JPH10282084A - Viscosity mixing ratio meter - Google Patents

Viscosity mixing ratio meter

Info

Publication number
JPH10282084A
JPH10282084A JP8695397A JP8695397A JPH10282084A JP H10282084 A JPH10282084 A JP H10282084A JP 8695397 A JP8695397 A JP 8695397A JP 8695397 A JP8695397 A JP 8695397A JP H10282084 A JPH10282084 A JP H10282084A
Authority
JP
Japan
Prior art keywords
water
viscosity
mixed liquid
thin tube
flow rate
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.)
Withdrawn
Application number
JP8695397A
Other languages
Japanese (ja)
Inventor
Masanori Tanaka
正紀 田中
Yoshimasa Fujiwara
嘉正 藤原
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.)
Mitsui Engineering and Shipbuilding Co Ltd
Original Assignee
Mitsui Engineering and Shipbuilding Co Ltd
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 Mitsui Engineering and Shipbuilding Co Ltd filed Critical Mitsui Engineering and Shipbuilding Co Ltd
Priority to JP8695397A priority Critical patent/JPH10282084A/en
Publication of JPH10282084A publication Critical patent/JPH10282084A/en
Withdrawn legal-status Critical Current

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  • Investigating Or Analyzing Materials Using Thermal Means (AREA)

Abstract

PROBLEM TO BE SOLVED: To measure the viscosity of a mixed liquid and the mixing ratio with water accurately by making constant the flow rate of an emulsified mixed liquid of water and oil and operating the viscosity from the pressure difference of a thin tube passing the mixed liquid whereas operating the ratio of water from the heating temperature difference of the mixed liquid. SOLUTION: A fixed volume pump 1, a thin tube 2 and a heater 3 are arranged in series and pressure gauges 5, 6 are provided at the inlet and outlet of the thin tube 2 while thermometers 8, 9 are provided at the inlet and outlet of the heater 3. A first operating unit 7 is previously inputted with the radius R and the length L of the thin tube 2 and the flow rate Q of an emulsified mixed liquid of water and oil is predetermined by the fixed volume pump 1. Consequently, the absolute viscosity η of an emulsion fuel can be operated according to formula I when the inlet and outlet pressures P1, P2 of the thin tube 2 are introduced. A second operating unit 10 is previously inputted with the specific heat λw of water, the specific heat λo of fuel, the flow rate Q and the heat quantity H. Consequently, the ratio of water α can be operated according to formula II when the inlet and outlet temperatures T1, T2 of the heater 3 are introduced.

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、エマルジョン化し
た水と油の混合液の粘度および水の比率を測定するため
の粘度混合比計に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a viscosity mixing ratio meter for measuring the viscosity of a mixture of emulsified water and oil and the ratio of water.

【0002】[0002]

【従来の技術】昨今、ディーゼル機関から排出される排
ガス中の窒素酸化物を低減するために、エマルジョン化
した水と燃料油の混合液を燃料としてディーゼル機関に
供給することがある。一般に、ディーゼル機関に供給す
る燃料(重油)は、その粘度がある範囲に入るように制
御され、粘度が基準より高い場合には、必要な粘度範囲
に収まるように燃料を加熱することが行われる。加熱温
度は、予め、分析した燃料の粘度から計算して求める。
このための線図は、粘度/温度線図として入手できる。
また、粘度を測定するために粘度計を用いることもあ
る。この場合は、粘度計の計測値に基づいて加熱温度が
調整される。
2. Description of the Related Art Recently, in order to reduce nitrogen oxides in exhaust gas discharged from a diesel engine, a mixed liquid of emulsified water and fuel oil is sometimes supplied to the diesel engine as fuel. Generally, the fuel (heavy oil) supplied to a diesel engine is controlled so that its viscosity falls within a certain range, and when the viscosity is higher than a standard, the fuel is heated to fall within a required viscosity range. . The heating temperature is calculated in advance from the analyzed viscosity of the fuel.
A diagram for this is available as a viscosity / temperature diagram.
A viscometer may be used to measure the viscosity. In this case, the heating temperature is adjusted based on the value measured by the viscometer.

【0003】一方、ディーゼル機関にエマルジョン化し
た水と燃料の混合液を供給する場合には、水と燃料の比
率を制御する必要がある。このとき、エマルジョン化し
た水と燃料の比率を直接測定できれば、制御も正確にな
ると共に、制御系も簡素化できる。しかしながら、市販
されている水分計は、測定範囲が1%以下のものが多
く、数十%もの含有水分を測定できる水分計は見当たら
ない。
On the other hand, when supplying a mixed liquid of emulsified water and fuel to a diesel engine, it is necessary to control the ratio of water to fuel. At this time, if the ratio of emulsified water to fuel can be directly measured, the control becomes accurate and the control system can be simplified. However, many commercially available moisture meters have a measurement range of 1% or less, and there is no moisture meter that can measure moisture content of several tens%.

【0004】上記のように、従来は、ディーゼル機関に
供給するエマルジョン燃料における水と燃料の混合比率
は、供給流量を制御することにより行われ、ディーゼル
機関に供給する燃料の加熱温度は、予め、分析した燃料
の粘度から計算で求めるか、あるいは、粘度計を監視し
て適正粘度になるように加熱温度を調整するかのいずれ
かによって行われている。
As described above, conventionally, the mixing ratio of water and fuel in the emulsion fuel supplied to the diesel engine is controlled by controlling the supply flow rate, and the heating temperature of the fuel supplied to the diesel engine is determined in advance. This is performed by either calculating from the analyzed viscosity of the fuel or by monitoring the viscometer and adjusting the heating temperature to obtain an appropriate viscosity.

【0005】従って、エマルジョン燃料の水分率と粘度
とを別々の計器で測定するため、価格の上昇を招くばか
りでなく、装置が複雑になり、ディーゼル機関への装着
も大変になる。
[0005] Therefore, since the water content and the viscosity of the emulsion fuel are measured by different instruments, not only does the price rise, but also the apparatus becomes complicated and the installation on a diesel engine becomes difficult.

【0006】[0006]

【発明が解決しようとする課題】本発明は、係る従来の
問題を解消するために案出されたものであり、エマルジ
ョン化した水と油の混合液の粘度および水の比率を比較
的簡単な一台の装置で精度良く測定できる粘度混合比計
を提供することにある。
SUMMARY OF THE INVENTION The present invention has been made in order to solve the above-mentioned conventional problems, and is intended to reduce the viscosity of a mixture of emulsified water and oil and the ratio of water to a relatively simple one. An object of the present invention is to provide a viscosity mixing ratio meter that can accurately measure with one device.

【0007】[0007]

【課題を解決するための手段】請求項1に記載の発明に
係る粘度混合比計は、エマルジョン化した水と油の混合
液の流量を一定にする流量制御装置と、該流量制御装置
によって流量規制された混合液を通す所定の半径と管長
とを有する細管と、該細管の入口及び出口に夫々設置さ
せた圧力計と、この両圧力計の圧力差から混合液の粘度
を演算する第1演算装置と、前記流量制御装置によって
流量規制された混合液を加熱する加熱器と、該加熱器の
入口及び出口に夫々設置させた温度計と、この両温度計
の温度差から水の比率を演算する第2演算装置と、から
なることを特徴とする。
According to a first aspect of the present invention, there is provided a viscosity mixing ratio meter for controlling a flow rate of a mixed liquid of emulsified water and oil, and a flow rate control apparatus for controlling a flow rate of the mixed liquid. A thin tube having a predetermined radius and a tube length through which the restricted mixture is passed, pressure gauges respectively installed at the inlet and the outlet of the narrow tube, and a first method for calculating the viscosity of the mixture from the pressure difference between the two pressure gauges. An arithmetic unit, a heater for heating the mixed liquid whose flow rate is controlled by the flow control device, thermometers respectively installed at the inlet and the outlet of the heater, and a water ratio based on a temperature difference between the two thermometers. And a second computing device for performing computation.

【0008】請求項1に記載の発明によれば、エマルジ
ョン化した水と油の混合液の流量Qは、流量制御装置に
よって決まり、細管の半径Rおよび管長Lも既知である
から細管の入口と出口の圧力差(P1−P2)が分かれ
ば、ポアズイユの式からエマルジョンの絶対粘度ηを求
めることができる。 η=π/8(P1−P2)/Q/R4 /L
According to the first aspect of the present invention, the flow rate Q of the mixture of emulsified water and oil is determined by the flow rate control device, and the radius R and length L of the thin tube are known. If the pressure difference at the outlet (P1−P2) is known, the absolute viscosity η of the emulsion can be obtained from the Poiseuille equation. η = π / 8 (P1−P2) / Q / R 4 / L

【0009】他方、加熱器、つまり、電気ヒーター電力
を一定にして加熱熱量Hを一定にし、水の比熱λw及び
燃料の比熱λoが既知であるから加熱器の入口と出口の
温度差(T2−T1)が分かれば、次式から水の比率α
を求めることができる。 α=(H/(T2−T1)/Q−λo)/(λw−λ
o)
On the other hand, since the specific heat λw of the heater and the specific heat λo of the fuel are known, the temperature difference between the inlet and the outlet of the heater (T2−T2) If T1) is known, the ratio of water α
Can be requested. α = (H / (T2−T1) / Q−λo) / (λw−λ
o)

【0010】[0010]

【発明の実施の形態】以下、図面により本発明の実施の
形態を説明する。図1は、本発明に係る粘度混合比計の
概略図であり、上流側から下流側に向かって定量ポンプ
1、所定の半径Rと管長Lとを有する細管2、加熱器3
が直列に配設されている。これらの機器1,2,3は、
配管4によって互いに連通されている。更に、細管2の
入口に第1の圧力計5を設置すると共にその出口に第2
の圧力計6を設置する。この2つの圧力計5及び6に接
続された第1の演算装置7は、次式(1)で表されるポ
アズイユの式から絶対粘度ηを演算するようになってい
る。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic view of a viscosity mixing ratio meter according to the present invention, in which a metering pump 1, a thin tube 2 having a predetermined radius R and a tube length L, and a heater 3 are arranged from upstream to downstream.
Are arranged in series. These devices 1, 2, 3
The pipes 4 communicate with each other. Further, a first pressure gauge 5 is installed at the inlet of the thin tube 2 and a second pressure gauge is installed at the outlet thereof.
Pressure gauge 6 is installed. The first arithmetic unit 7 connected to the two pressure gauges 5 and 6 calculates the absolute viscosity η from Poiseuille's equation represented by the following equation (1).

【0011】他方、上記加熱器3の入口に第1の温度計
8を設置すると共にその出口に第2の温度計9を設置す
る。この2つの温度計8及び9に接続された第2の演算
装置10は、次式(2)から水の比率αを演算するよう
になっている。次に、上記の粘度混合比計の作用につい
て説明する。上記の第1の演算装置7には、予め、細管
2の半径Rと管長Lとが入力されている。また、エマル
ジョン化した水と燃料油との混合液の流量Qも定量ポン
プ1によって決まっている。
On the other hand, a first thermometer 8 is provided at the inlet of the heater 3 and a second thermometer 9 is provided at the outlet thereof. The second arithmetic unit 10 connected to the two thermometers 8 and 9 calculates the water ratio α from the following equation (2). Next, the operation of the above-mentioned viscosity mixing ratio meter will be described. The radius R and the tube length L of the thin tube 2 are input to the first arithmetic unit 7 in advance. The flow rate Q of the mixture of the emulsified water and the fuel oil is also determined by the metering pump 1.

【0012】従って、第1の圧力計5によって測定した
細管2の入口圧力P1および第2の圧力計6によって測
定した細管2の出口圧力P2が演算装置7に導入される
と、この第1の演算装置7によってエマルジョン燃料の
絶対粘度ηが(1)式で示すポアズイユの式から演算さ
れる。
Therefore, when the inlet pressure P1 of the thin tube 2 measured by the first manometer 5 and the outlet pressure P2 of the thin tube 2 measured by the second manometer 6 are introduced into the arithmetic unit 7, the first pressure The arithmetic unit 7 calculates the absolute viscosity η of the emulsion fuel from the Poiseuille equation shown in the equation (1).

【0013】すなわち、 η=π/8(P1−P2)/Q/R4 /L ・・・・(1) 他方、第2の演算装置10には、予め、水の比熱λw、
燃料の比熱λo、上記混合液の流量Q、及び加熱器の加
熱熱量Hが入力されている。
That is, η = π / 8 (P1−P2) / Q / R 4 / L (1) On the other hand, the second arithmetic unit 10 previously stores the specific heat λw of water,
The specific heat λo of the fuel, the flow rate Q of the mixed liquid, and the heating heat H of the heater are input.

【0014】従って、第1の温度計8によって測定した
加熱器3の入口温度T1および第2の温度計9によって
測定した加熱器3の出口温度T2が第2の演算装置10
に導入されると、この第2の演算装置10によって次式
(2)からエマルジョン燃料における水の比率αが演算
される。
Therefore, the inlet temperature T1 of the heater 3 measured by the first thermometer 8 and the outlet temperature T2 of the heater 3 measured by the second thermometer 9 are determined by the second arithmetic unit 10
Is calculated by the second arithmetic unit 10 from the following equation (2).

【0015】すなわち、 α=(H/(T2−T1)/Q−λo)/(λw−λo) ・・・(2) 図2は、上記の粘度混合比計を燃料供給系に組み入れた
概略図であり、燃料主管15の途中から燃料を一部分流
して図1の計測装置へ流す。第1の演算器7によって演
算した絶対粘度ηの値に基づいて燃料加熱器(例えば、
電気ヒーター)のコントローラー14を制御するように
なっている。また、第2の演算装置10によって演算し
た水の比率αの値に基づいて水供給ポンプ16のコント
ローラー17をコントロールするようになっている。図
中、符号11は主燃料ポンプ、12はホモジナイザ、1
3は主ヒーター、19は水タンク、21は燃料タンク、
23は燃料噴射弁、25は混合液戻し管を示している。
なお、粘度混合比計については、図1にて説明したの
で、詳細な説明を省略する。以上の説明では、流量制御
装置として定量ポンプを用いたが、圧力差がある場合に
は、定量ポンプの代わりに流量制御弁を用いてもよい。
That is, α = (H / (T2−T1) / Q−λo) / (λw−λo) (2) FIG. 2 schematically shows the above-described viscosity mixing ratio meter incorporated in a fuel supply system. FIG. 3 is a diagram showing a state in which fuel flows partially from the middle of the fuel main pipe 15 and flows into the measuring device in FIG. 1. Based on the value of the absolute viscosity η calculated by the first calculator 7, the fuel heater (for example,
The controller 14 of the electric heater is controlled. Further, the controller 17 of the water supply pump 16 is controlled based on the value of the water ratio α calculated by the second calculation device 10. In the figure, reference numeral 11 denotes a main fuel pump, 12 denotes a homogenizer, 1
3 is a main heater, 19 is a water tank, 21 is a fuel tank,
Reference numeral 23 denotes a fuel injection valve, and reference numeral 25 denotes a mixed liquid return pipe.
Since the viscosity mixing ratio meter has been described with reference to FIG. 1, detailed description will be omitted. In the above description, the metering pump is used as the flow control device. However, when there is a pressure difference, a flow control valve may be used instead of the metering pump.

【0016】[0016]

【発明の効果】上記のように、本発明によれば、エマル
ジョン化した水と油の混合液の粘度および水の比率を比
較的簡単な一台の装置で精度良く測定できる。
As described above, according to the present invention, the viscosity of the mixture of emulsified water and oil and the ratio of water can be accurately measured with a relatively simple apparatus.

【0017】すなわち、本発明によれば、エマルジョン
化した水と油の混合液の流量Qは、流量制御装置によっ
て決まり、細管の半径Rおよび管長Lも既知であるから
細管の入口と出口の圧力差(P1−P2)が分かれば、
ポアズイユの式からエマルジョンの絶対粘度ηを求める
ことができる。
That is, according to the present invention, the flow rate Q of the mixture of emulsified water and oil is determined by the flow rate control device, and the radius R and length L of the thin tube are also known. If the difference (P1-P2) is known,
From the Poiseuille equation, the absolute viscosity η of the emulsion can be determined.

【0018】η=π/8(P1−P2)/Q/R4 /L 他方、加熱器、つまり、電気ヒーター電力を一定にして
加熱熱量Hを一定にし、水の比熱λw及び燃料の比熱λ
oが既知であるから加熱器の入口と出口の温度差(T2
−T1)が分かれば、次式から水の比率αを求めること
ができる。 α=(H/(T2−T1)/Q−λo)/(λw−λ
o) また、本発明では、粘度測定用細管及び加熱器に混合液
を供給する流量制御装置を共用するので、製造費の高騰
を抑えることができる。
Η = π / 8 (P1−P2) / Q / R 4 / L On the other hand, the heater, that is, the electric heat of the electric heater is kept constant, the heating heat H is kept constant, the specific heat λw of the water and the specific heat λ of the fuel
Since o is known, the temperature difference between the inlet and the outlet of the heater (T2
-T1), the ratio α of water can be determined from the following equation. α = (H / (T2−T1) / Q−λo) / (λw−λ
o) Further, in the present invention, since the flow rate control device for supplying the mixed liquid to the thin tube for viscosity measurement and the heater is shared, it is possible to suppress a rise in manufacturing cost.

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

【図1】本発明に係る粘度混合比計の概略図である。FIG. 1 is a schematic diagram of a viscosity mixing ratio meter according to the present invention.

【図2】図1の粘度混合比計を燃料供給系に組み入れた
状態を示す概略図である。
FIG. 2 is a schematic diagram showing a state in which the viscosity mixing ratio meter of FIG. 1 is incorporated in a fuel supply system.

【符号の説明】[Explanation of symbols]

1 流量制御装置 2 細管 3 加熱器 5,6 圧力
計 7 第1演算装置 8,9 温度
計 10 第2演算装置
DESCRIPTION OF SYMBOLS 1 Flow control device 2 Thin tube 3 Heater 5, 6 Pressure gauge 7 First computing device 8, 9 Thermometer 10 Second computing device

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 エマルジョン化した水と油の混合液の流
量を一定にする流量制御装置と、該流量制御装置によっ
て流量規制された混合液を通す所定の半径と管長とを有
する細管と、該細管の入口及び出口に夫々設置させた圧
力計と、この両圧力計の圧力差から混合液の粘度を演算
する第1演算装置と、前記流量制御装置によって流量規
制された混合液を加熱する加熱器と、該加熱器の入口及
び出口に夫々設置させた温度計と、この両温度計の温度
差から水の比率を演算する第2演算装置と、からなるこ
とを特徴とする粘度混合比計。
1. A flow control device for making a flow rate of a mixture of water and oil emulsified constant, a thin tube having a predetermined radius and a pipe length through which the flow of the mixture is regulated by the flow control device, Pressure gauges respectively installed at the inlet and the outlet of the thin tube, a first arithmetic unit for calculating the viscosity of the mixed liquid from the pressure difference between the two pressure gauges, and heating for heating the mixed liquid whose flow rate is regulated by the flow rate control device A viscometer, a thermometer installed at an inlet and an outlet of the heater, and a second calculating device for calculating a ratio of water from a temperature difference between the thermometers. .
JP8695397A 1997-04-04 1997-04-04 Viscosity mixing ratio meter Withdrawn JPH10282084A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8695397A JPH10282084A (en) 1997-04-04 1997-04-04 Viscosity mixing ratio meter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8695397A JPH10282084A (en) 1997-04-04 1997-04-04 Viscosity mixing ratio meter

Publications (1)

Publication Number Publication Date
JPH10282084A true JPH10282084A (en) 1998-10-23

Family

ID=13901248

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8695397A Withdrawn JPH10282084A (en) 1997-04-04 1997-04-04 Viscosity mixing ratio meter

Country Status (1)

Country Link
JP (1) JPH10282084A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001198513A (en) * 2000-01-17 2001-07-24 Dainippon Screen Mfg Co Ltd Substrate coating device
WO2002093147A1 (en) 2001-05-16 2002-11-21 Vaisala Oyj Method and apparatus for defining water content of a liquid.

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001198513A (en) * 2000-01-17 2001-07-24 Dainippon Screen Mfg Co Ltd Substrate coating device
JP4513999B2 (en) * 2000-01-17 2010-07-28 株式会社Sokudo Substrate coating device
WO2002093147A1 (en) 2001-05-16 2002-11-21 Vaisala Oyj Method and apparatus for defining water content of a liquid.
JP2004525383A (en) * 2001-05-16 2004-08-19 ヴァイサラ オーワイジェー Method and apparatus for determining the moisture content of a liquid
US7036356B2 (en) 2001-05-16 2006-05-02 Vaisala Oyj Method and apparatus for defining water content of a liquid

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