JP2002168139A - Feeding system for waste plastic generating oil - Google Patents

Feeding system for waste plastic generating oil

Info

Publication number
JP2002168139A
JP2002168139A JP2000368717A JP2000368717A JP2002168139A JP 2002168139 A JP2002168139 A JP 2002168139A JP 2000368717 A JP2000368717 A JP 2000368717A JP 2000368717 A JP2000368717 A JP 2000368717A JP 2002168139 A JP2002168139 A JP 2002168139A
Authority
JP
Japan
Prior art keywords
oil
mixed
supply line
line
generated
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2000368717A
Other languages
Japanese (ja)
Other versions
JP3866505B2 (en
Inventor
Kiyoshi Taguchi
口 清 田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Toshiba Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toshiba Corp filed Critical Toshiba Corp
Priority to JP2000368717A priority Critical patent/JP3866505B2/en
Publication of JP2002168139A publication Critical patent/JP2002168139A/en
Application granted granted Critical
Publication of JP3866505B2 publication Critical patent/JP3866505B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/06Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed
    • F02D19/08Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed simultaneously using pluralities of fuels
    • F02D19/081Adjusting the fuel composition or mixing ratio; Transitioning from one fuel to the other
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/06Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed
    • F02D19/0626Measuring or estimating parameters related to the fuel supply system
    • F02D19/0634Determining a density, viscosity, composition or concentration
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02DCONTROLLING COMBUSTION ENGINES
    • F02D19/00Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures
    • F02D19/06Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed
    • F02D19/0639Controlling engines characterised by their use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures peculiar to engines working with pluralities of fuels, e.g. alternatively with light and heavy fuel oil, other than engines indifferent to the fuel consumed characterised by the type of fuels
    • F02D19/0649Liquid fuels having different boiling temperatures, volatilities, densities, viscosities, cetane or octane numbers
    • F02D19/0657Heavy or light fuel oils; Fuels characterised by their impurities such as sulfur content or differences in grade, e.g. for ships
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Fuel-Injection Apparatus (AREA)
  • Output Control And Ontrol Of Special Type Engine (AREA)
  • Combined Controls Of Internal Combustion Engines (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • High-Pressure Fuel Injection Pump Control (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a feeding system for waste plastic generating oil capable of feeding a mixture of generation oil and A heavy oil mixed in an appropriate ratio to a combustion device. SOLUTION: This feeding system for waste plastic generating oil is equipped with a generation oil feeding line 2 for feeding the generation oil from a waste plastic processing device 30; a A heavy oil feeding line 3 for feeding the A heavy oil; and a mixing tank 1 for mixing the generation oil and the A heavy oil. The mixture oil from the mixing tank is fed to an engine 13 through a mixture oil line 31. A signal from a mixture oil viscosity sensor 10 of a mixture oil line 31 is inputted in a control device 18, and a generation oil control valve 4 and an A heavy oil control valve 5 are controlled with the control device 18.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は廃プラスチック生成
油をエンジンへ供給する廃プラスチック生成油供給シス
テムに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a waste plastic producing oil supply system for supplying waste plastic producing oil to an engine.

【0002】[0002]

【従来の技術】従来より、廃プラスチック処理装置によ
り廃プラスチックを処理して廃プラスチック生成油を生
成するシステムが開発されている。
2. Description of the Related Art Hitherto, a system has been developed in which a waste plastic processing apparatus treats waste plastic to produce waste plastic production oil.

【0003】廃プラスチック処理装置は最近のプロセス
技術であり、廃プラスチック処理装置から生成されるC
重油相当の生成油がディーゼルエンジンの燃料になるこ
とは知られているが、実例がないため具体的な制御方法
については未だ開発されていないのが実状である。その
ため、従来より適用している燃料ラインをそのまま生成
油に適用する方式が一般的に行われている。
[0003] Waste plastics processing equipment is a recent process technology, and the C generated from the waste plastics processing equipment is used.
It is known that heavy oil-equivalent oil can be used as fuel for diesel engines. However, there is no actual example, and a specific control method has not yet been developed. For this reason, a system in which a conventionally applied fuel line is directly applied to the generated oil is generally used.

【0004】また、生成油の分析は行われているが、デ
ィーゼルエンジン燃焼試験による結果を基にした制御方
式は開発されていない。
[0004] In addition, although the analysis of the produced oil has been performed, no control system based on the result of a diesel engine combustion test has been developed.

【0005】[0005]

【発明が解決しようとする課題】廃プラスチック処理装
置からの生成油をそのままディーゼルエンジンで燃焼し
た場合は、エンジン燃料である生成油の動粘度を一定の
値に維持し生成油の動粘度を一定に保つ必要がある。一
般的に動粘度は、A重油等の市販品燃料では常温で流動
状態であるため特に対策の必要はないが、廃プラスチッ
ク処理装置の生成油はC重油相当のものであり、常温で
は流動性はなく50℃以上で使用する必要がある。この
ため、廃プラスチック処理装置の生成油をそのままディ
ーゼルエンジンで燃焼する場合は、流動性がないためデ
ィーゼルエンジンへ安定して供給することがむずかし
い。
When the generated oil from the waste plastic processing apparatus is directly burned by a diesel engine, the kinematic viscosity of the generated oil as the engine fuel is maintained at a constant value and the kinematic viscosity of the generated oil is kept constant. Need to be kept. In general, the kinematic viscosity of a commercially available fuel such as fuel oil A does not require any special measures because it is in a fluid state at room temperature. However, the oil produced by the waste plastic processing equipment is equivalent to fuel oil C and has a fluidity at room temperature. And must be used at 50 ° C or higher. Therefore, when the oil produced by the waste plastic processing apparatus is directly burned by the diesel engine, it is difficult to supply the oil to the diesel engine stably because of lack of fluidity.

【0006】また、生成油には一般的にワックス分が多
く含まれ、これによりエンジン燃料フィルターの目づま
りが発生し、フィルタを頻繁に交換したり、そのまま放
置すると燃料がフィルタに詰まってエンジンが停止する
ことがある。
In addition, the generated oil generally contains a large amount of wax, which causes clogging of the engine fuel filter. If the filter is frequently replaced or left as it is, the fuel is clogged in the filter and the engine stops. May be.

【0007】本発明はこのような点を考慮してなされた
ものであり、流動性を確保すると同時に、A重油と生成
油とを適切に混合してエンジン燃料フィルタの目詰まり
を防止し、エンジンを適切に運転することができる廃プ
ラスチック生成油供給システムを提供することを目的と
する。
[0007] The present invention has been made in view of such a point, and while ensuring fluidity, appropriately mixing heavy fuel oil A and generated oil to prevent clogging of an engine fuel filter, It is an object of the present invention to provide a waste plastic production oil supply system capable of appropriately operating the oil supply system.

【0008】[0008]

【課題を解決するための手段】本発明は、廃プラスチッ
ク処理装置からの生成油が供給される生成油供給ライン
と、A重油が供給されるA重油供給ラインと、生成油供
給ラインからの生成油と、A重油供給ラインからのA重
油が混合して混合油が生成される混合タンクと、混合タ
ンクからの混合油が混合油ラインを経て供給される燃焼
装置と、生成油供給ラインおよびA重油供給ラインに各
々設けられた生成油制御弁およびA重油制御弁と、を備
え、混合油ラインに混合油粘度センサとを設け、混合油
粘度センサからの信号に基づいて、制御装置により生成
油制御弁およびA重油制御弁のうち少なくとも一方を制
御することを特徴とする廃プラスチック生成油供給シス
テムである。
SUMMARY OF THE INVENTION The present invention relates to a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, and a product from a product oil supply line. A mixing tank in which oil and heavy oil A from the heavy fuel oil supply line are mixed to produce a mixed oil; a combustion device in which the mixed oil from the mixing tank is supplied through the mixed oil line; A production oil control valve and an A heavy oil control valve respectively provided in the heavy oil supply line, and a mixed oil viscosity sensor is provided in the mixed oil line, and the produced oil is produced by the control device based on a signal from the mixed oil viscosity sensor. A waste plastic production oil supply system, wherein at least one of a control valve and an A fuel oil control valve is controlled.

【0009】本発明は、廃プラスチック処理装置からの
生成油が供給される生成油供給ラインと、A重油が供給
されるA重油供給ラインと、生成油供給ラインからの生
成油と、A重油供給ラインからのA重油が混合して混合
油が生成される混合タンクと、混合タンクからの混合油
が混合油ラインを経て供給される燃焼装置とを備え、混
合油ラインに混合油粘度センサと、混合油ヒータとを設
け、混合油粘度センサからの信号に基づいて、制御装置
により混合油ヒータを制御することを特徴とする廃プラ
スチック生成油供給システムである。
The present invention provides a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a fuel oil supply A A mixing tank in which the A fuel oil from the line is mixed to produce a mixed oil, and a combustion device in which the mixed oil from the mixing tank is supplied through the mixed oil line; a mixed oil viscosity sensor in the mixed oil line; A mixed plastic heater is provided, and a mixed plastic heater is controlled by a control device based on a signal from a mixed oil viscosity sensor.

【0010】本発明は、廃プラスチック処理装置からの
生成油が供給される生成油供給ラインと、A重油が供給
されるA重油供給ラインと、生成油供給ラインからの生
成油と、A重油供給ラインからのA重油が混合して混合
油が生成される混合タンクと、混合タンクからの混合油
が混合油ラインを経て供給される燃焼装置と、生成油供
給ラインおよびA重油供給ラインに各々設けられた生成
油制御弁およびA重油制御弁と、を備え、混合油ライン
に差圧センサを有する燃料フィルタを設け、差圧センサ
からの信号に基づいて、制御装置により生成油制御弁お
よびA重油制御弁のうち少なくとも一方を制御すること
を特徴とする廃プラスチック生成油供給システムであ
る。
The present invention provides a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a fuel oil A supply A mixing tank in which fuel oil A from the line is mixed to produce a mixed oil; a combustion device in which the mixed oil from the mixing tank is supplied through the mixed oil line; and a fuel oil supply line and a fuel oil A supply line. A fuel filter having a differential pressure sensor in the mixed oil line, and based on a signal from the differential pressure sensor, the control device generates the generated oil control valve and the A heavy oil control valve. A waste plastic production oil supply system, wherein at least one of the control valves is controlled.

【0011】本発明は、廃プラスチック処理装置からの
生成油が供給される生成油供給ラインと、A重油が供給
されるA重油供給ラインと、生成油供給ラインからの生
成油と、A重油供給ラインからのA重油が混合して混合
油が生成される混合タンクと、混合タンクからの混合油
が混合油ラインを経て供給される燃焼装置とを備え、A
重油供給ラインに混合油供給ラインに合流するバイパス
ラインを設け、混合油供給ラインのバイパスラインとの
合流点より上流側に混合油切換弁を設けるとともに、バ
イパスラインにA重油切換弁を設け、混合油ラインに差
圧センサを有する燃料フィルタを設け、差圧センサから
の信号に基づいて、制御装置により混合油切換弁および
A重油切換弁のうち少なくとも一方を制御することを特
徴とする廃プラスチック生成油供給システムである。
The present invention provides a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a fuel oil A supply A mixing tank in which A fuel oil from the line is mixed to produce a mixed oil, and a combustion device to which the mixed oil from the mixing tank is supplied through a mixed oil line;
A heavy oil supply line is provided with a bypass line that joins the mixed oil supply line, a mixed oil switching valve is provided upstream of the junction of the mixed oil supply line with the bypass line, and an A heavy oil switching valve is provided in the bypass line, Providing a fuel filter having a differential pressure sensor in an oil line, and controlling at least one of a mixed oil switching valve and an A heavy oil switching valve by a control device based on a signal from the differential pressure sensor; Oil supply system.

【0012】本発明は、廃プラスチック処理装置からの
生成油が供給される生成油供給ラインと、A重油が供給
されるA重油供給ラインと、生成油供給ラインからの生
成油と、A重油供給ラインからのA重油が混合して混合
油が生成される混合タンクと、混合タンクからの混合油
が混合油ラインを経て供給される燃焼装置とを備え、A
重油供給ラインに混合油供給ラインに合流するバイパス
ラインを設け、混合油供給ラインのバイパスラインとの
合流点より上流側に混合油切換弁を設けるとともに、バ
イパスラインにA重油切換弁を設け、燃焼装置に排ガス
ラインを設けるともに、この排ガスラインに排ガスセン
サを設け、排ガスセンサからの信号に基づいて、制御装
置により混合油切換弁およびA重油切換弁のうち少なく
とも一方を制御することを特徴とする廃プラスチック生
成油供給システムである。
[0012] The present invention provides a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a fuel oil supply A A mixing tank in which A fuel oil from the line is mixed to produce a mixed oil, and a combustion device to which the mixed oil from the mixing tank is supplied through a mixed oil line;
A heavy oil supply line is provided with a bypass line that joins the mixed oil supply line, a mixed oil switching valve is provided upstream of the junction of the mixed oil supply line with the bypass line, and a heavy oil switching valve A is provided in the bypass line, and combustion is performed. An exhaust gas line is provided in the device, an exhaust gas sensor is provided in the exhaust gas line, and at least one of the mixed oil switching valve and the A heavy oil switching valve is controlled by a control device based on a signal from the exhaust gas sensor. It is a waste plastic production oil supply system.

【0013】本発明は、廃プラスチック処理装置からの
生成油が供給される生成油供給ラインと、A重油が供給
されるA重油供給ラインと、生成油供給ラインからの生
成油と、A重油供給ラインからのA重油が混合して混合
油が生成される混合タンクと、混合タンクからの混合油
が混合油ラインを経て供給される燃焼装置とを備え、生
成油供給ラインに生成油フィルタおよび生成油粘度セン
サを設け、生成油粘度センサからの信号に基づいて、制
御装置により生成油フィルタを制御することを特徴とす
る廃プラスチック生成油供給システムである。
[0013] The present invention provides a product oil supply line to which product oil from a waste plastic processing apparatus is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a fuel oil supply A A mixing tank in which fuel oil A from the line is mixed to generate a mixed oil; and a combustion device in which the mixed oil from the mixing tank is supplied through the mixed oil line. An oil supply system for waste plastics, wherein an oil viscosity sensor is provided, and a control device controls a generated oil filter based on a signal from the generated oil viscosity sensor.

【0014】[0014]

【発明の実施の形態】第1の実施の形態 以下、図面を参照して本発明による廃プラスチック生成
油供給システムの実施の形態について説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS First Embodiment Hereinafter, an embodiment of a waste plastic oil supply system according to the present invention will be described with reference to the drawings.

【0015】図1および図2は廃プラスチック生成油供
給システムの第1の実施の形態を示す図である。
FIGS. 1 and 2 show a first embodiment of a waste plastic production oil supply system.

【0016】図1および図2に示すように、廃プラスチ
ック生成油供給システムは廃プラスチック処理装置30
からの生成油が供給される生成油供給ライン2と、A重
油が供給されるA重油供給ライン3と、生成油供給ライ
ン2からの生成油と、A重油供給ライン3からのA重油
が混合して混合油が生成される混合タンク1と、混合タ
ンク1からの混合油が混合ライン31を経て供給される
ディーゼルエンジン(燃焼装置)13とを備えている。
As shown in FIG. 1 and FIG.
Oil, a fuel oil supply line 2 to which fuel oil from A is supplied, a fuel oil supply line 3 to which fuel oil A is supplied, a fuel oil from the fuel oil supply line 2, and fuel oil A from the fuel oil A supply line 3 are mixed. And a diesel engine (combustion device) 13 to which the mixed oil from the mixing tank 1 is supplied through a mixing line 31.

【0017】このうち生成油供給ライン2には、生成油
フィルタ20、生成油制御弁4、生成油流量センサ6お
よび生成油粘度センサ19が順次取付けられている。ま
たA重油供給ライン3にはA重油制御弁5およびA重油
流量センサ7が順次取付けられている。
A generated oil filter 20, a generated oil control valve 4, a generated oil flow sensor 6, and a generated oil viscosity sensor 19 are sequentially attached to the generated oil supply line 2. An A fuel oil control valve 5 and an A fuel oil flow sensor 7 are sequentially attached to the A fuel oil supply line 3.

【0018】また混合油ライン31には、混合油ヒータ
8、混合油温度センサ9、混合油粘度センサ10、燃料
フィルタ11および混合油切換弁15が順次設けられ、
燃料フィルタ11には差圧センサ12が取付けられてい
る。
The mixed oil line 31 is provided with a mixed oil heater 8, a mixed oil temperature sensor 9, a mixed oil viscosity sensor 10, a fuel filter 11, and a mixed oil switching valve 15 sequentially.
A differential pressure sensor 12 is attached to the fuel filter 11.

【0019】さらに、A重油供給ライン3には、A重油
制御弁5およびA重油流量センサ7が設けられている。
またA重油供給ライン3に混合油供給ライン31に合流
するバイパスライン17が設けられ、このバイパスライ
ン17には、A重油切換弁16が取付けられている。な
お、混合油切換弁15は混合油供給ライン31のうち、
バイパスライン17との合流点より上流側に位置してい
る。
Further, the A fuel oil supply line 3 is provided with an A fuel oil control valve 5 and an A fuel oil flow sensor 7.
Further, a bypass line 17 that joins the mixed oil supply line 31 is provided in the A heavy oil supply line 3, and an A heavy oil switching valve 16 is attached to the bypass line 17. In addition, the mixed oil switching valve 15 is one of the mixed oil supply lines 31.
It is located upstream from the junction with the bypass line 17.

【0020】さらにディーゼルエンジン13には排ガス
ライン32が設けられ、この排ガスイラン32には排ガ
スセンサ14が取付けられている。
Further, the diesel engine 13 is provided with an exhaust gas line 32, and the exhaust gas Iran 32 is provided with an exhaust gas sensor 14.

【0021】また生成油流量センサ6、A重油流量セン
サ7、生成油粘度センサ19、混合油温度センサ9、混
合油粘度センサ10、および差圧センサ12からの信号
が制御装置18に送られるようになっている。さらに制
御装置18によって生成油フィルタ20、生成油制御弁
4、A重油制御弁5、混合油ヒータ8、およびディーゼ
ルエンジン13が制御されるようになっている。
Signals from the generated oil flow sensor 6, the A heavy oil flow sensor 7, the generated oil viscosity sensor 19, the mixed oil temperature sensor 9, the mixed oil viscosity sensor 10, and the differential pressure sensor 12 are sent to the controller 18. It has become. Further, the control device 18 controls the generated oil filter 20, the generated oil control valve 4, the A heavy oil control valve 5, the mixed oil heater 8, and the diesel engine 13.

【0022】図1において、燃料フィルタ11は燃料の
不純物を補足するものであり、その目詰まりによって発
生する差圧は差圧センサ12により検出される。また排
ガスセンサ14は、ディーゼルエンジン13の排気ガス
のNOx、SOx、CO、スモークなどを検出するセン
サである。また差圧センサ12が閉塞信号を発した場
合、または排ガスセンサ14が排ガス濃度異常信号を発
した場合に、混合油切換弁15は閉動作し、A重油切換
弁16は開動作する。さらに生成油粘度センサ19は、
生成油フィルタ20で清浄された生成油の粘度を測定す
る粘度センサである。さらに制御装置18は各センサか
らの信号を入力し、PID演算などの制御演算を行って
各制御対象に操作信号を出力する。
In FIG. 1, a fuel filter 11 supplements fuel impurities, and a differential pressure generated by the clogging is detected by a differential pressure sensor 12. Further, the exhaust gas sensor 14 is a sensor that detects NOx, SOx, CO, smoke, etc. of the exhaust gas of the diesel engine 13. Further, when the differential pressure sensor 12 issues a closing signal, or when the exhaust gas sensor 14 issues an exhaust gas concentration abnormal signal, the mixed oil switching valve 15 closes and the A heavy oil switching valve 16 opens. Further, the generated oil viscosity sensor 19
This is a viscosity sensor that measures the viscosity of the generated oil that has been cleaned by the generated oil filter 20. Further, the control device 18 receives a signal from each sensor, performs a control calculation such as a PID calculation, and outputs an operation signal to each control target.

【0023】次にこのような構成からなる本実施の形態
の作用について説明する。まず廃プラスチック処理装置
30により生成された生成油は、生成油供給ライン2に
より供給されるが、生成油は粘度が高く流動性が悪いた
め、A重油供給ラインより供給されるA重油と混合タン
ク1で混合され、その流動性が改善される。
Next, the operation of the present embodiment having the above configuration will be described. First, the generated oil generated by the waste plastic processing apparatus 30 is supplied through the generated oil supply line 2. However, since the generated oil has high viscosity and poor fluidity, it is mixed with the A heavy oil supplied from the A heavy oil supply line and the mixing tank. 1 to improve its flowability.

【0024】混合油タンク1内の混合油は、混合油ライ
ン31を経てディーゼルエンジン13へ送られる。また
ディーゼルエンジン13からの排ガスは排ガスライン3
2から外方へ排出される。
The mixed oil in the mixed oil tank 1 is sent to the diesel engine 13 through the mixed oil line 31. Exhaust gas from the diesel engine 13 is sent to the exhaust gas line 3
It is discharged from 2 to the outside.

【0025】この間、混合油粘度センサ10の信号が制
御装置18へ送られ、制御装置18の粘度制御機能21
ではあらかじめ設定された粘度設定値と混合粘度センサ
10の信号が比較され、混合油粘度センサ10からの信
号が設定粘度より高くなった場合には、制御装置18は
A重油制御弁5を開動作させ、A重油の量を増加させて
混合タンク1内の粘度を下げる(図2)。一方、混合油
粘度センサ10からの信号が設定粘度より低くなった場
合には、制御装置18はA重油制御弁5を閉動作させ、
A重油の量を低下させて混合タンク1内の粘度を上げ
る。
During this time, a signal from the mixed oil viscosity sensor 10 is sent to the control device 18 and the viscosity control function 21
Then, the preset viscosity set value is compared with the signal of the mixed viscosity sensor 10, and when the signal from the mixed oil viscosity sensor 10 becomes higher than the set viscosity, the control device 18 opens the heavy oil control valve 5. Then, the amount of Fuel Oil A is increased to lower the viscosity in the mixing tank 1 (FIG. 2). On the other hand, when the signal from the mixed oil viscosity sensor 10 becomes lower than the set viscosity, the control device 18 closes the A heavy oil control valve 5, and
The viscosity in the mixing tank 1 is increased by decreasing the amount of the heavy fuel oil A.

【0026】なお、生成油制御弁4は、予め設定された
生成油の流量となるよう制御装置18により制御される
が、生成油制御弁4をA重油制御弁5の代わりに混合油
粘度センサ10からの信号により制御してもよい。この
様に生成油とA重油の混合量(混合比率)を変えること
により、混合油はディーゼルエンジン燃料として適切な
粘度に制御される。なお、制御弁4,5は、電動機構ま
たはサーボ機構または油圧機構などいずれで動作させて
もよい。
The generated oil control valve 4 is controlled by the control device 18 so that the flow rate of the generated oil is set in advance. The generated oil control valve 4 is replaced with the heavy oil control valve 5 by a mixed oil viscosity sensor. It may be controlled by a signal from 10. By changing the mixing amount (mixing ratio) of the produced oil and the heavy oil A in this manner, the mixed oil is controlled to have an appropriate viscosity as a diesel engine fuel. The control valves 4 and 5 may be operated by an electric mechanism, a servo mechanism, a hydraulic mechanism, or the like.

【0027】以上のような本実施の形態において、エン
ジンの燃焼試験により生成油とA重油の混合燃料をエン
ジン燃料に使用する場合は、混合油の粘度を規定範囲に
すれば良い事を確認している。この結果を基に、混合油
タンク1内で混合される生成油とA重油の量を調節する
事により適切な粘度を得ることができ、最も簡単で経済
的な運転を行なうことができる。
In this embodiment as described above, it has been confirmed by a combustion test of the engine that when the mixed fuel of the generated oil and the heavy oil A is used as the engine fuel, the viscosity of the mixed oil should be within the specified range. ing. Based on this result, an appropriate viscosity can be obtained by adjusting the amounts of the product oil and heavy oil A mixed in the mixed oil tank 1, and the simplest and economical operation can be performed.

【0028】第2の実施の形態 次に本発明の第2の実施の形態について図3および図4
により説明する。
Second Embodiment Next, a second embodiment of the present invention will be described with reference to FIGS.
This will be described below.

【0029】第2の実施の形態は、制御装置18の構成
が異なるのみであり、他は第1の実施の形態と略同一で
ある。
The second embodiment differs from the first embodiment only in the configuration of the control device 18, but is otherwise the same as the first embodiment.

【0030】図3および図4に示すように、第2の実施
の形態は、混合油粘度センサ10からの信号に基づい
て、制御装置18により、目標温度となる様に混合油ヒ
ータ8を制御するものである。
As shown in FIGS. 3 and 4, in the second embodiment, the control device 18 controls the mixed oil heater 8 based on a signal from the mixed oil viscosity sensor 10 so as to reach a target temperature. Is what you do.

【0031】図3および図4に示すように、混合タンク
1より流出する混合油は混合油ヒータ8により加温さ
れ、燃料フィルタ11を経てディーゼルエンジン13に
供給されて燃焼される。燃料となる混合油の粘度は、デ
ィーゼルエンジン13で使用する範囲が決まっており、
混合油をその粘度に維持する必要がある。
As shown in FIGS. 3 and 4, the mixed oil flowing out of the mixing tank 1 is heated by a mixed oil heater 8, supplied to a diesel engine 13 through a fuel filter 11, and burned. The range of the viscosity of the mixed oil used as fuel is determined in the diesel engine 13.
The oil mixture must be maintained at that viscosity.

【0032】まず、混合油粘度センサ10の信号が制御
装置18内の「粘度−温度」特性機能23に入力する。
この「粘度−温度」特性を図3により説明する。図3は
「粘度−温度」特性曲線を示し、横軸に粘度、縦軸に温
度をとり混合油粘度センサ10からの信号を横軸の粘度
にプロットし、その時の温度を求めると目標温度が決定
される。
First, a signal from the mixed oil viscosity sensor 10 is input to a “viscosity-temperature” characteristic function 23 in the controller 18.
This "viscosity-temperature" characteristic will be described with reference to FIG. FIG. 3 shows a "viscosity-temperature" characteristic curve, in which the horizontal axis represents the viscosity and the vertical axis represents the temperature, and the signal from the mixed oil viscosity sensor 10 is plotted on the viscosity on the horizontal axis. It is determined.

【0033】この特性曲線は混合油の分析によって定め
られ、生成油の生成過程により成分や粘度が変動するた
め、それに適切に対応可能な温度となる様に特性曲線を
設定する。
This characteristic curve is determined by the analysis of the mixed oil. Since the components and the viscosity fluctuate depending on the production process of the produced oil, the characteristic curve is set so that the temperature can be appropriately adapted to the variation.

【0034】「粘度−温度」特性機能23において、
「粘度−温度」特性により決定された目標温度は、粘度
制御機能22に入力され、粘度制御機能22は目標温度
になる様に混合油ヒータ8を制御する。
In the "viscosity-temperature" characteristic function 23,
The target temperature determined by the "viscosity-temperature" characteristic is input to the viscosity control function 22, and the viscosity control function 22 controls the mixed oil heater 8 so as to reach the target temperature.

【0035】なお、図3に示すA、Cは設定の下限を示
し、B、Dは上限を示し、Eは混合油粘度センサ10の
信号に基づいて目標温度を求めた結果を示す。
A and C shown in FIG. 3 indicate the lower limit of the setting, B and D indicate the upper limit, and E indicates the result of obtaining the target temperature based on the signal of the mixed oil viscosity sensor 10.

【0036】他方、差圧センサ12からの信号を制御装
置18内の粘度制御機能22に入力し、差圧変化量に相
当する温度を目標温度の補正値として制御する。これ
は、燃料フィルタ11が目詰まりを起こすのを防ぐ目的
に行われ、差圧センサ12からの値が上昇した場合は、
燃料フィルタ11の目詰まりが発生したと判断し、目標
温度を上げて混合油ヒータ8を作動させ、燃料の流動性
を高める事によって燃料フィルタ11の通過を促進させ
る。次に、差圧センサ12からの値が規定値以下に下が
った場合は、燃料フィルタ11の目詰まりが解除された
と判断され、「粘度−温度」特性機能23の「粘度−温
度」特性曲線により決定される目標温度になる様に混合
油ヒータ8の制御が行われる。
On the other hand, a signal from the differential pressure sensor 12 is input to a viscosity control function 22 in the control device 18 to control a temperature corresponding to a differential pressure change amount as a correction value of a target temperature. This is performed for the purpose of preventing the fuel filter 11 from clogging, and when the value from the differential pressure sensor 12 increases,
It is determined that clogging of the fuel filter 11 has occurred, the target temperature is raised, the mixed oil heater 8 is operated, and the passage of the fuel filter 11 is promoted by increasing the fluidity of the fuel. Next, when the value from the differential pressure sensor 12 falls below the specified value, it is determined that the clogging of the fuel filter 11 has been released, and the “viscosity-temperature” characteristic curve of the “viscosity-temperature” characteristic function 23 is used. The control of the mixed oil heater 8 is performed so as to reach the determined target temperature.

【0037】本実施の形態によれば、混合油を温度制御
することにより流動性を改善することができ、生成油の
混合比率を高くする事ができるとともにディーゼルエン
ジンで燃焼する生成油を多くする事が可能となる。ま
た、燃料フィルタ11による閉塞によりエンジン停止す
ることがなくなる。また、「粘度−温度」特性機能23
による温度制御により、粘度変化に対応した温度設定が
可能になり、温度の変動を抑制する事が可能となる。
According to the present embodiment, the fluidity can be improved by controlling the temperature of the mixed oil, the mixing ratio of the generated oil can be increased, and the generated oil to be burned by the diesel engine can be increased. Things become possible. Further, the engine is not stopped due to the blockage by the fuel filter 11. The “viscosity-temperature” characteristic function 23
, Temperature setting corresponding to a change in viscosity becomes possible, and fluctuations in temperature can be suppressed.

【0038】第3の実施の形態 次に図5により本発明の第3の実施の形態について説明
する。第3の実施の形態は制御装置18の構成が異なる
のみであり、他は第1の実施の形態と同一である。図5
において、差圧センサ12からの信号が制御装置18内
の差圧制御機能24に入力される。この差圧制御機能2
4内では、差圧センサ12の信号があらかじめ設定され
た規定値を超えた場合は、燃料フィルタ11の目詰まり
が進行していると判断される。このとき差圧制御機能2
4はA重油制御弁5を開動作させ、このことにより混合
タンク1にA重油量が増加し、流動性が良くなった混合
油が燃料フィルタ11へ供給され、燃料フィルタ11の
目詰まりは徐々に解除に向かう。
Third Embodiment Next, a third embodiment of the present invention will be described with reference to FIG. The third embodiment is the same as the first embodiment except for the configuration of the control device 18. FIG.
, A signal from the differential pressure sensor 12 is input to a differential pressure control function 24 in the control device 18. This differential pressure control function 2
In 4, when the signal of the differential pressure sensor 12 exceeds a predetermined value, it is determined that the clogging of the fuel filter 11 is in progress. At this time, the differential pressure control function 2
4 opens the A fuel oil control valve 5, whereby the amount of the A fuel oil increases in the mixing tank 1 and the mixed oil having improved fluidity is supplied to the fuel filter 11, and the clogging of the fuel filter 11 is gradually reduced. Head to release.

【0039】次に、差圧センサ12の信号が規定値以下
になった場合は、燃料フィルタ11の目詰まりが解除さ
れたと判断され、初期設定の混合比率制御に戻す。すな
わち、例えば50%混合比率制御で設定された制御であ
れば、生成油流量センサ6からの信号と、A重油流量セ
ンサ7からの信号が等しくなるよう各制御弁4,5を差
圧制御機能24で制御する。
Next, when the signal from the differential pressure sensor 12 becomes equal to or less than the specified value, it is determined that the clogging of the fuel filter 11 has been released, and the control returns to the initially set mixing ratio control. That is, for example, in the case of the control set by the 50% mixing ratio control, the control valves 4 and 5 are controlled so that the signal from the generated oil flow sensor 6 and the signal from the A heavy oil flow sensor 7 become equal. 24.

【0040】本実施の形態によれば、混合タンク1に入
るA重油の量を増加することにより、混合油の粘度を下
げ、燃料フィルタ11が閉塞するのを防ぐ効果がある。
According to the present embodiment, the viscosity of the mixed oil is reduced by increasing the amount of the A-heavy oil entering the mixing tank 1, and the fuel filter 11 is prevented from being blocked.

【0041】第4の実施の形態 次に図6により、本発明の第4の実施の形態について説
明する。第4の実施の形態は制御装置18の構成が異な
るのみであり、他は第1の実施の形態と同一である。
Fourth Embodiment Next, a fourth embodiment of the present invention will be described with reference to FIG. The fourth embodiment is the same as the first embodiment except for the configuration of the control device 18.

【0042】図6に示すように、差圧センサ12が燃料
フィルタ11の閉塞を示す信号を発した場合、その信号
は制御装置18内の差圧・排ガス制御機能25に入力さ
れる。このとき燃料フィルタ11が閉塞と判断され、差
圧・排ガス制御機能25により混合油切換弁15に閉動
作信号が出力され、同時にA重油切換弁16に開動作信
号が出力される。これにより、混合油で運転中に燃料フ
ィルタ15の閉塞が発生した場合には、自動的にA重油
に切替わり、ディーゼルエンジン13が停止することな
く運転が継続される。なお制御装置18の差圧・排ガス
制御機能25により、混合油切換弁15またはA重油切
換弁16の少なくとも一方を制御してもよい。
As shown in FIG. 6, when the differential pressure sensor 12 generates a signal indicating that the fuel filter 11 is closed, the signal is input to a differential pressure / exhaust gas control function 25 in the control device 18. At this time, the fuel filter 11 is determined to be closed, and the differential pressure / exhaust gas control function 25 outputs a closing operation signal to the mixed oil switching valve 15 and simultaneously outputs an opening operation signal to the A heavy oil switching valve 16. Accordingly, when the fuel filter 15 is clogged during the operation with the mixed oil, the fuel oil is automatically switched to the A heavy oil, and the operation is continued without stopping the diesel engine 13. Note that the differential pressure / exhaust gas control function 25 of the control device 18 may control at least one of the mixed oil switching valve 15 and the A heavy oil switching valve 16.

【0043】また、図6において、排ガスセンサ14が
排ガス異常信号を発した場合に、その信号は制御装置1
8内の差圧・排ガス制御機能25に入力される。このと
きエンジン排気ガス異常と判断され、差圧・排ガス制御
機能25より混合油切換弁15に閉動作信号が出力さ
れ、同時にA重油切換弁16に開動作信号が出力され
る。これにより、混合油により運転中に、ディーゼルエ
ンジン13の排ガスが異常状態になった場合には、自動
的にA重油に切替わってディーゼルエンジン18からの
排気ガスは通常状態に戻り、ディーゼルエンジン13は
停止することなく運転が継続される。
In FIG. 6, when the exhaust gas sensor 14 emits an exhaust gas abnormality signal, the signal is transmitted to the control unit 1.
8 is input to a differential pressure / exhaust gas control function 25. At this time, it is determined that the engine exhaust gas is abnormal, and the differential pressure / exhaust gas control function 25 outputs a closing operation signal to the mixed oil switching valve 15 and simultaneously outputs an opening operation signal to the A heavy oil switching valve 16. Accordingly, when the exhaust gas of the diesel engine 13 is in an abnormal state during operation with the mixed oil, the diesel engine 18 is automatically switched to the heavy fuel oil A, and the exhaust gas from the diesel engine 18 returns to the normal state. The operation is continued without stopping.

【0044】ここで、排ガスは例えばNOx、SOx、
スモーク、COなどの濃度である。
Here, the exhaust gas is, for example, NOx, SOx,
It is the concentration of smoke, CO, etc.

【0045】燃料フィルタ11が閉塞した場合に、ディ
ーゼルエンジン13の運転を停止することなくバイパス
ライン17より供給されるA重油に切換えて運転を継続
することが可能である。
When the fuel filter 11 is closed, it is possible to switch to the heavy fuel oil A supplied from the bypass line 17 and continue the operation without stopping the operation of the diesel engine 13.

【0046】またディーゼルエンジンの排ガスが濃度異
常を起こした場合に、エンジンを停止することなくバイ
パスライン17より供給されるA重油に切換えて運転を
継続することが可能である。
When the concentration of the exhaust gas of the diesel engine is abnormal, the operation can be continued by switching to the heavy fuel oil A supplied from the bypass line 17 without stopping the engine.

【0047】第5の実施の形態 次に図7により、本発明の第5の実施の形態について説
明する。第5の実施の形態は制御装置18の作用が異な
るのみであり、他は第1の実施の形態と同一である。
Fifth Embodiment Next, a fifth embodiment of the present invention will be described with reference to FIG. The fifth embodiment is the same as the first embodiment except that the operation of the control device 18 is different.

【0048】生成油粘度センサ19の信号が制御装置1
8内のワックス除去機能26に入力され、生成油粘度が
規定値以上になった場合に、制御装置18内のワックス
除去機能26により生成油フィルタ20に清浄指令が発
せられて、生成油フィルタ20の洗浄が行われる。ま
た、生成油粘度が規定値以下になった場合は、生成油フ
ィルタ20の清浄指令を解除する。これは、生成油に含
入されているワックス成分が、混合油の混合比率を決定
する上で重要なファクターとして影響するため、混合タ
ンク1に混合する前にワックス成分を除去する事を目的
としている。
The signal from the generated oil viscosity sensor 19 is transmitted to the controller 1
When the generated oil viscosity is input to the wax removal function 26 in the controller 8 and the viscosity of the generated oil becomes equal to or more than the specified value, a cleaning command is issued to the generated oil filter 20 by the wax removal function 26 in the control device 18 and the generated oil filter 20 is controlled. Is performed. When the generated oil viscosity becomes equal to or less than the specified value, the cleaning instruction of the generated oil filter 20 is released. This is for the purpose of removing the wax component before mixing in the mixing tank 1 because the wax component contained in the produced oil has an important factor in determining the mixing ratio of the mixed oil. I have.

【0049】生成油はワックス成分を多く含んだ燃料で
あるため、これをそのまま混合タンク1に入れないでワ
ックス除去フィルタ20により除去する。このため混合
タンク1以降での混合量の制御が容易になる。
Since the generated oil is a fuel containing a large amount of wax components, it is removed by the wax removal filter 20 without directly entering the mixing tank 1. Therefore, the control of the mixing amount in the mixing tank 1 and thereafter becomes easy.

【0050】なお、上記各実施の形態において、上記制
御装置18は、上記各実施の形態における作用形態をす
べて含むように構成してもよい。
In each of the above embodiments, the control device 18 may be configured so as to include all the operation modes in the above embodiments.

【0051】各実施の形態を組合せることにより、ディ
ーゼルエンジン13に供給する混合燃料の動粘度を適切
な状態に維持し、流動性を確保することができる。ま
た、A重油と生成油の混合比率を適切に定めてエンジン
燃料フィルタ11の目詰まりを防止し、さらに、混合燃
料が燃料フィルタ11の閉塞やエンジンの排ガス異常な
どによってエンジンが停止するのを回避する事が可能と
なる。
By combining the embodiments, it is possible to maintain the kinetic viscosity of the mixed fuel supplied to the diesel engine 13 in an appropriate state, and to ensure fluidity. Further, the mixing ratio of the heavy oil A and the generated oil is appropriately determined to prevent the engine fuel filter 11 from being clogged, and further, the mixed fuel is prevented from being stopped due to the clogging of the fuel filter 11 or the engine exhaust gas abnormality. It is possible to do.

【0052】なお、上記実施の形態において、ディーゼ
ルエンジンへ燃料を供給する場合について説明したが、
ディーゼルエンジンだけでなく、ボイラーの燃料に使用
する場合なども本方式が適用可能である。
In the above embodiment, the case where fuel is supplied to the diesel engine has been described.
This method is applicable not only to diesel engines but also to fuels for boilers.

【0053】[0053]

【発明の効果】以上のように、本発明によれば、ディー
ゼルエンジン等の燃焼装置に供給する生成油とA重油の
混合燃料の粘度を適切な状態に維持し、流動性を確保す
ることが可能となる。 またA重油と生成油の混合比率
を適切に行うことが可能となり、生成油の燃焼量を最大
にすることができる。さらに燃料フィルタの目詰まりを
防止することが可能となり、目詰まりが発生した場合に
はA重油による運転が行われるためエンジンが停止する
ことがない。また、燃焼装置からの排気ガス濃度が異常
状態になった場合にも、A重油による運転に自動的に切
換えることが可能となり、エンジンの停止を回避するこ
とができる。
As described above, according to the present invention, it is possible to maintain the viscosity of the mixed fuel of the generated oil and the heavy fuel oil A to be supplied to a combustion device such as a diesel engine in an appropriate state, and to ensure fluidity. It becomes possible. In addition, the mixing ratio between the heavy oil A and the generated oil can be appropriately set, and the amount of combustion of the generated oil can be maximized. Further, clogging of the fuel filter can be prevented, and when clogging occurs, the engine is not stopped because the operation using heavy fuel oil A is performed. Further, even when the exhaust gas concentration from the combustion device becomes abnormal, it is possible to automatically switch to the operation using the heavy fuel oil A, and it is possible to avoid stopping the engine.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明による廃プラスチック生成油供給システ
ムの第1の実施の形態を示す系統図。
FIG. 1 is a system diagram showing a first embodiment of a waste plastic production oil supply system according to the present invention.

【図2】廃プラスチック生成油供給システムの制御装置
の作用を示す図。
FIG. 2 is a diagram showing an operation of a control device of the waste plastic production oil supply system.

【図3】「粘度−温度」特性機能の「粘度−温度」特性
を示す図。
FIG. 3 is a diagram showing a “viscosity-temperature” characteristic of a “viscosity-temperature” characteristic function.

【図4】本発明による廃プラスチック生成油供給システ
ムの第2の実施の形態を示す作用図。
FIG. 4 is an operation diagram showing a second embodiment of the waste plastic production oil supply system according to the present invention.

【図5】本発明による廃プラスチック生成油供給システ
ムの第3の実施の形態を示す作用図。
FIG. 5 is an operational view showing a third embodiment of the waste plastic production oil supply system according to the present invention.

【図6】本発明による廃プラスチック生成油供給システ
ムの第4の実施の形態を示す作用図。
FIG. 6 is an operational diagram showing a fourth embodiment of the waste plastic production oil supply system according to the present invention.

【図7】本発明による廃プラスチック生成油供給システ
ムの第5の実施の形態を示す作用図。
FIG. 7 is an operational view showing a fifth embodiment of the waste plastic production oil supply system according to the present invention.

【符号の説明】[Explanation of symbols]

1 混合タンク 2 生成油供給ライン 3 A重油供給ライン 4 生成油制御弁 5 A重油制御弁 6 生成油流量センサ 7 A重油流量センサ 8 混合油ヒータ 9 混合油温度センサ 10 混合油粘度センサ 11 燃料フィルタ 12 差圧センサ 13 ディーゼルエンジン 14 排ガスセンサ 15 混合油切換弁 16 A重油切換弁 17 バイパスライン 18 制御装置 19 生成油粘度センサ 20 生成油フィルタ 21 粘度制御機能 22 粘度制御機能 23 「粘度−温度」特性機能 24 差圧制御機能 25 差圧・排ガス制御機能 26 ワックス除去機能 REFERENCE SIGNS LIST 1 mixing tank 2 generated oil supply line 3 A heavy oil supply line 4 generated oil control valve 5 A heavy oil control valve 6 generated oil flow sensor 7 A heavy oil flow sensor 8 mixed oil heater 9 mixed oil temperature sensor 10 mixed oil viscosity sensor 11 fuel filter REFERENCE SIGNS LIST 12 differential pressure sensor 13 diesel engine 14 exhaust gas sensor 15 mixed oil switching valve 16 A heavy oil switching valve 17 bypass line 18 control device 19 generated oil viscosity sensor 20 generated oil filter 21 viscosity control function 22 viscosity control function 23 “viscosity-temperature” characteristic Function 24 Differential pressure control function 25 Differential pressure / exhaust gas control function 26 Wax removal function

フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F02D 45/00 364 F02D 45/00 364K 4H029 F02M 31/125 F02M 43/02 43/02 63/00 U 63/00 31/12 321D Fターム(参考) 3G060 AA02 BA19 CA01 CC02 FA04 GA04 3G066 AA07 AB03 AB06 AD02 BA12 BA32 BA43 DA01 DC11 DC24 DC25 3G084 AA01 BA11 BA26 DA34 EC03 FA14 FA29 FA31 3G092 AA02 AB04 AB12 BB01 DE01Y DE10Y EA02 EC03 FA15 FA36 HB01Z HB05Z HD05Z 4H013 AA06 4H029 CA15 CA16 Continuation of the front page (51) Int.Cl. 7 Identification symbol FI Theme coat II (reference) F02D 45/00364 F02D 45/00 364K 4H029 F02M 31/125 F02M 43/02 43/02 63/00 U 63/00 31 / 12 321D F-term (Reference) 3G060 AA02 BA19 CA01 CC02 FA04 GA04 3G066 AA07 AB03 AB06 AD02 BA12 BA32 BA43 DA01 DC11 DC24 DC25 3G084 AA01 BA11 BA26 DA34 EC03 FA14 FA29 FA31 3G092 AA02 AB04 AB12 BB01 DE02Y DEBZ15 FA05Z 4H013 AA06 4H029 CA15 CA16

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置と、 生成油供給ラインおよびA重油供給ラインに各々設けら
れた生成油制御弁およびA重油制御弁と、を備え、 混合油ラインに混合油粘度センサとを設け、 混合油粘度センサからの信号に基づいて、制御装置によ
り生成油制御弁およびA重油制御弁のうち少なくとも一
方を制御することを特徴とする廃プラスチック生成油供
給システム。
1. A product oil supply line to which a product oil from a waste plastic processing device is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from a product oil supply line, and a product oil from a fuel oil A supply line A mixing tank in which the mixed oil is mixed to produce a mixed oil, a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line, a generated oil supply line and a heavy oil supply line A generated oil control valve and an A fuel oil control valve, a mixed oil viscosity sensor is provided in the mixed oil line, and the control device controls the generated oil control valve and the A fuel oil control valve based on a signal from the mixed oil viscosity sensor. A waste plastic production oil supply system characterized by controlling at least one of them.
【請求項2】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置とを備え、 混合油ラインに混合油粘度センサと、混合油ヒータとを
設け、 混合油粘度センサからの信号に基づいて、制御装置によ
り混合油ヒータを制御することを特徴とする廃プラスチ
ック生成油供給システム。
2. A generated oil supply line to which the generated oil from the waste plastic processing apparatus is supplied, a heavy oil supply line to which the heavy oil A is supplied, a generated oil from the generated oil supply line, and a heavy oil supply line A mixing tank in which the fuel oil A is mixed to produce a mixed oil; and a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line. A waste plastic generation oil supply system, comprising: a heater; and a controller that controls the mixed oil heater based on a signal from the mixed oil viscosity sensor.
【請求項3】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置と、 生成油供給ラインおよびA重油供給ラインに各々設けら
れた生成油制御弁およびA重油制御弁と、を備え、 混合油ラインに差圧センサを有する燃料フィルタを設
け、 差圧センサからの信号に基づいて、制御装置により生成
油制御弁およびA重油制御弁のうち少なくとも一方を制
御することを特徴とする廃プラスチック生成油供給シス
テム。
3. A generated oil supply line to which the generated oil from the waste plastic processing apparatus is supplied, a A heavy oil supply line to which the A heavy oil is supplied, a generated oil from the generated oil supply line, and a A oil supply line A mixing tank in which the mixed oil is mixed to produce a mixed oil, a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line, a generated oil supply line and a heavy oil supply line A fuel filter having a differential pressure sensor is provided in the mixed oil line, and the generated oil control valve and the A heavy oil control valve are controlled by the control device based on a signal from the differential pressure sensor. A waste plastic producing oil supply system, wherein at least one of the two is controlled.
【請求項4】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置とを備え、 A重油供給ラインに混合油供給ラインに合流するバイパ
スラインを設け、 混合油供給ラインのバイパスラインとの合流点より上流
側に混合油切換弁を設けるとともに、バイパスラインに
A重油切換弁を設け、 混合油ラインに差圧センサを有する燃料フィルタを設
け、 差圧センサからの信号に基づいて、制御装置により混合
油切換弁およびA重油切換弁のうち少なくとも一方を制
御することを特徴とする廃プラスチック生成油供給シス
テム。
4. A generated oil supply line to which the generated oil from the waste plastic processing device is supplied; a heavy oil supply line to which the heavy A oil is supplied; a generated oil from the generated oil supply line; And a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line, and joins the mixed oil supply line with the A heavy oil supply line. A bypass line is provided, a mixed oil switching valve is provided upstream of a junction of the mixed oil supply line with the bypass line, an A heavy oil switching valve is provided in the bypass line, and a fuel filter having a differential pressure sensor in the mixed oil line is provided. Waste plastic characterized in that a control device controls at least one of a mixed oil switching valve and an A heavy oil switching valve based on a signal from a differential pressure sensor. Generated oil supply system.
【請求項5】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置とを備え、 A重油供給ラインに混合油供給ラインに合流するバイパ
スラインを設け、 混合油供給ラインのバイパスラインとの合流点より上流
側に混合油切換弁を設けるとともに、バイパスラインに
A重油切換弁を設け、 燃焼装置に排ガスラインを設けるともに、この排ガスラ
インに排ガスセンサを設け、 排ガスセンサからの信号に基づいて、制御装置により混
合油切換弁およびA重油切換弁のうち少なくとも一方を
制御することを特徴とする廃プラスチック生成油供給シ
ステム。
5. A product oil supply line to which product oil from a waste plastic processing device is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from the product oil supply line, and a product oil from the fuel oil A supply line And a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line, and joins the mixed oil supply line with the A heavy oil supply line. A bypass line is provided, a mixed oil switching valve is provided upstream of the junction of the mixed oil supply line with the bypass line, an A heavy oil switching valve is provided in the bypass line, and an exhaust gas line is provided in the combustion device. An exhaust gas sensor, and a control device controls at least one of the mixed oil switching valve and the A heavy oil switching valve based on a signal from the exhaust gas sensor. A waste plastic production oil supply system characterized by the following.
【請求項6】廃プラスチック処理装置からの生成油が供
給される生成油供給ラインと、 A重油が供給されるA重油供給ラインと、 生成油供給ラインからの生成油と、A重油供給ラインか
らのA重油が混合して混合油が生成される混合タンク
と、 混合タンクからの混合油が混合油ラインを経て供給され
る燃焼装置とを備え、 生成油供給ラインに生成油フィルタおよび生成油粘度セ
ンサを設け、 生成油粘度センサからの信号に基づいて、制御装置によ
り生成油フィルタを制御することを特徴とする廃プラス
チック生成油供給システム。
6. A product oil supply line to which product oil from a waste plastic processing device is supplied, a fuel oil A supply line to which fuel oil A is supplied, a product oil from the product oil supply line, and a product oil from the fuel oil A supply line A mixing tank in which the heavy oil A is mixed to produce a mixed oil, and a combustion device in which the mixed oil from the mixing tank is supplied through a mixed oil line. The generated oil filter and the generated oil viscosity are provided in the generated oil supply line. A waste plastic generation oil supply system, comprising: a sensor; and a control device that controls the generation oil filter based on a signal from the generation oil viscosity sensor.
JP2000368717A 2000-12-04 2000-12-04 Waste plastic generation oil supply system Expired - Fee Related JP3866505B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000368717A JP3866505B2 (en) 2000-12-04 2000-12-04 Waste plastic generation oil supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000368717A JP3866505B2 (en) 2000-12-04 2000-12-04 Waste plastic generation oil supply system

Publications (2)

Publication Number Publication Date
JP2002168139A true JP2002168139A (en) 2002-06-14
JP3866505B2 JP3866505B2 (en) 2007-01-10

Family

ID=18838881

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000368717A Expired - Fee Related JP3866505B2 (en) 2000-12-04 2000-12-04 Waste plastic generation oil supply system

Country Status (1)

Country Link
JP (1) JP3866505B2 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009063933A1 (en) * 2007-11-15 2009-05-22 Yanmar Co., Ltd. Fuel supply device and fuel supply method
JP2010203637A (en) * 2009-02-27 2010-09-16 Mitsubishi Heavy Ind Ltd Liquefied gas carrying vessel
JP2010275991A (en) * 2009-06-01 2010-12-09 Denso Corp Control device for fuel supply system
JP2011214734A (en) * 2010-03-31 2011-10-27 Maeda Road Constr Co Ltd Fuel treatment device and method for waste glycerin
JP2012087973A (en) * 2010-10-18 2012-05-10 Mitsubishi Heavy Ind Ltd Heavy oil combustion boiler
JP2013189932A (en) * 2012-02-13 2013-09-26 Blest:Kk Driving device and method of driving the same
EP2208881A4 (en) * 2007-11-15 2015-09-30 Yanmar Co Ltd Fuel supply apparatus and fuel supply method
JP2016070261A (en) * 2014-09-26 2016-05-09 新潟原動機株式会社 Fuel oil supply device of diesel engine

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8584657B2 (en) 2007-11-15 2013-11-19 Yanmar Co., Ltd. Fuel supply apparatus and fuel supply method
JP2009121367A (en) * 2007-11-15 2009-06-04 Yanmar Co Ltd Fuel supply device and fuel supply method
EP2211041A1 (en) * 2007-11-15 2010-07-28 Yanmar Co., Ltd. Fuel supply device and fuel supply method
WO2009063933A1 (en) * 2007-11-15 2009-05-22 Yanmar Co., Ltd. Fuel supply device and fuel supply method
US9689320B2 (en) 2007-11-15 2017-06-27 Yanmar Co., Ltd. Fuel supply apparatus and fuel supply method
EP2208881A4 (en) * 2007-11-15 2015-09-30 Yanmar Co Ltd Fuel supply apparatus and fuel supply method
EP2211041A4 (en) * 2007-11-15 2015-03-25 Yanmar Co Ltd Fuel supply device and fuel supply method
JP2010203637A (en) * 2009-02-27 2010-09-16 Mitsubishi Heavy Ind Ltd Liquefied gas carrying vessel
JP2010275991A (en) * 2009-06-01 2010-12-09 Denso Corp Control device for fuel supply system
JP2011214734A (en) * 2010-03-31 2011-10-27 Maeda Road Constr Co Ltd Fuel treatment device and method for waste glycerin
JP2012087973A (en) * 2010-10-18 2012-05-10 Mitsubishi Heavy Ind Ltd Heavy oil combustion boiler
JP2013189932A (en) * 2012-02-13 2013-09-26 Blest:Kk Driving device and method of driving the same
JP2016070261A (en) * 2014-09-26 2016-05-09 新潟原動機株式会社 Fuel oil supply device of diesel engine

Also Published As

Publication number Publication date
JP3866505B2 (en) 2007-01-10

Similar Documents

Publication Publication Date Title
US6256975B1 (en) Method for reliably removing liquid fuel from the fuel system of a gas turbine, and a device for carrying out the method
JP4564376B2 (en) LNG power generation plant and its operation method
US7832192B2 (en) Method for injecting a liquid mist into an intake duct
JP2002168139A (en) Feeding system for waste plastic generating oil
JP2007231949A (en) Variable extraction method for control of gas turbine
CN106194525A (en) A kind of bunker oil feeding mechanism and method
CN100532931C (en) Method and apparatus for optimizing a steam boiler system
US7284507B2 (en) Method and apparatus for the control of a spraying apparatus
JP5941224B2 (en) Water-mixed fuel generator
CN109989806B (en) Diesel engine high-pressure SCR (selective catalytic reduction) ventilation and pressure stabilization system
CN219083049U (en) Biomass boiler flue gas temperature control system
CN106342118B (en) Diesel engine rail pressure control control method
CN214406135U (en) Oil supply pipeline structure of oil-gas dual-purpose boiler
JP5525772B2 (en) Biomass liquid fuel combustion system
WO2017219351A1 (en) Cleaning system for a gas turbine engine
JP2001248802A (en) Soot blower
CN108980886B (en) Methanol fuel supply device and system
CN108194192B (en) Exhaust gas boiler energy control method based on diesel engine exhaust gas bypass device
DE102010037454A1 (en) Method for controlling air flow supplied to burner impinged with its output of exhaust section of internal combustion engine, involves controlling of air flow supplied to burner depending on air flow moving through air conveyor
JPH0968123A (en) Fuel temperature raising device
JP2001329863A (en) Combustion device for gas turbine and fuel supply method for gas turbine
JP2554492Y2 (en) Control device for pressurized fluidized bed boiler
CN102830355A (en) Automatic cooling system for motor test
JPH0233458A (en) Operating method for diesel engine
CN208124315U (en) A kind of liquid waste spray gun control system and incinerator

Legal Events

Date Code Title Description
A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20060711

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20060904

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20060929

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20061005

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101013

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111013

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111013

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121013

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees