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JP2021116171A - System and method for delivering particulate air - Google Patents

System and method for delivering particulate air Download PDF

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JP2021116171A
JP2021116171A JP2020011581A JP2020011581A JP2021116171A JP 2021116171 A JP2021116171 A JP 2021116171A JP 2020011581 A JP2020011581 A JP 2020011581A JP 2020011581 A JP2020011581 A JP 2020011581A JP 2021116171 A JP2021116171 A JP 2021116171A
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powder
ship
granular material
air delivery
inclination
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JP7388210B2 (en
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達也 市川
Tatsuya Ichikawa
達也 市川
航 中野
Wataru Nakano
航 中野
慶太郎 田中
Keitaro Tanaka
慶太郎 田中
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Ube Machinery Corp Ltd
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Abstract

To provide a system and a method for delivering particulate air that can reduce operator's work when delivering particulate to a ground silo by simultaneously operating two or more cellar pumps of a ship.SOLUTION: A system for delivering particulate air 10 in the present invention comprises a pressure sensor 20 that measures an inlet pressure to a dust collector 8 of a ground silo 7 when simultaneously delivering particulate to a ground silo 7 from two or more cellar-type air delivery units of a ship, freight remaining amount sensors 30a, 30b that detect remaining amounts of particulate to be supplied to respective ones of the cellar-type air delivery units, an inclination sensor 40 that detects an inclination of the ship, and a control section 50 that controls to regulate the air flow rate through the cellar-type air delivery units in a manner that a measurement value of the pressure sensor 20 satisfies a set value and, when a measurement value of the freight remaining amount sensor 30a, 30b exceeds a remaining amount-set value or a measurement value of the inclination sensor 40 goes below a set value, alternately operates a rake-up unit 9 for the particulate and eliminates a load shortage or an inclination of the ship.SELECTED DRAWING: Figure 1

Description

本発明はタンク内の粉粒体を連続的に送出可能な粉粒体空気送出システム、粉粒体空気送出方法に関する。 The present invention relates to a powder / granular material air delivery system capable of continuously delivering powder / granular material in a tank, and a powder / granular material air delivery method.

大量の粉粒体を専用船で運搬して港湾内の地上サイロに荷下ろしする際に粉粒体空気送出装置(以下、セラ式空気送出装置ということあり)が利用されている。通常の運転方法は、粉粒体を運搬してきた船舶に設置された空気送出装置により、地上に設置された受け入れサイロ内へ粉粒体を空気送出している。
粉粒体空気送出装置は、一般的に二槽で1組の双胴型が多く、交互に受け入れ又は排出を自動的に繰り返してほぼ連続的に送出作業が行えるようにしている。この送出圧縮空気は船舶に設置されたエンジン駆動のコンプレッサで圧送空気を発生させている。運搬する船舶の粉粒体量が多い場合には、二槽で1組の空気送出装置を複数設置して短時間で荷揚げ作業が完了できるように同時運転を行う場合もある。
When a large amount of powder or granular material is transported by a dedicated ship and unloaded to a ground silo in a port, a powder or granular material air delivery device (hereinafter, also referred to as a ceramic air delivery device) is used. In the normal operation method, the powder or granular material is air-delivered into the receiving silo installed on the ground by the air delivery device installed on the ship that has carried the powder or granular material.
Generally, the powder / granular material air delivery device is often a catamaran type in two tanks, and automatically repeats receiving or discharging alternately so that the sending work can be performed almost continuously. This pumped air is pumped by an engine-driven compressor installed on the ship. When the amount of powder or granular material of the ship to be transported is large, a plurality of sets of air delivery devices may be installed in two tanks and simultaneously operated so that the unloading work can be completed in a short time.

また各港の受け入れ設備の仕様(スペック)は様々で、受け入れ先によって異なる。一例として地上サイロの受け入れ能力はサイロ側に設置された集塵機の能力で船からの送出量が制限されてしまう。このとき時間当たりの送出量と風量は比例関係にあり、短時間で送出する場合は地上サイロのサイズだけでなく固気分離する集塵機の能力も求められる。従って、荷下ろし時には船側のオペレータが地上サイロの集塵機能力に合わせて手動で空気送出装置を操作している。
しかし粉粒体の船荷が多い場合、セラ式空気送出装置の2槽を交互に切り替えながら操作したり、受け入れ量のばらつき、荷切れが無いように粉粒体の供給量を調整したり、船荷の送出後に船の傾きが発生しないようにバランス良く荷下ろしするなどオペレータの作業が多くなる。特に専用船に搭載されるセラ式空気送出装置の場合には、港湾内において短時間で荷下ろし又は積み荷することが求められるため負担が大きい。
特許文献1に開示の運転方法は、一方のタンクへの供給空気をその圧送完了前に他方のタンクへ切り替えて供給することにより、バグフィルタの容量を軽減させている。しかし、集塵機の負担は供給空気の切り替え時だけでなく荷切れ、投入量のばらつきによっても発生する。
In addition, the specifications of the receiving equipment at each port vary, and differ depending on the receiving destination. As an example, the capacity of the ground silo is limited by the capacity of the dust collector installed on the silo side. At this time, the amount of air sent out per hour and the amount of air flow are in a proportional relationship, and when sending out in a short time, not only the size of the ground silo but also the ability of the dust collector to separate the solid air is required. Therefore, at the time of unloading, the operator on the ship side manually operates the air delivery device according to the dust collecting function of the ground silo.
However, when there is a large load of powder or granular material, the two tanks of the Cera type air delivery device can be operated while switching alternately, the amount of powder or granular material supplied can be adjusted so that there is no variation in the amount received or the load is cut off, or the cargo is loaded. There is a lot of work for the operator, such as unloading the ship in a well-balanced manner so that the ship does not tilt after it is delivered. In particular, in the case of a ceramic air delivery device mounted on a dedicated ship, the burden is heavy because it is required to unload or load in a short time in the port.
The operation method disclosed in Patent Document 1 reduces the capacity of the bug filter by switching the supply air to one tank to the other tank before the completion of pumping. However, the burden on the dust collector is generated not only when the supply air is switched, but also when the load is exhausted and the input amount varies.

特開昭62−105819号公報Japanese Unexamined Patent Publication No. 62-105819

本発明が解決しようとする課題は、上記従来技術の問題点に鑑み、船舶の2以上のセラポンプを同時運転して地上サイロへ粉粒体を送出する際にオペレータ作業を軽減できる粉粒体空気送出システム、粉粒体空気送出方法を提供することにある。 The problem to be solved by the present invention is that, in view of the above-mentioned problems of the prior art, the powder or granular material air that can reduce the operator's work when the powder or granular material is sent to the ground silo by simultaneously operating two or more ceramic pumps of the ship. The purpose of the present invention is to provide a delivery system and a method for delivering powder or granular material air.

本発明は、上記課題を解決するための第1の手段として、船舶の2以上のセラ式空気送出部から地上サイロへ粉粒体を同時送出するときに前記地上サイロの集塵機の入口圧力を測定する圧力センサと、
前記セラ式空気送出部の夫々へ供給する粉粒体の残量を検出する船荷残量センサと、
前記船舶の傾きを検出する傾斜センサと、
前記圧力センサの測定値が設定値を満たすように前記セラ式空気送出部の風量を調整して、前記船荷残量センサの測定値が残量設定値を下回ったとき、又は前記傾斜センサの測定値が設定範囲外のときに前記粉粒体の掻き寄せ部を交互に運転して荷切れ又は前記船舶の傾きを解消する制御を行う制御部と、
を備えたことを特徴とする粉粒体空気送出システムを提供することにある。
上記第1の手段によれば、集塵機の集塵能力を超えない最大圧力で、荷切れ又は船舶の傾きで投入量のばらつきによる不連続運転を回避して安定した粉粒体の送出を実現できる。
According to the present invention, as a first means for solving the above problems, the inlet pressure of the dust collector of the ground silo is measured when the powder or granular material is simultaneously delivered to the ground silo from two or more ceramic air delivery units of the ship. Pressure sensor and
A cargo level sensor that detects the remaining amount of powder and granules supplied to each of the ceramic air delivery units, and a cargo level sensor.
An inclination sensor that detects the inclination of the ship and
The air volume of the ceramic air delivery unit is adjusted so that the measured value of the pressure sensor satisfies the set value, and when the measured value of the cargo remaining amount sensor falls below the remaining amount set value, or the measurement of the inclination sensor. When the value is out of the set range, the control unit that alternately operates the scraping portion of the powder and granules to control to eliminate the load shortage or the inclination of the ship, and the control unit.
It is an object of the present invention to provide a powder or granular material air delivery system characterized by the above.
According to the first means, stable delivery of powder or granular material can be realized at a maximum pressure that does not exceed the dust collecting capacity of the dust collector, avoiding discontinuous operation due to variation in the input amount due to out of cargo or inclination of the ship. ..

本発明は、上記課題を解決するための第2の手段として、船舶の2以上のセラ式空気送出部から地上サイロへ粉粒体を同時送出するときに前記地上サイロの集塵機の入口圧力の設定値を満たすように前記セラ式空気送出部の風量を制御する工程と、
前記セラ式空気送出部へ供給する前記粉粒体の船内残量が設定値を下回ったとき、又は前記傾斜センサの測定値が設定範囲外のときに、前記セラ式空気送出部へ前記粉粒体を夫々供給する掻き寄せ部を交互に運転して荷切れ又は船舶の傾きを解消する制御を行う工程と、
を有することを特徴とする粉粒体空気送出方法を提供することにある。
上記第2の手段によれば、集塵機の集塵能力を超えない最大圧力で、荷切れ又は船舶の傾きで投入量のばらつきによる不連続運転を回避して安定した粉粒体の送出を実現できる。
The present invention, as a second means for solving the above problems, sets the inlet pressure of the dust collector of the ground silo when the powder or granular material is simultaneously delivered to the ground silo from two or more ceramic air delivery units of the ship. A step of controlling the air volume of the ceramic air delivery unit so as to satisfy the value, and
When the remaining amount of the powder or granular material supplied to the ceramic air delivery unit falls below the set value, or when the measured value of the tilt sensor is out of the set range, the powder or granular material is sent to the ceramic air delivery unit. The process of alternately operating the scraping parts that supply the body and controlling to eliminate the load shortage or the inclination of the ship.
It is an object of the present invention to provide a method for delivering powder or granular material air, which comprises the above.
According to the second means, stable delivery of powder or granular material can be realized at a maximum pressure that does not exceed the dust collecting capacity of the dust collector, avoiding discontinuous operation due to variations in the input amount due to out of cargo or inclination of the ship. ..

本発明によれば、地上サイロの集塵機の集塵能力を超えない最大圧力で運転できる。また複数の高圧タンクから同時供給の際、荷切れ又は船舶の傾きに起因する投入量のばらつきによる不連続運転を回避でき、オペレータの作業負担を軽減できる。 According to the present invention, it can be operated at a maximum pressure that does not exceed the dust collecting capacity of the dust collector of the ground silo. Further, when simultaneously supplying from a plurality of high-pressure tanks, it is possible to avoid discontinuous operation due to variations in the input amount due to out of cargo or inclination of the ship, and it is possible to reduce the work load of the operator.

本発明の粉粒体空気送出システムの構成概略図である。It is a structural schematic diagram of the powder / granular material air delivery system of this invention. 本発明の粉粒体空気送出方法のフロー図である。It is a flow chart of the powder-granular material air delivery method of this invention.

本発明の粉粒体空気送出システム、粉粒体空気送出方法の実施形態について、図面を参照しながら、以下詳細に説明する。 An embodiment of the powder or granular material air delivery system and the powder or granular material air delivery method of the present invention will be described in detail below with reference to the drawings.

[粉粒体空気送出システム10]
図1は、本発明の粉粒体空気送出システムの構成概略図である。
まず船舶に搭載された粉粒体空気送出装置の搬送方法を以下に示す。船輸送して接岸した船舶の粉粒体が、複数(本実施形態では2つ)の供給部1a,1b(バケットコンベアなど)によってセラ式空気送出部(粉粒体空気送出部、セラポンプともいう)2a,2bの上部まで搬送される。
高圧タンク3の上部には受入弁4が設置されている。粉粒体を受け入れる際、空気圧シリンダによって受入弁4を開放して粉粒体をタンク内に受け入れる。
高圧タンク3のあらかじめ設定した量まで粉粒体を受け入れた後、受入弁4を閉じてタンク内への供給を停止する。
次に高圧タンク3の下部に設けた排出弁5を開放し、タンク内に圧縮空気を供給して高圧タンク3に接続した輸送管6内の抵抗によってタンク内圧を上昇させる。搬送時のタンク内圧は一般的に0.39〜0.69MPa程度の高圧に保持しながら粉粒体を地上サイロ7へ輸送管6を経由して送出する。セラ式空気送出部2a,2bの輸送原理はタンク内の高圧空気と粉粒体の混合体をタンク内圧よりも低い供給先へ圧力差を利用して送出している。この送出プロセスはバッチ式となり、一般的には2槽で一組の双胴型が多く適用されている。供給部1a,1bから高圧タンク3に粉粒体を受け入れて搬送を繰り返して、ほぼ自動的かつ連続的に送出作業が行えるようにしている。粉粒体が多い場合には複数組のセラ式空気送出部2a,2bを設置して同時運転している。本実施形態の粉粒体空気送出システム10は、2以上のセラ式空気送出部2a,2bを備えて粉粒体を同時送出可能な船舶を対象としている。
[Powder and granular material air delivery system 10]
FIG. 1 is a schematic configuration diagram of the powder or granular material air delivery system of the present invention.
First, the method of transporting the powder / granular material air delivery device mounted on the ship is shown below. A plurality of (two in this embodiment) supply units 1a and 1b (bucket conveyor, etc.) of a ship transported by ship and berthed at the shore are used as a sera-type air delivery unit (powder / granular material air delivery unit, also referred to as a sera pump). ) It is transported to the upper part of 2a and 2b.
A receiving valve 4 is installed above the high-pressure tank 3. When receiving the powder or granular material, the receiving valve 4 is opened by the pneumatic cylinder to receive the powder or granular material in the tank.
After receiving the powder or granular material up to a preset amount in the high-pressure tank 3, the receiving valve 4 is closed to stop the supply into the tank.
Next, the discharge valve 5 provided at the bottom of the high-pressure tank 3 is opened, compressed air is supplied into the tank, and the tank internal pressure is increased by the resistance in the transport pipe 6 connected to the high-pressure tank 3. The internal pressure of the tank during transportation is generally maintained at a high pressure of about 0.39 to 0.69 MPa, and the powder or granular material is sent to the ground silo 7 via the transport pipe 6. The transportation principle of the Cera-type air delivery units 2a and 2b is to send a mixture of high-pressure air and powder or granular material in the tank to a supply destination lower than the tank internal pressure by using a pressure difference. This delivery process is a batch type, and in general, a set of catamaran type with two tanks is often applied. The powder or granular material is received from the supply units 1a and 1b into the high-pressure tank 3 and repeatedly conveyed so that the delivery work can be performed almost automatically and continuously. When there are a large number of powders and granules, a plurality of sets of ceramic air delivery units 2a and 2b are installed and operated at the same time. The powder / granular material air delivery system 10 of the present embodiment is intended for a ship provided with two or more ceramic air delivery units 2a and 2b and capable of simultaneously delivering powder / granular material.

前記地上サイロ7には粉粒体と空気を固気分離する集塵機8を取り付けている。本実施形態の粉粒体空気送出装置10は、集塵機8の入り口圧力を測定可能な圧力センサ20を取り付けている。圧力センサ20は後述する制御部50と電気的に接続し測定値を送信可能に構成している。
前記供給部1a,1bには船内の粉粒体を供給するスクリューコンベア、チェーンコンベアなどの掻き寄せ部9a,9bを夫々取り付けている。掻き寄せ部9a,9b及び供給部1a,1bは2以上のセラ式空気送出部2a,2bごとに取り付けている。掻き寄せ部9a,9bの近辺には船舶の粉粒体の残量を測定可能な船荷残量センサ30a,30bを取り付けている。船荷残量センサ30a,30bは後述する制御部50と電気的に接続し測定値を送信可能に構成している。
船舶は粉粒体の部分的な送出作業によって偏りが生じ、船体が傾いてしまう場合がある。船体が傾くと粉粒体の送出量にばらつきが生じることがある。このため船舶には船体の傾きを測定可能な傾斜センサ40を取り付けている。傾斜センサ40は後述する制御部50と電気的に接続し測定値を送信可能に構成している。
The above-ground silo 7 is equipped with a dust collector 8 that separates powder and granules from air. The powder or granular material air delivery device 10 of the present embodiment is equipped with a pressure sensor 20 capable of measuring the inlet pressure of the dust collector 8. The pressure sensor 20 is electrically connected to the control unit 50, which will be described later, so that the measured value can be transmitted.
The supply units 1a and 1b are each equipped with scraping portions 9a and 9b such as a screw conveyor and a chain conveyor that supply powder and granules in the ship. The scraping portions 9a and 9b and the supply portions 1a and 1b are attached to each of two or more ceramic air delivery portions 2a and 2b. In the vicinity of the scraping portions 9a and 9b, the cargo remaining amount sensors 30a and 30b capable of measuring the remaining amount of powder and granules of the ship are attached. The remaining load sensors 30a and 30b are electrically connected to the control unit 50, which will be described later, so that the measured values can be transmitted.
The ship may be biased due to the partial delivery work of the powder or granular material, and the hull may be tilted. If the hull is tilted, the amount of powder or granular material delivered may vary. Therefore, the ship is equipped with a tilt sensor 40 capable of measuring the tilt of the hull. The tilt sensor 40 is electrically connected to a control unit 50, which will be described later, so that the measured value can be transmitted.

制御部50は、圧力センサ20の測定値を受信可能とし、この測定値に基づいてセラ式空気送出部2a,2bのコンプレッサの風量を調整する制御を行っている。本実施形態の集塵機8の入口圧力の設定値は集塵機8の集塵能力の最大圧力に設定している。最大圧力を超えると集塵機に負荷が掛かり安定した送出作業が妨げられてしまう。集塵機圧力はセラ式空気送出部2a,2bの風量によって決まるため、集塵圧力の設定値を満たすようにセラ式空気送出部2a,2bのコンプレッサで風量を制御部50により増減制御している。
また制御部50は、船荷残量センサ30a,30bの測定値及び傾斜センサ40の測定値を受信可能とし、この測定値に基づいて粉粒体の掻き寄せ部9a,9bを交互に運転する制御を行っている。荷切れ、又は粉粒体の送出量がばらつくと安定した送出ができず、集塵機8に負荷が掛かるため、いずれかの船荷残量センサ30a,30bの測定値があらかじめ設定した残量設定値を下回ったときに船荷残量センサ30a,30bを取り付けた掻き寄せ部9a,9bを運転させて粉粒体を該当する供給部1a,1bへ供給するように制御を行っている。
さらに送出作業によって船舶の粉粒体が減少してくると船体が傾き、粉粒体の送出量にばらつきが生じてしまう。そこであらかじめ船体が水平となる設定値を設定し、傾斜センサ40の測定値が設定範囲外のときに粉粒体の掻き寄せ部9a,9bを交互に運転して船舶の粉粒体を均して傾きを解消するように制御を行っている。
The control unit 50 makes it possible to receive the measured value of the pressure sensor 20, and controls to adjust the air volume of the compressor of the ceramic air delivery units 2a and 2b based on the measured value. The set value of the inlet pressure of the dust collector 8 of the present embodiment is set to the maximum pressure of the dust collecting capacity of the dust collector 8. If the maximum pressure is exceeded, a load will be applied to the dust collector and stable delivery work will be hindered. Since the dust collector pressure is determined by the air volume of the Cera type air delivery units 2a and 2b, the air volume is controlled by the control unit 50 by the compressor of the Cera type air delivery unit 2a and 2b so as to satisfy the set value of the dust collection pressure.
Further, the control unit 50 makes it possible to receive the measured values of the remaining load sensors 30a and 30b and the measured values of the inclination sensor 40, and controls to alternately operate the powder and granular material scraping units 9a and 9b based on the measured values. It is carried out. If the load is exhausted or the amount of powder or granular material to be delivered varies, stable delivery will not be possible and the dust collector 8 will be overloaded. When the amount falls below the limit, the scraping units 9a and 9b to which the load remaining amount sensors 30a and 30b are attached are operated to control the powder and granular material to be supplied to the corresponding supply units 1a and 1b.
Further, when the amount of powder or granular material of the ship is reduced by the sending operation, the hull is tilted and the amount of powder or granular material to be sent out varies. Therefore, a set value for the hull to be horizontal is set in advance, and when the measured value of the tilt sensor 40 is out of the set range, the powder and granular material scraping portions 9a and 9b are alternately operated to level the powder and granular material of the ship. The control is performed so as to eliminate the tilt.

[粉粒体空気送出方法]
図2は、本発明の粉粒体空気送出方法のフロー図である。
1号セラ式空気送出部2aの運転を開始する(ステップ1)。高圧タンク3のあらかじめ設定した量まで粉粒体を受け入れた後、高圧タンク3の下部に設けた排出弁5を開放し、粉粒体を地上サイロ7へ輸送管6を経由して送出する。
集塵機8の入口圧力が設定値外か否か判定する(ステップ2)。
入口圧力が設定値外のとき(NO)、圧力センサ20の測定値が設定値を満たすように1号セラ式空気送出部2aのコンプレッサにより風量を増減調整する(ステップ3)。
入口圧力が設定値のとき(YES)、2号セラ式空気送出部2bの運転を開始する(ステップ4)。高圧タンク3のあらかじめ設定した量まで粉粒体を受け入れた後、高圧タンク3の下部に設けた排出弁5を開放し、粉粒体を地上サイロ7へ輸送管6を経由して送出する。
1号及び2号セラ式空気送出部2a,2bが同時運転の状態となる(ステップ5)。
集塵機8の入口圧力が設定値外か否か判定する(ステップ6)。1号セラ式空気送出部2aの風量調整は完了しているため、2号セラ式空気送出部2bの風量調整を行う。
[Powder and granular material air delivery method]
FIG. 2 is a flow chart of the powder / granular material air delivery method of the present invention.
The operation of the No. 1 ceramic air delivery unit 2a is started (step 1). After receiving the powder or granular material up to a preset amount of the high pressure tank 3, the discharge valve 5 provided at the lower part of the high pressure tank 3 is opened, and the powder or granular material is sent to the ground silo 7 via the transport pipe 6.
It is determined whether or not the inlet pressure of the dust collector 8 is outside the set value (step 2).
When the inlet pressure is outside the set value (NO), the air volume is increased or decreased by the compressor of the No. 1 ceramic air delivery unit 2a so that the measured value of the pressure sensor 20 satisfies the set value (step 3).
When the inlet pressure is the set value (YES), the operation of the No. 2 ceramic air delivery unit 2b is started (step 4). After receiving the powder or granular material up to a preset amount of the high pressure tank 3, the discharge valve 5 provided at the lower part of the high pressure tank 3 is opened, and the powder or granular material is sent to the ground silo 7 via the transport pipe 6.
The No. 1 and No. 2 ceramic air delivery units 2a and 2b are in the state of simultaneous operation (step 5).
It is determined whether or not the inlet pressure of the dust collector 8 is outside the set value (step 6). Since the air volume adjustment of the No. 1 Cera type air delivery unit 2a has been completed, the air volume adjustment of the No. 2 Cera type air delivery unit 2b is performed.

入口圧力が設定値外のとき(NO)、圧力センサ20の測定値が設定値を満たすように2号セラ式空気送出部2bのコンプレッサにより風量を増減調整する(ステップ7)。
入口圧力が設定値のとき(YES)、以降、集塵機が最大圧力の状態で粉粒体の送出作業を実施できる。粉粒体の送出作業中は、船荷残量センサ30a,30bにより1号及び2号船内粉粒体残量を測定する。また傾斜センサ40により船舶の傾きを測定する(ステップ8)。
船荷残量センサ30a,30bの測定値が粉粒体の残量設定値を下回った場合、1号及び2号用船内粉粒体の掻き寄せ部9a,9bを交互運転して、粉粒体の荷切れ、送出量のばらつきを解消する(ステップ9)。
船舶の傾きが設定範囲外か否か判定する(ステップ10)。
船舶の傾きが設定範囲外のとき(YES)、1号及び2号用船内粉粒体の掻き寄せ部9a,9bを交互運転して、船舶に残っている粉粒体を均して粉粒体の送出作業によって発生した船舶の傾きを解消する(ステップ11)。
船舶の傾きが設定範囲内のとき(NO)、1号及び2号用船内粉粒体の残量が0(積み荷を全量排出した)か否か判定する(ステップ12)。
粉粒体の残量がある場合(YES)、ステップ8以降の工程を繰り返す。
一方、残量が0の場合(NO)、送出作業を終了する。
When the inlet pressure is outside the set value (NO), the air volume is increased or decreased by the compressor of the No. 2 ceramic air delivery unit 2b so that the measured value of the pressure sensor 20 satisfies the set value (step 7).
When the inlet pressure is the set value (YES), the powder / granular material delivery operation can be performed with the dust collector at the maximum pressure thereafter. During the powder / granular material delivery work, the remaining amount of powder / granular material in the No. 1 and No. 2 ships is measured by the cargo remaining amount sensors 30a and 30b. Further, the inclination of the ship is measured by the inclination sensor 40 (step 8).
When the measured values of the remaining load sensors 30a and 30b are lower than the remaining amount set value of the powder or granular material, the scraping portions 9a and 9b of the powder and granular material in the ship for No. 1 and No. 2 are alternately operated to obtain the powder or granular material. (Step 9).
It is determined whether or not the inclination of the ship is out of the set range (step 10).
When the inclination of the ship is out of the set range (YES), the scraping portions 9a and 9b of the powder and granular materials in the ship for Nos. 1 and 2 are alternately operated to even out the powder and granular materials remaining on the ship. Eliminate the tilt of the ship caused by the body delivery work (step 11).
When the inclination of the ship is within the set range (NO), it is determined whether or not the remaining amount of the powder or granular material in the ship for No. 1 and No. 2 is 0 (the entire load is discharged) (step 12).
If there is a remaining amount of powder or granular material (YES), the steps after step 8 are repeated.
On the other hand, when the remaining amount is 0 (NO), the sending operation is terminated.

このような本発明によれば、集塵機の集塵能力を超えない最大圧力で、荷切れ又は船舶の傾きで投入量のばらつきによる不連続運転を回避して安定した粉粒体の送出を実現できる。
以上、本発明の好ましい実施形態について説明した。しかしながら、本発明は、上記実施形態に何ら制限されることなく、本発明の主旨を逸脱しない範囲において、種々の変更が可能である。
また、本発明は、実施形態において示された組み合わせに限定されることなく、種々の組み合わせによって実施可能である。
According to the present invention as described above, it is possible to realize stable delivery of powder or granular material at a maximum pressure that does not exceed the dust collecting capacity of the dust collector, avoiding discontinuous operation due to variation in the input amount due to out of cargo or inclination of the ship. ..
The preferred embodiment of the present invention has been described above. However, the present invention is not limited to the above embodiment, and various modifications can be made without departing from the gist of the present invention.
Further, the present invention is not limited to the combinations shown in the embodiments, and can be implemented by various combinations.

1a,1b 供給部
2a,2b セラ式空気送出部
3 高圧タンク
4 受入弁
5 排出弁
6 輸送管
7 地上サイロ
8 集塵機
9a,9b 掻き寄せ部
10 粉粒体空気送出システム
20 圧力センサ
30a,30b 船荷残量センサ
40 傾斜センサ
50 制御部
1a, 1b Supply part 2a, 2b Cera type air delivery part 3 High pressure tank 4 Receiving valve 5 Discharge valve 6 Transport pipe 7 Ground silo 8 Dust collector 9a, 9b Scraping part 10 Powder / granular material air delivery system 20 Pressure sensor 30a, 30b Remaining amount sensor 40 Tilt sensor 50 Control unit

Claims (2)

船舶の2以上のセラ式空気送出部から地上サイロへ粉粒体を同時送出するときに前記地上サイロの集塵機の入口圧力を測定する圧力センサと、
前記セラ式空気送出部の夫々へ供給する粉粒体の残量を検出する船荷残量センサと、
前記船舶の傾きを検出する傾斜センサと、
前記圧力センサの測定値が設定値を満たすように前記セラ式空気送出部の風量を調整して、前記船荷残量センサの測定値が残量設定値を下回ったとき、又は前記傾斜センサの測定値が設定範囲外のときに前記粉粒体の掻き寄せ部を交互に運転して荷切れ又は前記船舶の傾きを解消する制御を行う制御部と、
を備えたことを特徴とする粉粒体空気送出システム。
A pressure sensor that measures the inlet pressure of the dust collector of the ground silo when the powder or granular material is simultaneously sent from two or more ceramic air delivery parts of the ship to the ground silo.
A cargo level sensor that detects the remaining amount of powder and granules supplied to each of the ceramic air delivery units, and a cargo level sensor.
An inclination sensor that detects the inclination of the ship and
The air volume of the ceramic air delivery unit is adjusted so that the measured value of the pressure sensor satisfies the set value, and when the measured value of the cargo remaining amount sensor falls below the remaining amount set value, or the measurement of the inclination sensor. When the value is out of the set range, the control unit that alternately operates the scraping portion of the powder and granules to control to eliminate the load shortage or the inclination of the ship, and the control unit.
A powder / granular material air delivery system characterized by being equipped with.
船舶の2以上のセラ式空気送出部から地上サイロへ粉粒体を同時送出するときに前記地上サイロの集塵機の入口圧力の設定値を満たすように前記セラ式空気送出部の風量を制御する工程と、
前記セラ式空気送出部へ供給する前記粉粒体の船内残量が設定値を下回ったとき、又は前記傾斜センサの測定値が設定範囲外のときに、前記セラ式空気送出部へ前記粉粒体を夫々供給する掻き寄せ部を交互に運転して荷切れ又は船舶の傾きを解消する制御を行う工程と、
を有することを特徴とする粉粒体空気送出方法。
A step of controlling the air volume of the ceramic air delivery unit so as to satisfy the set value of the inlet pressure of the dust collector of the ground silo when the powder or granular material is simultaneously transmitted from two or more ceramic air delivery units of the ship to the ground silo. When,
When the remaining amount of the powder or granular material supplied to the ceramic air delivery unit falls below the set value, or when the measured value of the tilt sensor is out of the set range, the powder or granular material is sent to the ceramic air delivery unit. The process of alternately operating the scraping parts that supply the body and controlling to eliminate the load shortage or the inclination of the ship.
A method for delivering powder or granular material air, which comprises.
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03195904A (en) * 1989-12-26 1991-08-27 Ohbayashi Corp Measuring apparatus for volume of substance loaded in carrying vessel
JPH11316012A (en) * 1998-04-30 1999-11-16 Nkk Corp Pressure control method for incinerator in refuse incinerator
JP2002234619A (en) * 2001-02-09 2002-08-23 Hitachi Plant Eng & Constr Co Ltd Mechanical unloader
JP2009040544A (en) * 2007-08-08 2009-02-26 Hitachi Plant Mechanics Co Ltd Valve structure of sera type pneumatic transportation device

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03195904A (en) * 1989-12-26 1991-08-27 Ohbayashi Corp Measuring apparatus for volume of substance loaded in carrying vessel
JPH11316012A (en) * 1998-04-30 1999-11-16 Nkk Corp Pressure control method for incinerator in refuse incinerator
JP2002234619A (en) * 2001-02-09 2002-08-23 Hitachi Plant Eng & Constr Co Ltd Mechanical unloader
JP2009040544A (en) * 2007-08-08 2009-02-26 Hitachi Plant Mechanics Co Ltd Valve structure of sera type pneumatic transportation device

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