Since the metal scrap transport unit has a steam injection port connected to the steam supply unit and formed on the peripheral wall of the transport path of the metal scrap transport unit, the saturated steam and It is possible to efficiently decompose the deposits of metal scraps by injecting superheated steam, and the heat decomposition efficiency and stability are excellent.
(8) When a plurality of steam injection ports are arranged along the longitudinal direction of the transport path, saturated steam and / or superheated steam can be efficiently distributed over the entire length of the transport path, and the contact efficiency with metal scraps can be improved. Since it can be increased, the supply amount of saturated steam and / or superheated steam can be reduced, and energy saving is excellent. In addition, when the steam injection port is arranged on the downstream end side of the transport path, the flow of saturated steam and / or superheated steam is countercurrent to the metal scrap transported along the transport path. The kimono and saturated steam and / or superheated steam can be reliably brought into contact and thermally decomposed, and the efficiency of the heat decomposition treatment is excellent.

ここで、金属屑供給部がスクレーパーコンベアやスクリューコンベア等を備えることにより、多量の金属屑を連続的に処理することができ、装置の自動化が容易で操作性、作業効率性に優れる。尚、金属屑供給部にはシャッター式の計量ダンパー等を備えてもよい。
尚、金属屑供給部に予備加熱部を設けることにより、金属屑搬送部における処理時間を短縮することができる。また、搬送路内で発生する分解ガスや蒸気を利用して予備加熱を行ってもよい。
尚、金属屑供給部の前後にスライドゲート等を設けることが好ましい。これにより、金属屑搬送部の気密性を上げ、酸素濃度を制御することができ、金属屑の酸化を防ぐことができるためである。
金属屑搬送部の撹拌部は、金属屑を撹拌しながら搬送路に沿って搬送できるものであればよく、羽根の形状や配置等は適宜、選択することができる。
Here, when the metal scrap supply unit includes a scraper conveyor, a screw conveyor, or the like, a large amount of metal scrap can be continuously processed, the apparatus can be easily automated, and the operability and work efficiency are excellent. The metal scrap supply unit may be provided with a shutter-type weighing damper.
In addition, the processing time in a metal waste conveyance part can be shortened by providing a preheating part in a metal waste supply part. Moreover, you may preheat using the decomposition gas and vapor | steam which generate | occur | produce in a conveyance path.
In addition, it is preferable to provide a slide gate etc. before and behind the metal scrap supply part. Thereby, it is because the airtightness of a metal scrap conveyance part can be raised, oxygen concentration can be controlled, and the oxidation of metal scrap can be prevented.
The stirrer of the metal scrap transporting part only needs to be capable of transporting along the transport path while stirring the metal scrap, and the shape and arrangement of the blades can be appropriately selected.

金属屑のサイズを調整するために、金属屑の破断や切断等を行う剪断式(一軸剪断破砕機等)や衝撃式(ハンマークラッシャー等)の前処理装置を金属屑供給部の上流側に設けてもよい。金属屑のサイズを調整することで、撹拌部を回転させるモーターの回転数の調整が容易になり作業性を向上させることができる。
金属屑処理装置の乾燥の対象となる金属屑としては、アルミニウム、亜鉛、銅、鉄等の金属や、真鍮、アルミニウム、ステンレス等の合金類を切削加工や研削加工等で金属加工する際に発生する金属屑や切削屑、シュレッダー屑のほか、各種缶等の金属製品の使用済み屑、金属切粉等を固めたブリケット、ダイカストのバリの塊等の様々な形状の金属屑を用いることができ、特に材質や形状を限定するものではない。
金属加工で使用される切削油剤として、日本工業規格(JIS K2241)における不水溶性切削油剤(N1種、N2種、N3種、N4種)や、水溶性切削油剤(A1種、A2種、A3種)及び、これらの混合物が挙げられる。また、一般的に切削油剤には、添加剤として、極圧添加剤、乳化剤(潤滑剤)、防錆剤、防食剤、界面活性剤、消泡剤、防腐剤等が添加されているがこれらを含んでいてもよい。水溶性切削油剤は、水で希釈して使用するが、このように水を含んでいてもよい。尚、切削油剤には切削油の他研削油も含まれる。
In order to adjust the size of the metal scrap, a shearing type (uniaxial shear crusher, etc.) or impact type (hammer crusher, etc.) pretreatment device that breaks or cuts the metal scrap is provided upstream of the metal scrap supply unit. May be. By adjusting the size of the metal scrap, it is easy to adjust the number of rotations of the motor that rotates the stirring unit, and the workability can be improved.
Metal scraps to be dried by the scrap metal processing equipment are generated when metals such as aluminum, zinc, copper and iron, and alloys such as brass, aluminum and stainless steel are machined by cutting or grinding. In addition to metal scraps, cutting scraps, shredder scraps, used scraps of metal products such as various cans, briquettes hardened with metal chips, die cast burr lump, etc. The material and shape are not particularly limited.
As cutting fluids used in metal processing, water-insoluble cutting fluids (N1, N2, N3, N4) and water-soluble cutting fluids (A1, A2, A3) in Japanese Industrial Standards (JIS K2241). Seeds) and mixtures thereof. In general, cutting oils are added with extreme pressure additives, emulsifiers (lubricants), rust inhibitors, anticorrosives, surfactants, antifoaming agents, preservatives, etc. as additives. May be included. The water-soluble cutting fluid is diluted with water and used, but may contain water in this way. The cutting fluid includes grinding oil as well as cutting oil.

飽和蒸気の温度は100℃〜200℃、過熱蒸気の温度は150℃〜600℃が好ましく、飽和蒸気及び/又は過熱蒸気の供給圧力は50kPa〜500kPaが好ましい。蒸気供給部としては、ボイラー等により発生する乾き飽和蒸気をさらに加熱し、飽和蒸気の圧力に相当するより高い温度の過熱蒸気を発生させる過熱蒸気発生装置が好適に用いられる。バルブの開閉により、飽和蒸気及び/又は過熱蒸気を選択的に金属屑搬送部に供給することができる。
蒸気供給部は金属屑搬送部の搬送路と接続され、搬送路の内部に飽和蒸気及び/又は過熱蒸気を供給する。蒸気供給部と搬送路の接続位置は適宜、選択することができ、搬送路の所望の位置から搬送路の内部へ飽和蒸気及び/又は過熱蒸気を噴射させることができる。特に、搬送路の長手方向に沿って複数の蒸気噴射口を設けた場合、蒸気噴射口1箇所当りの蒸気圧力を下げて効率的に蒸気を供給することができ、蒸気が過剰に供給されて搬送路から排出されることを防止でき、省エネルギー性に優れる。また、蒸気噴射口から噴射される蒸気圧力を下げることにより、粉塵爆発の危険性があるアルミニウム等の微粉の飛散を防ぐことができ、安全性に優れる。尚、過熱蒸気中では極低酸素雰囲気となるため、金属屑の酸化劣化が少なく、金属回収の歩留りを高めることができ、高品質性、リサイクル性に優れる。
The temperature of the saturated steam is preferably 100 ° C. to 200 ° C., the temperature of the superheated steam is preferably 150 ° C. to 600 ° C., and the supply pressure of the saturated steam and / or superheated steam is preferably 50 kPa to 500 kPa. As the steam supply unit, a superheated steam generator that further heats dry saturated steam generated by a boiler or the like and generates superheated steam having a higher temperature corresponding to the pressure of the saturated steam is preferably used. By opening and closing the valve, saturated steam and / or superheated steam can be selectively supplied to the metal scrap conveying section.
The steam supply unit is connected to the conveyance path of the metal scrap conveyance unit, and supplies saturated steam and / or superheated steam to the inside of the conveyance path. The connection position between the steam supply unit and the transport path can be selected as appropriate, and saturated steam and / or superheated steam can be injected from the desired position of the transport path into the transport path. In particular, when a plurality of steam injection ports are provided along the longitudinal direction of the transport path, the steam pressure per one steam injection port can be lowered to efficiently supply the steam, and the steam is supplied excessively. It can be prevented from being discharged from the transport path and has excellent energy savings. Further, by reducing the pressure of the steam injected from the steam injection port, it is possible to prevent scattering of fine powders such as aluminum, which has a risk of dust explosion, and is excellent in safety. In addition, since it becomes a very low oxygen atmosphere in superheated steam, there is little oxidation deterioration of a metal scrap, the yield of metal collection | recovery can be improved, and it is excellent in high quality and recyclability.

金属屑搬送部は加熱炉内に横架してもよい。金属屑搬送部の搬送路の外周が加熱炉で囲まれるため、加熱炉と搬送路との間に熱風を吹き込むことにより、搬送路を外部から加熱することができ、搬送路内部の温度低下を防いで付着物を短時間で加熱分解することができ、効率性に優れる。尚、熱風を発生させるための加熱源としては、バーナーや電気ヒーター等を用いてもよいし、過熱蒸気を生成した後の排熱や付着物を加熱分解した際に発生する分解ガスを回収して燃焼させた後の排熱等を利用してもよい。搬送路を外部から加熱する際の温度は300℃〜650℃が好ましい。外部加熱の温度が300℃より低くなるにつれ、搬送路内の温度も低くなり、金属屑に付着した油分等の分解に必要な熱エネルギーを飽和蒸気及び/又は過熱蒸気で賄うことになって、加熱分解の効率、省エネルギー性が低下し易くなる傾向があり、好ましくない。また、外部加熱の温度が650℃より高くなるにつれ、搬送路内の温度も高くなり、搬送している金属屑が溶融して搬送路や撹拌部等に付着し易くなる傾向があり、機器の破損等につながるおそれがあるため好ましくない。
尚、搬送路の外周をウレタンフォーム、ポリエチレンフォーム、グラスウール等の保温材(断熱材)で覆ってもよい。
The metal scrap conveyance unit may be placed horizontally in the heating furnace. Since the outer periphery of the conveyance path of the metal scrap conveyance part is surrounded by a heating furnace, the conveyance path can be heated from outside by blowing hot air between the heating furnace and the conveyance path, and the temperature inside the conveyance path is reduced. The deposits can be decomposed by heating in a short time, and the efficiency is excellent. As a heating source for generating hot air, a burner, an electric heater or the like may be used, or exhaust gas generated after generating superheated steam or decomposition gas generated when pyrolyzing deposits is recovered. It is also possible to use exhaust heat after combustion. As for the temperature at the time of heating a conveyance path from the outside, 300 to 650 degreeC is preferable. As the temperature of the external heating becomes lower than 300 ° C., the temperature in the conveyance path also becomes lower, and the thermal energy necessary for the decomposition of oil etc. adhering to the metal scrap is to be covered with saturated steam and / or superheated steam, There is a tendency that the efficiency of heat decomposition and energy saving are liable to decrease, which is not preferable. Moreover, as the temperature of external heating becomes higher than 650 ° C., the temperature in the transport path also increases, and the metal scrap being transported tends to melt and easily adhere to the transport path, the stirring unit, etc. This is not preferable because it may lead to damage.
In addition, you may cover the outer periphery of a conveyance path with heat insulating materials (heat insulating material), such as urethane foam, polyethylene foam, and glass wool.

搬送路内の圧力は、大気圧又は僅かに正圧に維持することが好ましい。付着物の加熱分解によって搬送路の内部で分解ガス(可燃性ガス)が生成されており、負圧にした場合、外気を吸い込んで酸素濃度が上昇し、装置内で着火して爆発する可能性があるためである。
尚、付着物の加熱分解によって発生する分解ガスは、熱交換器で冷却した後、湿式スクラバーで捕集することにより、未燃ガスの爆発や分解ガスに同伴して排出されるアルミニウム等の微粉による粉塵爆発を防ぐことができ、安全性に優れる。また、分解ガスを冷却して得られる油分と水分は、エマルジョン化して燃料として再利用することもできる。
尚、付着物の加熱分解によって発生する分解ガスの安全な処理、脱臭等の目的で、燃焼処理してもよい。
ガス排出口の数、形状、大きさ、配置等は適宜、選択することができる。金属屑が搬送路の内部を上流から下流に向かって移動するにつれ、付着物の加熱、分解が進行し、分解ガスが発生するので、ガス排出口は搬送路の少なくとも下流側に配置することが好ましい。尚、搬送路の全長に渡って複数のガス排出口を設けた場合、搬送路全体から斑無く効率的に分解ガスを排出することができる。
また、ガス導通路は搬送路の周壁の外側でガス排出口と連通して分解ガスを金属屑搬送部から排出することができればよく、その出口の位置は適宜、選択することができる。
蒸気噴射口の数や配置は、適宜、選択することができる。
尚、搬送路の周壁に孔をあけて蒸気噴射口を形成し、搬送路の周壁の外周面側で蒸気供給部と連結することにより、搬送路の内部に突起物がなく、撹拌部との干渉を防ぐことができ、撹拌部と搬送路の内周面との隙間を小さくして飽和蒸気及び/又は過熱蒸気のショートパスを防止できる。
The pressure in the conveyance path is preferably maintained at atmospheric pressure or slightly positive pressure. Decomposition gas (combustible gas) is generated inside the conveyance path due to thermal decomposition of the deposits, and if negative pressure is taken, the outside air is sucked in, the oxygen concentration rises, and it may ignite and explode in the device Because there is.
The cracked gas generated by the thermal decomposition of the deposits is cooled by a heat exchanger and then collected by a wet scrubber, resulting in an unburned gas explosion or a fine powder such as aluminum discharged along with the cracked gas. It prevents dust explosion caused by, and is excellent in safety. The oil and water obtained by cooling the cracked gas can be emulsified and reused as fuel.
In addition, you may carry out a combustion process for the objective of the safe process of the decomposition gas generated by the thermal decomposition of a deposit | attachment, deodorizing, etc.
The number, shape, size, arrangement, and the like of the gas discharge ports can be selected as appropriate. As metal debris moves from upstream to downstream in the transport path, the deposits are heated and decomposed to generate decomposition gas. Therefore, the gas discharge port may be arranged at least on the downstream side of the transport path. preferable. In addition, when a plurality of gas discharge ports are provided over the entire length of the transport path, the decomposition gas can be discharged efficiently from the entire transport path.
Moreover, the gas conduction path only needs to be able to communicate with the gas discharge port outside the peripheral wall of the transfer path and discharge the decomposition gas from the metal scrap transfer section, and the position of the outlet can be selected as appropriate.
The number and arrangement of the steam injection ports can be selected as appropriate.
In addition, by making a hole in the peripheral wall of the transport path to form a steam injection port and connecting it to the steam supply unit on the outer peripheral surface side of the peripheral wall of the transport path, there is no protrusion inside the transport path, Interference can be prevented, and the gap between the stirring unit and the inner peripheral surface of the transport path can be reduced to prevent a short path of saturated steam and / or superheated steam.

請求項2に記載の発明は、請求項1に記載の金属屑処理装置であって、前記撹拌部が、回転軸の外周に配設された螺旋状の羽根と、前記回転軸の長手方向と平行に配設され前記羽根の外周側を連結補強する連結撹拌部と、を備えた構成を有している。
この構成により、請求項1の作用、効果に加え、以下の作用、効果を有する。
(1)撹拌部が、回転軸の外周に配設された螺旋状の羽根と、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、搬送路と近接する羽根の外周側において連結撹拌部で金属屑を掻き上げるようにして撹拌することができ、金属屑と飽和蒸気及び/又は過熱蒸気を確実に接触させて金属屑の表面に付着した付着物を効率的に加熱分解しながら搬送することができ、省エネルギー性、付着物除去の効率性に優れる。
(2)撹拌部が、螺旋状の羽根を有することにより、様々な形状や嵩比重の金属屑に対して、撹拌部を回転させるモーターの回転数を制御するだけで、搬送路内の金属屑の滞留時間を正確にコントロールして付着物を確実に加熱分解することができ、加熱分解処理の確実性、安定性に優れる。
(3)撹拌部が、回転軸の外周に配設された螺旋状の羽根と、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、スクリューフィーダーと同等の剛性と搬送効率、金属屑の搬送の定量性を保つことができ、付着物の加熱分解の効率性に優れる。
(4)撹拌部が、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、撹拌部の強度を向上させることができるので、羽根の厚みを薄くして撹拌部の軽量化を図り、羽根の外周部と搬送路内表面との摩擦を軽減することができ、金属屑搬送部の耐久性、長寿命性に優れる。
(5)撹拌部が、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、撹拌部の剛性を保つことができ、ブリケットやダイカストのバリ等の塊状の金属屑或いは様々な形状や比重の金属屑に対しても、羽根の変形や破損等の発生を効果的に防止して、金属屑を確実に搬送することができ、金属屑の搬送の信頼性、確実性に優れる。
(6)撹拌部の螺旋状の羽根が回転軸の外周に配設されているので、十分な剛性を確保して撓みや変形を防止して撹拌部を確実に回転させることができ、動作の安定性に優れる。
Invention of Claim 2 is the metal scrap processing apparatus of Claim 1, Comprising: The said stirring part is a helical blade | wing arrange | positioned on the outer periphery of a rotating shaft, The longitudinal direction of the said rotating shaft, And a connecting stirrer arranged in parallel to connect and reinforce the outer peripheral side of the blade.
With this configuration, the following actions and effects are provided in addition to the actions and effects of the first aspect.
(1) The stirrer has a spiral blade disposed on the outer periphery of the rotating shaft and a connecting stirring unit disposed in parallel to the longitudinal direction of the rotating shaft to reinforce the outer peripheral side of the blade. It is possible to stir by scraping metal scraps at the connecting stirrer on the outer peripheral side of the blades close to the road, and the metal scraps and saturated steam and / or superheated steam are brought into contact with each other and adhered to the surface of the metal scraps. The deposit can be transported while being efficiently decomposed by heat, and is excellent in energy saving and deposit removal efficiency.
(2) Since the stirring unit has spiral blades, metal scraps in the transport path can be controlled simply by controlling the number of revolutions of the motor that rotates the stirring unit for metal scraps of various shapes and bulk specific gravity. It is possible to accurately heat and decompose the deposit by accurately controlling the residence time of the resin, and it is excellent in the reliability and stability of the heat decomposition treatment.
(3) The agitating part has a spiral blade disposed on the outer periphery of the rotating shaft and a connecting stirring unit disposed in parallel to the longitudinal direction of the rotating shaft to reinforce the outer peripheral side of the blade. It can maintain the same rigidity and transport efficiency as the feeder and the quantitativeness of the transport of metal scraps, and is excellent in the efficiency of thermal decomposition of deposits.
(4) Since the stirrer has a connecting stirrer that is arranged in parallel with the longitudinal direction of the rotating shaft and that reinforces the outer peripheral side of the vane, the strength of the stirrer can be improved. By reducing the thickness of the agitator, the friction between the outer peripheral portion of the blade and the inner surface of the conveyance path can be reduced, and the durability and long life of the metal scrap conveyance unit are excellent.
(5) The stirrer has a connecting stirrer that is arranged in parallel with the longitudinal direction of the rotating shaft and connects and reinforces the outer peripheral side of the blades, whereby the rigidity of the stirrer can be maintained, such as briquettes and die cast burrs, etc. It is possible to effectively prevent the occurrence of deformation and breakage of blades, and to reliably transport metal scrap, even if it is a lump of metal scrap or metal scrap of various shapes and specific gravity. Excellent reliability and reliability.
(6) Since the spiral blades of the stirring unit are disposed on the outer periphery of the rotating shaft, sufficient stirring can be ensured to prevent bending and deformation, and the stirring unit can be reliably rotated. Excellent stability.

ここで、連結撹拌部は螺旋状の羽根の外周側を固定できるものであればよく、形状や配置等は、適宜、選択することができる。例えば、角鋼や丸鋼等の棒材或いは角パイプや丸パイプ等の筒状部材を用いてもよいが、平鋼(フラットバー)等の板状部材を用いることにより、金属屑との接触面積を確保することができ、金属屑を効率的に掻き上げて撹拌効果を高めることができる。連結撹拌部は螺旋状の羽根の外周側で隣接する羽根同士を回転軸の長手方向に沿うように連結補強することにより、剛性を確保することができる。尚、連結撹拌部の数は適宜、選択することができるが、円周方向に間隔を空けて2箇所乃至8箇所設けることが好ましい。連結撹拌部の数が1箇所だけになると、羽根が変形し易くなり、撹拌部全体の剛性が低下して撓みが発生し易くなると共に撹拌効果が低下し易くなる傾向があり、8箇所より多くなるにつれ、撹拌に寄与しない連結撹拌部が増え、撹拌部全体の重量が増加して撹拌部の回転に必要なエネルギーが増大し、金属屑の撹拌効率性、省エネルギー性が低下し易くなる傾向があり、いずれも好ましくない。   Here, the connection stirring part should just be what can fix the outer peripheral side of a helical blade | wing, and a shape, arrangement | positioning, etc. can be selected suitably. For example, rods such as square steel and round steel, or cylindrical members such as square pipes and round pipes may be used, but by using a plate-like member such as flat steel, the contact area with metal scraps Can be ensured, and scrap metal can be efficiently scraped to enhance the stirring effect. The connecting stirring unit can ensure rigidity by connecting and reinforcing adjacent blades along the longitudinal direction of the rotating shaft on the outer peripheral side of the spiral blade. In addition, although the number of connection stirring parts can be selected suitably, it is preferable to provide 2 thru | or 8 places at intervals in the circumferential direction. When the number of the connected stirring parts is only one, the blades are easily deformed, the rigidity of the whole stirring part is lowered, the bending is likely to occur, and the stirring effect tends to be lowered, and the number of the stirring parts is more than eight. As it becomes, the number of connected agitation parts that do not contribute to agitation increases, the weight of the whole agitation part increases, the energy required for rotation of the agitation part increases, and the metal scrap agitation efficiency and energy saving tend to decrease. Yes, neither is preferred.

請求項3に記載の発明は、請求項に記載の金属屑処理装置であって、前記金属屑搬送部の前記ガス排出口が、螺旋状の前記羽根のピッチと同等の間隔で複数配置された構成を有している。
この構成により、請求項の作用、効果に加え、以下の作用、効果を有する。
(1)金属屑搬送部のガス排出口が、螺旋状の羽根のピッチと同等の間隔で複数配置されているので、撹拌部の回転中に、螺旋状の羽根の間に形成された各々の空間とガス排出口を確実に連通させ、金属屑の付着物が加熱分解されて発生する分解ガスを確実かつ効率的に排出することができ、分解ガスの排出の確実性、効率性に優れる。
According to a third aspect of the invention, a metal scrap processing apparatus according to claim 1, wherein the gas outlet of the scrap metal conveying portion, a plurality of arranged with equal spacing and pitch of the spiral of the vane It has a configuration.
With this configuration, the operation of claim 1, in addition to the effects, has the following operations and effects.
(1) Since a plurality of gas discharge ports of the metal scrap conveying unit are arranged at intervals equivalent to the pitch of the spiral blades, each of the gas discharge ports formed between the spiral blades during the rotation of the stirring unit The space and the gas discharge port are reliably communicated, and the cracked gas generated by the thermal decomposition of the deposits of the metal scrap can be discharged reliably and efficiently, and the discharge gas is reliably and efficiently discharged.

ここで、複数のガス排出口を螺旋状の羽根のピッチと同等の間隔で配置することにより、撹拌部の回転中に、螺旋状の羽根の間に形成された各々の空間が必ずガス排出口の位置と重なって連通するので、各々のガス排出口から確実かつ効率的に分解ガスを排出することができる。   Here, by arranging a plurality of gas discharge ports at intervals equivalent to the pitch of the spiral blades, each space formed between the spiral blades is surely formed during rotation of the stirring unit. Therefore, the cracked gas can be discharged from each gas discharge port reliably and efficiently.

請求項4に記載の発明は、請求項1又は2に記載の金属屑処理装置であって、前記蒸気噴射口が、前記撹拌部の螺旋状の前記羽根のピッチと同等の間隔で複数形成された構成を有している。A fourth aspect of the present invention is the metal scrap disposal apparatus according to the first or second aspect, wherein a plurality of the steam injection ports are formed at an interval equal to the pitch of the spiral blades of the stirring unit. It has a configuration.
この構成により、請求項1又は2の作用、効果に加え、以下の作用、効果を有する。  With this configuration, the following actions and effects are provided in addition to the actions and effects of the first or second aspect.
蒸気噴射口を螺旋状の羽根のピッチと同等の間隔で配置した場合、撹拌部の回転中に、螺旋状の羽根の間に形成された各々の空間が必ず蒸気噴射口の位置と重なって連通するので、各々の蒸気噴射口から空間に確実かつ効率的に飽和蒸気及び/又は過熱蒸気を供給することができる。When the steam injection ports are arranged at an interval equal to the pitch of the spiral blades, each space formed between the spiral blades always overlaps and communicates with the position of the spiral blades during rotation of the stirring unit. Therefore, saturated steam and / or superheated steam can be reliably and efficiently supplied to the space from each steam injection port.

請求項に記載の発明は、請求項1、3又は4の内いずれか1項に記載の金属屑処理装置であって、前記金属屑搬送部の前記ガス導通路の出口が前記金属屑供給部と連結された構成を有している。
この構成により、請求項1、3又は4内いずれか1項の作用、効果に加え、以下の作用、効果を有する。
(1)金属屑搬送部のガス導通路の出口が金属屑供給部と連結されることにより、搬送路内で金属屑の付着物が加熱分解されて発生する分解ガスを金属屑供給部から系外に確実に排出することができると共に、分解ガスの熱を有効に利用して、金属屑供給部から供給される金属屑を予備加熱することができ、金属屑搬送部における処理時間を短縮することが可能で省エネルギー性に優れる。
Invention of Claim 5 is a metal waste processing apparatus of any one of Claim 1, 3 or 4 , Comprising: The exit of the said gas conduction path of the said metal waste conveyance part is said metal waste supply It has the structure connected with the part.
With this configuration, in addition to the operation and effect of any one of claims 1, 3 and 4 , the following operation and effect are provided.
(1) By connecting the outlet of the gas conduction path of the metal scrap conveying section to the metal scrap supplying section, the decomposition gas generated by the thermal decomposition of the deposits of the metal scrap in the conveying path is generated from the metal scrap supplying section. As well as being able to discharge to the outside reliably, it is possible to preheat the metal scrap supplied from the metal scrap supply section by effectively using the heat of the cracked gas, and shorten the processing time in the metal scrap transport section It is possible and excellent in energy saving.

ここで、金属屑搬送部のガス導通路の出口が金属屑供給部に連結されていればよく、ガス導通路から金属屑供給部までの経路は適宜、選択することができるが、ガス導通路を搬送路の長手方向と平行に配置し、ガス導通路の端部の出口を金属屑供給部と連結することが好ましい。これにより、ガス導通路から金属屑供給部までの経路を最短にして分解ガスを効率的に排出することができ、分解ガスから周囲への放熱を押え、金属屑供給部での予備加熱に効率的に利用することができる。尚、ガス導通路の出口と金属屑供給部との連結位置を金属屑供給部の下流側に配置することにより、分解ガスを金属屑と確実に接触させることができ、排熱を有効利用することができる。   Here, it is only necessary that the outlet of the gas conduction path of the metal scrap conveyance unit is connected to the metal scrap supply unit, and the path from the gas conduction path to the metal scrap supply unit can be appropriately selected. Are arranged in parallel with the longitudinal direction of the transport path, and the outlet of the end of the gas conduction path is preferably connected to the metal scrap supply section. This makes it possible to efficiently discharge the cracked gas by minimizing the path from the gas conduction path to the metal scrap supply part, suppresses heat radiation from the cracked gas to the surroundings, and is efficient for preheating in the metal scrap supply part. Can be used. In addition, by arrange | positioning the connection position of the exit of a gas conduction path and a metal waste supply part in the downstream of a metal waste supply part, a cracked gas can be made to contact metal waste reliably and waste heat is utilized effectively. be able to.

実施の形態1の金属屑処理装置の構成を示す模式正面図The schematic front view which shows the structure of the metal scrap processing apparatus of Embodiment 1. FIG. (a)実施の形態1の金属屑処理装置の金属屑搬送部を示す要部断面模式正面図 (b)図2(a)のA−A線矢視模式端面断面図(A) A-A taken along the line schematic end face cross-sectional view of a main portion sectional schematic front view showing a scrap metal conveying portion of the metal scrap processing device of Embodiment 1 (b) FIGS. 2 (a)

本発明の金属屑処理装置について、以下図面を参照しながら説明する。なお、本発明は以下に説明する実施の形態に限定されるものではない。
(実施の形態1)
図1は実施の形態1の金属屑処理装置の構成を示す模式正面図である。
図1中、1はアルミニウム、亜鉛、銅、鉄等の金属や真鍮、アルミニウム、ステンレス等の合金の加工時或いはこれらの金属製品の廃棄時に発生する金属屑に付着した切削油や研削油等の切削油剤、塗料、防錆剤等の各種付着物の加熱分解に用いられる実施の形態1における金属屑処理装置、2は金属屑処理装置1の金属屑搬送部、3は金属屑搬送部2の筒状の搬送路、3aは搬送路3の周壁、4は搬送路3の上流側に連設された金属屑処理装置1の金属屑供給部、5は搬送路3の下流側に連設された金属屑処理装置1の金属屑排出部、6はボイラー等により発生する乾き飽和蒸気を加熱して過熱蒸気を発生させ金属屑搬送部2に飽和蒸気及び/又は過熱蒸気を供給する金属屑処理装置1の蒸気供給部である。
The metal scrap processing apparatus of the present invention will be described below with reference to the drawings. The present invention is not limited to the embodiments described below.
(Embodiment 1)
FIG. 1 is a schematic front view showing the configuration of the metal scrap disposal apparatus of the first embodiment.
In FIG. 1, reference numeral 1 denotes cutting oil, grinding oil, or the like adhering to metal scrap generated when processing a metal such as aluminum, zinc, copper, or iron, or an alloy such as brass, aluminum, or stainless steel, or discarding these metal products. The metal waste disposal apparatus in Embodiment 1 used for thermal decomposition of various deposits such as cutting fluid, paint, rust preventive agent, etc., 2 is the metal waste transportation section of the metal waste disposal apparatus 1, and 3 is the metal waste transportation section 2. A cylindrical conveyance path, 3 a is a peripheral wall of the conveyance path 3, 4 is a metal scrap supply unit of the metal scrap processing apparatus 1 connected to the upstream side of the transport path 3, and 5 is connected to the downstream side of the transport path 3. The metal scrap discharge part of the scrap metal processing apparatus 1, 6 is a metal scrap treatment for heating dry saturated steam generated by a boiler or the like to generate superheated steam and supplying the steam and / or superheated steam to the metal scrap transporting section 2. It is a steam supply part of the apparatus 1.

金属屑供給部4は連続的又は間欠的に金属屑を供給できるものであればよい。金属屑供給部4がスクレーパーコンベアやスクリューコンベア等を備える場合は、多量の金属屑を連続的に処理することができ、装置の自動化が容易で操作性、作業効率性に優れる。また、金属屑供給部4にシャッター式の計量ダンパー等を備えてもよい。
尚、金属屑供給部4の前後にスライドゲート等を設けた場合、金属屑搬送部2の搬送路3内の気密性を上げ、酸素濃度を制御することができ、金属屑の酸化を防ぐことができる。
また、金属屑のサイズを調整するために、金属屑の破断や切断等を行う剪断式(一軸剪断破砕機等)や衝撃式(ハンマークラッシャー等)の前処理装置を金属屑供給部4の上流側に設けた場合、金属屑のサイズを調整することができ、加熱分解の効率性を向上させることができる。
The metal waste supply part 4 should just be what can supply metal waste continuously or intermittently. In the case where the metal scrap supply unit 4 includes a scraper conveyor, a screw conveyor, or the like, a large amount of metal scrap can be processed continuously, the apparatus can be easily automated, and the operability and work efficiency are excellent. Further, the metal scrap supply unit 4 may be provided with a shutter-type weighing damper or the like.
In addition, when a slide gate etc. are provided before and behind the metal waste supply part 4, the airtightness in the conveyance path 3 of the metal waste conveyance part 2 can be raised, oxygen concentration can be controlled, and oxidation of metal waste can be prevented. Can do.
Further, in order to adjust the size of the metal scrap, a pretreatment device of a shear type (uniaxial shear crusher etc.) or an impact type (hammer crusher etc.) for breaking or cutting the metal scrap is provided upstream of the metal scrap supply unit 4. When provided on the side, the size of the metal scrap can be adjusted, and the efficiency of the thermal decomposition can be improved.

次に、実施の形態1の金属屑処理装置の金属屑搬送部の詳細について説明する。
図2(a)は実施の形態1の金属屑処理装置の金属屑搬送部を示す要部断面模式正面図であり、図2(b)は図2(a)のA−A線矢視模式端面面図である。
図2(a)中、10は搬送路3に内挿された撹拌部、11は撹拌部10の回転軸、12は回転軸11の外周に配設された撹拌部10の螺旋状の羽根、12aは螺旋状の羽根12の間に形成された搬送路3内の空間、13は回転軸11の長手方向と平行に配設され羽根12の外周側を180度間隔で連結補強する2箇所の連結撹拌部、14は搬送路3の周壁3aの上面側に形成された複数のガス排出口、15は搬送路3の周壁3aの外側で複数のガス排出口14と連通し搬送路3内で金属屑の付着物が加熱分解されて発生する分解ガスを金属屑搬送部2から排出するガス導通路、15aはガス導通路15の端部に形成され金属屑供給部4の下流端部に連結されるガス導通路15の出口、16は撹拌部10の回転軸11の一端部に連結された金属屑搬送部2の駆動モーターである。
Next, the detail of the metal scrap conveyance part of the metal scrap processing apparatus of Embodiment 1 is demonstrated.
Fig.2 (a) is a principal part cross-section schematic front view which shows the metal scrap conveyance part of the metal scrap processing apparatus of Embodiment 1, FIG.2 (b) is a schematic view on the AA line of Fig.2 (a). it is an end cross-sectional view.
In FIG. 2A, 10 is a stirring unit inserted in the conveyance path 3, 11 is a rotating shaft of the stirring unit 10, 12 is a spiral blade of the stirring unit 10 disposed on the outer periphery of the rotating shaft 11, 12a is a space in the conveyance path 3 formed between the spiral blades 12, and 13 is arranged in parallel with the longitudinal direction of the rotary shaft 11 and is connected to the outer peripheral side of the blades 12 at 180 ° intervals. The connected agitation unit, 14 is a plurality of gas discharge ports formed on the upper surface side of the peripheral wall 3a of the conveyance path 3, and 15 is in communication with the plurality of gas discharge ports 14 outside the peripheral wall 3a of the conveyance path 3 in the conveyance path 3 A gas conduction path 15a for discharging the cracked gas generated when the deposits of metal scrap are thermally decomposed from the metal scrap conveying section 2, 15a is formed at the end of the gas conduction path 15 and is connected to the downstream end of the metal scrap supply section 4. The outlet of the gas conduction path 15, 16 is a metal connected to one end of the rotating shaft 11 of the stirring unit 10 A driving motor of the transport unit 2.

ガス排出口14の形状や大きさは適宜、選択することができるが、ガス排出口14を螺旋状の羽根12のピッチと同等の間隔で配置した場合、撹拌部10の回転中に、螺旋状の羽根12の間に形成された各々の空間12aが必ずガス排出口14の位置と重なって連通するので、各々のガス排出口14から確実かつ効率的に分解ガスを排出することができる。
撹拌部10の連結撹拌部13は螺旋状の羽根12の外周側を固定できるものであればよいが、平鋼(フラットバー)等の板状部材が好適に用いられる。連結撹拌部13により、螺旋状の羽根12の外周側で隣接する羽根同士を回転軸の長手方向に沿うように連結補強することにより、剛性を確保して羽根12の変形を防止することができる。また、連結撹拌部13が平板状であることにより、金属屑との接触面積を確保することができ、金属屑を効率的に掻き上げて撹拌効果を高めることができる。本実施の形態では、連結撹拌部13を円周方向に180度の間隔を空けて2箇所に配置したが、連結撹拌部13の数は、2箇所乃至8箇所の範囲で選択することが好ましい。連結撹拌部13の数が1箇所だけになると、羽根12が変形し易くなり、撹拌部10全体の剛性が低下して撓みが発生し易くなると共に撹拌効果が低下し易くなる傾向があり、8箇所より多くなるにつれ、撹拌に寄与しない連結撹拌部13が増え、撹拌部10全体の重量が増加して撹拌部10の回転に必要なエネルギーが増大し、金属屑の撹拌効率性、省エネルギー性が低下し易くなる傾向があることがわかったためである。
The shape and size of the gas discharge port 14 can be selected as appropriate. However, when the gas discharge ports 14 are arranged at an interval equivalent to the pitch of the spiral blades 12, a spiral shape is generated during the rotation of the stirring unit 10. Since each space 12a formed between the blades 12 necessarily overlaps and communicates with the position of the gas discharge port 14, the decomposition gas can be discharged from each gas discharge port 14 reliably and efficiently.
Although the connection stirring part 13 of the stirring part 10 should just be what can fix the outer peripheral side of the helical blade | wing 12, plate-shaped members, such as a flat steel (flat bar), are used suitably. By connecting and reinforcing the adjacent blades on the outer peripheral side of the spiral blade 12 along the longitudinal direction of the rotation shaft by the connection stirring unit 13, rigidity can be ensured and deformation of the blade 12 can be prevented. . Moreover, when the connection stirring part 13 is flat form, a contact area with metal waste can be ensured, metal scrap can be efficiently scraped up and the stirring effect can be heightened. In the present embodiment, the connected agitation units 13 are arranged at two positions with an interval of 180 degrees in the circumferential direction, but the number of the connected agitation units 13 is preferably selected in the range of 2 to 8 locations. . When the number of the connected stirring portions 13 is only one, the blade 12 is likely to be deformed, the rigidity of the stirring portion 10 as a whole is lowered and bending is likely to occur, and the stirring effect tends to be lowered. As the number of parts increases, the number of connected stirring parts 13 that do not contribute to stirring increases, the weight of the stirring part 10 as a whole increases, the energy required for rotation of the stirring part 10 increases, and the stirring efficiency and energy saving performance of the metal scrap are increased. This is because it has been found that there is a tendency to decrease.

図2(b)中、17は金属屑搬送部2の搬送路3の一側部に配設され蒸気供給部6(図1参照)と接続される蒸気供給管、18は蒸気供給管17と連通し搬送路3の長手方向に沿って配置された複数の蒸気噴射口である。
蒸気噴射口18の形状や配置は適宜、選択することができるが、搬送路3の長手方向に沿って複数の蒸気噴射口18を設けることにより、搬送路3の全長にわたって効率的に飽和蒸気及び/又は過熱蒸気を行き渡らせることができ、金属屑との接触効率を高めることができるので、飽和蒸気及び/又は過熱蒸気の供給量を低減することが可能で、省エネルギー性に優れる。また、蒸気噴射口18の1箇所当りの蒸気圧力を下げて効率的に蒸気を供給することができ、蒸気が過剰に供給されてショートパスすることを防止でき、省エネルギー性に優れる。さらに、蒸気噴射口18から噴射される蒸気圧力を下げることにより、粉塵爆発の危険性があるアルミニウム等の微粉の飛散を防ぐことができ、安全性に優れる。
尚、搬送路3の周壁3aに孔をあけて蒸気噴射口18を形成し、搬送路3の周壁3aの外周面側で蒸気供給管17と連通させることにより、搬送路3の内部に突起物がなく、撹拌部10の羽根12との干渉を防ぐことができ、羽根12の外周面と搬送路3の内周面との隙間を小さくして飽和蒸気及び/又は過熱蒸気のショートパスを防止できる。また、蒸気噴射口18を螺旋状の羽根12のピッチと同等の間隔で配置した場合、撹拌部10の回転中に、螺旋状の羽根12の間に形成された各々の空間12aが必ず蒸気噴射口18の位置と重なって連通するので、各々の蒸気噴射口18から空間12aに確実かつ効率的に飽和蒸気及び/又は過熱蒸気を供給することができる。
In FIG. 2B, 17 is a steam supply pipe disposed on one side of the transport path 3 of the metal scrap transport section 2 and connected to the steam supply section 6 (see FIG. 1), 18 is a steam supply pipe 17 and These are a plurality of vapor injection ports arranged along the longitudinal direction of the communication conveyance path 3.
The shape and arrangement of the steam injection port 18 can be selected as appropriate. However, by providing a plurality of steam injection ports 18 along the longitudinal direction of the transport path 3, saturated steam and Since the superheated steam can be spread and the contact efficiency with the metal scrap can be increased, the supply amount of saturated steam and / or superheated steam can be reduced, and the energy saving property is excellent. Further, it is possible to efficiently supply the steam by lowering the steam pressure per one point of the steam injection port 18, and it is possible to prevent the steam from being supplied excessively and to make a short pass, and the energy saving property is excellent. Furthermore, by lowering the vapor pressure injected from the vapor injection port 18, scattering of fine powders such as aluminum having a risk of dust explosion can be prevented, and the safety is excellent.
In addition, a hole is formed in the peripheral wall 3a of the conveyance path 3 to form a vapor injection port 18, and the protrusion is formed inside the conveyance path 3 by communicating with the steam supply pipe 17 on the outer peripheral surface side of the peripheral wall 3a of the conveyance path 3. And can prevent interference with the blade 12 of the agitating unit 10 and reduce the gap between the outer peripheral surface of the blade 12 and the inner peripheral surface of the transport path 3 to prevent a short path of saturated steam and / or superheated steam. it can. Further, when the steam injection ports 18 are arranged at an interval equivalent to the pitch of the spiral blades 12, each space 12 a formed between the spiral blades 12 is necessarily steam-injected during the rotation of the stirring unit 10. Since it overlaps and communicates with the position of the port 18, saturated steam and / or superheated steam can be reliably and efficiently supplied from each of the steam injection ports 18 to the space 12 a.

以上のように構成された実施の形態1の金属屑処理装置の動作について説明する。
図1の蒸気供給部6から供給される飽和蒸気及び/又は過熱蒸気は、蒸気供給管17を通り、各々の蒸気噴射口18から金属屑搬送部2の搬送路3の内部に噴射される。
また、図1の金属屑供給部4から供給された金属屑は搬送路3の上流側に投入される。
図2において駆動モーター16で撹拌部10を回転させることにより、金属屑は搬送路3に沿って下流側(図2(a)の右側から左側)に搬送される。金属屑が搬送路3を通過する間に、蒸気噴射口18から噴射される100℃〜200℃の飽和蒸気及び/又は150℃〜600℃の過熱蒸気により、金属屑に付着した水分が蒸発し、切削油剤、塗料、防錆剤等の付着物が加熱分解され、除去される。
付着物が除去された金属屑は搬送路3の下流側の金属屑排出部5から排出され、回収されて金属資源として再利用される。
Operation | movement of the metal waste processing apparatus of Embodiment 1 comprised as mentioned above is demonstrated.
Saturated steam and / or superheated steam supplied from the steam supply unit 6 in FIG. 1 passes through the steam supply pipe 17 and is injected into the inside of the conveyance path 3 of the metal scrap conveyance unit 2 from each vapor injection port 18.
Moreover, the metal scrap supplied from the metal scrap supply part 4 of FIG. 1 is thrown into the upstream side of the conveyance path 3.
In FIG. 2, the metal scrap is transported downstream (from the right side to the left side in FIG. 2A) along the transport path 3 by rotating the stirring unit 10 with the drive motor 16. While the metal debris passes through the transport path 3, the moisture adhering to the metal debris evaporates due to the saturated steam of 100 ° C. to 200 ° C. and / or the overheated steam of 150 ° C. to 600 ° C. ejected from the steam injection port 18. Deposits such as cutting fluid, paint, and rust preventive are thermally decomposed and removed.
The metal scrap from which the deposits have been removed is discharged from the metal scrap discharge section 5 on the downstream side of the transport path 3, and is collected and reused as a metal resource.

図2において金属屑供給部4にはブロワ(図示せず)が接続されており、付着物の加熱分解によって搬送路3の内部で発生した分解ガスや蒸気は吸引され、ガス排出口14からガス導通路15を通り、金属屑供給部4を経由して系外に排出される。このとき、分解ガスの熱を有効に利用して、金属屑供給部4から供給される金属屑を予備加熱することができ、金属屑搬送部2における処理時間を短縮することができる。排出された分解ガスは、熱交換器で冷却した後、湿式スクラバーで捕集することにより、未燃ガスの爆発や分解ガスに同伴して排出されるアルミニウム等の微粉による粉塵爆発を防ぐことができる。このとき、分解ガスを冷却して得られる油分と水分は、エマルジョン化して燃料として再利用することもできる。尚、付着物の加熱分解によって発生する分解ガスの安全な処理、脱臭等の目的で、燃焼処理してもよく、さらにその排熱を金属屑の予備加熱に利用してもよい。
尚、金属屑が搬送路3の内部を上流から下流に向かって移動するにつれ、付着物の加熱、分解が進行し、分解ガスが発生するので、搬送路3の少なくとも下流側に1乃至複数のガス排出口14は設ければよいが、本実施の形態のように搬送路3のほぼ全長に渡って複数のガス排出口14を設けることにより、搬送路3の内部で発生した分解ガスを搬送路3全体から効率的に排出させることができる。
また、本実施の形態では、ガス導通路15の出口15aを金属屑供給部4に接続することにより、分解ガスの熱を利用して金属屑の予備加熱を行ったが、必ずしもガス導通路15の出口15aを金属屑供給部4に接続する必要はなく、ガス導通路15から排出される分解ガスを直接、熱交換器で冷却してもよいし、過熱蒸気発生装置等の加熱に利用してもよい。
In FIG. 2, a blower (not shown) is connected to the metal scrap supply unit 4, and the decomposition gas and vapor generated inside the conveyance path 3 due to thermal decomposition of the deposits are sucked and gas is discharged from the gas discharge port 14. It passes through the conduction path 15 and is discharged out of the system via the metal scrap supply unit 4. At this time, by effectively utilizing the heat of the cracked gas, the metal scrap supplied from the metal scrap supply unit 4 can be preheated, and the processing time in the metal scrap transport unit 2 can be shortened. The discharged cracked gas is cooled by a heat exchanger and collected by a wet scrubber to prevent explosion of unburned gas and dust explosion caused by fine powder such as aluminum discharged along with cracked gas. it can. At this time, the oil and water obtained by cooling the cracked gas can be emulsified and reused as fuel. In addition, you may carry out a combustion process for the objective of the safe process of the decomposition gas generated by the thermal decomposition of a deposit | attachment, a deodorizing, etc., and you may utilize the waste heat for the preliminary heating of a metal scrap.
As the metal scrap moves from the upstream side to the downstream side of the conveyance path 3, the deposits are heated and decomposed to generate decomposition gas. The gas discharge port 14 may be provided, but by providing a plurality of gas discharge ports 14 over almost the entire length of the transfer path 3 as in the present embodiment, the cracked gas generated inside the transfer path 3 is transferred. It can be efficiently discharged from the entire path 3.
Further, in the present embodiment, by connecting the outlet 15a of the gas conduction path 15 to the metal waste supply unit 4, the metal waste is preheated using the heat of the cracked gas. It is not necessary to connect the outlet 15a of the gas to the metal scrap supply unit 4, and the cracked gas discharged from the gas conduction path 15 may be directly cooled by a heat exchanger or used for heating a superheated steam generator or the like. May be.

実施の形態1における金属屑処理装置によれば、以下の作用を有する。
(1)金属屑搬送部の上流側に連設された金属屑供給部と、金属屑搬送部の下流側に連設された金属屑排出部と、金属屑搬送部に飽和蒸気及び/又は過熱蒸気を供給する蒸気供給部を有することにより、金属屑供給部から供給された金属屑が金属屑搬送部で搬送されて金属屑排出部から排出されるまでの間に、金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を、蒸気供給部から供給される飽和蒸気及び/又は過熱蒸気によって短時間で加熱分解して取り除くことができ、省エネルギー性に優れる。
(2)金属屑搬送部が、筒状の搬送路と、搬送路に内挿された撹拌部を有することにより、撹拌部で金属屑を搬送しながら、蒸気供給部から供給される飽和蒸気及び/又は過熱蒸気と金属屑を確実に接触させて、金属屑の表面に付着した付着物を効率的に加熱分解することができ、付着物除去の効率性、確実性に優れる。
(3)金属屑搬送部が、搬送路の周壁の上面側に形成された1以上のガス排出口と、搬送路の周壁の外側でガス排出口と連通し金属屑の付着物が加熱分解されて発生する分解ガスを金属屑搬送部から排出するガス導通路を有することにより、金属屑の付着物が加熱分解されて発生する分解ガスを各々のガス排出口から確実かつ効率的に排出させ、ガス導通路に沿ってスムーズに移動させて金属屑搬送部から系外に排出することができ、分解ガスの排出性に優れる。
(4)筒状の搬送路に撹拌部が内挿されることにより、ロータリーキルン等に比べて無駄な空間が少なく、装置をコンパクト化することができ、省スペース性に優れると共に、放熱ロスも少なく、加熱の効率性に優れる。
(5)乾燥処理材等を使用することなく飽和蒸気及び/又は過熱蒸気のみで金属屑の付着物を加熱分解して除去することができ、省資源性に優れると共に、金属屑に乾燥処理材等が付着することがなく、乾燥処理材等を分離する機構や工程が不要で、付着物のない金属屑を得ることができ、また酸化による劣化も防ぐことができるため、高歩留まりで金属屑のリサイクル性に優れる。
(6)撹拌部の回転数を制御するだけで搬送路内の金属屑の滞留時間をコントロールすることができるので、金属屑の大きさ、形状、嵩比重或いは付着物の種類等に応じて、必要な滞留時間を設定することにより、金属屑の付着物を確実に加熱分解することができ、操作性、汎用性、処理効率性に優れる。
(7)撹拌部が、回転軸の外周に配設された螺旋状の羽根と、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、搬送路と近接する羽根の外周側において連結撹拌部で金属屑を掻き上げるようにして撹拌することができ、金属屑と飽和蒸気及び/又は過熱蒸気を確実に接触させて金属屑の表面に付着した付着物を効率的に加熱分解しながら搬送することができ、省エネルギー性、付着物除去の効率性に優れる。
(8)撹拌部が、螺旋状の羽根を有することにより、様々な形状や嵩比重の金属屑に対して、撹拌部を回転させるモーターの回転数を制御するだけで、搬送路内の金属屑の滞留時間を正確にコントロールして付着物を確実に加熱分解することができ、加熱分解処理の確実性、安定性に優れる。
(9)撹拌部が、回転軸の外周に配設された螺旋状の羽根と、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、スクリューフィーダーと同等の剛性と搬送効率、金属屑の搬送の定量性を保つことができ、付着物の加熱分解の効率性に優れる。
(10)撹拌部が、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、撹拌部の強度を向上させることができるので、羽根の厚みを薄くして撹拌部の軽量化を図り、羽根の外周部と搬送路内表面との摩擦を軽減することができ、金属屑搬送部の耐久性、長寿命性に優れる。
(11)撹拌部が、回転軸の長手方向と平行に配設され羽根の外周側を連結補強する連結撹拌部を有することにより、撹拌部の剛性を保つことができ、ブリケットやダイカストのバリ等の塊状の金属屑或いは様々な形状や比重の金属屑に対しても、羽根の変形や破損等の発生を効果的に防止して、金属屑を確実に搬送することができ、金属屑の搬送の信頼性、確実性に優れる。
(12)撹拌部の螺旋状の羽根が回転軸の外周に配設されているので、十分な剛性を確保して撓みや変形を防止して撹拌部を確実に回転させることができ、動作の安定性に優れる。
(13)金属屑搬送部のガス排出口が、螺旋状の羽根のピッチと同等の間隔で複数配置されている場合、撹拌部の回転中に、螺旋状の羽根の間に形成された各々の空間とガス排出口を確実に連通させ、金属屑の付着物が加熱分解されて発生する分解ガスを確実かつ効率的に排出することができ、分解ガスの排出の確実性、効率性に優れる。
(14)金属屑搬送部が、蒸気供給部と連結され金属屑搬送部の搬送路の周壁に形設された蒸気噴射口を有するので、蒸気噴射口から搬送路の内部に確実に飽和蒸気及び/又は過熱蒸気を噴射して金属屑の付着物を効率的に加熱分解することができ、加熱分解の効率性、安定性に優れる。
(15)金属屑搬送部のガス導通路の出口が金属屑供給部と連結されることにより、搬送路内で金属屑の付着物が加熱分解されて発生する分解ガスを金属屑供給部から系外に確実に排出することができると共に、分解ガスの熱を有効に利用して、金属屑供給部から供給される金属屑を予備加熱することができ、金属屑搬送部における処理時間を短縮することが可能で省エネルギー性に優れる。
According to the metal scrap processing apparatus in Embodiment 1, it has the following effects.
(1) Scrap supply and / or superheated metal scrap supply section connected to the upstream side of the metal scrap transport section, metal scrap discharge section connected to the downstream side of the metal scrap transport section, and metal scrap transport section By having the steam supply part that supplies steam, the metal scrap supplied from the metal scrap supply part is transported by the metal scrap transport part and discharged from the metal scrap discharge part. Various deposits such as oil, paint, and rust preventive agent can be removed by thermal decomposition in a short time with saturated steam and / or superheated steam supplied from the steam supply unit, which is excellent in energy saving.
(2) Since the metal scrap conveyance unit has a cylindrical conveyance path and an agitation unit inserted in the conveyance path, saturated vapor supplied from the steam supply unit while conveying the metal scrap in the agitation unit and It is possible to reliably contact the superheated steam and the metal scrap, and to efficiently decompose the deposit attached to the surface of the metal scrap, thereby improving the efficiency and certainty of removing the deposit.
(3) One or more gas exhaust ports formed on the upper surface side of the peripheral wall of the transport path are connected to the gas exhaust port on the outer side of the peripheral wall of the transport path, and the metal scrap deposit is thermally decomposed. By having a gas conduction path that discharges the cracked gas generated from the metal scrap conveying part, the cracked gas generated by the thermal decomposition of the deposit of metal scrap is reliably and efficiently discharged from each gas discharge port, It can be smoothly moved along the gas conduction path and discharged out of the system from the metal scrap conveying section, and the decomposition gas discharge is excellent.
(4) The stirrer is inserted into the cylindrical conveyance path, so that there is less wasted space than a rotary kiln, etc., the device can be made compact, it is excellent in space saving, and there is little heat loss. Excellent heating efficiency.
(5) It is possible to remove metal waste deposits by thermal decomposition only with saturated steam and / or superheated steam without using a drying treatment material, etc. Is not attached, and there is no need for a mechanism or process for separating the dry processing material, etc., and it is possible to obtain metal scrap without deposits and to prevent deterioration due to oxidation. Excellent recyclability.
(6) Since it is possible to control the residence time of the metal scraps in the transport path only by controlling the number of revolutions of the stirring unit, according to the size, shape, bulk specific gravity or the kind of deposits of the metal scraps, By setting the necessary residence time, the deposits of metal scrap can be surely thermally decomposed, and the operability, versatility, and processing efficiency are excellent.
(7) The stirrer has a spiral blade disposed on the outer periphery of the rotating shaft and a connecting stirring unit disposed in parallel with the longitudinal direction of the rotating shaft to reinforce the outer peripheral side of the blade. It is possible to stir by scraping metal scraps at the connecting stirrer on the outer peripheral side of the blades close to the road, and the metal scraps and saturated steam and / or superheated steam are brought into contact with each other and adhered to the surface of the metal scraps. The deposit can be transported while being efficiently decomposed by heat, and is excellent in energy saving and deposit removal efficiency.
(8) Since the stirring unit has spiral blades, metal scraps in the conveyance path can be controlled simply by controlling the number of revolutions of the motor that rotates the stirring unit for metal scraps of various shapes and bulk specific gravity. It is possible to accurately heat and decompose the deposit by accurately controlling the residence time of the resin, and it is excellent in the reliability and stability of the heat decomposition treatment.
(9) Since the stirring unit has a spiral blade disposed on the outer periphery of the rotating shaft and a connecting stirring unit that is disposed in parallel with the longitudinal direction of the rotating shaft and reinforces the outer peripheral side of the blade, the screw It can maintain the same rigidity and transport efficiency as the feeder and the quantitativeness of the transport of metal scraps, and is excellent in the efficiency of thermal decomposition of deposits.
(10) Since the stirrer has a connecting stirrer that is arranged in parallel with the longitudinal direction of the rotating shaft and that reinforces the outer peripheral side of the blade, the strength of the stirrer can be improved. By reducing the thickness of the agitator, the friction between the outer peripheral portion of the blade and the inner surface of the conveyance path can be reduced, and the durability and long life of the metal scrap conveyance unit are excellent.
(11) The stirrer has a connecting stirrer that is arranged in parallel with the longitudinal direction of the rotating shaft and connects and reinforces the outer peripheral side of the blades, whereby the rigidity of the stirrer can be maintained, such as briquettes and die cast burrs, etc. It is possible to effectively prevent the occurrence of deformation and breakage of blades, and to reliably transport metal scrap, even if it is a lump of metal scrap or metal scrap of various shapes and specific gravity. Excellent reliability and reliability.
(12) Since the spiral blades of the stirring unit are arranged on the outer periphery of the rotating shaft, the stirring unit can be reliably rotated by ensuring sufficient rigidity and preventing bending and deformation. Excellent stability.
(13) When a plurality of gas discharge ports of the metal scrap conveying unit are arranged at intervals equivalent to the pitch of the spiral blades, each of the gas discharge ports formed between the spiral blades during the rotation of the stirring unit The space and the gas discharge port are reliably communicated, and the cracked gas generated by the thermal decomposition of the deposits of the metal scrap can be discharged reliably and efficiently, and the discharge gas is reliably and efficiently discharged.
(14) Since the metal scrap transport unit has a steam injection port connected to the steam supply unit and formed on the peripheral wall of the transport path of the metal scrap transport unit, the saturated steam and It is possible to efficiently decompose the deposits of metal scraps by injecting superheated steam, and the heat decomposition efficiency and stability are excellent.
(15) By connecting the outlet of the gas conduction path of the metal scrap conveying section to the metal scrap supplying section, the decomposition gas generated by the thermal decomposition of the metal scrap deposits in the transport path is generated from the metal scrap supplying section. As well as being able to discharge to the outside reliably, it is possible to preheat the metal scrap supplied from the metal scrap supply section by effectively using the heat of the cracked gas, and shorten the processing time in the metal scrap transport section It is possible and excellent in energy saving.

本発明は、金属屑に付着した切削油剤、塗料、防錆剤等の各種付着物を短時間で確実かつ効率的に加熱分解して取り除くことができ、高歩留まりで処理能力が高く、省資源性、省エネルギー性に優れると共に、コンパクトで安全性、取扱い性、省スペース性に優れた金属屑処理装置の提供を行い、金属屑の有効利用を促進して環境保護、省資源化に貢献することができる。   The present invention can remove various deposits such as cutting fluids, paints, and rust preventives adhering to metal scraps by heat and decomposition in a short time and with high yield, high processing capacity, and resource saving. Contribute to environmental protection and resource saving by promoting the effective use of metal scraps by providing compact, safe, easy-to-use, and space-saving metal scrap disposal equipment. Can do.

1 金属屑処理装置
2 金属屑搬送部
3 搬送路
3a 周壁
4 金属屑供給部
5 金属屑排出部
6 蒸気供給部
10 撹拌部
11 回転軸
12 羽根
12a 空間
13 連結撹拌部
14 ガス排出口
15 ガス導通路
15a 出口
16 駆動モーター
17 蒸気供給管
18 蒸気噴射口
DESCRIPTION OF SYMBOLS 1 Metal waste processing apparatus 2 Metal waste conveyance part 3 Conveyance path 3a Perimeter wall 4 Metal waste supply part 5 Metal waste discharge part 6 Steam supply part 10 Stirring part 11 Rotating shaft 12 Blade 12a Space 13 Connection stirring part 14 Gas discharge port 15 Gas guide Passage 15a Outlet 16 Drive motor 17 Steam supply pipe 18 Steam injection port

Claims (5)

金属屑の付着物を飽和蒸気及び/又は過熱蒸気で加熱分解する金属屑処理装置であって、
金属屑搬送部と、前記金属屑搬送部の上流側に連設された金属屑供給部と、前記金属屑搬送部の下流側に連設された金属屑排出部と、前記金属屑搬送部の搬送路の一側部に配設され前記飽和蒸気及び/又は前記過熱蒸気を供給する蒸気供給部と接続された蒸気供給管と、前記蒸気供給管と連通し前記搬送路の側壁に孔をあけて形成された複数の蒸気噴射口と、を有し、前記金属屑搬送部が、筒状の搬送路と、前記搬送路に内挿された撹拌部と、前記搬送路の周壁の上面側に形成された1以上のガス排出口と、前記搬送路の前記周壁の外側で前記ガス排出口と連通し前記金属屑の付着物が加熱分解されて発生する分解ガスを前記金属屑搬送部から排出するガス導通路と、を備えたことを特徴とする金属屑処理装置。
A metal scrap disposal device that thermally decomposes deposits of metal scrap with saturated steam and / or superheated steam,
A metal scrap conveying section, a metal scrap supplying section connected to the upstream side of the metal scrap transport section, a metal scrap discharging section connected to the downstream side of the metal scrap transport section, and the metal scrap transport section. A steam supply pipe disposed on one side of the transport path and connected to the steam supply section for supplying the saturated steam and / or the superheated steam, and a hole is formed in the side wall of the transport path in communication with the steam supply pipe. A plurality of vapor injection ports formed on the upper surface side of the peripheral wall of the conveyance path, the metal scrap conveyance unit, the cylindrical conveyance path, the stirring unit inserted in the conveyance path One or more formed gas discharge ports and the gas discharge port communicated with the gas discharge port outside the peripheral wall of the transfer path, and the decomposition gas generated by the thermal decomposition of the deposits of the metal scrap is discharged from the metal scrap transfer unit. A metal waste disposal apparatus comprising a gas conduction path.
前記撹拌部が、回転軸の外周に配設された螺旋状の羽根と、前記回転軸の長手方向と平行に配設され前記羽根の外周側を連結補強する連結撹拌部と、を備えたことを特徴とする請求項1に記載の金属屑処理装置。 The stirring unit includes a spiral blade disposed on the outer periphery of the rotating shaft, and a connecting stirring unit that is disposed in parallel with the longitudinal direction of the rotating shaft and connects and reinforces the outer peripheral side of the blade. The metal scrap processing apparatus according to claim 1, wherein: 前記金属屑搬送部の前記ガス排出口が、螺旋状の前記羽根のピッチと同等の間隔で複数配置されていることを特徴とする請求項に記載の金属屑処理装置。 The metal waste processing apparatus according to claim 1 , wherein a plurality of the gas discharge ports of the metal waste transport unit are arranged at intervals equivalent to a pitch of the spiral blades. 前記蒸気噴射口が、前記撹拌部の螺旋状の前記羽根のピッチと同等の間隔で複数形成されていることを特徴とする請求項1又は2に記載の金属屑処理装置。3. The metal scrap processing apparatus according to claim 1, wherein a plurality of the steam injection ports are formed at an interval equivalent to a pitch of the spiral blades of the stirring unit. 前記金属屑搬送部の前記ガス導通路の出口が前記金属屑供給部と連結されていることを特徴とする請求項1、3又は4の内いずれか1項に記載の金属屑処理装置。 5. The metal scrap processing apparatus according to claim 1, wherein an outlet of the gas conduction path of the metal scrap transport unit is connected to the metal scrap supply unit.
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JP2008024388A (en) * 2006-07-19 2008-02-07 Mitsubishi Materials Corp Screw conveyer
JP2011012326A (en) * 2009-07-06 2011-01-20 Morikawa Sangyo Kk Method for cleaning and drying machining chip and method for reusing casting material with the use of treated machining chip
JP2012179592A (en) * 2011-02-10 2012-09-20 Uni Kikai Kk Separation device
JP2013046882A (en) * 2011-08-27 2013-03-07 Vioce Co Ltd Drying device of sludge or the like

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