JP5178256B2 - Solidified product manufacturing apparatus and method for grinding sludge - Google Patents

Solidified product manufacturing apparatus and method for grinding sludge Download PDF

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JP5178256B2
JP5178256B2 JP2008064526A JP2008064526A JP5178256B2 JP 5178256 B2 JP5178256 B2 JP 5178256B2 JP 2008064526 A JP2008064526 A JP 2008064526A JP 2008064526 A JP2008064526 A JP 2008064526A JP 5178256 B2 JP5178256 B2 JP 5178256B2
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grinding
sludge
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正三 後藤
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/04Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams
    • B30B9/047Control arrangements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B30PRESSES
    • B30BPRESSES IN GENERAL
    • B30B9/00Presses specially adapted for particular purposes
    • B30B9/02Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
    • B30B9/04Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams
    • B30B9/06Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams co-operating with permeable casings or strainers
    • B30B9/067Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams co-operating with permeable casings or strainers with a retractable abutment member closing one end of the press chamber

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  • Mechanical Engineering (AREA)
  • Treatment Of Sludge (AREA)

Description

この発明は、研削ラインで発生した研削スラッジ、例えば、転がり軸受の内外輪や転動体等の鉄系構成部品、その他の軸受用鋼材の研削スラッジをブリケットに固形化する研削スラッジの固形化物製造装置および製造方法に関する。   The present invention relates to a grinding sludge solidified product manufacturing apparatus for solidifying grinding sludge generated in a grinding line, for example, iron-based components such as inner and outer rings of rolling bearings, rolling elements, and other grinding steel sludge into briquettes. And a manufacturing method.

転がり軸受の内外輪や転動体等の鉄系構成部品は、焼入れの後、転走面等に研削が施される。研削により生じた粉状の切削屑は、クーラントと共にスラッジとして機外に流して排出し、ろ過の後、クーラントを研削に再利用する。ろ過により残った研削スラッジは、汚泥として埋め立て処理される。
しかし、研削スラッジの埋め立ては、環境の面から好ましくないばかりでなく、産廃処理場の行き詰まりから、今後、埋め立て処理ができなくなることは明白である。研削で生じた研削屑の量は、切削等に比べて少ないが、軸受等のような量産ラインでは、その発生量は多量となる。
Iron-based components such as inner and outer rings of rolling bearings and rolling elements are ground on the rolling surfaces after quenching. Powdered cutting waste generated by grinding flows out as a sludge to the outside of the machine and is discharged, and after filtration, the coolant is reused for grinding. The grinding sludge remaining after filtration is landfilled as sludge.
However, it is clear that landfilling of grinding sludge is not preferable from the viewpoint of the environment, and that landfill processing will not be possible in the future due to the dead end of the industrial waste treatment plant. The amount of grinding waste generated by grinding is smaller than that of cutting or the like, but in a mass production line such as a bearing, the amount generated is large.

このため、研削スラッジを圧搾することにより固形化し、絞り出されたクーラントを再利用すると共に、その固形化物(以下、「ブリケット」という)を製鋼材として再利用することが検討されている。特許文献1および特許文献2には、研削スラッジを固形化する装置ないしは方法について開示されている。特許文献1では、温度、クーラントの含有率、加圧速度の変化および加圧圧力の変化を検出して、加圧速度を制御することが述べられている。また、特許文献2では、一定昇圧速度での圧搾の方法が述べられている。
特許第3907917号公報 特許第3979137号公報
For this reason, it is considered that the coolant that has been solidified by squeezing the grinding sludge and reused the squeezed coolant and that the solidified product (hereinafter referred to as “briquette”) is reused as a steel product. Patent Documents 1 and 2 disclose an apparatus or method for solidifying grinding sludge. Patent Document 1 describes that the pressurization speed is controlled by detecting changes in temperature, coolant content, pressurization speed, and pressurization pressure. Patent Document 2 describes a method of squeezing at a constant pressure increase speed.
Japanese Patent No. 3907717 Japanese Patent No. 3979137

上記のような研削スラッジの固形化において、成形圧力や成形速度を最適に設定しても、研削スラッジの性状が、例えば、ろ過などの前処理工程での仕上がり状況により変動すると、成形性が悪くなる場合がある。また、金型の摩耗によっても成形性が影響される。より具体的には、当初良好な成形がなされていても、例えば、研削スラッジにおけるクーラントの含有率が高くなると、あるいは、金型の摩耗が進行すると、成形時に金型隙間から研削スラッジが空気やクーラントと共に噴出し、正常な成形ができない場合がある。この場合、成形速度を下げて噴出を避ける調整がなされるが、安全をみて下げ過ぎると処理能力が低下する。また、研削スラッジの性状の変動や金型の摩耗に応じて成形条件を調整するのは煩雑で、効率の良い稼動、安定した稼動が実現できなかった。   In the solidification of grinding sludge as described above, even if the molding pressure and molding speed are set optimally, if the properties of the grinding sludge fluctuate depending on the finishing conditions in the pretreatment process such as filtration, the moldability is poor. There is a case. The moldability is also affected by the wear of the mold. More specifically, even if good molding is initially performed, for example, when the content of coolant in the grinding sludge increases or when the wear of the mold progresses, the grinding sludge is removed from the mold gap during molding. It may be sprayed with coolant and normal molding may not be possible. In this case, adjustment is made to reduce the molding speed to avoid ejection, but if it is too low for safety reasons, the processing capacity will be reduced. In addition, it is complicated to adjust the molding conditions according to the change in properties of the grinding sludge and the wear of the mold, and efficient operation and stable operation cannot be realized.

特許文献1には、所定の圧力および所定の圧縮速度に制御する方法が述べられているが、研削スラッジの加圧成形の際に、空気やヘドロ状スラッジの噴出に伴うと思われる成形圧の圧力変動に着眼した対応は述べられていない。また、特許文献2は、良好な仕上がり状態を得るための一定昇圧速度の有効性を述べているだけで、上記同様の成形圧の圧力変動に着眼した対応は述べられていない。   Patent Document 1 describes a method of controlling to a predetermined pressure and a predetermined compression speed, but the pressure of the molding pressure that is likely to be accompanied by the ejection of air or sludge sludge during pressure molding of the grinding sludge. No response has been described focusing on pressure fluctuations. Further, Patent Document 2 only describes the effectiveness of a constant pressure increase speed for obtaining a good finished state, and does not describe the correspondence focusing on the pressure fluctuation of the molding pressure similar to the above.

この発明の目的は、加圧シリンダによる圧搾によって研削スラッジを固形化する際に、研削スラッジなどの噴出に伴う成形圧の圧力変動があっても、これを自動的に調整して固形化を円滑に行い、装置の効率よい稼動を実現することができる研削スラッジの固形化物製造装置および製造方法を提供することである。   The object of the present invention is to smooth the solidification by automatically adjusting the pressure fluctuation of the molding pressure accompanying the ejection of the grinding sludge, etc., when the grinding sludge is solidified by pressing with a pressure cylinder. And providing a grinding sludge solidified material manufacturing apparatus and manufacturing method capable of realizing efficient operation of the apparatus.

この発明に係る研削スラッジの固形化物製造装置は、研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造装置であって、前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを備え、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させる加圧速度制御手段を設けたことを特徴とする。 The grinding sludge solidified product manufacturing apparatus according to the present invention is a method for producing a solidified product of a ground sludge that is produced by solidifying a concentrated sludge obtained by filtering a coolant-containing grinding sludge generated in a grinding line by pressing with a pressure cylinder. an apparatus, wherein a pressure sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, extracting only rapid change process and signal processing apparatus for the a pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal is set to come to exceed the constant change rate, provided the inflation speed control means for adjusting in accordance with the setting based on the pressurization rate of the pressure cylinder to the pressing speed adjusting means And wherein the door.

この発明に係る研削スラッジの固形化物製造方法は、研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造方法であって、前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを用い、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させることを特徴とする。 A method for producing a solidified product of a grinding sludge according to the present invention is a method for producing a solidified product of a ground sludge in which a concentrated sludge obtained by filtering a coolant-containing grinding sludge generated in a grinding line is solidified by pressing with a pressure cylinder to produce a solidified product. a method, a pressure detection sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, extracting only rapid change process and signal processing apparatus for, the use of a pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal is set to come to exceed the constant change rate, and wherein the to be adjusted according to set criteria for pressurization rate of the pressure cylinder to the pressing speed adjusting means.

この発明の構成によると、研削ラインで発生したクーラント含有の研削スラッジはろ過されて濃縮スラッジとされ、加圧シリンダによる圧搾によって固形化物とされる。この時、研削スラッジの圧搾時に、加圧シリンダの圧力が圧力センサによって監視され、この圧力センサによる信号が信号処理装置によって処理される。そして、信号処理装置により検出される加圧時の圧力が設定変動率よりも急激な変動があったときに、加圧速度調整手段に加圧シリンダの加圧速度を設定基準に従って調整させる。したがって、加圧時において、加圧速度や研削スラッジの性状によって、装置の隙間から研削スラッジが空気やクーラントと共に噴出して正常な成形ができない事態になっても、加圧シリンダの加圧速度が自動的に調整され、速やかに正常な状態に復帰する。因みに、良好な固形化物を得るには、加圧速度を遅くする方が望ましいが、処理能力が低下することになる。しかし、加圧時の圧力の急激な変動があったときに加圧速度が自動的に調整されるから、処理効率と成形品(固形化物)の歩留まりとをバランスさせ、効率良くかつ安定した装置の稼動を実現することができる。   According to the configuration of the present invention, the coolant-containing grinding sludge generated in the grinding line is filtered to be concentrated sludge, and solidified by pressing with a pressure cylinder. At this time, when the grinding sludge is squeezed, the pressure of the pressure cylinder is monitored by the pressure sensor, and the signal from the pressure sensor is processed by the signal processing device. Then, when the pressure at the time of pressurization detected by the signal processing apparatus fluctuates more rapidly than the set fluctuation rate, the pressurization speed adjusting means adjusts the pressurization speed of the pressurization cylinder according to the set standard. Therefore, during pressurization, the pressurization speed of the pressurizing cylinder is not affected by the pressurization speed and properties of the grinding sludge, even if the grinding sludge is ejected from the gap between the devices together with air or coolant and normal molding cannot be performed. It is automatically adjusted and quickly returns to normal. Incidentally, in order to obtain a good solidified product, it is desirable to reduce the pressurization speed, but the processing ability will be lowered. However, since the pressurization speed is automatically adjusted when there is a sudden change in pressure during pressurization, an efficient and stable device that balances the processing efficiency and the yield of the molded product (solidified product). Can be realized.

この発明に係る研削スラッジの固形化物製造装置は、研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造装置であって、前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを備え、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させる加圧速度制御手段を設けたため、簡便な方法で、装置の隙間から研削スラッジが空気やクーラントと共に噴出して正常な成形ができない事態になっても、速やかに正常な状態に復帰させることができ、装置の効率の良い稼動および安定した稼動を実現させることができる。 The grinding sludge solidified product manufacturing apparatus according to the present invention is a method for producing a solidified product of a ground sludge that is produced by solidifying a concentrated sludge obtained by filtering a coolant-containing grinding sludge generated in a grinding line by pressing with a pressure cylinder. an apparatus, wherein a pressure sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, extracting only rapid change process and signal processing apparatus for the a pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal is set to come to exceed the constant change rate, provided the inflation speed control means for adjusting in accordance with the setting based on the pressurization rate of the pressure cylinder to the pressing speed adjusting means Therefore, even if grinding sludge is ejected with air and coolant from the gaps of the equipment through a simple method and normal molding cannot be performed, it can be quickly returned to the normal state and the equipment can be operated efficiently. In addition, stable operation can be realized.

この発明に係る研削スラッジの固形化物製造方法は、研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造方法であって、前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを用い、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させることとしたため、上記と同様に、簡便な方法で、装置の隙間から研削スラッジが空気やクーラントと共に噴出して正常な成形ができない事態になっても、速やかに正常な状態に復帰させることができ、装置の効率の良い稼動および安定した稼動を実現させることができる。
A method for producing a solidified product of a grinding sludge according to the present invention is a method for producing a solidified product of a ground sludge in which a concentrated sludge obtained by filtering a coolant-containing grinding sludge generated in a grinding line is solidified by pressing with a pressure cylinder to produce a solidified product. a method, a pressure detection sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, extracting only rapid change process and signal processing apparatus for, the use of a pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal is set to come to exceed the constant change rate, since it was decided to adjust according to the set reference pressurization rate of the pressure cylinder to the pressing speed adjusting means, the and the In addition, even when grinding sludge is ejected from the gaps between the devices together with air and coolant and normal molding cannot be performed by a simple method, the normal operation can be quickly resumed and the equipment can be operated efficiently. In addition, stable operation can be realized.

この発明に係る研削スラッジの固形化物製造装置の一実施形態を図1ないし図5と共に説明する。図1および図2に示す固形化物製造装置Aおいて、ホッパー1には、図示しない研削ラインで発生したクーラントを含有する研削スラッジを濾過した濃縮スラッジ(研削スラッジ)Mが貯蔵される。ホッパー1の下端には、モータ2aを駆動源とするスクリューフィーダ2が設置されており、このスクリューフィーダ2の給送側先端は、垂直に設置された筒状投入部3の筒内に臨んでいる。ホッパー1とスクリューフィーダ2とにより、スラッジ供給手段が構成される。投入部3内には、投入シリンダ3aのロッドの先端に固定されたプッシャー3bが配置され、ロッドの伸縮動作に伴うプッシャー3bの投入部3内の軸心方向に沿った上下動により、スクリューフィーダ2から給送される濃縮スラッジMを下方に押しやるように構成されている。投入部3の下部には、内部が圧搾室4aとなるシリンダ4が水平に設置され、その周胴部の上部には上記投入部3の下端部と連通する投入口4bが設けられている。   An embodiment of a grinding sludge solidified product producing apparatus according to the present invention will be described with reference to FIGS. In the solidified material manufacturing apparatus A shown in FIGS. 1 and 2, the hopper 1 stores concentrated sludge (grinding sludge) M obtained by filtering grinding sludge containing coolant generated in a grinding line (not shown). A screw feeder 2 using a motor 2a as a drive source is installed at the lower end of the hopper 1, and the feed-side tip of the screw feeder 2 faces the cylinder of the cylindrical insertion portion 3 installed vertically. Yes. The hopper 1 and the screw feeder 2 constitute sludge supply means. A pusher 3b fixed to the tip of the rod of the making cylinder 3a is disposed in the making portion 3, and the screw feeder is moved up and down along the axial center direction in the making portion 3 of the pusher 3b as the rod expands and contracts. The concentrated sludge M fed from 2 is pushed downward. A cylinder 4 whose inside is a compression chamber 4 a is horizontally installed at the lower part of the charging part 3, and a charging port 4 b communicating with the lower end of the charging part 3 is provided at the upper part of the peripheral body part.

上記筒状の圧搾室4aは両端が開口されており、この両端開口部より、加圧パンチ5および受圧パンチ7が対向関係で挿入されている。加圧パンチ5および受圧パンチ7は、それぞれ、油圧で作動する加圧シリンダ6,8の伸縮ロッド6a,8aの先端に連結されており、上記投入口4bから圧搾室4a内に投入された濃縮スラッジMは、加圧パンチ5の圧搾室4a内への進入により加圧パンチ5および受圧パンチ7の間で挟圧されて、後記するブリケット(固形化物)bに成形される。加圧シリンダ6は、油圧ポンプ9および油圧制御装置(加圧速度調整手段)10に油圧管路11を介して接続されており、この油圧管路11の途中には、圧力検出センサ12が配設されている。受圧パンチ7側の加圧シリンダ8は、油圧供給系(図示せず)に接続されていて、受圧パンチ7は、圧搾室4aの一端から出入りさせられるが、図1および図2ではその油圧系の図示を省略している。   Both ends of the cylindrical compression chamber 4a are opened, and the pressure punch 5 and the pressure receiving punch 7 are inserted in an opposing relationship from the openings at both ends. The pressure punch 5 and the pressure receiving punch 7 are connected to the distal ends of the telescopic rods 6a and 8a of the pressure cylinders 6 and 8 that are operated by hydraulic pressure, respectively, and the concentration charged into the pressing chamber 4a from the input port 4b. The sludge M is sandwiched between the pressure punch 5 and the pressure receiving punch 7 by the pressure punch 5 entering the squeezing chamber 4a, and formed into a briquette (solidified material) b described later. The pressurizing cylinder 6 is connected to a hydraulic pump 9 and a hydraulic control device (pressurizing speed adjusting means) 10 via a hydraulic line 11, and a pressure detection sensor 12 is arranged in the middle of the hydraulic line 11. It is installed. The pressure cylinder 8 on the pressure receiving punch 7 side is connected to a hydraulic pressure supply system (not shown), and the pressure receiving punch 7 is made to enter and exit from one end of the pressing chamber 4a, but in FIG. 1 and FIG. Is omitted.

上記圧力検出センサ12で監視検出される圧力信号は、信号処理装置13で処理され、その信号処理結果を機械制御装置(加圧速度制御手段)14に送り、この加圧速度制御手段14は設定基準14aに基づき加圧速度調整手段10に油圧流量を調整させ、加圧シリンダ6の加圧速度の調整を行うようにしている。設定基準14aの内容は、適宜設定すれば良いが、例えば、後述の制御動作を行わせる内容とされる。加圧速度調整手段10としては、機械的な流量調整バルブやサーボバルブ等が用いられる。加圧速度制御手段14による加圧シリンダ6の加圧速度の調整についての詳細は後記する。   The pressure signal monitored and detected by the pressure detection sensor 12 is processed by the signal processing device 13, and the signal processing result is sent to the machine control device (pressurization speed control means) 14, and the pressurization speed control means 14 is set. Based on the reference 14a, the pressurizing speed adjusting means 10 adjusts the hydraulic flow rate to adjust the pressurizing speed of the pressurizing cylinder 6. The content of the setting reference 14a may be set as appropriate. As the pressurizing speed adjusting means 10, a mechanical flow rate adjusting valve, a servo valve or the like is used. Details of the adjustment of the pressurization speed of the pressurization cylinder 6 by the pressurization speed control means 14 will be described later.

上記構成の固形化物製造装置Aによる固形化物(研削スラッジのブリケット)bの成形要領について説明する。図1において、受圧パンチ7を圧搾室4aの先側開口部内に位置させ、また加圧パンチ5を圧搾室4aの後側開口部内に位置させた状態で、スクリューフィーダ2を作動させる。これにより、ホッパー1内の濃縮スラッジMを、投入部3および投入口4bを経て圧搾室4a内の両パンチ5,7間に供給投入する。このとき、投入シリンダ3aを作動させ、プッシャー3bの上下往復動作により、濃縮スラッジMを圧搾室4a内に押し込むように投入する。   The formation procedure of the solidified product (grinding sludge briquette) b by the solidified product manufacturing apparatus A having the above configuration will be described. In FIG. 1, the screw feeder 2 is operated in a state where the pressure receiving punch 7 is positioned in the front opening of the pressing chamber 4a and the pressure punch 5 is positioned in the rear opening of the pressing chamber 4a. As a result, the concentrated sludge M in the hopper 1 is supplied and supplied between the punches 5 and 7 in the pressing chamber 4a through the input part 3 and the input port 4b. At this time, the charging cylinder 3a is operated, and the concentrated sludge M is charged into the pressing chamber 4a by the reciprocating motion of the pusher 3b.

所定量の濃縮スラッジMが圧搾室4a内に投入されると、スクリューフィーダ2を停止させると共に、図2に示すようにプッシャー3bを上方に後退させた状態に維持する。受圧パンチ7を静止させた状態で、加圧シリンダ6を作動させてロッド6aを伸張させ、加圧パンチ5を圧搾室4a内に進入駆動させることによって、両パンチ5,7間で濃縮スラッジMを圧搾してブリケットbに成形する。成形されたブリケットbは、その後、加圧シリンダ8が作動して、図3に示すように受圧パンチ7が後退し、加圧パンチ5がさらに前進することにより、圧搾室4aより排出される。ブリケットbを排出後、両パンチ5,7は元の位置に戻って待機する。   When a predetermined amount of concentrated sludge M is introduced into the pressing chamber 4a, the screw feeder 2 is stopped and the pusher 3b is moved backward as shown in FIG. With the pressure receiving punch 7 stationary, the pressure cylinder 6 is operated to extend the rod 6a, and the pressure punch 5 is driven into the pressing chamber 4a to drive the concentrated sludge M between the punches 5 and 7. Squeezed into a briquette b. Thereafter, the formed briquette b is discharged from the pressing chamber 4a when the pressure cylinder 8 is operated, the pressure receiving punch 7 is moved backward as shown in FIG. 3, and the pressure punch 5 is further moved forward. After discharging the briquette b, the punches 5 and 7 return to their original positions and wait.

上記成形過程は、当初の油圧流量(加圧速度)の設定で正常にブリケットbが成形される状態を示している。図4(A)の実線は、成形時の当初の加圧速度の設定で、濃縮スラッジMなどが噴出しない正常な状態で加圧成形がなされた場合の圧力検出センサ12による検出信号の変化を示している。すなわち、加圧シリンダ6による加圧に伴い、加圧シリンダ6の圧力は、緩やかに上昇し、当該圧力が設定値P0に達した時点で一定時間保持した後、加圧を終了する。加圧の終了と共に圧力は急激に降下して元の状態に戻る。図4(B)は加圧成形過程で濃縮スラッジMなどの噴出が生じた場合の圧力検出センサ12による検出信号の変化を示している。時間tにおいて噴出が生じ、その時に急激な圧力変動が発生している。   The molding process shows a state in which the briquette b is normally molded at the initial hydraulic flow rate (pressurization speed). The solid line in FIG. 4A shows the change in the detection signal by the pressure detection sensor 12 when the pressure molding is performed in a normal state where the concentrated sludge M or the like is not ejected by the initial setting of the pressure speed at the time of molding. Show. That is, with the pressurization by the pressurization cylinder 6, the pressure of the pressurization cylinder 6 gradually increases, and after the pressure reaches the set value P0, the pressurization is terminated after being held for a certain time. With the end of pressurization, the pressure drops rapidly and returns to the original state. FIG. 4B shows a change in the detection signal by the pressure detection sensor 12 when the concentrated sludge M or the like is ejected in the pressure molding process. Ejection occurs at time t, and sudden pressure fluctuations occur at that time.

図5は、上記のような急激な圧力変動が発生した場合の、信号処理装置13による信号処理結果を示している。信号処理装置13は、電気的信号フィルター処理により、緩やかな圧力変化分を除き、急激な変化のみを取り出し、その信号が閾値(設定変動率)L0を超えたら、濃縮スラッジMなどの噴出が発生したと判断し、その噴出が発生したとの信号を加圧速度制御手段14に送る。加圧速度調整手段10には、予め油圧の流量Q1,Q2・・・Qn(Q1>Q2>・・・Qn、Qnが最小)が設定されており、加圧速度制御手段14の指令で流量の選定がなされるように構成されている。   FIG. 5 shows a signal processing result by the signal processing device 13 when the above rapid pressure fluctuation occurs. The signal processing device 13 takes out only a rapid change except for a gradual pressure change by electrical signal filter processing, and when the signal exceeds a threshold value (set fluctuation rate) L0, ejection of concentrated sludge M or the like occurs. A signal that the ejection has occurred is sent to the pressurization speed control means 14. In the pressurizing speed adjusting means 10, hydraulic flow rates Q1, Q2... Qn (Q1> Q2>... Qn, Qn are minimum) are set in advance. Is selected.

当初、油圧流量Qkで機械の運転を開始し、加圧速度制御手段14が信号処理装置13より濃縮スラッジMなどの噴出が発生したとの信号を受けると、加圧速度制御手段14は、設定基準14aに従って、加圧速度調整手段10に指令し、指令を受けた加圧速度調整手段10は、油圧流量をQk+1に切り替え、油圧流量を下げることで、加圧シリンダ6の加圧速度を下げるよう調整する。加圧速度を下げた場合の圧力検出センサ12による検出圧力の信号変化を図4(A)の破線で示す。図4(A)の破線が示すとおり、加圧シリンダ6の加圧速度を下げることにより、設定圧力P0に達するまでの時間は遅れるが、濃縮スラッジMなどの噴出に伴う急激な圧力変化がなくなっていることが理解される。   Initially, the operation of the machine is started at the hydraulic flow rate Qk, and when the pressurization speed control means 14 receives a signal from the signal processing device 13 that ejection of concentrated sludge M or the like has occurred, the pressurization speed control means 14 The pressurization speed adjusting means 10 is commanded according to the reference 14a, and the pressurization speed adjusting means 10 that receives the command switches the hydraulic flow rate to Qk + 1 and lowers the hydraulic flow rate, thereby lowering the pressurization speed of the pressurizing cylinder 6. Adjust as follows. A change in the signal of the detected pressure by the pressure detection sensor 12 when the pressurization speed is lowered is indicated by a broken line in FIG. As shown by the broken line in FIG. 4A, the pressure until the set pressure P0 is reached by reducing the pressurization speed of the pressurization cylinder 6, but the rapid pressure change associated with the ejection of the concentrated sludge M is eliminated. It is understood that

このように加圧シリンダ6の加圧速度を下げた状態で運転を継続すると、機械のサイクルタイムが長いままになり、処理能力が低下する。そこで、例えばこの状態でm個連続して濃縮スラッジMなどの噴出が発生しなかったときは、加圧速度制御手段14は、設定基準14aに従って、加圧速度調整手段10に指令し、油圧流量をQk+1からQkに切り替え、加圧流量を上げることで加圧速度を上げるように調整する。また、油圧流量の調整の際、流量をQnまで下げても濃縮スラッジMなどの噴出発生が収まらない場合、異常とみなして機械を停止するようにしても良い。このような、機械停止シーケンスも予め設定基準14aに設定させておくことができる。   If the operation is continued with the pressurizing speed of the pressurizing cylinder 6 being lowered in this way, the cycle time of the machine remains long, and the processing capacity decreases. Therefore, for example, when m pieces of concentrated sludge M or the like have not been continuously ejected in this state, the pressurization speed control means 14 instructs the pressurization speed adjustment means 10 according to the setting standard 14a to Is switched from Qk + 1 to Qk, and the pressurization speed is adjusted by increasing the pressurization flow rate. In addition, when adjusting the hydraulic flow rate, if the generation of ejection of concentrated sludge M or the like does not stop even if the flow rate is reduced to Qn, it may be regarded as abnormal and the machine may be stopped. Such a machine stop sequence can also be set in advance in the setting reference 14a.

研削ラインで発生したクーラント含有の研削スラッジを濾過した濃縮スラッジMを加圧シリンダ6による圧搾によってブリケットbに固形化する従来の固形化物製造装置の場合、加圧シリンダ6による加圧速度を早くすると、金型(圧搾室4a、加圧パンチ5および受圧パンチ7)の隙間から、濃縮スラッジMが空気やクーラントと共に噴出し、正常な成形固形化ができない場合がある。そのため、良好なブリケットbを得るには、加圧シリンダ6による加圧速度を遅くする方が良いが、処理能力の点から加圧速度を早くすることが求められる。また、濃縮スラッジMの含水率や嵩密度などの性状は、例えばろ過などの前処理工程での仕上がり状況により変動し、さらには金型(同上)の摩耗度合いも変化する。このため、濃縮スラッジMの性状に応じて、あるいは金型の摩耗度に応じて、加圧シリンダ6による加圧速度を調整することが望ましいが、この調整は煩雑であり、調整を怠れば良好なブリケットbが得られなかったり、処理の能力が低下したりする。   In the case of the conventional solidified material manufacturing apparatus that solidifies the bridging b by concentrating sludge M obtained by filtering the coolant-containing grinding sludge generated in the grinding line, the pressurization speed by the pressurization cylinder 6 is increased. The concentrated sludge M may be ejected together with air and coolant from the gaps between the molds (the pressing chamber 4a, the pressure punch 5 and the pressure receiving punch 7), and normal molding and solidification may not be performed. Therefore, in order to obtain a good briquette b, it is better to reduce the pressurization speed by the pressurization cylinder 6, but it is required to increase the pressurization speed from the viewpoint of processing capability. Further, the properties such as the moisture content and bulk density of the concentrated sludge M vary depending on the finished state in a pretreatment process such as filtration, and the degree of wear of the mold (same as above) also changes. For this reason, it is desirable to adjust the pressurizing speed by the pressurizing cylinder 6 according to the properties of the concentrated sludge M or according to the degree of wear of the mold, but this adjustment is complicated, and it is good if the adjustment is neglected. A briquette b cannot be obtained, or the processing ability is reduced.

そこで、この実施形態の固形化物製造装置Aの場合、加圧シリンダ6による圧搾の際、加圧シリンダ6の圧力を監視する圧力検出センサ12により、濃縮スラッジMなどの噴出に伴う急激な圧力変化を検出すると、加圧速度制御手段14が、加圧速度調整手段10に前記加圧シリンダ6の加圧速度を設定基準14aに従って自動調整させるようにしている。このため、上記のような煩雑な調整作業が不要となり、また調整を怠るような事態も生じないから、良好なブリケットbが歩留まりよく得られ、装置の効率良い稼動、および安定した稼動が実現できる。   Therefore, in the case of the solidified material manufacturing apparatus A of this embodiment, when pressure is applied by the pressurizing cylinder 6, the pressure detection sensor 12 that monitors the pressure of the pressurizing cylinder 6 causes an abrupt pressure change accompanying ejection of the concentrated sludge M or the like. Is detected, the pressurization speed control means 14 causes the pressurization speed adjustment means 10 to automatically adjust the pressurization speed of the pressurizing cylinder 6 in accordance with the setting standard 14a. For this reason, the troublesome adjustment work as described above is not necessary, and a situation in which the adjustment is neglected does not occur. Therefore, a good briquette b can be obtained with a high yield, and the apparatus can be operated efficiently and stably. .

なお、研削ラインで発生する研削スラッジに含有するクーラントとしては、水溶性クーラントおよび油性クーラントがあるが、この発明の固形化物製造装置および製造方法は、いずれのクーラントを含有する研削スラッジの固形化にも適用される。また、転がり軸受の内外輪や転動体等の鉄系構成部品、その他の軸受用鋼材の研削スラッジをブリケットに固形化する場合に好ましく採用される。   As the coolant contained in the grinding sludge generated in the grinding line, there are water-soluble coolant and oil-based coolant. Also applies. Further, it is preferably employed when grinding sludge of iron-based components such as inner and outer rings of rolling bearings, rolling elements, and other bearing steel materials is solidified into briquettes.

この発明の一実施形態に係る固形化物製造装置における研削スラッジの供給過程を示す概念図である。It is a conceptual diagram which shows the supply process of the grinding sludge in the solidified material manufacturing apparatus which concerns on one Embodiment of this invention. 同固形化物製造装置における研削スラッジの圧搾過程を示す概念図である。It is a conceptual diagram which shows the pressing process of the grinding sludge in the solidified material manufacturing apparatus. 同固形化物製造装置において成形されたブリケットを排出する過程での圧搾室に対する加圧パンチおよび受圧パンチの動作状態を示す図である。It is a figure which shows the operation state of the pressure punch with respect to the pressing chamber in the process in which the briquette shape | molded in the solidified material manufacturing apparatus is discharged | emitted, and a pressure receiving punch. (A)(B)は、加圧シリンダによる圧搾成形の際の、圧力検出センサによる検出信号の変化を示すグラフであり、(A)は正常な成形状態の場合を示し、(B)は濃縮スラッジなどの噴出が生じた場合を示している。(A) (B) is a graph which shows the change of the detection signal by a pressure detection sensor in the case of compression molding by a pressure cylinder, (A) shows the case of a normal molding state, (B) is concentration. This shows the case where sludge erupts. 圧力検出センサによる検出信号を信号処理装置で処理した結果を示すグラフである。It is a graph which shows the result of having processed the detection signal by a pressure detection sensor with the signal processor.

符号の説明Explanation of symbols

4a…圧搾室
6…加圧シリンダ
10…加圧速度調整手段
12…圧力検出センサ
13…信号処理装置
14…加圧速度制御手段
14a…設定基準
M…濃縮スラッジ(研削スラッジ)
L0…閾値(設定変動率)
A…固形化物製造装置
4a ... Compression chamber 6 ... Pressure cylinder 10 ... Pressure speed adjusting means 12 ... Pressure detection sensor 13 ... Signal processing device 14 ... Pressure speed control means 14a ... Setting standard M ... Concentrated sludge (grinding sludge)
L0 ... threshold (set fluctuation rate)
A ... Solidified product manufacturing equipment

Claims (2)

研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造装置であって、
前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを備え、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させる加圧速度制御手段を設けたことを特徴とする研削スラッジの固形化物製造装置。
A grinding sludge solidified product producing apparatus for producing a solidified product by solidifying a concentrated sludge obtained by filtering coolant-containing grinding sludge generated in a grinding line by pressing with a pressure cylinder,
A pressure detection sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, signal processing for performing processing to extract only rapid change comprising a device, a pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal exceeds the setting change rate and a to come, the pressurization rate adjusting means to said pressure cylinder rate of pressurizing solidified manufacturing apparatus of the grinding sludge, characterized in that a pressurization rate control means for adjusting in accordance with the setting reference.
研削ラインで発生したクーラント含有の研削スラッジをろ過した濃縮スラッジを、加圧シリンダによる圧搾によって固形化して固形化物を製造する研削スラッジの固形化物製造方法であって、
前記加圧シリンダの圧力を監視する圧力検出センサと、この圧力検出センサの信号につき、電気的信号フィルター処理によって、緩やかな圧力変化分を除き、急激な変化のみを取り出す処理を行う信号処理装置と、前記加圧シリンダの加圧速度を調整する加圧速度調整手段とを用い、前記信号処理装置により検出される加圧時の信号を監視して、この信号が設定変動率を超えたときに、前記加圧速度調整手段に前記加圧シリンダの加圧速度を設定基準に従って調整させることを特徴とする研削スラッジの固形化物製造方法。
A method for producing a solidified product of a grinding sludge in which a concentrated sludge obtained by filtering coolant-containing grinding sludge generated in a grinding line is solidified by pressing with a pressure cylinder to produce a solidified product,
A pressure detection sensor for monitoring the pressure of the pressure cylinder, per signal of the pressure detection sensor, the electric signal filtering, except for gradual pressure variation, signal processing for performing processing to extract only rapid change using the device, the pressurization rate adjusting means for adjusting the pressurization rate of the pressure cylinder, monitors the signals under pressure detected by the signal processor, the signal exceeds the setting change rate and a to come, solidified manufacturing method of grinding swarf, characterized in that to adjust according to the set reference pressurization rate of the pressure cylinder to the pressing speed adjusting means.
JP2008064526A 2008-03-13 2008-03-13 Solidified product manufacturing apparatus and method for grinding sludge Expired - Fee Related JP5178256B2 (en)

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JP2720119B2 (en) * 1991-09-11 1998-02-25 ファナック株式会社 Powder molding machine with overload prevention device
JP3907917B2 (en) * 2000-04-28 2007-04-18 Ntn株式会社 Solidified product manufacturing equipment for grinding sludge
JP3963247B2 (en) * 2000-04-28 2007-08-22 Ntn株式会社 Solidified product manufacturing equipment for grinding sludge
JP3907975B2 (en) * 2001-07-03 2007-04-18 Ntn株式会社 Solidified product manufacturing equipment for grinding sludge
JP3979137B2 (en) * 2002-03-22 2007-09-19 株式会社ジェイテクト Method and apparatus for solidifying grinding sludge
JP2003311488A (en) * 2002-04-19 2003-11-05 San-Ai Engineering Co Ltd Compression method utilizing automatic compressor and automatic compressor

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CN105157041A (en) * 2015-09-01 2015-12-16 浙江富春江环保热电股份有限公司 Feed air-drying sludge charging delivery device and charging delivery control method thereof
CN105157041B (en) * 2015-09-01 2017-08-11 浙江富春江环保热电股份有限公司 Feeding wind device for conveying dried sludge into boiler conveying device and its enter stove conveyance control method

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