TWI670413B - Fuel oil transfer system - Google Patents

Fuel oil transfer system Download PDF

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Publication number
TWI670413B
TWI670413B TW106127230A TW106127230A TWI670413B TW I670413 B TWI670413 B TW I670413B TW 106127230 A TW106127230 A TW 106127230A TW 106127230 A TW106127230 A TW 106127230A TW I670413 B TWI670413 B TW I670413B
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Taiwan
Prior art keywords
fuel oil
transfer
storage tank
inflow pipe
pump
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TW106127230A
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Chinese (zh)
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TW201835443A (en
Inventor
千千波孝泰
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日商北新產業股份有限公司
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17DPIPE-LINE SYSTEMS; PIPE-LINES
    • F17D1/00Pipe-line systems
    • F17D1/08Pipe-line systems for liquids or viscous products
    • F17D1/14Conveying liquids or viscous products by pumping
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67DDISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D7/00Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes
    • B67D7/06Details or accessories
    • B67D7/80Arrangements of heating or cooling devices for liquids to be transferred
    • B67D7/82Heating only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B63SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
    • B63HMARINE PROPULSION OR STEERING
    • B63H21/00Use of propulsion power plant or units on vessels
    • B63H21/38Apparatus or methods specially adapted for use on marine vessels, for handling power plant or unit liquids, e.g. lubricants, coolants, fuels or the like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67DDISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D7/00Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes
    • B67D7/04Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes for transferring fuels, lubricants or mixed fuels and lubricants
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67DDISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D7/00Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes
    • B67D7/06Details or accessories
    • B67D7/58Arrangements of pumps
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B67OPENING, CLOSING OR CLEANING BOTTLES, JARS OR SIMILAR CONTAINERS; LIQUID HANDLING
    • B67DDISPENSING, DELIVERING OR TRANSFERRING LIQUIDS, NOT OTHERWISE PROVIDED FOR
    • B67D7/00Apparatus or devices for transferring liquids from bulk storage containers or reservoirs into vehicles or into portable containers, e.g. for retail sale purposes
    • B67D7/06Details or accessories
    • B67D7/78Arrangements of storage tanks, reservoirs or pipe-lines
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M31/00Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture
    • F02M31/02Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture for heating
    • F02M31/12Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture for heating electrically
    • F02M31/125Fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M31/00Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture
    • F02M31/02Apparatus for thermally treating combustion-air, fuel, or fuel-air mixture for heating
    • F02M31/16Other apparatus for heating fuel

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • General Engineering & Computer Science (AREA)
  • Ocean & Marine Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Water Supply & Treatment (AREA)
  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Feeding And Controlling Fuel (AREA)

Abstract

[課題] 提供可抑制在被貯留在複數槽桶的燃料油的消耗發生不必要浪費的燃料油移送系統。   [技術內容] 一種燃料油移送系統,是在使用燃料油分離槽桶3的燃料油將移送目的地的燃料油貯藏槽桶(2B)預熱的移送路徑使用第1輔助流入管(10),在移送起源地的燃料油貯藏槽桶(2A)的燃料油是從移送泵(6)被吐出朝向移送目的地的燃料油貯藏槽桶(2B)被移送的移送路徑使用第2輔助流入管(100)及迂迴燃料油路(101),從移送起源地朝移送目的地的燃料油貯藏槽桶移送燃料油時,將流動於第2輔助流入管(100)的燃料油的一部分透過第1輔助流入管(10)朝移送泵(6)側還流。[Problem] To provide a fuel oil transfer system capable of suppressing unnecessary waste of fuel oil stored in a plurality of tanks. [Technical Content] A fuel oil transfer system uses a first auxiliary inflow pipe (10) in a preheating transfer path of a fuel oil storage tank bucket (2B) to which a fuel oil is to be transferred using a fuel oil separation tank bucket 3, The fuel oil in the fuel oil storage tank barrel (2A) of the transfer origin is discharged from the transfer pump (6) toward the transfer destination. The fuel oil storage tank barrel (2B) is transferred using a second auxiliary inflow pipe ( 100) and the bypass fuel oil path (101), when transferring the fuel oil from the transfer origin fuel tank to the transfer destination fuel oil storage tank, a part of the fuel oil flowing through the second auxiliary inflow pipe (100) is passed through the first auxiliary The inflow pipe (10) returns to the transfer pump (6).

Description

燃料油移送系統Fuel oil transfer system

[0001] 本發明,是有關於燃料油移送系統,進一步詳細的話,有關於在燃料油貯藏槽桶之間將燃料油移換用的燃料油移送系統。[0001] The present invention relates to a fuel oil transfer system. More specifically, the present invention relates to a fuel oil transfer system for transferring fuel oil between fuel oil storage tanks.

[0002] 船舶和發電機等的鍋爐所使用的燃料油,是被收容在槽桶等的貯留部,被供給至內燃機關等地被消耗。且,與燃料油不同,也將以內燃機關等的主機為對象的潤滑油與燃料油同樣地被收容在槽桶等的貯留部地使用。   船舶所使用的燃料油和潤滑油的貯留部,是具有對應性狀的種類和不同的貯留量等準備複數槽桶的情況(例如專利文獻1)。   在專利文獻1中揭示了,將藉由由內燃機關被消耗而減少了的潤滑油補充時選擇將性狀不同的潤滑油貯藏的複數槽桶之中的一個的構成。   從性狀不同的潤滑油選擇,是為了藉由供給適合內燃機關內的潤滑油的性狀的潤滑劑,防止成為內燃機關中的運轉狀況惡化的原因的潤滑劑的不足。   [0003] 在專利文獻1所揭示的構成,雖是與燃料油不同,但是將被供給至內燃機關內的物質作為對象從複數槽桶供給的點,概念上是與燃料油共通。   但是在專利文獻1所揭示的構成,是只有以選擇複數槽桶的其中任一為前提,但未考慮將具有與燃料油相同性狀的對象物由槽桶彼此移送。   因此,因為在槽桶內殘餘的少量的燃料油未被消耗的狀態下被放置,所以對於抑制燃料消耗的不必要浪費的節能的實施是成為不利。 [先前技術文獻] [專利文獻]   [0004]   [專利文獻1] 日本特開2015-86866號公報[0002] Fuel oil used in boilers such as ships and generators is stored in storage units such as tanks, and is consumed by being supplied to an internal combustion engine and the like. In addition, unlike fuel oil, lubricating oil targeted at a host engine such as an internal combustion engine engine is used in a storage portion such as a tank, as well as fuel oil.燃料 The storage sections for fuel oil and lubricating oil used in ships are cases where multiple tanks are prepared (for example, Patent Document 1), which have corresponding characteristics and different storage amounts.专利 Patent Document 1 discloses a configuration in which one of a plurality of tanks storing lubricating oils having different properties is selected when replenishing the lubricating oil reduced by being consumed by the internal combustion engine.选择 Lubricants with different characteristics are selected in order to prevent the shortage of lubricants that cause deterioration of the operating conditions in the internal combustion engine by supplying lubricants that are suitable for the internal lubrication of the internal combustion engine. [0003] Although the structure disclosed in Patent Document 1 is different from fuel oil, it is conceptually common to fuel oil in that a point supplied from a plurality of tanks as a target is a substance supplied to an internal combustion engine. However, the configuration disclosed in Patent Document 1 is based on the premise that any one of a plurality of tanks is selected, and transfer of objects having the same properties as the fuel oil from the tanks to each other is not considered. Therefore, since a small amount of fuel oil remaining in the tank is left unconsumed, the implementation of energy saving for suppressing unnecessary waste of fuel consumption becomes disadvantageous. [Prior Art Document] [Patent Document] [0004] [Patent Document 1] Japanese Patent Laid-Open No. 2015-86866

[本發明所欲解決的課題]   [0005] 在此,本發明的課題,是提供可抑制被貯留在複數槽桶的燃料油的消耗發生不必要浪費的燃料油移送系統。尤其是,提供一種在複數槽桶彼此進行燃料油的移送時一邊防止燃料油的黏度上昇和流動阻力的增加一邊可移換燃料油的燃料油移送系統。 [用以解決課題的手段]   [0006] 為了解決此課題,本發明,是一種燃料油移送系統,是將從複數燃料油貯藏槽桶之中的一個藉由移送泵被移送的燃料油藉由燃料油分離槽桶被加熱,對於藉由將加熱終了的燃料油藉由流下泵返回至前述燃料油貯藏槽桶與該燃料油貯藏槽桶內的燃料油混合使前述燃料油貯藏槽桶內的燃料油的溫度可部分地提高,具備:將前述一個燃料油貯藏槽桶作為移送起源地,將這以外作為移送目的地的燃料油貯藏槽桶時,可從前述燃料油分離槽桶朝前述移送目的地的燃料油貯藏槽桶或是從該燃料油分離槽桶朝前述移送泵的燃料油吸引側移送燃料油的第1輔助流入管、及與前述移送泵的燃料油吐出側及第1輔助流入管之間連通的第2輔助流入管、及與該第1輔助流入管分岐可朝前述移送目的地的燃料油貯藏槽桶移送燃料油的迂迴燃料油路,可選擇:將前述移送目的地的燃料油貯藏槽桶的燃料油預熱時使用前述第1輔助流入管將前述燃料油分離槽桶的加熱終了的燃料油與前述移送目的地的燃料油貯藏槽桶的燃料油混合用的移送路徑、及使用前述第2輔助流入管及前述迂迴燃料油路將前述移送起源地的燃料油貯藏槽桶的燃料油朝前述移送目的地的燃料油貯藏槽桶導入的移送路徑,且朝向朝移送目的地的燃料油貯藏槽桶移送燃料油時使用前述第1輔助流入管朝前述移送泵的燃料油導入側將移送起源地的燃料油的一部分還流動。 [發明的效果]   [0007] 依據本發明的話,因為可以將燃料油貯藏槽桶內的燃料油移換,所以不會殘留燃料沒有不必要的消耗。尤其是,移換時,因為可以抑制燃料油的流動阻力,所以圓滑的移換可容易地進行。[Problems to be Solved by the Present Invention] [0005] An object of the present invention is to provide a fuel oil transfer system capable of suppressing unnecessary waste of fuel oil stored in a plurality of tanks. In particular, the present invention provides a fuel oil transfer system capable of exchanging fuel oil while preventing the viscosity of the fuel oil from increasing and increasing the flow resistance when the plurality of tanks are transferring fuel oil to each other. [Means to Solve the Problem] [0006] In order to solve the problem, the present invention is a fuel oil transfer system, which is a fuel oil transferred from one of a plurality of fuel oil storage tanks by a transfer pump through The fuel oil separation tank is heated. The fuel oil in the fuel oil storage tank is mixed with the fuel oil in the fuel oil storage tank by returning the heated fuel oil to the fuel oil storage tank by a pump. The temperature of the fuel oil can be partially increased, and the fuel oil storage tank can be used as a transfer origin and the fuel oil storage tank can be transferred from the fuel oil separation tank to the above The destination fuel oil storage tank or the first auxiliary inflow pipe for transferring fuel oil from the fuel oil separation tank to the fuel oil suction side of the transfer pump, and the fuel oil discharge side and the first auxiliary A second auxiliary inflow pipe communicating between the inflow pipes and a bypass fuel oil path that branches off from the first auxiliary inflow pipe and can transfer fuel oil to the fuel oil storage tank barrel of the transfer destination. Optional: When preheating the fuel oil in the fuel oil storage tank of the transfer destination, use the first auxiliary inflow pipe to separate the heated fuel oil in the fuel oil separation tank and the fuel oil storage tank of the transfer destination. The fuel oil mixing transfer path of the barrel, and the second auxiliary inflow pipe and the bypass fuel oil path are used to introduce the fuel oil of the fuel oil storage tank barrel of the transfer origin to the fuel oil storage tank barrel of the transfer destination. When the fuel oil is transferred toward the fuel oil storage tank barrel of the transfer destination, the first auxiliary inflow pipe is used to flow a part of the fuel oil at the origin to the fuel oil introduction side of the transfer pump. [Effects of the Invention] [0007] According to the present invention, since the fuel oil in the fuel oil storage tank can be replaced, there is no unnecessary consumption of residual fuel. In particular, since the flow resistance of the fuel oil can be suppressed during the replacement, the smooth replacement can be easily performed.

[0009] 以下,說明實施本發明用的形態。   第1圖,是實施本發明用的形態的燃料油移送系統所使用的燃料油移送裝置1的構成。   燃料油移送裝置1,是具備與包含一對的複數燃料油貯藏槽桶2連通的燃料油分離槽桶3、燃料油常用槽桶4。   燃料油分離槽桶3,是將燃料油加熱所使用的槽桶,藉由無圖示的加熱器,使燃料油被加熱至其中一例的70~80℃的溫度。   [0010] 燃料油貯藏槽桶2及燃料油分離槽桶3是藉由移送管5被連通,在其中途處中,被配置有移送泵6、溫度感測器7及壓力感測器8。   溫度感測器7,是例如測量移送泵6的燃料充油口側即吸入側的溫度。   壓力感測器8,是為了監視被吸入移送泵6內的燃料油的壓力變化而設置。壓力變化,是為了判斷對應燃料油的黏度變化的流動阻力的變化所使用。尤其是,黏度變高流動阻力增加的情況時,移送泵6的入口側的壓力是成為真空化傾向。因此,真空化傾向的壓力變化被檢出的話,將燃料油的黏度下降用的加熱是成為必要。   在燃料油分離槽桶3中,設有將藉由移送泵6被吸入的燃料油的液面檢出用的液位感測器9。   液位感測器9,是可以檢出燃料油朝燃料油分離槽桶3內被導入規定量時的液面的感測器。液位感測器9,是檢出燃料油被導入燃料油分離槽桶3內規定量的話,為了停止移送泵6的驅動所使用。   感測器,不限定於上述的位置,也被設置在燃料油貯藏槽桶2的內部(第5圖參照。此感測器LG1、LG2,是將燃料油貯藏槽桶內的燃料殘量藉由液位或是壓力檢出的殘量感測器。   [0011] 燃料油常用槽桶4,是將被加熱的燃料油清淨化之後,為了暫時地貯留,並朝向內燃機關等供給燃料油所使用的槽桶。燃料油貯藏槽桶2及燃料油常用槽桶4是藉由吸入管10被連通,在其中途處中,被配置有流下泵11。被貯留在燃料油常用槽桶4的燃料油的一部分是藉由流下泵11朝燃料油貯藏槽桶2流下將燃料油貯藏槽桶2內的燃料油的溫度提高。   此情況時的流下泵11的名稱的理由,是將燃料油常用槽桶4配置於比燃料油貯藏槽桶2更高的位置的構成作為前提。即是因為將燃料油從上位的燃料油常用槽桶4朝比此下位的燃料油貯藏槽桶2流下的方式吐出的意思,而表現成流下。   [0012] 在第1圖所示的構成中,採用燃料油分離槽桶3及燃料油常用槽桶4各別與吸入管10連通的構成。因此,以可以設定從這些雙方的槽桶3、4或是其中任一的槽桶朝向燃料油貯藏槽桶2的加熱終了的燃料油的流路的方式在各槽桶3、4的燃料油的出口的流路設有閥12。   [0013] 以上的燃料油移送裝置1,是使藉由移送泵6從燃料油貯藏槽桶2朝燃料油分離槽桶3被吸入的燃料油被加熱,被加熱的燃料油被清淨化並被導入燃料油常用槽桶4,被貯留的燃料油是朝內燃機關等被供給。   暫時地被貯留在燃料油分離槽桶3及或是燃料油常用槽桶4的燃料油的一部分,是藉由流下泵11而返回至燃料油貯藏槽桶2。此結果,燃料油貯藏槽桶2內的燃料油是藉由與被加熱的燃料油混合而部分地被加熱至36~40℃。   [0014] 在本實施例中,泵彼此的運轉時間,例如,移送泵6是15分鐘程度且流下泵11是45分鐘程度被選擇地交互地運轉。在此時間之中,移送泵6的運轉時間,是例如,可以對應於藉由前述的燃料油分離槽桶3內的液位感測器9而使燃料油的液面被檢出為止的時間。即,移送泵6的旋轉數,在由依據驅動電流等的額定的流量將燃料油流動時的運轉時間內使燃料油的液面藉由液位感測器9被檢出的話可以判斷為燃料油的流動阻力不會產生的燃料油的黏度,超過此運轉時間的情況時可以判斷為燃料油的黏度較高流動性差。且,液位感測器9,是檢出被導入燃料油分離槽桶3內的燃料油到達規定量的話,將移送泵6的運轉停止防止燃料油溢出。   又,停泊中無任何燃料油消耗時,移送泵6的運轉時間會縮短,液位感測器9作動為止的時間是成為例如6分鐘程度。   [0015] 使用移送泵6從燃料油貯藏槽桶2朝向燃料油分離槽桶3將燃料油吸入的路徑,是在第1圖由符號F1~F5顯示。使用流下泵11從燃料油常用槽桶4朝向燃料油貯藏槽桶2使燃料油流下的路徑,是在第2圖由箭頭F10~F13顯示。   使用這種構成的燃料油移送裝置1,其主要部分的構成已被揭示在本申請人的前案也就是日本特開2012-17123號公報。   [0016] 具備以上的構成的燃料油移送裝置1,是使用抑止燃料油的流動阻力增加的加熱方法。   此情況的加熱,是指藉由將被加熱的燃料油與未被加熱的燃料油混合使未被加熱的燃料油的溫度提高的意思。   以下,說明使用燃料油移送裝置所實行的加熱方法。   [0017] 燃料油移送裝置1,是可選擇:燃料油的黏度較低且流動阻力少的情況時被實行的通常運轉模式、及上述黏度較高且流動阻力增加的情況時被實行的加熱運轉模式的其中任一。通常運轉模式,是對應液位感測器9的作動狀態運轉的移送泵6及朝燃料油貯藏槽桶2內進行燃料油的供給的流下泵11被交互地運轉使燃料油被循環的模式。加熱運轉模式,是除了將移送泵6強制地停止以外,將在移送泵6的吸入側被攔截的燃料油加熱,並且也藉由返回至燃料油貯藏槽桶2的燃料油而將燃料油貯藏槽桶2內的燃料油加熱的模式。加熱運轉模式,是使在移送泵6側被攔截的燃料油的黏度到達不會增加流動阻力的值為止實行較佳。   實行加熱運轉模式用的條件,可使用以下舉例的參數作為資料。   即,參數,是至少使用朝移送泵6被吸入的燃料油的溫度、壓力及移送泵6的運轉時間。有關移送泵6的運轉時間,是如前述,參照:液位感測器9作動為止的運轉時間、和在移送泵6本身所具備的正時器的計時時間。這些各參數的全部或是其中任一個或是複數,是與加熱所必要的規定條件一致的話,加熱運轉模式就被實行。   [0018] 以下,對於實行此運轉模式用的構成及作用使用第3圖說明。   移送泵6及流下泵11,是將其運轉狀態,藉由第3圖所示的控制部20而被控制。   [0019] 控制部20,是使被設置在移送管5的溫度感測器7、壓力感測器8、液位感測器9,與輸入側連接。移送泵6的驅動部及流下泵11的驅動部是分別被連接在控制部20的輸出側。移送泵6及流下泵11,皆是使用藉由使馬達(在第1、2圖中,由符號M1、M2顯示的構件)被旋轉控制而可以將流量和流速控制的型式。   [0020] 在第3圖中符號15,是例如,將各泵6、11的運轉時間和燃料油的流量等顯示用及為了將燃料消耗量進一步返回量等的必要條件輸入所使用的操作盤,符號16是正時器。   正時器16,是例如,測量從移送泵6運轉開始的時點至藉由液位感測器9進行液面檢出為止的所需時間。因此,移送泵6一邊運轉一邊由液位感測器9所產生的液面檢出為止的運轉時間過長時可以判斷為黏度較高流動阻力較大。換言之,移送泵6的運轉時間是過度地變長時流動於移送泵6的燃料油的黏度較高,可以判斷為在流動阻力大的狀態下。移送泵6,是也有自己具備測量運轉時間的正時器的情況。在此情況下,移送泵6是在本身的正時器預先被設定的運轉時間以上運轉時可以判斷為在燃料油的黏度較高且流動阻力較高的狀態下。   移送泵6,是具備:超過預先被設定的運轉時間時,強制地被停止的如後說明的加熱運轉模式。   [0021] 且判斷燃料油的黏度是流動阻力增加的黏度的規定條件所使用的監視對象項目,可以將移送泵6的驅動源所使用的馬達的驅動電流值作為對象。   驅動電流值,雖是為了獲得預先被設定的馬達的旋轉數、扭矩而被決定,但是旋轉數和扭矩變化的情況時使復歸至原來的狀態地變化,特別是旋轉數和扭矩下降的情況時驅動電流值上昇。在此,可以藉由監視驅動電流值上昇的情況判斷燃料油的黏度上昇,進行運轉模式的切換。   [0022] 藉由控制部20被選擇的通常運轉模式,是一邊保溫在燃料油的黏度不會增加流動阻力的值的情況一邊使燃料油循環。依據此運轉模式的話,抑制被貯藏在燃料油貯藏槽桶2內的燃料油的溫度降低防止黏度變高的狀態被維持。   通常運轉模式時的控制部20,是監視:被導入移送泵6的燃料油的溫度、壓力及移送泵6的運轉時間,進一步被外加在移送泵6的驅動源也就是馬達的驅動電流值的變化。   這些的監視對象項目,是作為判斷例如以下舉例的4種類的案例發生的情況時燃料油的黏度變化,特別是黏度上昇的規定條件使用。   (1)燃料油的黏度上昇且到達流動阻力增加的溫度以下的情況。   (2)移送泵6的燃料油導入側的壓力變化是真空化傾向發生狀態的情況。   (3)液位感測器9作動為止的移送泵6的運轉時間是長大化的情況。   (4)對於移送泵6的驅動源的驅動電流值是上昇的情況。   未滿足這些的規定條件且燃料油的黏度上昇未發生的情況時,實行通常運轉模式。   在通常運轉模式實行時,交互地反覆從燃料油貯藏槽桶2朝燃料油分離槽桶3將燃料油吸入的循環及將燃料油分離槽桶3及或是燃料油常用槽桶4內的一部分的燃料油朝向燃料油貯藏槽桶2流下的循環。但是,即使是循環中途處,也可對應液位感測器9的作動使移送泵6被停止。此運轉模式實行時的各泵6、11的運轉狀態是顯示於操作盤15。   [0023] 上述監視對象項目的監視被繼續,通常運轉模式被實行時,該監視對象項目的規定條件的全部、其中任一個或是複數是一致的情況時,從通常運轉模式切換至加熱運轉模式。   [0024] 在加熱運轉模式中,移送泵6強制地被停止,將流下泵11運轉使被加熱的燃料油朝燃料油貯藏槽桶2流動。此時,被加熱的燃料油,是一邊與在移送泵6的燃料油吸入側被攔截的燃料油混合一邊朝向燃料油貯藏槽桶2流動。燃料油,是例如,對於過濾器(在第2圖由符號FT顯示的構件)逆流地流動的話,可發揮將過濾器的堵塞消解的功能。   [0025] 在控制部20中,監視對象項目之中的溫度、壓力雖可直接藉由感測器監視,但是有關於使用液位感測器9將液面檢出為止的移送泵6的運轉時間,是依據第4圖所示的狀態判別是否實行加熱運轉模式。   在第4圖中,縱軸是顯示燃料油的量(液位感測器9作動的量),橫軸是顯示時間。   在同圖中,隨著燃料油的黏度變高,將移送泵6一定輸出的情況時液位感測器9作動為止的時間變長。   因此,以黏度較低的燃料油朝燃料油分離槽桶3內被導入至液位感測器9作動為止的時間(第4圖中,由符號T顯示的時間)為基準,比該時間更長大化的情況(在第4圖中,由符號T1顯示的時間)可以判斷為燃料油的黏度較高。又,在移送泵6本身具備正時器的情況中,將正時器的設定時間及實際的運轉時間比較,實際的運轉時間是長大化的情況可以判斷為燃料油的黏度較高。   [0026] 監視對象項目的規定條件的全部、或是一部分或是複數是一致的情況時加熱運轉模式被選擇的話,被加熱的燃料油是朝向燃料油貯藏槽桶2被送出。由此,不是只有與燃料油貯藏槽桶2內的燃料油直接混合,在移送泵6的吸入側被攔截的燃料油也被混合,可以將燃料油的溫度上昇。其結果,因為燃料油是在燃料油被吸入移送泵6前夕的油路被加熱,所以可以確保流入移送泵6的燃料油的黏度下降。   [0027] 監視對象項目也就是溫度、壓力、移送泵的運轉時間進一步移送泵的馬達中的驅動電流值的變化是到達將黏度上昇消解的條件,與規定條件不一致的情況時,是復歸至通常運轉模式。   [0028] 使用以上的加熱方法的燃料油移送裝置1的特徵,是在來自複數槽桶的燃料油的移換時,一邊抑制燃料油的黏度上昇和流動阻力的增加一邊可以移送。以下,說明獲得此特徵用的構成。   [0029] 第5圖,是對於為了將如第1圖所示的構成作為對象設定燃料油的移送路徑所使用的開閉閥附加符號,並且附加一部分的構成的圖。   在第5圖所示的構成及在第1圖所示的構成的不同是如下。   即,具備以從相當於一個燃料油貯藏槽桶的移送起源地的燃料油貯藏槽桶2A將移送目的地的燃料油貯藏槽桶2B的雙方直接連通的關係將燃料油移換的構成的點。具體而言,將從如第1圖所示的燃料油分離槽桶3與移送泵6的燃料油吸入側連通的吸入管10作為第1輔助流入管使用且使用吸入管10的一部分被分岐的第2輔助流入管100的點。   [0030] 第1輔助流入管10,是雖構成從燃料油分離槽桶3被吐出的加熱終了的燃料油朝移送泵6的燃料油吸入側混合的路徑,但是與和後述的第2輔助流入管連續的迂迴燃料油路101連通。第1輔助流入管10,是為了將移送目的地的燃料油貯藏槽桶2B內的燃料油加熱,可將燃料油分離槽桶3的加熱終了的燃料油朝向移送目的地的燃料油貯藏槽桶2B移送的路徑。   [0031] 第2輔助流入管100,是連通移送泵6的燃料油吐出側及第1輔助流入管10之間,進一步,設有與第1輔助流入管10分岐且與移送目的地的燃料油貯藏槽桶2B的燃料油導入側連接的迂迴燃料油路101。第2輔助流入管100,是將從移送泵6被吐出的燃料油朝向迂迴燃料油路101作為移送的流路使用。   迂迴燃料油路101,是使流動於第2輔助流入管100的燃料油朝向移送目的地的燃料油貯藏槽桶2B被移送用的油路。因此,第2輔助流入管100及迂迴燃料油路101,是將從移送起源地的燃料油貯藏槽桶2A藉由移送泵6被汲起的燃料油,直接朝移送目的地的燃料油貯藏槽桶2B的燃料油導入側混合的情況時使用。   在第1輔助流入管10中,設有將流下泵11代用的第1流下泵11,在第2輔助流入管100中,設有與其連通的迂迴燃料油路101第2流下泵110。   在與第1輔助流入管10及第2輔助流入管100連通的迂迴燃料油路101中,在第1、第2流下泵11、110的燃料油吐出側設有可將燃料油加熱的加熱器111、111H。   [0032] 在作為移送管5、第1輔助流入管使用的吸入管10、第2輔助流入管100及迂迴燃料油路101中,被配置有設定燃料油的移送路徑用的開閉閥V1~V8。   這些開閉閥V1~V8,是藉由移送泵6及第1、第2流下泵11、110的驅動用馬達M1、M2、M3的驅動控制所使用的控制部20而被控制開閉狀態。   [0033] 控制部20,是在將使用中的燃料油貯藏槽桶2A的燃料油移換至成為其他的新的移送目的地的燃料油貯藏槽桶2B時設定燃料油的移送路徑。此情況的移換,是使用中的燃料油貯藏槽桶2A的殘量少的情況,或是在使用中的燃料油貯藏槽桶2A意料外的事態產生而有必要的移換的情況等作為對象被實行。   控制部20,是進行對應藉由現階段使用中且相當於移送起源地的燃料油貯藏槽桶2A的殘量感測器LG1被檢出的燃料殘量將燃料油移換至移送目的地的燃料油貯藏槽桶2B的處理。藉由意料外的事態等將燃料油移換的情況時,其指令是從操作盤15側被發出的話,與對應殘量實行的情況同樣實行移換作業。   [0034] 進行移換時的燃料油的移送狀態,是在第6圖被顯示。   將燃料油在移換時,為了消解到達移送目的地的燃料油貯藏槽桶2B的燃料油的溫度較低,如第6圖(A)所示,從燃料油分離槽桶3使加熱終了的燃料油朝移送目的地的燃料油貯藏槽桶2B的燃料油導入側被移送。這種燃料油的移送路徑,是可以使用作為將燃料油朝移送目的地的燃料油貯藏槽桶2B的預熱油路。此結果,可獲得朝移送目的地的燃料油貯藏槽桶2B被移送的燃料油的黏度上昇被抑制且移送阻力少的狀態。因此,此處理,是在移送之前,作為將燃料油圓滑地移送用的準備使用。   從燃料油分離槽桶3朝向移送目的地的燃料油貯藏槽桶2B移送加熱終了的燃料油時控制部20,是為了設定移送路徑而將開閉閥V7開放。被設置在燃料油分離槽桶3的開閉閥12也同樣地被開放使燃料油被移送。   [0035] 接著,移送目的地的燃料油貯藏槽桶2B內的燃料油的溫度是藉由預熱或是已經到達不會導致黏度上昇的溫度時,從移送起源地的燃料油貯藏槽桶2A朝向移送目的地的燃料油貯藏槽桶2B使燃料油被移送。   為了燃料油的移送,使用第6圖(B)所示的移送路徑。即,以可以從移送起源地的燃料油貯藏槽桶2A朝向移送目的地的燃料油貯藏槽桶2B移送燃料油的方式,使用第2輔助流入管100及迂迴燃料油路101。   被設置在迂迴燃料油路101的加熱器111H,是為了防止流動於此的燃料油的溫度成為導致黏度上昇的溫度而被加熱控制。因此,因為可以防止受到流動於迂迴燃料油路101的燃料油放熱和周邊溫度的影響而成為導致黏度上昇的溫度,所以可以將燃料油的移送阻力不會增大地移送。   [0036] 在本實施例中,藉由使用第1輔助流入管10與第2輔助流入管100連通的構成,如第6圖(B)的細線的箭頭所示,可以將流動於迂迴燃料油路101的燃料油的一部分朝第1輔助流入管10分流。   流動於第1輔助流入管10的燃料油的量,是比對於藉由移送泵6被移送的燃料油的全量朝向迂迴燃料油路101流動的燃料油的量更少,例如30%程度的量。因此,來自移送起源地的燃料油貯藏槽桶2A的燃料油,是70%的量朝移送目的地的燃料油貯藏槽桶2B被移送,比此量更少30%的量是朝移送泵6的燃料油吸引(導入)側被移送。此結果,成為被導入移送泵6的燃料油的黏度上昇的原因的溫度下降被矯正,移送泵6的負荷增大被抑制。被設置在第1輔助流入管10的加熱器111,是與被設置在迂迴燃料油路101的加熱器111H同樣地,為了防止流動的燃料油的溫度是成為導致黏度上昇的溫度地被加熱控制。   [0037] 控制部20,是為了設定第6圖(B)所示的移送路徑,而沿著燃料油的流動將開閉閥V1、V3、V8、V7、及V6、V5開放。   在各開閉閥之中,被設置在第1輔助流入管10的開閉閥V5、V6,是對於被設置在第2輔助流入管100、迂迴燃料油路101的開閉閥V7、V8將打開量減少,將油路節流。尤其是,因為藉由將開閉閥V7的開放量比開閉閥V8的全開更減少,迂迴燃料油路101比第2輔助流入管100更節流,所以可以朝向第1輔助流入管100移送燃料油。開閉閥V7的開放量,是設定成可獲得前述的第1輔助流入管100中的燃料油的量的量較佳。   控制部20,是將流動於第2輔助流入管100的燃料油的一部分朝第1輔助流入管10分流時,使用與前述的加熱運轉模式不同的條件。即,加熱運轉模式,是以移送泵6強制地被停止的場合作為前提進行,但是第6圖(B)所示的狀態,是以移送泵6運轉被繼續為前提。因此,移送泵6的燃料油吸引(導入)側的燃料油的溫度是被維持不導致黏度上昇的溫度是成為重要。在此,在本實施例中,調整燃料油朝移送泵6的燃料油吸引(導入)側的混合率防止燃料油的溫度下降。   [0038] 依據以上的實施例的燃料油移送系統的話,朝被導入移送泵6的燃料油的溫度及移送目的地的燃料油貯藏槽桶被移送的燃料油的溫度,可以維持在黏度上昇不會發生的溫度。   尤其是,從移送起源地朝移送目的地的燃料油貯藏槽桶的燃料油的移送,是可以將燃料油貯藏槽桶彼此連通地進行。由此,與從燃料油分離槽桶3供給至移送目的地的燃料油貯藏槽桶2B的情況不同,在燃料油分離槽桶3可以抑制燃料油的減少。且,因為可在連通的槽桶間的移送路將預熱終了的燃料油或是加熱終了的燃料油混合來防止燃料油的溫度下降,所以可一邊防止黏度上昇一邊圓滑地移送燃料油。 [產業上的可利用性]   [0039] 本發明,因為是可以將燃料油貯藏槽桶內的燃料油移換至新的燃料油貯藏槽桶,所以不會讓殘留少的燃料油貯藏槽桶內的燃料油放置,可以加以使用。由此,在燃料的消耗沒有不必要浪費的點,可利用性高。   尤其是,因為將被移換的燃料藉由槽桶彼此的連通而移換,所以可以抑制燃料油從燃料油分離槽桶的吐出量,且,可以抑制被移送的燃料油的溫度下降地移換的點,可利用性高。[0009] Hereinafter, embodiments for carrying out the present invention will be described. Fig. 1 shows a configuration of a fuel oil transfer device 1 used in a fuel oil transfer system according to an embodiment of the present invention. (2) The fuel oil transfer device 1 includes a fuel oil separation tank 3 and a fuel oil common tank 4 that communicate with a plurality of fuel oil storage tanks 2 including a pair. The fuel oil separation tank 3 is a tank used to heat the fuel oil, and the fuel oil is heated to a temperature of 70 to 80 ° C. by a heater (not shown). [0010] The fuel oil storage tank bucket 2 and the fuel oil separation tank bucket 3 are communicated via a transfer pipe 5. In the middle, a transfer pump 6, a temperature sensor 7, and a pressure sensor 8 are arranged. The radon temperature sensor 7 measures, for example, the temperature on the fuel fill port side, that is, the suction side of the transfer pump 6. The pressure sensor 8 is provided to monitor the pressure change of the fuel oil sucked into the transfer pump 6. The pressure change is used to determine a change in flow resistance corresponding to a change in the viscosity of the fuel oil. In particular, when the viscosity increases and the flow resistance increases, the pressure on the inlet side of the transfer pump 6 tends to become vacuum. Therefore, if a pressure change in the vacuum tendency is detected, heating for reducing the viscosity of the fuel oil becomes necessary.燃料 The fuel oil separation tank barrel 3 is provided with a liquid level sensor 9 for detecting the liquid level of the fuel oil sucked by the transfer pump 6. The liquid level sensor 9 is a sensor capable of detecting a liquid level when a predetermined amount of fuel oil is introduced into the fuel oil separation tank 3. The liquid level sensor 9 is used to stop the driving of the transfer pump 6 when a predetermined amount of fuel oil is introduced into the fuel oil separation tank 3. The sensor is not limited to the above-mentioned position, and is also installed inside the fuel oil storage tank barrel 2 (refer to FIG. 5. The sensors LG1 and LG2 borrow the remaining fuel amount in the fuel oil storage tank barrel. Residual volume sensor detected by liquid level or pressure. [0011] The fuel oil common tank 4 is used for temporarily storing the fuel oil after it has been purified, and then supplies it to the internal combustion engine. The fuel oil storage tank 2 and the fuel oil common tank 4 are connected through a suction pipe 10, and a flow-down pump 11 is arranged in the middle. The fuel stored in the fuel oil common tank 4 A part of the oil is caused to flow down the fuel oil storage tank barrel 2 by the down-flow pump 11 to raise the temperature of the fuel oil in the fuel oil storage tank barrel 2. The reason for the name of the down-flow pump 11 in this case is to use a common fuel oil tank The premise is that the barrel 4 is disposed at a higher position than the fuel oil storage tank barrel 2. That is, the fuel oil is discharged from the upper fuel oil commonly used tank 4 toward the lower fuel oil storage tank 2 Meaning, and manifested as shed. [0012] In the configuration shown in FIG. 1, a configuration is adopted in which the fuel oil separation tank 3 and the fuel oil common tank 4 communicate with the suction pipe 10. Therefore, the tank 3, 4 or any one of the tanks faces the fuel oil storage tank 2. The fuel oil flow path of the heated fuel tank is provided with a valve 12 at the fuel tank outlet flow path of each tank 3, 4. 4 [0013] The above fuel oil transfer device 1 heats the fuel oil sucked from the fuel oil storage tank bucket 2 toward the fuel oil separation tank bucket 3 by the transfer pump 6, and the heated fuel oil is purified and introduced into the fuel oil. The conventional fuel tank 4 is supplied with the fuel oil stored in the internal combustion engine, etc. A part of the fuel oil temporarily stored in the fuel oil separation tank 3 or the fuel oil common tank 4 is passed through the pump 11 Then, it returns to the fuel oil storage tank barrel 2. As a result, the fuel oil in the fuel oil storage tank barrel 2 is partially heated to 36 to 40 ° C. by mixing with the heated fuel oil. [0014] In this implementation In the example, the operating time of the pumps is, for example, the transfer pump 6 is The 15-minute pump and the down-flow pump 11 are selected to operate alternately at 45-minute intervals. During this time, the operation time of the transfer pump 6 may correspond to, for example, the liquid in the tank 3 by the aforementioned fuel oil separation tank. The time until the liquid level of the fuel oil is detected by the position sensor 9. That is, the number of rotations of the transfer pump 6 allows the fuel oil to operate during the operating time when the fuel oil flows at a rated flow rate based on a driving current or the like. If the liquid level is detected by the liquid level sensor 9, it can be judged that the viscosity of the fuel oil will not be caused by the flow resistance of the fuel oil. When the operating time is exceeded, it can be judged that the viscosity of the fuel oil is high and the fluidity is poor. In addition, the liquid level sensor 9 detects that the fuel oil introduced into the fuel oil separation tank 3 reaches a predetermined amount, and stops the operation of the transfer pump 6 to prevent the fuel oil from overflowing. Also, there is no fuel oil in the park. When consumed, the operating time of the transfer pump 6 is shortened, and the time until the liquid level sensor 9 operates is, for example, approximately 6 minutes. [0015] The path for drawing fuel oil from the fuel oil storage tank barrel 2 toward the fuel oil separation tank barrel 3 using the transfer pump 6 is shown by symbols F1 to F5 in FIG. 1. The flow path of the fuel oil from the fuel oil tank 4 to the fuel oil storage tank 2 using the down pump 11 is shown by arrows F10 to F13 in FIG. 2. (2) The fuel oil transfer device 1 using such a configuration has been disclosed in the previous application of the present applicant, which is Japanese Patent Application Laid-Open No. 2012-17123. [0016] The fuel oil transfer device 1 having the above configuration is a heating method that uses an increase in the flow resistance of the fuel oil to suppress the increase.加热 Heating in this case means that the temperature of the unheated fuel oil is increased by mixing the heated fuel oil with the unheated fuel oil. Below, the heating method using the fuel oil transfer device will be described. [0017] The fuel oil transfer device 1 can be selected from a normal operation mode to be executed when the viscosity of the fuel oil is low and the flow resistance is small, and a heating operation to be executed when the viscosity is high and the flow resistance is increased. Any of the patterns. The normal operation mode is a mode in which the transfer pump 6 and the down-flow pump 11 for supplying fuel oil into the fuel oil storage tank 2 are operated alternately in response to the operating state of the liquid level sensor 9 to circulate the fuel oil. In the heating operation mode, in addition to forcibly stopping the transfer pump 6, the fuel oil intercepted on the suction side of the transfer pump 6 is heated, and the fuel oil is also stored by the fuel oil returned to the fuel oil storage tank 2. Heating mode of the fuel oil in the tank 2. The heating operation mode is preferably performed until the viscosity of the fuel oil intercepted on the side of the transfer pump 6 reaches a value that does not increase the flow resistance.的 For the conditions used to execute the heating operation mode, the following example parameters can be used as data. That is, the parameters are at least the temperature and pressure of the fuel oil sucked toward the transfer pump 6 and the operating time of the transfer pump 6. Regarding the operation time of the transfer pump 6, as described above, reference is made to the operation time until the liquid level sensor 9 operates, and the timing time of the timer provided in the transfer pump 6 itself. If all or any of these parameters are in accordance with the predetermined conditions necessary for heating, the heating operation mode is executed. [0018] Hereinafter, the configuration and function for implementing this operation mode will be described using FIG. 3. (2) The transfer pump 6 and the down-flow pump 11 are controlled in the operating state by the control unit 20 shown in FIG. 3. [0019] The control unit 20 connects the temperature sensor 7, the pressure sensor 8, and the liquid level sensor 9 provided on the transfer pipe 5 to the input side. The drive unit of the transfer pump 6 and the drive unit of the down pump 11 are connected to the output side of the control unit 20, respectively. The transfer pump 6 and the down-flow pump 11 both use a type in which the flow rate and the flow rate can be controlled by rotating the motor (the components shown by the symbols M1 and M2 in Figs. 1 and 2). [0020] In FIG. 3, reference numeral 15 is an operation panel used for displaying, for example, the operating time of each of the pumps 6, 11 and the flow rate of the fuel oil, etc., and inputting necessary conditions for further returning the fuel consumption amount and the like. The symbol 16 is a timer. The timer 16 measures, for example, the time required from the point when the operation of the transfer pump 6 is started to the time when the liquid level is detected by the liquid level sensor 9. Therefore, when the transfer pump 6 is running, the operating time until the liquid level detection by the liquid level sensor 9 is detected is too long, it can be judged that the viscosity is high and the flow resistance is large. In other words, when the operation time of the transfer pump 6 is excessively long, the viscosity of the fuel oil flowing in the transfer pump 6 is high, and it can be determined that the flow resistance is large. The transfer pump 6 may have its own timing for measuring the operation time. In this case, when the transfer pump 6 is operated for more than the operation time set in advance of its own timer, it can be determined that the fuel oil has a high viscosity and a high flow resistance. The transfer pump 6 is provided with a heating operation mode described later that is forcibly stopped when the preset operation time is exceeded. [0021] In addition, the monitoring target item used to determine the viscosity of the fuel oil is a predetermined condition for increasing the viscosity of the flow resistance, and the drive current value of the motor used for the drive source of the transfer pump 6 may be targeted. Although the drive current value is determined in order to obtain the preset number of rotations and torque of the motor, when the number of rotations and torque changes, the original state is changed, especially when the number of rotations and torque decreases. The drive current value increases. Here, the increase in the viscosity of the fuel oil can be determined by monitoring the increase in the driving current value, and the operation mode can be switched. [0022] The normal operation mode selected by the control unit 20 circulates the fuel oil while maintaining the viscosity of the fuel oil without increasing the value of the flow resistance. According to this operation mode, a state in which the temperature of the fuel oil stored in the fuel oil storage tank 2 is suppressed from decreasing and the viscosity is prevented from being increased is maintained. The control unit 20 in the normal operation mode monitors: the temperature and pressure of the fuel oil introduced into the transfer pump 6 and the operating time of the transfer pump 6 are further added to the drive source of the transfer pump 6, that is, the drive current value of the motor Variety. These monitoring items are used as a predetermined condition for determining the viscosity change of the fuel oil, especially the viscosity increase, when the following four types of cases occur. (1) The case where the viscosity of the fuel oil increases and reaches a temperature below the temperature at which the flow resistance increases. (2) The pressure change on the fuel oil introduction side of the transfer pump 6 may be a state in which a tendency to vacuum occurs. (3) The operation time of the transfer pump 6 until the liquid level sensor 9 is operated is increased. (4) In the case where the drive current value of the drive source of the transfer pump 6 is increased.通常 If these conditions are not met and the increase in the viscosity of the fuel oil does not occur, the normal operation mode is implemented. During the execution of the normal operation mode, the cycle of sucking fuel oil from the fuel oil storage tank 2 to the fuel oil separation tank 3 and the fuel oil separation tank 3 and a part of the fuel oil common tank 4 are alternately repeated. Circulation of the fuel oil flowing down towards the fuel oil storage tank barrel 2. However, even in the middle of the cycle, the transfer pump 6 may be stopped in response to the operation of the liquid level sensor 9. The operation states of the pumps 6 and 11 when this operation mode is executed are displayed on the operation panel 15. [0023] When the monitoring of the monitoring target item is continued, and when the normal operation mode is performed, when all or any of the predetermined conditions of the monitoring target item match, the normal operation mode is switched to the heating operation mode. . [0024] In the heating operation mode, the transfer pump 6 is forcibly stopped, and the down-flow pump 11 is operated to cause the heated fuel oil to flow toward the fuel oil storage tank 2. At this time, the heated fuel oil flows toward the fuel oil storage tank 2 while being mixed with the fuel oil intercepted on the fuel oil suction side of the transfer pump 6. The fuel oil is, for example, a filter (a member shown by the symbol FT in FIG. 2) flows countercurrently and functions to resolve the filter clogging. [0025] In the control unit 20, although the temperature and pressure in the monitoring target items can be directly monitored by a sensor, the operation of the transfer pump 6 until the liquid level is detected using the liquid level sensor 9 is related. The time is based on the state shown in Fig. 4 to determine whether or not to execute the heating operation mode.第 In Fig. 4, the vertical axis indicates the amount of fuel oil (the amount of operation of the liquid level sensor 9), and the horizontal axis indicates the time. In the same figure, as the viscosity of the fuel oil becomes higher, the time required for the liquid level sensor 9 to operate becomes longer when the transfer pump 6 has a constant output. Therefore, based on the time (the time shown by the symbol T in FIG. 4) until the fuel oil having a relatively low viscosity is introduced into the fuel oil separation tank 3 and the liquid level sensor 9 is actuated, the time is longer than this time. When it grows up (the time shown by the symbol T1 in FIG. 4), it can be determined that the viscosity of the fuel oil is high. In addition, in the case where the transfer pump 6 itself is provided with a timer, it can be determined that the viscosity of the fuel oil is high when the set time of the timer is compared with the actual operation time, and the actual operation time is increased. [0026] When all, a part, or a plurality of predetermined conditions of the monitoring target items are consistent, if the heating operation mode is selected, the heated fuel oil is sent toward the fuel oil storage tank 2. Accordingly, not only the fuel oil is directly mixed with the fuel oil in the fuel oil storage tank 2, but also the fuel oil intercepted on the suction side of the transfer pump 6 is also mixed, and the temperature of the fuel oil can be increased. As a result, since the fuel oil is heated in the oil passage immediately before the fuel oil is sucked into the transfer pump 6, it is possible to ensure that the viscosity of the fuel oil flowing into the transfer pump 6 decreases. [0027] The monitoring target items, that is, the temperature, pressure, and operating time of the transfer pump, are further changed when the drive current value of the transfer pump motor reaches a condition for dissolving the viscosity rise, and when the conditions do not agree with the predetermined conditions, it returns to normal. Operation mode. [0028] A feature of the fuel oil transfer device 1 using the above heating method is that the fuel oil can be transferred while suppressing an increase in the viscosity of the fuel oil and an increase in flow resistance when the fuel oil is transferred from a plurality of tanks. The configuration for obtaining this feature will be described below. [0029] FIG. 5 is a diagram in which a part of the configuration is added to the on-off valve used to set the fuel oil transfer path using the configuration shown in FIG. 1 as a target. The difference between the structure shown in FIG. 5 and the structure shown in FIG. 1 is as follows. That is, a point is provided in which the fuel oil is transferred from a fuel oil storage tank bucket 2A corresponding to the origin of the transfer of one fuel oil storage tank, and the fuel oil storage tank bucket 2B of the transfer destination is directly connected. . Specifically, the suction pipe 10 communicating from the fuel oil separation tank barrel 3 shown in FIG. 1 to the fuel oil suction side of the transfer pump 6 is used as a first auxiliary inflow pipe and a part of the suction pipe 10 is divided. Point of the second auxiliary inflow pipe 100. [0030] Although the first auxiliary inflow pipe 10 constitutes a path for mixing the heated fuel oil discharged from the fuel oil separation tank 3 toward the fuel oil suction side of the transfer pump 6, it is combined with a second auxiliary inflow described later The pipe is continuously connected to the fuel oil path 101. The first auxiliary inflow pipe 10 is for heating the fuel oil in the fuel oil storage tank barrel 2B of the transfer destination, and can heat the heated fuel oil in the fuel oil separation tank 3 toward the fuel oil storage tank barrel of the transfer destination. 2B transfer path. [0031] The second auxiliary inflow pipe 100 communicates between the fuel oil discharge side of the transfer pump 6 and the first auxiliary inflow pipe 10, and is further provided with fuel oil that is divergent from the first auxiliary inflow pipe 10 and from the transfer destination. The bypass fuel oil passage 101 connected to the fuel oil introduction side of the storage tank barrel 2B. The second auxiliary inflow pipe 100 is used as a flow path for transferring the fuel oil discharged from the transfer pump 6 toward the bypass fuel oil path 101. The bypass fuel oil passage 101 is an oil passage for transferring the fuel oil flowing through the second auxiliary inflow pipe 100 toward the fuel oil storage tank barrel 2B to be transferred. Therefore, the second auxiliary inflow pipe 100 and the bypass fuel oil path 101 are the fuel oil drawn up from the fuel oil storage tank barrel 2A of the transfer origin by the transfer pump 6 directly to the fuel oil storage tank of the transfer destination. It is used when the fuel oil introduction side of the barrel 2B is mixed. The first auxiliary inflow pipe 10 is provided with a first down pump 11 which replaces the down pump 11, and the second auxiliary inflow pipe 100 is provided with a bypass fuel oil path 101 and a second down pump 110 which communicate with the first down pump 110. In the bypass fuel oil passage 101 communicating with the first auxiliary inflow pipe 10 and the second auxiliary inflow pipe 100, a heater capable of heating the fuel oil is provided on the fuel oil discharge side of the first and second down pumps 11, 110. 111, 111H. [0032] In the suction pipe 10 used as the transfer pipe 5, the first auxiliary inflow pipe, the second auxiliary inflow pipe 100, and the bypass fuel oil passage 101, on-off valves V1 to V8 for setting a fuel oil transfer path are arranged. . The on-off valves V1 to V8 are controlled to be opened and closed by a control unit 20 used for driving control of the drive motors M1, M2, and M3 of the transfer pump 6 and the first and second down pumps 11 and 110. [0033] The control unit 20 sets the fuel oil transfer path when the fuel oil in the fuel oil storage tank bucket 2A in use is switched to the fuel oil storage tank bucket 2B which is another new transfer destination. The replacement in this case is a case where the remaining amount of the fuel oil storage tank bucket 2A in use is small, or a situation where an unexpected situation occurs during the use of the fuel oil storage tank bucket 2A and the necessary replacement is required. Subject is implemented. The control unit 20 responds to the fuel remaining amount detected by the remaining amount sensor LG1 of the fuel oil storage tank barrel 2A which is currently in use and corresponds to the origin of the transfer. Treatment of oil storage tank barrel 2B. When the fuel oil is changed due to an unexpected situation or the like, if the command is issued from the operation panel 15 side, the changeover operation is performed in the same manner as in the case where the corresponding residual amount is executed. [0034] The transfer state of the fuel oil during the replacement is shown in FIG. 6. When the fuel oil is exchanged, in order to dissolve the temperature of the fuel oil reaching the fuel oil storage tank barrel 2B at the transfer destination, as shown in FIG. 6 (A), the fuel oil is separated from the tank barrel 3 to complete the heating. The fuel oil is transferred toward the fuel oil introduction side of the fuel oil storage tank barrel 2B of the transfer destination. This fuel oil transfer path is a preheating oil path that can be used as a fuel oil storage tank barrel 2B for transferring fuel oil to a transfer destination. As a result, it is possible to obtain a state in which the viscosity increase of the fuel oil to be transferred toward the fuel oil storage tank 2B to be transferred is suppressed, and the transfer resistance is small. Therefore, this process is used as preparation for smooth transfer of fuel oil before transfer. When the heated fuel oil is transferred from the fuel oil separation tank 3 to the transfer destination fuel oil storage tank 2B, the control unit 20 opens the on-off valve V7 to set the transfer path. Similarly, the on-off valve 12 provided in the fuel oil separation tank barrel 3 is opened to transfer fuel oil. [0035] Next, when the temperature of the fuel oil in the fuel oil storage tank barrel 2B of the transfer destination is preheated or has reached a temperature that does not cause viscosity rise, the fuel oil storage tank barrel 2A from the place of origin is transferred. The fuel oil storage tank 2B toward the transfer destination causes the fuel oil to be transferred. For the transfer of fuel oil, use the transfer path shown in Figure 6 (B). That is, the second auxiliary inflow pipe 100 and the bypass fuel oil path 101 are used so that the fuel oil can be transferred from the fuel oil storage tank bucket 2A of the transfer origin to the fuel oil storage tank bucket 2B of the transfer destination. The heater 111H provided in the bypass fuel oil path 101 is heated and controlled in order to prevent the temperature of the fuel oil flowing therefrom from becoming a temperature that causes viscosity to rise. Therefore, it is possible to prevent the temperature of the fuel oil from increasing due to the heat of the fuel oil flowing through the detoured fuel oil path 101 and the surrounding temperature, so that the fuel oil can be transferred without increasing its resistance. [0036] In this embodiment, by using a configuration in which the first auxiliary inflow pipe 10 and the second auxiliary inflow pipe 100 are communicated with each other, as shown by a thin arrow in FIG. A part of the fuel oil in the path 101 is branched toward the first auxiliary inflow pipe 10. The amount of the fuel oil flowing through the first auxiliary inflow pipe 10 is smaller than the amount of the fuel oil flowing toward the bypass fuel oil path 101 with respect to the entire amount of the fuel oil transferred by the transfer pump 6, for example, an amount of about 30% . Therefore, 70% of the fuel oil from the fuel oil storage tank barrel 2A of the transfer origin is transferred toward the fuel oil storage tank barrel 2B of the transfer destination, and 30% less than this amount is directed toward the transfer pump 6 The fuel oil suction (introduction) side is transferred. As a result, the temperature drop that causes the viscosity of the fuel oil introduced into the transfer pump 6 to rise is corrected, and an increase in the load on the transfer pump 6 is suppressed. The heater 111 provided in the first auxiliary inflow pipe 10 is heated and controlled in order to prevent the temperature of the flowing fuel oil from becoming a temperature that causes the viscosity to rise, similarly to the heater 111H provided in the bypass fuel oil path 101. . [0037] The control unit 20 opens the on-off valves V1, V3, V8, V7, and V6, V5 in order to set the transfer path shown in FIG. 6 (B) along the flow of the fuel oil. Among the on-off valves, the on-off valves V5 and V6 provided in the first auxiliary inflow pipe 10 reduce the opening amount of the on-off valves V7 and V8 provided in the second auxiliary inflow pipe 100 and the bypass fuel oil path 101. Throttle the oil circuit. In particular, since the opening amount of the on-off valve V7 is reduced more than the full opening of the on-off valve V8, the bypass fuel oil path 101 is more throttled than the second auxiliary inflow pipe 100, so the fuel oil can be transferred toward the first auxiliary inflow pipe 100. . The opening amount of the on-off valve V7 is preferably set to an amount that can obtain the amount of fuel oil in the first auxiliary inflow pipe 100 described above. The knuckle control unit 20 uses a condition different from the aforementioned heating operation mode when a part of the fuel oil flowing through the second auxiliary inflow pipe 100 is branched toward the first auxiliary inflow pipe 10. That is, the heating operation mode is performed on the premise that the transfer pump 6 is forcibly stopped, but the state shown in FIG. 6 (B) is based on the premise that the operation of the transfer pump 6 is continued. Therefore, it is important that the temperature of the fuel oil on the fuel oil suction (introduction) side of the transfer pump 6 is maintained at a temperature that does not cause an increase in viscosity. Here, in this embodiment, the mixing ratio of the fuel oil toward the fuel oil suction (introduction) side of the transfer pump 6 is adjusted to prevent the temperature of the fuel oil from decreasing. [0038] According to the fuel oil transfer system of the above embodiment, the temperature of the fuel oil introduced into the transfer pump 6 and the temperature of the fuel oil transferred to the fuel oil storage tank barrel at the transfer destination can be maintained at a viscosity that does not increase. What will happen to the temperature. In particular, the transfer of fuel oil from the fuel oil storage tank barrel to the transfer destination can be performed by connecting the fuel oil storage tank barrel to each other. Accordingly, unlike the case where the fuel oil storage tank bucket 2B is supplied from the fuel oil separation tank bucket 3 to the transfer destination, the fuel oil separation tank bucket 3 can suppress a decrease in fuel oil. In addition, since the pre-heated fuel oil or the heated fuel oil can be mixed in the transfer path between the connected tanks to prevent the temperature of the fuel oil from falling, the fuel oil can be smoothly transferred while preventing the viscosity from rising. [Industrial Applicability] [0039] The present invention allows the fuel oil in the fuel oil storage tank to be replaced with a new fuel oil storage tank, so it does not allow the fuel oil storage tank with a small amount of residue. The fuel oil is placed inside and can be used. Thereby, there is no unnecessary waste of fuel consumption, and the availability is high. In particular, since the fuel to be replaced is exchanged through the communication between the tanks, the amount of fuel oil discharged from the fuel oil separation tank can be suppressed, and the temperature of the transferred fuel oil can be suppressed from decreasing. The point of change is high.

[0040][0040]

1‧‧‧燃料油移送系統所使用的燃料油移送裝置Fuel oil transfer device used in 1‧‧‧ fuel oil transfer system

2‧‧‧燃料油貯藏槽桶2‧‧‧ fuel oil storage tank barrel

2A‧‧‧移送起源地的燃料油貯藏槽桶2A‧‧‧ barrels of fuel oil storage tanks of origin

2B‧‧‧移送目的地的燃料油貯藏槽桶2B‧‧‧ Fuel tanks for transfer destination

3‧‧‧燃料油分離槽桶3‧‧‧ fuel oil separation tank

4‧‧‧燃料油常用槽桶4‧‧‧Fuel oil tanks

5‧‧‧移送管5‧‧‧ transfer tube

6‧‧‧移送泵6‧‧‧ transfer pump

7‧‧‧溫度感測器7‧‧‧ temperature sensor

8‧‧‧壓力感測器8‧‧‧ Pressure Sensor

10‧‧‧第1輔助流入管所使用的吸入管10‧‧‧ Suction tube for the first auxiliary inflow tube

11‧‧‧相當於第1流下泵的流下泵11‧‧‧ equivalent to the first downflow pump

20‧‧‧控制部20‧‧‧Control Department

100‧‧‧第2輔助流入管100‧‧‧ 2nd auxiliary inflow pipe

101‧‧‧迂迴燃料油路101‧‧‧ detour fuel oil road

110‧‧‧第2流下泵110‧‧‧Second flow pump

111、111H‧‧‧加熱器111, 111H‧‧‧ heater

LG1、LG2‧‧‧殘量感測器LG1, LG2‧‧‧Residual sensor

V1~V8‧‧‧開閉閥V1 ~ V8‧‧‧Open and close valve

[0008]   [第1圖] 顯示本發明的實施例的燃料油移送系統所使用的燃料油移送裝置的構成及燃料油加熱時的燃料油的流動的示意圖。   [第2圖] 顯示由如第1圖所示的燃料油移送裝置實行的燃料移送時的燃料油的流動的示意圖。   [第3圖] 說明如第1圖所示的燃料油移送裝置所使用的控制部的構成用的方塊圖。   [第4圖] 說明在如第3圖所示的控制部所實施的規定條件判別所使用的原理用的線圖。   [第5圖] 說明以如第1圖所示的構成為前提的燃料油移送系統的構成用的示意圖。   [第6圖] 說明以如第5圖所示的構成作為對象的燃料油的移送狀態用的示意圖。[0008] [FIG. 1] A schematic diagram showing a configuration of a fuel oil transfer device used in a fuel oil transfer system according to an embodiment of the present invention and a flow of fuel oil when the fuel oil is heated. [Fig. 2] A schematic diagram showing the flow of fuel oil during fuel transfer by the fuel oil transfer device shown in Fig. 1. [Figure 3] A block diagram for explaining the configuration of a control unit used in the fuel oil transfer device shown in Figure 1.第 [Fig. 4] A line diagram for explaining the principle used for determining a predetermined condition implemented by the control unit shown in Fig. 3. [FIG. 5] A schematic diagram for explaining the configuration of a fuel oil transfer system based on the configuration shown in FIG. [Fig. 6] A schematic diagram for explaining the transfer state of the fuel oil having the configuration shown in Fig. 5 as a target.

Claims (3)

一種燃料油移送系統,是將從複數燃料油貯藏槽桶之中的一個藉由移送泵被移送的燃料油藉由燃料油分離槽桶被加熱,對於藉由將加熱終了的燃料油藉由流下泵返回至前述燃料油貯藏槽桶與該燃料油貯藏槽桶內的燃料油混合使前述燃料油貯藏槽桶內的燃料油的溫度可部分地提高,具備:將前述一個燃料油貯藏槽桶作為移送起源地,將這以外作為移送目的地的燃料油貯藏槽桶時,可從前述燃料油分離槽桶朝前述移送目的地的燃料油貯藏槽桶或是從該燃料油分離槽桶朝前述移送泵的燃料油吸引側移送燃料油的第1輔助流入管、及與前述移送泵的燃料油吐出側及第1輔助流入管之間連通的第2輔助流入管、及與該第1輔助流入管分岐可朝前述移送目的地的燃料油貯藏槽桶移送燃料油的迂迴燃料油路,可選擇:將前述移送目的地的燃料油貯藏槽桶的燃料油預熱時使用前述第1輔助流入管將前述燃料油分離槽桶的加熱終了的燃料油與前述移送目的地的燃料油貯藏槽桶的燃料油混合用的移送路徑、及使用前述第2輔助流入管及前述迂迴燃料油路將前述移送起源地的燃料油貯藏槽桶的燃料油朝前述移送目的地的燃料油貯藏槽桶導入的移送路徑,且朝向朝移送目的地的燃料油貯藏槽桶移送燃料油時使用前述第1輔助流入管朝前述移送泵的燃料油導入側將移送起源地的燃料油的一部分還流。A fuel oil transfer system is one in which fuel oil transferred from a plurality of fuel oil storage tanks by a transfer pump is heated by a fuel oil separation tank, and the fuel oil that has been heated by flowing down The pump returns to the fuel oil storage tank and the fuel oil in the fuel oil storage tank mixes the fuel oil in the fuel oil storage tank to partially increase the temperature. The fuel oil storage tank is provided with: From the origin of the transfer, when the fuel oil storage tanks other than the transfer destination are moved from the fuel oil separation tank to the fuel oil storage tank or the fuel oil separation tank, The first auxiliary inflow pipe for transferring fuel oil on the fuel oil suction side of the pump, and the second auxiliary inflow pipe communicating with the fuel oil discharge side and the first auxiliary inflow pipe of the transfer pump, and the first auxiliary inflow pipe. The divergent fuel oil circuit that can transfer fuel oil to the fuel oil storage tank barrel of the transfer destination can be selected: when the fuel oil of the fuel oil storage tank barrel of the transfer destination is preheated Using the first auxiliary inflow pipe to transfer the heated fuel oil in the fuel oil separation tank and the fuel oil in the fuel oil storage tank in the transfer destination, and using the second auxiliary inflow pipe and the When the fuel oil path is detoured and the fuel oil from the fuel oil storage tank barrel at the origin is transferred to the fuel oil storage tank barrel at the transfer destination, and the fuel oil is transferred toward the fuel oil storage tank barrel at the transfer destination Using the first auxiliary inflow pipe, a part of the fuel oil to be transferred is returned to the fuel oil introduction side of the transfer pump. 如申請專利範圍第1項的燃料油移送系統,其中,在前述第1輔助流入管設有第1流下泵,在前述第2輔助流入管設有第2流下泵,在前述第1、第2流下泵的燃料油吐出側分別設有加熱器。For example, the fuel oil transfer system in the first scope of the patent application, wherein the first auxiliary inflow pipe is provided with a first down pump, the second auxiliary inflow pipe is provided with a second down pump, and the first, second, and second pumps are provided. Heaters are provided on the fuel oil discharge side of the down pump. 如申請專利範圍第1或2項的燃料油移送系統,其中,從前述移送起源地的燃料油貯藏槽桶朝移送目的地的燃料油移送槽桶移送燃料油時,對於流動於前述第2輔助流入管及迂迴燃料油路的燃料油的量可將流動於第1輔助流入管的燃料油的量減少地設定。For example, if the fuel oil transfer system according to item 1 or 2 of the scope of patent application is for transferring fuel oil from the fuel oil storage tank barrel of the transfer origin to the fuel oil transfer tank barrel of the transfer destination, the fuel oil flowing in the second auxiliary The amount of fuel oil flowing into the inflow pipe and the bypass fuel oil passage can be set to reduce the amount of fuel oil flowing through the first auxiliary inflow pipe.
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