WO2019017259A1 - Fuel production apparatus using animal and vegetable oils and used lubricants as raw materials, fuel supply system, and fuel production and supply method using same - Google Patents

Fuel production apparatus using animal and vegetable oils and used lubricants as raw materials, fuel supply system, and fuel production and supply method using same Download PDF

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Publication number
WO2019017259A1
WO2019017259A1 PCT/JP2018/026221 JP2018026221W WO2019017259A1 WO 2019017259 A1 WO2019017259 A1 WO 2019017259A1 JP 2018026221 W JP2018026221 W JP 2018026221W WO 2019017259 A1 WO2019017259 A1 WO 2019017259A1
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Prior art keywords
raw material
fuel
animal
tank
oil
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PCT/JP2018/026221
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French (fr)
Japanese (ja)
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前田和幸
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前田和幸
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Publication of WO2019017259A1 publication Critical patent/WO2019017259A1/en

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • 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
    • F02M37/00Apparatus or systems for feeding liquid fuel from storage containers to carburettors or fuel-injection apparatus; Arrangements for purifying liquid fuel specially adapted for, or arranged on, internal-combustion engines
    • F02M37/22Arrangements for purifying liquid fuel specially adapted for, or arranged on, internal-combustion engines, e.g. arrangements in the feeding system
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Definitions

  • the present invention relates to a fuel production apparatus and fuel supply system using animal and vegetable oil and used lubricating oil as a raw material, and fuel production and supply method using the same, in detail: (1) Oil collected from animals and plants and used animal and plant activity Fuel production apparatus and fuel supply system using edible oil etc. as a raw material, fuel production / supply method using the same, and (2) Fuel production apparatus made from petroleum based and biological lubricating oils such as used lubricating oil and the like The present invention relates to a fuel supply system and a fuel production / supply method using the same.
  • the fuel production apparatus includes a filter for animal and vegetable oil and used lubricating oil, a heated raw material storage tank kept warm and an overflow function to the raw material storage tank, and a heated raw material supply tank, a filtration device, heating Equipment, centrifuge, sedimentation system, controller and pump installed between the equipment, flow meter, flow control valve, solenoid valve, drain valve, level sensor and pressure sensor,
  • the fuel production method used is a method to make the animal and vegetable oil and the used lubricating oil usable as a fuel for a boiler or engine using only physical methods such as filtration, heating, centrifugation, sedimentation and pressurization. That's right.
  • Utilization of renewable energy such as animal and vegetable fuels is required as a technology to cope with global warming.
  • development of recycled energy technology that utilizes used lubricating oil and the like as thermal energy is required.
  • oil collected from animals and plants and used lubricating oils have characteristics such as high viscosity and inclusion of impurities, and when used as fuel for boilers and diesel engines as they are, precipitates cause fuel injection There is a concern that the fuel pump and the injection nozzle that constitute the device may be defective. Therefore, in recent years, chemical treatment such as "methyl esterification” has been carried out to remove glycerin from raw materials animal and vegetable oils, thereby converting animal and vegetable oils into properties similar to light oils such as fatty acid methyl esters. Fuel (biodiesel fuel) is used.
  • the viscosity of animal and vegetable oils and used lubricating oils is about 10 times higher than that of light oil and heavy oil, which are usually used as fuel for boilers and diesel engines (the dynamic viscosity of light oil and heavy oil at 40 ° C is Since the kinematic viscosity of animal or vegetable oil or used lubricating oil at the same temperature is 40 cSt or more at 4 to 5 cSt), the energy to reduce the viscosity to the same level as light oil or A heavy oil by heating it I need.
  • the present invention can be used as a fuel by heating animal and vegetable oils and used lubricating oils to a relatively high temperature (eg 60 ° C.) below the boiling point of water and continuously performing repeated filtration, centrifugation and sedimentation. While reforming it to properties and enabling continuous supply to boilers and diesel engines, By pressurizing it to a relatively high pressure (for example, 0.5 MPa), it is possible to make the fuel injection device of the boiler or engine work well even in a relatively high viscosity state (20 to 30 cSt). To aim.
  • a relatively high temperature eg 60 ° C.
  • a relatively high pressure for example, 0.5 MPa
  • the invention according to claim 1 uses only physical methods such as filtration, heating, centrifugation, sedimentation and pressurization, using as raw materials animal and vegetable oils that are renewable energy and used lubricating oils that are recycled energy.
  • An insulated raw material storage tank provided with a filter and an overflow mechanism adjacent to it and provided with an overflow mechanism to the raw material storage tank, and an insulated raw material supply tank, a filter, a heater, a centrifuge, a precipitation system, a controller and the like It consists of a pump, flow meter, flow control valve, solenoid valve, drain valve, level sensor and pressure sensor installed between the equipment,
  • the animal or vegetable oil or the used lubricating oil stored in the raw material storage tank via the filter flows out from the outlet provided at the lower level of the raw material storage tank, and is used as a raw material filter, raw material circulation pump, raw material heater, centrifugal After being led to the lower position in the raw material
  • Consecutive heating, centrifugal separation, precipitation by forming a raw material circulation path that joins the flow path leading to the pump, passes through the raw material circulation pump, the raw material heater, the centrifuge, and the raw material flow meter and returns to the raw material supply tank again.
  • the raw material supply tank is always kept at full level (full) by partially overflowing from the raw material supply tank and flowing into the raw material storage tank, the raw material heated by the raw material heater Is continuously supplied to the raw material storage tank and the raw material supply tank, so that each heated tank does not need a heating device.
  • the remainder flows out of the outlet installed at the upper level of the feed tank, and is supplied to the boiler engine through the fuel consumption flow meter, the fuel supply pump, the fuel heater, and the fuel filter.
  • a fuel circulation passage is provided which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler or engine or immediately before that, and a fuel circulation passage joining with the passage from the consumed fuel flow meter to the fuel supply pump is provided
  • the circulation valve it has the structure and function that it does not need auxiliary fuel for starting the boiler engine.
  • the invention according to claim 2 flows out from the outlet installed at the lower level of the raw material storage tank, passes through the raw material filtration device, the raw material circulation pump, the raw material heater, the centrifuge, and the raw material flow meter to the raw material supply tank.
  • Leading animal and vegetable oil or used lubricating oil It flows out from the outlet installed at the lower level of the feed tank, is led to the suction side of the feed circulation pump through the feedthrough flow meter and circulating feed flow control valve, and the flow path from the feed filtration device to the feed circulation pump
  • the animal or vegetable oil or the used lubricating oil combined with the oil is led to the lower position in the tank by the introduction pipe installed in the fuel supply tank and flows out.
  • Substances and water with a density higher than oil move downward from the outlet, mostly at the lower level of the feed tank. It flows out from the installed outlet, passes through the circulating feed flow meter and circulating feed flow control valve, joins with the flow path from the feed filtration device to the feed circulation pump, and a part of it stays in the bottom of the tank, The remainder move upward in the feed tank, and most of them flow out from the outlet located at the upper level of the feed tank, and the fuel consumption flow meter, fuel feed pump, fuel heater and fuel filter As it passes through the boiler engine, part of it overflows from the raw material supply tank and continues to the raw material storage tank, and it flows out from the outlet provided at the upper level of the raw material supply tank.
  • the animal or vegetable oil or the used lubricating oil leading to the boiler engine is reformed into properties usable for the boiler engine by repeated effective precipitation in the feed tank.
  • Substances and water with a density greater than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils or used lubricating oils, are accumulated at the bottom of the feed tank, By opening the drain valve installed at the bottom of the raw material supply tank, substances or materials with a density greater than oil, such as metals, minerals, and minute contaminants contained in the animal and vegetable oil accumulated in the tank bottom or used lubricating oil Water has the function of being removed from fuel production equipment and fuel supply systems that are made from animal and vegetable oils and used lubricating oils.
  • the invention according to claim 3 is characterized in that the flow rate of the animal or vegetable oil or the used lubricating oil which flows out from the outlet provided at the lower level of the raw material storage tank, passes through the raw material filtering device and reaches the raw material circulation pump. From the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet installed at the upper level of the raw material supply tank and passes through the consumed fuel flow meter, fuel supply pump, fuel heater, and fuel filter to the boiler engine As well as (for example, 1.5 times) It flows out from the outlet installed at the lower level of the raw material supply tank and is led to the suction side of the raw material circulation pump through the circulating raw material flow meter and circulating raw material flow control valve, and the flow path from the raw material filtration device to the raw material circulation pump The flow rate of the combined animal and vegetable oil or used lubricating oil, Equal to the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet located at the upper level of the feed tank through the consumed fuel flow meter,
  • the temperature can be maintained at a relatively high temperature (for example, 50 ° C. or higher) without directly heating the raw material storage tank and the raw material supply tank, thereby promoting the precipitation action in both tanks.
  • the invention according to claim 4 is characterized in that the flow rate of the animal or vegetable oil or the used lubricating oil which flows out from the outlet provided at the lower level of the raw material storage tank, passes through the raw material filtering device and reaches the raw material circulation pump It is less than the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet installed at the upper level and reaches the boiler / engine, and the overflow from the raw material supply tank to the raw material storage tank ceases and oil in the raw material supply tank If the face drops, This is detected by the level sensor installed in the raw material supply tank and an alarm is issued,
  • the solenoid valve installed in the middle of the flow path that flows out from the outlet installed at the medium level of the raw material supply tank and joins the flow path from the consumed fuel flow meter to the fuel supply pump was opened from the closed state While switching to the state, By switching from an open state to a closed state a solenoid valve installed in the flow path that flows out of the outlet installed at the upper level of the raw material supply tank and
  • the invention according to claim 5 is characterized in that the fuel supply pump is provided with a bypass flow path, a bypass fuel flow control valve is installed in the middle thereof, and the fuel flow rate bypassing the fuel supply pump is adjusted and supplied to the boiler engine.
  • a relatively high pressure for example, 0.5 MPa
  • a relatively high-pressure fuel is supplied to the fuel injection device of the boiler engine, and the fuel injection device is good without lowering the viscosity of the fuel oil to the same extent as A heavy oil or light oil (without raising the fuel oil temperature) It has a function that can perform the operation.
  • the invention according to claim 6 is directed to a fuel circulation flow which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler engine or just before that, and joins the flow path from the fuel consumption flow meter to the fuel supply pump.
  • the present invention heats an animal and vegetable oil and a used lubricating oil to a relatively high temperature (eg, 60 ° C.) lower than the boiling point of water and continuously repeatedly filters, centrifuges and precipitates them so that they can be used as fuel It reforms and continuously supplies it to a boiler or diesel engine, while pressurizing it to a relatively high pressure (for example, 0.5 MPa), the viscosity of the fuel supplied to the boiler or engine is as high as A heavy oil or light oil
  • a relatively high pressure for example, 0.5 MPa
  • FIG. 1 is a conceptual view of a fuel production apparatus and a fuel supply system which use animal and vegetable oils and a used lubricating oil as raw materials according to this embodiment.
  • Fuel production equipment and fuel supply system A which uses animal oil and vegetable oil and used lubricating oil as raw materials, as shown in FIG. 1, use only physical methods such as (1) filtration, heating, centrifugation, sedimentation and pressurization. , Animal and vegetable oils and used lubricating oils can be reformed to properties and conditions that can be used as fuels for boilers and engines, (2) heating, centrifugation, and sedimentation repeated continuously, animal and vegetable oils and used lubricants Since the process of heating to the boiling point of water (100 ° C.
  • the fuel supply pump is provided with a bypass flow path, a bypass fuel flow control valve is provided along the way, and the pressure of the fuel supplied to the boiler engine is compared
  • a relatively high pressure for example, 0.5 MPa
  • the energy for heating the fuel can be suppressed to a low level in order to reduce the viscosity of the fuel supplied to the boiler engine to the same value as light oil or A heavy oil.
  • the fuel production apparatus and fuel supply system A which uses animal and vegetable oil and used lubricating oil as raw materials, have a raw material storage tank TK1 provided with a filter FL1 and a level sensor LS1 and a level sensor LS2 adjacent thereto.
  • the raw material storage tank TK1 is provided with a level sensor LS1.
  • the level sensor LS1 exceeds the standard oil level position (level) and the standard oil surface position during operation If the level falls below the level, an alarm will be issued and action will be taken.
  • the level sensor LS2 is installed in the raw material supply tank TK2, and the oil level position (level) at which the overflow from the raw material supply tank to the raw material storage tank ceases and the oil level position (level) is higher than the raw material supply tank.
  • An alarm is issued when the installation position of the solenoid valve and the installation position of the middle feed valve of the raw material supply tank are reached, and measures (actions) for each are urged.
  • the oil is heated by the fuel heater HT2 to increase fluidity (viscosity decreases), and the fuel filter FL3 removes contaminants contained in the animal or vegetable oil or the used lubricating oil, and It has a structure and a function that the pressure of the fuel supplied to the boiler engine can be set to a relatively high pressure (for example, 0.5 MPa) by the supply pump PM2 and the bypass fuel flow control valve CV2 installed in the flow path bypassing it.
  • a relatively high pressure for example, 0.5 MPa
  • a drain valve DV1 is installed at the lowest part, Substances and water with a density greater than oil, such as metals, minerals, etc., contained in animal and vegetable oil or used lubricating oil accumulated in the tank bottom by opening the drain valve DV1 use animal and vegetable oil and used lubricating oil as raw materials It is discharged out of the fuel production system and the fuel supply system A.
  • the animal and vegetable oil and the used lubricating oil which flowed out from the outlet provided at the lower level of the raw material supply tank TK2 pass through the circulating raw material flow meter FM2 and the circulating raw material flow rate adjustment valve CV1 (raw material circulating passage CL1-2)
  • the circulation path which joins the flow path from the raw material filter FL2 to the raw material circulation pump PM1 passes through the raw material circulation pump PM1, the raw material heater HT1, the centrifugal separator CSP and the raw material flow meter FM1 and returns again to the raw material supply tank TK2.
  • the lower level of the raw material storage tank means that the density is higher than that of oils such as metals and minerals contained in animal and vegetable oils and used lubricating oil, which move to the bottom of the raw material storage tank due to sedimentation in the raw material storage tank. It means a position having a distance from the bottom to such an extent that large substances and moisture are not inhaled.
  • the lower levels of the feed supply tank move to the bottom of the feed supply tank due to sedimentation in the feed supply tank and stay there, metals, minerals and minute contaminants contained in animal and vegetable oils and used lubricating oil It means a position with a distance from the bottom to such an extent that it does not inhale substances and moisture whose density is greater than oil content such as things.
  • the flow rate of the raw material flowing through 1 can be set to any value.
  • the raw material filter FL2 and the fuel filter FL3 are constituted by two filters each housed in two filter holders installed in parallel in the flow path of the raw material and the fuel, and the inlet side and the outlet of each filter A valve is provided on the side, and all the valves are normally open, but by closing the valves provided on the inlet and outlet sides of either filter, fuels derived from animal and vegetable oil and used lubricating oil are used.
  • the filter can be replaced even while the manufacturing device and the fuel supply system are in operation.
  • pressure sensor PS1 or PS2 and solenoid valve at the outlet side of either one of the two filter holders installed in each filtration device in the raw material filtration device or in the inlet side of the fuel filtration device.
  • the solenoid valve is closed under normal operating conditions.
  • a filter capable of capturing 25 to 100 ⁇ m (the collection accuracy depends on the combination with the filter FL1 installed in the raw material storage tank TK) contained in animal and vegetable oils or used lubricating oil in the raw material filtration device If the (element) is stored and the pressure at the filter outlet detected by the pressure sensor PS1 falls below the set value (if the filter is clogged),
  • the fuel filter contains a filter (element) capable of capturing contaminants of about 10 ⁇ m contained in animal or vegetable oil or used lubricating oil, and the pressure at the filter inlet detected by the pressure sensor PS2 Is higher than the set value (if the filter is clogged),
  • the raw material heater HT1 heats the animal or vegetable oil used as a raw material or the used lubricating oil to increase fluidity (the viscosity decreases), so that it is more than oil components such as metals and minerals which could not be removed in the raw material storage tank TK1.
  • the high density material and the minute impurities having a density difference with the oil contained in the animal and vegetable oil and the used lubricating oil are effectively removed by the centrifuge CSP, and the raw material storage tank TK1 and the raw material supply tank TK2 It is possible to effectively carry out the precipitation action in
  • the centrifugal separator CSP is a substance or water having a density greater than that of oils such as metals and minerals which can not be removed by precipitation in the raw material storage tank TK1 and the raw material supply tank TK2, and oil contained in animal and vegetable oils and used lubricating oils. It has a function to remove contaminants (such as sludge contained in used lubricating oil) having a higher density than that. For this reason, it becomes an essential component when using a used lubricating oil as a raw material, but when using an animal and vegetable oil as a raw material, sufficient filtration and precipitation are performed using a filtration device and a precipitation system, (1) As shown in FIG. 1, by providing a flow path for bypassing the centrifuge and installing the centrifuge bypass valve CSV, the operation is performed without using the centrifuge. (2) Remove the centrifuge itself from the components. The choice can be made.
  • FIG. 2 is a conceptual view showing an effective precipitation method in the raw material supply tank.
  • the raw material supply flow path CL1-1 joins the raw material circulation flow path CL1-2 on the suction side of the raw material circulation pump and becomes a raw material circulation flow path CL1.
  • Raw material heater HT1 The tube inserted into the raw material supply tank TK2 is lowered through the centrifuge CSP, and flows out into the tank at a position close to the bottom of the tank.
  • V-UP the velocity of upward flow in the tank
  • V-DN the velocity of animal and vegetable oils and used lubricating oil
  • D-FO the viscosity
  • the viscosity
  • DIA the diameter of metals and minerals and minute impurities contained in animal and vegetable oils and used lubricating oils, and be D
  • D the density
  • Settling velocity (terminal velocity) V-ST [m / s] in fluid of impurities such as metals, minerals, moisture, and microparticles, which have higher density than oil, contained in oil is the following equation (Stokes' equation) Indicated by.
  • the inner diameter of the raw material supply tank is D-TK2 [m]
  • the flow rate of animal and vegetable oil and used lubricating oil flowing into the tank through the pipe inserted in this tank is Q-TK2 [m 3 / s]
  • the flow rate of animal and vegetable oil and used lubricating oil rising upwards Q-UP [m 3 / s] flowed out from the outlet located at the lower level of the tank, and led to the material circulation channel CL1-2
  • the flow rate of oil and used lubricating oil is Q-DN [m 3 / s]
  • the animal and vegetable oil and used lubricating oil that flowed to the lower level of the raw material supply tank TK2 will have a flow velocity V- UP [m / s] is expressed by the following equation.
  • FIG. 3 is a control block diagram showing an apparatus and method for always making the raw material supply tank TK2 full level (full state).
  • the level sensor LS2 installed in the raw material supply tank TK2 shown in FIG. 1 detects this and issues an alarm.
  • FIG. 3 shows a control block diagram showing an apparatus and method for setting the temperature of fuel supplied to a boiler / fuel lower than usual
  • FIG. 3 shows a control block diagram showing an apparatus and method for setting the temperature of fuel supplied to a boiler / fuel lower than usual
  • FIG. 4 shows a conceptual diagram showing the operation of a fuel injection pump.
  • the fuel injection pump provided on the diesel engine is fuel-filled around its periphery, and slides longitudinally in a barrel (pump housing) provided with fuel suction holes on its side. It is comprised by the plunger.
  • the plunger moves below the fuel suction port, fuel is sucked, but the suction rate (the amount of suction per unit time) is proportional to the diameter of the fuel suction port and the viscosity of the fuel, but the diameter of the fuel suction port is It is decided by the specification of the fuel injection pump.
  • the fuel supply pump PM2 is provided with a bypass flow path, and the fuel supply pump bypass fuel flow control valve CV2 is provided in the middle thereof, so that the pressure of fuel supplied to the boiler engine B & E is relatively high (for example 0.5). (MPa) can be set.
  • MPa can be set. This increases the pressure of the fuel filling the periphery of the pump housing (by supplying a relatively high pressure of fuel to the fuel injection system of the boiler engine) and causes the fuel to move when the plunger moves below the fuel inlet.
  • the fuel injection device can be operated well without lowering the viscosity of the fuel oil to the same level as heavy oil or light oil (without raising the temperature of the fuel oil) by pressing the fuel pump into the pump housing of the fuel pump. It becomes.
  • the pressure sensor PS3 detects the pressure of fuel supplied to the boiler engine B & E, and adjusts the opening degree of the bypass fuel flow control valve CV2 installed in the bypass flow path of the fuel supply pump,
  • the pressure of the fuel supplied to can be set to a relatively high pressure (e.g. 0.5 MPa).
  • a relatively high pressure e.g. 0.5 MPa
  • the fuel circulation valve FCV is closed so that the fuel does not flow into the fuel circulation channel CL2, but flows out from the outlet provided at the upper level of the raw material supply tank TK2 and consumed fuel All animal and vegetable oils or used lubricating oils supplied to the boiler engine B & E (through the fuel supply flow path FSL) through the flow meter FM3, fuel supply pump PM2, fuel heater TH2 and fuel filter FL3 are all boiler engines It is consumed.
  • the temperature of the fuel supply channel FSL is lowered due to the shutdown of the apparatus or for some reason, the temperature of the fuel stagnated in the channel (flows in the channel) is lowered, and the viscosity of the fuel is If it becomes unsuitable for the B & E fuel injection system, by opening the fuel circulation valve FCV installed in the fuel circulation channel CL2, The fuel staying in the fuel supply flow path FSL (flowing in the flow path) is led to the suction side of the fuel supply pump PM2 from immediately before the fuel injection device outlet of the boiler engine B & E or the fuel injection device of the boiler engine A fuel circulation channel CL2 is formed which merges with the flow channel from the fuel flow meter FM3 to the fuel supply pump PM2.
  • the fuel drawn into the fuel injection pump PM2 is pressurized by the fuel injection pump and then heated by the fuel heater HT2 and passes through the fuel filter FL3 to the fuel injection device of the boiler engine (or just before the fuel injection device) As a result, the fuel is again drawn into the fuel supply pump PM2 through the fuel circulation channel CL2. Even when the boiler engine is stopped, the temperature (viscosity) of the fuel is raised to the temperature (viscosity) suitable for the fuel injection device of the boiler engine, and the auxiliary fuel and auxiliary device are activated when the boiler engine starts. It has structures and functions that you do not need.

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  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
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Abstract

[Problem] To provide: a fuel production apparatus that uses used lubricants and animal and plant oils as raw materials, said apparatus being capable of giving used lubricants and animal and plant oils the properties and a state enabling said oils and lubricants to be continuously supplied to a boiler or engine, while requiring a minimum input of energy; a fuel supply system; and a fuel production and supply method that use the same. [Solution] Provided is an apparatus for continuously producing and supplying fuel having properties and being in a state that allows the fuel to be used in a boiler or engine by repeating physical methods involving filtering, heating, centrifuging, precipitating, and pressurizing used lubricants and animal and plant oils containing used plant oils. The apparatus consists of a raw material storage tank provided with a filter, and a raw material supply tank adjacent to the raw material storage tank, a filtration device, a heater, a centrifuge, a precipitation system, and a controller. The apparatus further consists of pumps, flowmeters, flowmeter adjustment valves, solenoid valves, drain valves, level sensors, and pressure sensors, which are installed between the abovementioned devices.

Description

動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法Fuel production apparatus and fuel supply system using animal and vegetable oils and used lubricating oil as raw materials, and fuel production and supply method using the same
 本発明は、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法、詳しくは、(1)動植物から採取した油や使用済みの動植物性食用油などを原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法及び(2)使用済み潤滑油などの石油系及び生物系の潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法に関する。ここで、(1)燃料製造装置は、動植物油及び使用済み潤滑油の濾過器を備え保温された原料貯蔵タンク及び原料貯蔵タンクへのオーバーフロー機能を備え保温された原料供給タンク、濾過装置、加熱器、遠心分離機、沈殿システム、コントローラ及びそれらの機器の間に設置されたポンプ、流量計、流量調整弁、電磁弁、ドレン弁、レベルセンサー及び圧力センサーから構成され、(2)それを用いた燃料製造方法とは、濾過、加熱、遠心分離、沈殿及び加圧という物理的手法のみを用いて、動植物油及び使用済み潤滑油をボイラーやエンジンの燃料として使用できる性状及び状態にする方法をさす。 The present invention relates to a fuel production apparatus and fuel supply system using animal and vegetable oil and used lubricating oil as a raw material, and fuel production and supply method using the same, in detail: (1) Oil collected from animals and plants and used animal and plant activity Fuel production apparatus and fuel supply system using edible oil etc. as a raw material, fuel production / supply method using the same, and (2) Fuel production apparatus made from petroleum based and biological lubricating oils such as used lubricating oil and the like The present invention relates to a fuel supply system and a fuel production / supply method using the same. Here, (1) The fuel production apparatus includes a filter for animal and vegetable oil and used lubricating oil, a heated raw material storage tank kept warm and an overflow function to the raw material storage tank, and a heated raw material supply tank, a filtration device, heating Equipment, centrifuge, sedimentation system, controller and pump installed between the equipment, flow meter, flow control valve, solenoid valve, drain valve, level sensor and pressure sensor, (2) The fuel production method used is a method to make the animal and vegetable oil and the used lubricating oil usable as a fuel for a boiler or engine using only physical methods such as filtration, heating, centrifugation, sedimentation and pressurization. That's right.
 地球温暖化対応技術として、動植物性燃料などの再生可能エネルギーの活用が求められている。また限られた資源の有効利用として、使用済み潤滑油などを熱エネルギーとして活用するリサイクルエネルギー技術の開発が求められている。しかしながら、動植物から採取された油や使用済み潤滑油は粘度が高い、不純物を含むなどの特徴を有しており、そのままボイラーやディーゼルエンジン等の燃料として使用した場合には、析出物により燃料噴射装置を構成する燃料ポンプや噴射ノズルに不具合を発生することが懸念される。そこで、近年では、「メチルエステル化」などの化学的処理を実施して原料である動植物油からグリセリンを取り除くことで、動植物油を脂肪酸メチルエステルなどの軽油に近い性状に変換した「ディーゼル自動車用燃料(バイオディーゼル燃料)」が使用されている。 Utilization of renewable energy such as animal and vegetable fuels is required as a technology to cope with global warming. In addition, as effective utilization of limited resources, development of recycled energy technology that utilizes used lubricating oil and the like as thermal energy is required. However, oil collected from animals and plants and used lubricating oils have characteristics such as high viscosity and inclusion of impurities, and when used as fuel for boilers and diesel engines as they are, precipitates cause fuel injection There is a concern that the fuel pump and the injection nozzle that constitute the device may be defective. Therefore, in recent years, chemical treatment such as "methyl esterification" has been carried out to remove glycerin from raw materials animal and vegetable oils, thereby converting animal and vegetable oils into properties similar to light oils such as fatty acid methyl esters. Fuel (biodiesel fuel) is used.
このバイオディーゼル燃料は、例えば、特許文献1に記載されているように、化学的な手法を用いるため、複雑かつ高コストな工程を必要とする。 This biodiesel fuel requires a complicated and expensive process to use a chemical method as described in, for example, Patent Document 1.
特開2008-111098号公報JP 2008-111098 A
これに対し、例えば特許文献2に記載されているように、化学的な手法を用いず、食用廃油から沈殿、濾過、加熱という物理的手法のみを用いてボイラー等の燃料を生産できるとの報告もあるが、
一般に食用廃油などから燃料を製造するには、沈殿、濾過により夾雑物を取り除くとともに、加熱により水分を分離させるという工程を必要とする。
On the other hand, for example, as described in Patent Document 2, there is a report that fuel such as a boiler can be produced using only physical methods such as precipitation, filtration and heating from waste food oil without using chemical methods. There is also
In general, in order to produce fuel from edible waste oil and the like, it is necessary to remove impurities by precipitation and filtration, and to separate water by heating.
特許第5545637号Patent No. 5545637
 しかしながら、加熱により水分を分離させるために、動植物油及び使用済み潤滑油を水の沸点(大気
圧下においては100℃)まで加熱するとともにこれを気化させるために多量のエネルギーを投入する必要があり、再生可能エネルギーとしての活用や熱エネルギーのリサイクル活
用という趣旨に相反する。また、動植物油及び使用済み潤滑油の粘度は、通常、ボイラーやディーゼルエンジン用の燃料として
使用されている軽油やA重油に比べると約10倍高い(40℃における軽油やA重油の動粘度が4~5 cStに対して、同じ温度における動植物油又は使用済み潤滑油の動粘度は40 cSt以上)ため、これを加熱することにより軽油やA重油と同程度の粘度まで低下させるためのエネルギーを必要とする。
However, in order to separate water by heating, it is necessary to heat animal and vegetable oils and used lubricating oils to the boiling point of water (100 ° C under atmospheric pressure) and to input a large amount of energy in order to vaporize it. Contradicts the purpose of utilizing renewable energy and recycling thermal energy. In addition, the viscosity of animal and vegetable oils and used lubricating oils is about 10 times higher than that of light oil and heavy oil, which are usually used as fuel for boilers and diesel engines (the dynamic viscosity of light oil and heavy oil at 40 ° C is Since the kinematic viscosity of animal or vegetable oil or used lubricating oil at the same temperature is 40 cSt or more at 4 to 5 cSt), the energy to reduce the viscosity to the same level as light oil or A heavy oil by heating it I need.
 そこで本発明は、動植物油及び使用済み潤滑油を水の沸点以下の比較的高温(例えば60℃)まで加熱するとともに、連続して繰り返し濾過、遠心分離及び沈殿を行うことにより、燃料として使用できる性状に改質してボイラーやディーゼルエンジンに連続して供給できるようにするとともに、
これを加圧して比較的高圧(例えば0.5MPa)にすることにより、比較的高粘度の状態(20~30 cSt)でもボイラーやエンジンの燃料噴射装置が良好に作動するような状態にすることを目的とする。
Therefore, the present invention can be used as a fuel by heating animal and vegetable oils and used lubricating oils to a relatively high temperature (eg 60 ° C.) below the boiling point of water and continuously performing repeated filtration, centrifugation and sedimentation. While reforming it to properties and enabling continuous supply to boilers and diesel engines,
By pressurizing it to a relatively high pressure (for example, 0.5 MPa), it is possible to make the fuel injection device of the boiler or engine work well even in a relatively high viscosity state (20 to 30 cSt). To aim.
請求項1に記載の発明は、再生可能エネルギーである動植物性油やリサイクルエネルギーである使用済み潤滑油を原料として、濾過、加熱、遠心分離、沈殿及び加圧という物理的手法のみを用いて燃料化する燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法であって、
濾過器を備え保温された原料貯蔵タンクと、それに隣接されて原料貯蔵タンクへのオーバーフロー機構を備えるとともに保温された原料供給タンク、濾過装置、加熱器、遠心分離機、沈殿システム、コントローラ及びそれらの機器の間に設置されたポンプ、流量計、流量調整弁、電磁弁、ドレン弁、レベルセンサー及び圧力センサーから構成され、
濾過器を経て原料貯蔵タンク内に貯蔵された動植物油又は使用済み潤滑油は、原料貯蔵タンクの下位レベルに設置された取出口から流出し、原料濾過装置、原料循環ポンプ、原料加熱器、遠心分離機、原料流量計を経て原料供給タンク内に設置された導入管により原料供給タンク内の下部位置に導かれて流出した後、
その一部は、原料供給タンクの下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれて、原料濾過装置から原料循環ポンプに至る流路と合流して、原料循環ポンプ,原料加熱器、遠心分離機、原料流量計を経て再び原料供給タンクに戻る原料循環経路を形成することにより連続して加熱、遠心分離、沈殿を繰り返し、
その一部は、原料供給タンクからオーバーフローして(溢れ出て)原料貯蔵タンクに流入することにより、原料供給タンクは常にフルレベル(満杯)の状態に保たれ、原料加熱器によって加熱された原料が原料貯蔵タンクと原料供給タンクに連続的に供給されることにより、保温されたそれぞれのタンクは加熱装置を必要としなくなるとともに、
残りは、原料供給タンクの上位レベルに設置された取出口から流出して、消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに供給され、
燃料供給ポンプにバイパス流路を設けてその途中に燃料供給ポンプのバイパス燃料流量調整弁を設けることにより、ボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定できるという構造と機能を持つとともに、
ボイラー・エンジンの燃料噴射装置出口又はその直前から燃料供給ポンプの吸入側に導かれて、消費燃料流量計から燃料供給ポンプに至る流路と合流する燃料循環流路を設けるとともに、その途中に燃料循環弁を設置することにより、ボイラー・エンジンの起動時に助燃用燃料などを必要としないという構造と機能を持っている。
The invention according to claim 1 uses only physical methods such as filtration, heating, centrifugation, sedimentation and pressurization, using as raw materials animal and vegetable oils that are renewable energy and used lubricating oils that are recycled energy. Fuel production apparatus and fuel supply system, and fuel production / supply method using the same;
An insulated raw material storage tank provided with a filter and an overflow mechanism adjacent to it and provided with an overflow mechanism to the raw material storage tank, and an insulated raw material supply tank, a filter, a heater, a centrifuge, a precipitation system, a controller and the like It consists of a pump, flow meter, flow control valve, solenoid valve, drain valve, level sensor and pressure sensor installed between the equipment,
The animal or vegetable oil or the used lubricating oil stored in the raw material storage tank via the filter flows out from the outlet provided at the lower level of the raw material storage tank, and is used as a raw material filter, raw material circulation pump, raw material heater, centrifugal After being led to the lower position in the raw material supply tank by the introduction pipe installed in the raw material supply tank through the separator and the raw material flow meter, it flows out,
Part of it flows out from the outlet installed at the lower level of the feed tank, is led to the suction side of the feed circulation pump through the circulating feed flow meter and the circulation feed flow control valve, and the feed is circulated from the feed filtration device. Consecutive heating, centrifugal separation, precipitation by forming a raw material circulation path that joins the flow path leading to the pump, passes through the raw material circulation pump, the raw material heater, the centrifuge, and the raw material flow meter and returns to the raw material supply tank again. Repeat
The raw material supply tank is always kept at full level (full) by partially overflowing from the raw material supply tank and flowing into the raw material storage tank, the raw material heated by the raw material heater Is continuously supplied to the raw material storage tank and the raw material supply tank, so that each heated tank does not need a heating device.
The remainder flows out of the outlet installed at the upper level of the feed tank, and is supplied to the boiler engine through the fuel consumption flow meter, the fuel supply pump, the fuel heater, and the fuel filter.
A structure in which the pressure of fuel supplied to the boiler / engine can be set to a relatively high pressure (for example, 0.5 MPa) by providing a bypass flow passage in the fuel supply pump and providing a bypass fuel flow control valve for the fuel supply pump in the middle thereof. Along with
A fuel circulation passage is provided which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler or engine or immediately before that, and a fuel circulation passage joining with the passage from the consumed fuel flow meter to the fuel supply pump is provided By installing the circulation valve, it has the structure and function that it does not need auxiliary fuel for starting the boiler engine.
請求項2に記載の発明は、原料貯蔵タンクの下位レベルに設置された取出口から流出し、原料濾過装置、原料循環ポンプ、原料加熱器、遠心分離機及び原料流量計を経て原料供給タンクに至る動植物油又は使用済み潤滑油と、
原料供給タンクの下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれて、原料濾過装置から原料循環ポンプに至る流路と合流した動植物油又は使用済み潤滑油は、燃料供給タンク内に設置された導入管によりタンク内の下部位置に導かれて流出し、

 動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は流出口から下方へ向かって移動し、そのほとんどは原料供給タンク下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て、原料濾過装置から原料循環ポンプに至る流路と合流するとともに、その一部はタンク底部に滞留し、
 残りは原料供給タンク内を上方に向かって移動し、そのほとんどは原料供給タンクの上位レベルに設置された取出口から流出して消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至るとともに、その一部は原料供給タンクからオーバーフローして原料貯蔵タンクに至るという過程を連続的に繰り返すことにより、原料供給タンクの上位レベルに設置された取出口から流出してボイラー・エンジンに至る動植物油又
は使用済み潤滑油は、原料供給タンクにおいて効果的な沈殿が繰り返し行なわれることによりボイラー・エンジンに使用可能な性状に改質されるとともに、
動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は原料供給タンク底部に蓄積され、
 原料供給タンク底部に設置されたドレン弁を開けることにより、タンク底部に蓄積された動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムから除去されるという機能を持っている。
The invention according to claim 2 flows out from the outlet installed at the lower level of the raw material storage tank, passes through the raw material filtration device, the raw material circulation pump, the raw material heater, the centrifuge, and the raw material flow meter to the raw material supply tank. Leading animal and vegetable oil or used lubricating oil,
It flows out from the outlet installed at the lower level of the feed tank, is led to the suction side of the feed circulation pump through the feedthrough flow meter and circulating feed flow control valve, and the flow path from the feed filtration device to the feed circulation pump The animal or vegetable oil or the used lubricating oil combined with the oil is led to the lower position in the tank by the introduction pipe installed in the fuel supply tank and flows out.

Substances and water with a density higher than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils or used lubricating oils, move downward from the outlet, mostly at the lower level of the feed tank. It flows out from the installed outlet, passes through the circulating feed flow meter and circulating feed flow control valve, joins with the flow path from the feed filtration device to the feed circulation pump, and a part of it stays in the bottom of the tank,
The remainder move upward in the feed tank, and most of them flow out from the outlet located at the upper level of the feed tank, and the fuel consumption flow meter, fuel feed pump, fuel heater and fuel filter As it passes through the boiler engine, part of it overflows from the raw material supply tank and continues to the raw material storage tank, and it flows out from the outlet provided at the upper level of the raw material supply tank. The animal or vegetable oil or the used lubricating oil leading to the boiler engine is reformed into properties usable for the boiler engine by repeated effective precipitation in the feed tank.
Substances and water with a density greater than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils or used lubricating oils, are accumulated at the bottom of the feed tank,
By opening the drain valve installed at the bottom of the raw material supply tank, substances or materials with a density greater than oil, such as metals, minerals, and minute contaminants contained in the animal and vegetable oil accumulated in the tank bottom or used lubricating oil Water has the function of being removed from fuel production equipment and fuel supply systems that are made from animal and vegetable oils and used lubricating oils.
請求項3に記載の発明は、原料貯蔵タンクの下位レベルに設置された取出口から流出して原料濾過装置を経て原料循環ポンプに至る動植物油又は使用済み潤滑油の流量を、
原料供給タンクの上位レベルに設置された取出口から流出して、消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至る動植物油又は使用済み潤滑油の流量よりも多く(例えば1.5倍)なるように設定するとともに、
原料供給タンクの下位レベルに設置された取出口から流出して循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれ、原料濾過装置から原料循環ポンプに至る流路と合流する動植物油又は使用済み潤滑油の流量を、
原料供給タンクの上位レベルに設置された取出口から流出して消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至る動植物油又は使用済み潤滑油の流量と等しくなるように設定することにより、
動植物油又は使用済み潤滑油は原料供給タンクから常時オーバーフローして(溢れ出て)原料貯蔵タンクに至り、原料供給タンクは常にフルレベル(満杯)の状態となるとともに、
原料加熱器によって加熱された動植物油又は使用済み潤滑油が原料貯蔵タンクと原料供給タンクに連続的に供給されることにより、
動植物油又は使用済み潤滑油を原料貯蔵タンクから原料供給タンクに移送する際の動力、配管及び原料供給タンクの液面制御を必要としなくなるとともに、
原料貯蔵タンク及び原料供給タンクを直接加熱することなくその温度を比較的高温(例えば50℃以上)に保持し、これにより両タンクにおける沈殿作用を促進させることができる。
The invention according to claim 3 is characterized in that the flow rate of the animal or vegetable oil or the used lubricating oil which flows out from the outlet provided at the lower level of the raw material storage tank, passes through the raw material filtering device and reaches the raw material circulation pump.
From the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet installed at the upper level of the raw material supply tank and passes through the consumed fuel flow meter, fuel supply pump, fuel heater, and fuel filter to the boiler engine As well as (for example, 1.5 times)
It flows out from the outlet installed at the lower level of the raw material supply tank and is led to the suction side of the raw material circulation pump through the circulating raw material flow meter and circulating raw material flow control valve, and the flow path from the raw material filtration device to the raw material circulation pump The flow rate of the combined animal and vegetable oil or used lubricating oil,
Equal to the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet located at the upper level of the feed tank through the consumed fuel flow meter, fuel feed pump, fuel heater, and fuel filter to the boiler engine By setting to be
The animal or vegetable oil or the used lubricating oil constantly overflows (overflows) from the raw material supply tank and reaches the raw material storage tank, and the raw material supply tank is always at full level (full).
By continuously supplying the raw material storage tank and the raw material supply tank with the animal and vegetable oil or the used lubricating oil heated by the raw material heater,
There is no need for motive power for transferring animal and vegetable oil or used lubricating oil from the raw material storage tank to the raw material supply tank, and control of the level of piping and raw material supply tank,
The temperature can be maintained at a relatively high temperature (for example, 50 ° C. or higher) without directly heating the raw material storage tank and the raw material supply tank, thereby promoting the precipitation action in both tanks.
請求項4に記載の発明は、原料貯蔵タンクの下位レベルに設置された取出口から流出して原料濾過装置を経て原料循環ポンプに至る動植物油又は使用済み潤滑油の流量が、原料供給タンクの上位レベルに設置された取出口から流出してボイラー・エンジンに至る動植物
油又は使用済み潤滑油の流量よりも少なくなり、原料供給タンクから原料貯蔵タンクへのオーバーフローが途絶えて、原料供給タンクの油面が低下した場合、
原料供給タンクに設置したレベルセンサーによりこれを検知して警報を発し、
原料供給タンク中位レベルに設置された取出口から流出して、消費燃料流量計から燃料供給ポンプに至る流路に合流する流路の途中に設置された電磁弁を、閉じた状態から開いた状態に切り替えるととも
に、
原料供給タンク上位レベルに設置された取出口から流出して、消費燃料流量計に至る流路に設置された電磁弁を、開いた状態から閉じた状態に切り替えることにより、
原料供給タンクの液面が、原料供給タンク中位レベルに設置された取出口に至る前にボイラー・エンジンを停止する等の燃料供給システムの安全に関する動作を行う機能を持たせることができる。
The invention according to claim 4 is characterized in that the flow rate of the animal or vegetable oil or the used lubricating oil which flows out from the outlet provided at the lower level of the raw material storage tank, passes through the raw material filtering device and reaches the raw material circulation pump It is less than the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet installed at the upper level and reaches the boiler / engine, and the overflow from the raw material supply tank to the raw material storage tank ceases and oil in the raw material supply tank If the face drops,
This is detected by the level sensor installed in the raw material supply tank and an alarm is issued,
The solenoid valve installed in the middle of the flow path that flows out from the outlet installed at the medium level of the raw material supply tank and joins the flow path from the consumed fuel flow meter to the fuel supply pump was opened from the closed state While switching to the state,
By switching from an open state to a closed state a solenoid valve installed in the flow path that flows out of the outlet installed at the upper level of the raw material supply tank and reaches the fuel consumption flow meter.
It is possible to have the function of performing safety-related operations of the fuel supply system such as stopping the boiler engine before the liquid level of the raw material supply tank reaches the outlet set at the medium level of the raw material supply tank.
請求項5に記載の発明は、燃料供給ポンプにバイパス流路を設けてその途中にバイパス燃料流量調整弁を設置し、燃料供給ポンプをバイパスする燃料の流量を調整してボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定することにより、
ボイラー・エンジンの燃料噴射装置に比較的高圧の燃料を供給し、燃料油の粘度をA重油や軽油と同程度まで低下させることなく(燃料油温度を上昇させることなく)燃料噴射装置が良好な作動を行うことができるような機能を備える。
The invention according to claim 5 is characterized in that the fuel supply pump is provided with a bypass flow path, a bypass fuel flow control valve is installed in the middle thereof, and the fuel flow rate bypassing the fuel supply pump is adjusted and supplied to the boiler engine. By setting the fuel pressure to a relatively high pressure (for example, 0.5 MPa),
A relatively high-pressure fuel is supplied to the fuel injection device of the boiler engine, and the fuel injection device is good without lowering the viscosity of the fuel oil to the same extent as A heavy oil or light oil (without raising the fuel oil temperature) It has a function that can perform the operation.
請求項6に記載の発明は、ボイラー・エンジンの燃料噴射装置出口又はその直前から燃料供給ポンプの吸入側に導かれて、消費燃料流量計から燃料供給ポンプに至る流路と合流する燃料循環流路を設けるとともに、燃料循環流路に燃料循環弁を設置することにより、
ボイラー・エンジンの起動時又は停止時における燃料の温度(粘度)を燃料噴射装置に適した状態にするような構造と機能を有し、ボイラー・エンジンの起動時に助燃用燃料や助燃装置を必要としない。
The invention according to claim 6 is directed to a fuel circulation flow which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler engine or just before that, and joins the flow path from the fuel consumption flow meter to the fuel supply pump. By installing a fuel circulation valve in the fuel circulation channel while
It has the structure and function to make the temperature (viscosity) of the fuel at the start or stop of the boiler engine suitable for the fuel injection device, and it is necessary to use the auxiliary fuel or auxiliary device at the start of the boiler engine. do not do.
 本発明は、動植物油及び使用済み潤滑油を、水の沸点以下の比較的高温(例えば60℃)まで加熱するとともに、連続して繰り返し濾過、遠心分離及び沈殿を行い、燃料として使用できる性状に改質してボイラーやディーゼルエンジンに連続的に供給するとともに、これを加圧して比較的高圧(例えば0.5MPa)にして、ボイラーやエンジンに供給する燃料の粘度をA重油や軽油と同程度まで低下させることなく(加熱に要するエネルギーを軽減して)、燃料噴射装置が良好な作動を行うことができるようにすることにより、再生可能エネルギーである動植物性油やリサイクルエネルギーである使用済み潤滑油に投入するエネルギーを最小限にすることができる、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法を提供することができる。 The present invention heats an animal and vegetable oil and a used lubricating oil to a relatively high temperature (eg, 60 ° C.) lower than the boiling point of water and continuously repeatedly filters, centrifuges and precipitates them so that they can be used as fuel It reforms and continuously supplies it to a boiler or diesel engine, while pressurizing it to a relatively high pressure (for example, 0.5 MPa), the viscosity of the fuel supplied to the boiler or engine is as high as A heavy oil or light oil By reducing the energy required for heating (by reducing the energy required for heating) and enabling the fuel injection device to perform a good operation, used oil which is renewable energy and used lubricating oil which is recycled energy Fuel production system and fuel supply system using animal and vegetable oils and used It is possible to provide a fuel production and supply method using.
本実施形態としての動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムの概念図。BRIEF DESCRIPTION OF THE DRAWINGS The conceptual diagram of the fuel manufacturing apparatus and fuel supply system which use animal and vegetable oil and used lubricating oil as a raw material as this embodiment as a raw material. 原料供給タンクにおける効果的な沈殿方法を示す概念図。The conceptual diagram which shows the effective precipitation method in a raw material supply tank. 制御ブロック図。Control block diagram. 燃料噴射ポンプの作動を示す概念図。The conceptual diagram which shows the action | operation of a fuel injection pump.
以下に、本発明に係る実施形態について図面を参照しながら説明する。図1は、本実施形態としての動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムの概念図である。 Hereinafter, embodiments according to the present invention will be described with reference to the drawings. FIG. 1 is a conceptual view of a fuel production apparatus and a fuel supply system which use animal and vegetable oils and a used lubricating oil as raw materials according to this embodiment.
 動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムAは、図1に示すよう
に、(1)濾過、加熱、遠心分離、沈殿及び加圧という物理的手法のみを用いて、動植物油及び使用済み潤滑油をボイラーやエンジンの燃料として使用できる性状及び状態に改質できる、(2)その際に、加熱、遠心分離、沈殿を連続して繰り返し、動植物油及び使用済み潤滑油中に含まれる水分を除去することにより、水の沸点(大気圧下においては100℃)以上まで加熱し、更にこれを蒸発させることにより水分を除去するという工程を必要としないため、温度上昇と気化に必要なエネルギーを削減できる、(3)保温された燃料貯蔵タンクと燃料供給タンクを隣接させ、燃料供給タンクの原料を常時フルレベ
ル(満杯)にするとともにその一部を原料貯蔵タンクにオーバーフローさせることにより、原料貯蔵タ
ンクから原料供給タンクに原料を移送する際の動力、配管及び原料供給タンクの液面制御を必要としないとともに、原料を連続的に循環させるため循環経路のいずれか1箇所に加熱装置を設けることにより、
原料貯蔵タンクと原料供給タンクの加熱装置を必要としない、(4)燃料供給ポンプにバイパス流路を設けてその途中にバイパス燃料流量調整弁を設け、ボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定することにより、ボイラー・エンジンに供給する燃料の粘度を軽油やA重油と同等の値まで低減するために燃料を加熱するエネルギーを低く抑えることができ、動植物油及び使用済み潤滑油を燃料化する際に投入するエネルギー及び、ボイラーやエンジンに供給する際に投入するエネルギーを低く抑えつつ高品質の燃料を製造・供給することが可能となる。
Fuel production equipment and fuel supply system A which uses animal oil and vegetable oil and used lubricating oil as raw materials, as shown in FIG. 1, use only physical methods such as (1) filtration, heating, centrifugation, sedimentation and pressurization. , Animal and vegetable oils and used lubricating oils can be reformed to properties and conditions that can be used as fuels for boilers and engines, (2) heating, centrifugation, and sedimentation repeated continuously, animal and vegetable oils and used lubricants Since the process of heating to the boiling point of water (100 ° C. under atmospheric pressure) or higher and removing the water by evaporating it is not required by removing the water contained in the oil, the temperature rise And the energy required for vaporization can be reduced, (3) Keep the fuel storage tank and fuel supply tank adjacent to each other and keep the fuel supply tank full level (full) at all times By partially overflowing the raw material storage tank, it is not necessary to control the power when transferring the raw material from the raw material storage tank to the raw material supply tank, control the level of piping and the raw material supply tank, and continuously circulate the raw material. Therefore, by providing a heating device at any one place in the circulation path,
(4) The fuel supply pump is provided with a bypass flow path, a bypass fuel flow control valve is provided along the way, and the pressure of the fuel supplied to the boiler engine is compared By setting the pressure to a relatively high pressure (for example, 0.5 MPa), the energy for heating the fuel can be suppressed to a low level in order to reduce the viscosity of the fuel supplied to the boiler engine to the same value as light oil or A heavy oil. And, it is possible to manufacture and supply high quality fuel while keeping low the energy input when converting used lubricating oil into fuel and the energy input when supplying it to a boiler or an engine.
(小規模原料供給流路CL1-1と原料循環流路CL1-2及びCL1と燃料供給流路FSLの機能)
 動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムAは、図1に示すように、濾過器FL1及びレベルセンサーLS1を備えた原料貯蔵タンクTK1とそれに隣接されたレベルセンサーLS2を備えた原料供給タンクTK2、原料濾過装置FL2、原料加熱器HT1、遠心分離機CSP、原料貯蔵タンクTK1及び原料供給タンクTK2を用いた沈殿システム、燃料加熱器HT2、燃料濾過装置FL3及びそれらの機器の間に設置された原料循環ポンプPM1、燃料供給ポンプPM2、原料流量計FM1、循環原料流量計FM2、消費燃料流量計FM3、循環原料流量調整弁CV1、バイパス燃料流量調整弁CV2、電磁弁EV1, EV2, EV3, EV4、ドレン弁DV1、DV2及び圧力センサーPS1, PS2, PS3から構成されている。
この構成要素のうち、(1) -1-原料貯蔵タンクTK1から流出し、原料濾過装置FL2を経て原料循環ポンプPM1の吸入側に至る原料供給流路CL1-1と、
-2-原料供給タンクTK2から流出して循環原料流量計FM2、循環原料流量調整弁CV1を経て原料循環ポンプPM1の吸入側に合流する原料循環流路CL1-2及び、
-3- 原料供給流路CL1-1と原料循環流路CL1-2が合流して、原料過熱器HT1、遠心分離機CSP及び原料流量計FM1を経て原料供給タンクに至る原料循環流路CL1により、動植物油又は使用済み潤滑油は原料加熱器HT1により加熱されて流動性が増した(粘度が低下した)状態で、動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分が原料貯蔵タンクTK1と原料供給タンクTK2における沈殿作用により除去されるとともに、遠心分離によりその他の油分よりも密度が大きな物質(例えば潤滑油中に含まれるスラッジ等)が除去される。
-4- 原料貯蔵タンクTK1にはレベルセンサーLS1が設置されており、原料の補給の際に基準となる油面位置(レベル)を上回った場合と、運転の際に基準となる油面位置(レベル)を下回った場合に警報を発して、それぞれに対する対応(処置)を促す。
原料供給タンクTK2にはレベルセンサーLS2が設置されており、原料供給タンクから原料貯蔵タンクへのオーバーフローが途絶える油面位置(レベル)になった場合と、油面位置(レベル)が原料供給タンク高位電磁弁の設置位置と原料供給タンク中位電磁弁の設置位置の中間位置になった場合に警報を発して、それぞれに対する対応(処置)を促す。
次に(2)原料供給タンクTK2から消費燃料流量計FM3、燃料供給ポンプPM2、燃料加熱器HT2、燃料濾過装置FL3、ボイラー・エンジンB&Eに至る燃料供給流路FSLにおいて、動植物油又は使用済み潤滑油は、燃料加熱器HT2により加熱されて流動性が増した(粘度が低下した)状態で、燃料濾過装置FL3により動植物油又は使用済み潤滑油中に含まれる夾雑物が除去されるとともに、燃料供給ポンプPM2とそれをバイパスする流路に設置されたバイパス燃料流量調整弁CV2により、ボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定できるという構造と機能を持つ。
(Functions of the small-scale material supply passage CL1-1, the material circulation passage CL1-2 and CL1, and the fuel supply passage FSL)
As shown in FIG. 1, the fuel production apparatus and fuel supply system A, which uses animal and vegetable oil and used lubricating oil as raw materials, have a raw material storage tank TK1 provided with a filter FL1 and a level sensor LS1 and a level sensor LS2 adjacent thereto. The raw material supply tank TK2, the raw material filtration device FL2, the raw material heater HT1, the centrifugal separator CSP, the precipitation system using the raw material storage tank TK1 and the raw material supply tank TK2, the fuel heater HT2, the fuel filtration device FL3 and the like Equipment installed between material circulation pump PM1, fuel supply pump PM2, material flow meter FM1, circulating material flow meter FM2, consumption fuel flow meter FM3, circulating material flow adjustment valve CV1, bypass fuel flow adjustment valve CV2, solenoid valve It consists of EV1, EV2, EV3, EV4, drain valves DV1, DV2, and pressure sensors PS1, PS2, PS3.
Among these components, (1) -1- a raw material supply flow path CL1-1 which flows out from the raw material storage tank TK1 and reaches the suction side of the raw material circulation pump PM1 through the raw material filter FL2;
-2- a raw material circulation channel CL1-2 which flows out from the raw material supply tank TK2 and joins the suction side of the raw material circulation pump PM1 through the circulating raw material flow meter FM2 and the circulating raw material flow adjustment valve CV1;
-3- The raw material supply flow path CL1-1 and the raw material circulation flow path CL1-2 join together, and the raw material circulation flow path CL1 reaching the raw material supply tank via the raw material superheater HT1, the centrifuge CSP and the raw material flow meter FM1 , Animal and vegetable oil or used lubricating oil is heated by raw material heater HT1 to increase fluidity (viscosity decreased), metals, minerals and minute impurities contained in animal and vegetable oil or used lubricating oil And other substances having a density higher than that of the oil, etc. are removed by sedimentation in the raw material storage tank TK1 and the raw material supply tank TK2, and substances having a density larger than the other oils by centrifugal separation (eg, contained in lubricating oil Sludge etc) is removed.
-4- The raw material storage tank TK1 is provided with a level sensor LS1. When the raw material is replenished, the level sensor LS1 exceeds the standard oil level position (level) and the standard oil surface position during operation If the level falls below the level, an alarm will be issued and action will be taken.
The level sensor LS2 is installed in the raw material supply tank TK2, and the oil level position (level) at which the overflow from the raw material supply tank to the raw material storage tank ceases and the oil level position (level) is higher than the raw material supply tank. An alarm is issued when the installation position of the solenoid valve and the installation position of the middle feed valve of the raw material supply tank are reached, and measures (actions) for each are urged.
Next, (2) animal or vegetable oil or used lubrication in the fuel supply flow path FSL from the raw material supply tank TK2 to the consumed fuel flow meter FM3, the fuel supply pump PM2, the fuel heater HT2, the fuel filter FL3 and the boiler engine B & E. The oil is heated by the fuel heater HT2 to increase fluidity (viscosity decreases), and the fuel filter FL3 removes contaminants contained in the animal or vegetable oil or the used lubricating oil, and It has a structure and a function that the pressure of the fuel supplied to the boiler engine can be set to a relatively high pressure (for example, 0.5 MPa) by the supply pump PM2 and the bypass fuel flow control valve CV2 installed in the flow path bypassing it.
以下、項目別に具体的に説明すると、
〔原料貯蔵タンクによる1次濾過〕
 動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムAにおいて、原料となる動植物油又は使用済み潤滑油は、原料貯蔵タンクの上部に設けられた取り入れ口から濾過器FL1を経
て原料貯蔵タンクに流入され、動植物油又は使用済み潤滑油は原料貯蔵タンクに貯蔵される。この際、動植物油又は使用済み潤滑油中に含まれる金属や鉱物等の油分よりも密度が大きな物質及び水分が沈殿により原料貯蔵タンクの底部向かって下降していく。原料貯蔵タンクの底部には傾斜があり、動植物油又は使用済み潤滑油中に含まれる金属や鉱物等の油分よりも密度が大きな物質及び水分は底部の傾斜に沿って移動し、最低部に滞留する。図に示すように、最低部にはドレン弁DV1が設置されており、
ドレン弁DV1を開くことによりタンク底部に滞留した動植物油又は使用済み潤滑油中に含まれる金属や鉱物等の油分よりも密度が大きな物質及び水分は、動植物油及び使用済み潤滑油を原料とする燃料製
造装置及び燃料供給システムAの外に排出される。
Below, if you explain concretely according to item,
[Primary filtration by raw material storage tank]
In the fuel production apparatus and fuel supply system A which uses animal oil and vegetable oil and used lubricating oil as raw materials, the animal oil or vegetable oil or used lubricating oil as raw material passes through the filter FL1 from the intake provided at the upper part of the raw material storage tank. It flows into the raw material storage tank, and the animal and vegetable oil or the used lubricating oil is stored in the raw material storage tank. At this time, substances and water having a density greater than oil components such as metals and minerals contained in animal and vegetable oils or used lubricating oils are precipitated toward the bottom of the raw material storage tank. There is a slope at the bottom of the raw material storage tank, and substances and water with higher density than oils such as metals and minerals contained in animal and vegetable oil or used lubricating oil move along the slope of the bottom and stay at the lowest Do. As shown in the figure, a drain valve DV1 is installed at the lowest part,
Substances and water with a density greater than oil, such as metals, minerals, etc., contained in animal and vegetable oil or used lubricating oil accumulated in the tank bottom by opening the drain valve DV1 use animal and vegetable oil and used lubricating oil as raw materials It is discharged out of the fuel production system and the fuel supply system A.
 〔原料供給流路CL1-1と原料循環流路CL1-2及びCL1による加熱、遠心分離、沈殿の繰り返し〕
原料貯蔵タンクTK1の低位レベルに設置された取出口から流出した動植物油及び使用済み潤滑油は、原料濾過装置FL2を経て原料循環ポンプPM1の吸入側に至る(原料供給流路CL1-1)。
一方、原料供給タンクTK2の下位レベルに設置された取り出し口から流出した動植物油及び使用済み潤滑油は、循環原料流量計FM2、循環原料流量調整弁CV1を経て(原料循環流路CL1-2)、原料濾過装置FL2から原料循環ポンプPM1に至る流路と合流して、原料循環ポンプPM1,原料加熱器HT1、遠心分離機CSP及び原料流量計FM1を経て再び原料供給タンクTK2に戻る循環経路(原料循環流路CL1-2及びCL1)を形成することにより、連続して加熱、遠心分離、沈殿を繰り返す。
[Heating by the raw material supply flow path CL1-1 and the raw material circulation flow path CL1-2 and CL1, repetition of centrifugation, precipitation]
The animal and vegetable oil and the used lubricating oil which flowed out from the outlet provided at the lower level of the raw material storage tank TK1 pass through the raw material filtering device FL2 and reach the suction side of the raw material circulating pump PM1 (raw material supply flow path CL1-1).
On the other hand, the animal and vegetable oil and the used lubricating oil which flowed out from the outlet provided at the lower level of the raw material supply tank TK2 pass through the circulating raw material flow meter FM2 and the circulating raw material flow rate adjustment valve CV1 (raw material circulating passage CL1-2) The circulation path which joins the flow path from the raw material filter FL2 to the raw material circulation pump PM1, passes through the raw material circulation pump PM1, the raw material heater HT1, the centrifugal separator CSP and the raw material flow meter FM1 and returns again to the raw material supply tank TK2. By forming the raw material circulation channels CL1-2 and CL1), heating, centrifugation and precipitation are repeated continuously.
〔原料貯蔵タンク及び原料供給タンクの下位レベル〕
原料貯蔵タンクの下位レベルとは、原料貯蔵タンク内における沈殿作用により原料貯蔵タンクの底部に移動して滞留する、動植物油及び使用済み潤滑油中に含まれる金属や鉱物等の油分よりも密度が大きな物質及び水分を吸入しない程度に底部からの距離を持つ位置を意味する。
原料供給タンクの下位レベルもこれと同様に、原料供給タンク内における沈殿作用により原料供給タンクの底部に移動して滞留する、動植物油及び使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分を吸入しない程度に底部からの距離を持つ位置を意味する。  
[Lower level of raw material storage tank and raw material supply tank]
The lower level of the raw material storage tank means that the density is higher than that of oils such as metals and minerals contained in animal and vegetable oils and used lubricating oil, which move to the bottom of the raw material storage tank due to sedimentation in the raw material storage tank. It means a position having a distance from the bottom to such an extent that large substances and moisture are not inhaled.
Similarly, the lower levels of the feed supply tank move to the bottom of the feed supply tank due to sedimentation in the feed supply tank and stay there, metals, minerals and minute contaminants contained in animal and vegetable oils and used lubricating oil It means a position with a distance from the bottom to such an extent that it does not inhale substances and moisture whose density is greater than oil content such as things.
 〔供給原料流路CL1-1を流れる原料の流量調整〕
原料循環流路CL1-2及びCL1において、原料流量計FM1及び循環原料流量計FM2によって供給原料流路CL1-1における流量を計測(CL1-1=FM1-FM2)するとともに、原料循環ポンプPM1の駆動モータの回転数をコントローラCTRにより制御することにより、供給原料流路CL1-
1を流れる原料の流量を任意の値に設定できる。
[Rate adjustment of the raw material flowing through the feed raw material channel CL1-1]
In the raw material circulation flow paths CL1-2 and CL1, the flow rate in the raw material flow path CL1-1 is measured (CL1-1 = FM1-FM2) by the raw material flow meter FM1 and the circulating raw material flow meter FM2, and By controlling the rotational speed of the drive motor by the controller CTR, the feed material flow path CL1-
The flow rate of the raw material flowing through 1 can be set to any value.
  〔原料濾過装置 FL2と燃料濾過装置FL3〕
 原料濾過装置FL2及び燃料濾過装置FL3は、原料及び燃料の流路に並列に設置された各2個のフィルターホルダーに収納された各2個のフィルターにより構成され、それぞれのフィルターの入口側と出口側にバルブを設け、全てのバルブは通常開いた状態であるが、いずれかのフィルターの入口側と出口側に設けられたバルブを閉じることにより、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムが作動中でもフィルターを交換することができる構造となっている。
 また、それぞれの濾過装置に設置された各2個のフィルターホルダーの、原料濾過装置においてはいずれか一方の出口側、燃料濾過装置においてはいずれか一方の入口側に圧力センサーPS1又はPS2と電磁弁EV1又はEV2が設けられており、通常の運転状態においてはこの電磁弁は閉じた状態であるが、
 原料濾過装置には、動植物油又は使用済み潤滑油中に含まれる25~100μm(捕集精度は原料貯蔵タンクTK1に設置された濾過器FL1との組み合わせによって決まる)の夾雑物を捕捉可能なフィルター(エレメント)が収納されており、圧力センサーPS1によって検知されるフィルター出口の圧力が設定値を下回った場合(フィルターが詰まった場合)に、
燃料濾過装置には、動植物油又は使用済み潤滑油中に含まれる約10μmの夾雑物を捕捉可能なフィルター(エレメント)が収納されており、圧力センサーPS2によって検知されるフィルター入口の圧力 
が設定値を上回った場合(フィルターが詰まった場合)に、
自動的に電磁弁EV1又はEV2が開き、もう一方のフィルターも作動させることにより、原料又は燃料の流量を確保できるような構造となっている。
[Raw material filter FL2 and fuel filter FL3]
The raw material filter FL2 and the fuel filter FL3 are constituted by two filters each housed in two filter holders installed in parallel in the flow path of the raw material and the fuel, and the inlet side and the outlet of each filter A valve is provided on the side, and all the valves are normally open, but by closing the valves provided on the inlet and outlet sides of either filter, fuels derived from animal and vegetable oil and used lubricating oil are used. The filter can be replaced even while the manufacturing device and the fuel supply system are in operation.
In addition, pressure sensor PS1 or PS2 and solenoid valve at the outlet side of either one of the two filter holders installed in each filtration device in the raw material filtration device or in the inlet side of the fuel filtration device. Although the EV1 or EV2 is provided, the solenoid valve is closed under normal operating conditions.
A filter capable of capturing 25 to 100 μm (the collection accuracy depends on the combination with the filter FL1 installed in the raw material storage tank TK) contained in animal and vegetable oils or used lubricating oil in the raw material filtration device If the (element) is stored and the pressure at the filter outlet detected by the pressure sensor PS1 falls below the set value (if the filter is clogged),
The fuel filter contains a filter (element) capable of capturing contaminants of about 10 μm contained in animal or vegetable oil or used lubricating oil, and the pressure at the filter inlet detected by the pressure sensor PS2
Is higher than the set value (if the filter is clogged),
By opening the solenoid valve EV1 or EV2 automatically and operating the other filter, the flow rate of the raw material or fuel can be secured.
 〔原料加熱器HT1〕
原料加熱器HT1により、原料となる動植物油又は使用済み潤滑油は加熱されて流動性を増す(粘度が
低下する)ことにより、原料貯蔵タンクTK1において除去できなかった金属や鉱物等の油分よりも密度が大きな物質や動植物油及び使用済み潤滑油中に含まれる油分との密度差を持つ微小な夾雑物を遠心分離機CSPにおいて効果的に除去されるとともに、原料貯蔵タンクTK1及び原料供給タンクTK2にお
ける沈殿作用を効果的に行わせることが可能となる。
[Raw material heater HT1]
The raw material heater HT1 heats the animal or vegetable oil used as a raw material or the used lubricating oil to increase fluidity (the viscosity decreases), so that it is more than oil components such as metals and minerals which could not be removed in the raw material storage tank TK1. The high density material and the minute impurities having a density difference with the oil contained in the animal and vegetable oil and the used lubricating oil are effectively removed by the centrifuge CSP, and the raw material storage tank TK1 and the raw material supply tank TK2 It is possible to effectively carry out the precipitation action in
〔遠心分離機CSP〕
遠心分離機CSPは、原料貯蔵タンクTK1及び原料供給タンクTK2における沈殿作用において除去できなかった金属や鉱物等の油分よりも密度が大きな物質や水分及び動植物油及び使用済み潤滑油中に含まれる油分よりも密度が大きな夾雑物(例えば、使用済み潤滑油に含まれるスラッジなど)を除去する機能を有する。このため、使用済み潤滑油を原料とする場合は必須の構成要素となるが、動植物油を原料とする場合は濾過装置及び沈殿システムを用いて十分な濾過、沈殿を行うことにより、
(1)図1に示すように、遠心分離機をバイパスする流路を設けて遠心分離機バイパス弁CSVを設置することにより、遠心分離機を使用しないで運転する。
(2)遠心分離機そのものを構成要素から除外する。
という選択が可能となる。
[Centrifuge CSP]
The centrifugal separator CSP is a substance or water having a density greater than that of oils such as metals and minerals which can not be removed by precipitation in the raw material storage tank TK1 and the raw material supply tank TK2, and oil contained in animal and vegetable oils and used lubricating oils. It has a function to remove contaminants (such as sludge contained in used lubricating oil) having a higher density than that. For this reason, it becomes an essential component when using a used lubricating oil as a raw material, but when using an animal and vegetable oil as a raw material, sufficient filtration and precipitation are performed using a filtration device and a precipitation system,
(1) As shown in FIG. 1, by providing a flow path for bypassing the centrifuge and installing the centrifuge bypass valve CSV, the operation is performed without using the centrifuge.
(2) Remove the centrifuge itself from the components.
The choice can be made.
(原料供給タンクTK2による2次沈殿)
〔TK2内における動植物油及び使用済み潤滑油中に含まれる、油分よりも密度が大きな金属、鉱物、水分及び微小粒子の挙動〕
図2に、原料供給タンクにおける効果的な沈殿方法を示す概念図を示す。原料供給流路CL1-1は原料循環ポンプの吸入側で原料循環流路CL1-2と合流して原料循環流路CL1となって、
原料加熱器HT1、
遠心分離機CSPを経て原料供給タンクTK2内に挿入された管を下降し、タンク底面に近い位置でタンク内に流出する。
その半分以上は原料供給タンクTK2の上方に向かって上昇し、タンクの上位レベルに設置された取り出し口から流出して、燃料供給流路FSLを経てボイラー・エンジンB&Eに至るとともに、オーバーフローして(溢れ出て)原料貯蔵タンクTK1に流入する。
残りの半分近くは、下降して原料供給タンクTK2の下位レベルに設置された取出口から流出して、原料循環流路(CL1-2)に至るとともに、更に下降して原料供給タンクTK2の底部に蓄積する。
この時、タンク内において上方へ向かう流れの速度をV-UP [ m/s ]、タンク内において下方へ向かう流れの速度をV-DN [ m/s ]、動植物油及び使用済み潤滑油の密度をD-FO、粘度をη、動植物油及び使用済み潤滑油中に含まれる金属・鉱物及び微小な夾雑物等や水分の直径をDIA、密度をD-MAとすると、動植物油及び使用済み潤滑油中に含まれる、油分よりも密度が大きな金属、鉱物、水分及び微小粒子等の夾雑物の流体中における沈降速度(終端速度)V-ST [ m/s ] は次式(ストークスの式)により示される。
                                    

(式1) 
Figure JPOXMLDOC01-appb-I000001




                         
ストークスの式(1)で示される「動植物油及び使用済み潤滑油中に含まれる油分よりも密度が大きな金属、鉱物、水分及び微小粒子等の夾雑物の下降速度」とタンク内における上方へ向かう流れの速度V-UPが、-1- 等しいと上方へ向かう流れの中に停止し、-2- V-STがV-UPよりも小さいと上方へ向かう
流れとともに上昇し、-3- V-STがV-UPよりも大きいと流れに逆らって下降し、そのほとんどは原料供給タンク下位レベルに設置された取り出し口から流出して原料循環流路CL1-2に導かれるが、一部は取出口を通過して原料供給タンク最下部に蓄積された後、ドレン弁DV2を開くことにより動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムAの外に排出される。
(Secondary precipitation by raw material supply tank TK2)
[The behavior of metals, minerals, water, and microparticles with a density higher than oil contained in animal and vegetable oils and used lubricating oils in TK2]
FIG. 2 is a conceptual view showing an effective precipitation method in the raw material supply tank. The raw material supply flow path CL1-1 joins the raw material circulation flow path CL1-2 on the suction side of the raw material circulation pump and becomes a raw material circulation flow path CL1.
Raw material heater HT1,
The tube inserted into the raw material supply tank TK2 is lowered through the centrifuge CSP, and flows out into the tank at a position close to the bottom of the tank.
More than half of the amount rises upward above the raw material supply tank TK2, flows out from the outlet provided at the upper level of the tank, passes through the fuel supply passage FSL, reaches the boiler engine B & E, and overflows ( Overflows) into the raw material storage tank TK1.
Nearly the other half descends and flows out from the outlet provided at the lower level of the raw material supply tank TK2, reaches the raw material circulation channel (CL1-2), and further descends to the bottom of the raw material supply tank TK2. Accumulate in
At this time, the velocity of upward flow in the tank is V-UP [m / s], the velocity of downward flow in the tank is V-DN [m / s], the density of animal and vegetable oils and used lubricating oil Let D-FO be the viscosity, η be the viscosity, DIA be the diameter of metals and minerals and minute impurities contained in animal and vegetable oils and used lubricating oils, and be D, and let D be the density. Settling velocity (terminal velocity) V-ST [m / s] in fluid of impurities such as metals, minerals, moisture, and microparticles, which have higher density than oil, contained in oil is the following equation (Stokes' equation) Indicated by.


(Formula 1)
Figure JPOXMLDOC01-appb-I000001





"The downward velocity of contaminants such as metals, minerals, moisture, and microparticles with a density higher than that contained in animal and vegetable oils and used lubricating oils" shown by the Stokes formula (1) and upward in the tank The flow velocity V-UP stops in the upward flow when equal to -1-, and rises with the upward flow if -2- V-ST is smaller than V-UP, -3- V- If ST is greater than V-UP, it descends against the flow, and most of it flows out from the outlet located at the lower level of the feed tank and is led to the feed circulation channel CL1-2, but a part is removed. After passing through the outlet and being accumulated at the lowermost part of the raw material supply tank, the drain valve DV2 is opened and the mixture is discharged out of the fuel manufacturing apparatus and fuel supply system A using animal oil and vegetable oil and used lubricating oil as raw materials.
〔2次濾過を効果的に行う方法-1〕
原料供給タンクの内径をD-TK2 [ m ]とし、このタンクに挿入された管を通ってタンク内に流入する動植物油及び使用済み潤滑油の流量を Q-TK2 [ m3/s ] とし、上方に向かって上昇する動植物油及び使用済み潤滑油の流量をQ-UP [ m3/s ]、タンク下位レベルに設置された取り出し口から流出して原料循環流路CL1-2に導かれる動植物油及び使用済み潤滑油の流量をQ-DN [ m3/s ]すると、原料供給タンクTK2の下位レベルに流入した動植物油及び使用済み潤滑油が、タンク内を上方へ向かう流れの速度V-UP [ m/s ] は次式により示される。

(式2)
Figure JPOXMLDOC01-appb-I000002
     
                              
                                    
                                    
 動植物油及び使用済み潤滑油が、原料供給タンク内を上方へ向かう流れの速度V-UP [ m/s ]を示す式(2)において、Q-TK2 = Q-UP + Q-DN より、Q-UP = Q-TK2 - Q-DN であるが、原料供給タンク下位レベルに設置された取り出し口から流出して原料循環流路CL1-2に導かれる動植物油及び使用済み潤滑油の流量Q-DNは、循環原料流量計FM2及び循環原料流量調整弁CV1により、ボイラー・エンジンの燃料消費量と等しくなるように設定される(ある値を取る)ので、原料供給タンクの内径D-TK2 [ m ]に対する原料供給タンクへ流入する動植物油及び使用済み潤滑油の単位時間あたりの流量Q-TK2 [ m3/s ]を少なくすることにより、原料供給タンク内において上方へ向かう流れの速度をV-UP [ m/s ]の値が小さくなり、2次濾過を効果的に行うことができる。
[Method of effectively performing secondary filtration-1]
The inner diameter of the raw material supply tank is D-TK2 [m], and the flow rate of animal and vegetable oil and used lubricating oil flowing into the tank through the pipe inserted in this tank is Q-TK2 [m 3 / s], The flow rate of animal and vegetable oil and used lubricating oil rising upwards Q-UP [m 3 / s], flowed out from the outlet located at the lower level of the tank, and led to the material circulation channel CL1-2 If the flow rate of oil and used lubricating oil is Q-DN [m 3 / s], the animal and vegetable oil and used lubricating oil that flowed to the lower level of the raw material supply tank TK2 will have a flow velocity V- UP [m / s] is expressed by the following equation.

(Formula 2)
Figure JPOXMLDOC01-appb-I000002




In the formula (2) in which the animal and vegetable oil and the used lubricating oil show the flow velocity V-UP [m / s] upward in the raw material supply tank, Q-TK2 = Q-UP + Q-DN, Q -UP = Q-TK2-Q-DN, but the flow rate of animal and vegetable oil and used lubricating oil that flows out from the outlet located at the lower level of the raw material supply tank and is led to the raw material circulation channel CL1-2 DN is set to be equal to (takes a certain value) the fuel consumption of the boiler / engine by the circulating feed flow meter FM2 and the circulating feed flow control valve CV1, so the inner diameter D-TK2 of the feed tank is by reducing the flow rate Q-TK2 per unit time of the animal or vegetable oil and used lubricating oil to flow into the raw material supply tank [m 3 / s] for], the velocity of flow directed upward in the material supply tank V- The value of UP [m / s] becomes small and secondary filtration can be performed effectively.
  〔2次濾過を効果的に行う方法-2〕
 ストークスの式(1)より、動植物油及び使用済み潤滑油中に含まれる金属、鉱物、水分などの油分よりも密度が大きな物質及び微小粒子等の夾雑物の直径DIA、密度D-MA及び動植物油及び使用済み潤滑油の密度D-FOを一定とすると、沈降速度(沈殿効果)は動植物油及び使用済み潤滑油の粘度ηが小さいほど早くなる(改善される)。
このことから、原料供給タンク内における動植物油及び使用済み潤滑油の温度を高くして粘度を低下させることにより沈殿効果は改善されることになる。
しかし、温度を高くするには加熱に要するエネルギーを投入する必要があること、本装置に多く使用されている流量計、流量調整弁、電磁弁、レベルセンサー、圧力センサーには耐熱温度があること、タンク内の温度を高くするほど周囲との温度差が大きくなり、放熱損失等の熱損失が増加すること等を考慮する必要がある。
[Method of effectively performing secondary filtration-2]
From the Stokes' equation (1), the diameter DIA, density D-MA and flora and fauna of substances such as metals and minerals contained in animal and vegetable oils and used lubricating oils and contaminants such as microparticles having a density greater than oil such as water Assuming that the density D-FO of the oil and the used lubricating oil is constant, the sedimentation velocity (precipitating effect) becomes faster (improved) as the viscosity η of the animal and vegetable oils and the used lubricating oil decreases.
From this, the precipitation effect is improved by raising the temperature of the animal and vegetable oil and the used lubricating oil in the raw material supply tank to lower the viscosity.
However, in order to raise the temperature, it is necessary to input the energy required for heating, and the flowmeter, flow control valve, solenoid valve, level sensor, and pressure sensor that are often used in this device have a heat resistant temperature As the temperature in the tank is increased, the temperature difference with the surroundings becomes larger, and it is necessary to consider that the heat loss such as the heat radiation loss increases.
 〔ドレン弁DV1, DV2の機能〕
動植物油及び使用済み潤滑油は原料貯蔵タンクTK1と原料供給タンクTK2において、連続して繰り返し行われる加熱と沈殿作用により、動植物油及び使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分が除去される。
具体的には、原料貯蔵タンクTK1及び原料供給タンクTK2の底部に滞留する動植物油及び使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は、
原料貯蔵タンクTK1及び原料供給タンクTK2の底部にそれぞれ設置されたドレン弁DV1及びDV2を定期的に開くことにより、燃料製造装置Aの外に排出される。
[Function of drain valve DV1, DV2]
The animal and vegetable oil and the used lubricating oil are contained in the raw material storage tank TK1 and the raw material supply tank TK2 continuously and repeatedly by heating and settling, and metals, minerals and minute impurities contained in the animal and vegetable oil and the used lubricating oil Substances and water with higher density than oil and the like are removed.
Specifically, substances and moisture with a density greater than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils and used lubricating oils, which are retained at the bottom of the raw material storage tank TK1 and the raw material supply tank TK2 ,
The drain valves DV1 and DV2 installed at the bottom of the raw material storage tank TK1 and the raw material supply tank TK2 are discharged to the outside of the fuel manufacturing apparatus A by periodically opening them.
 (原料供給タンク液面(レベル)が低下しても安全性を確保するための装置と方法)
図3は原料供給タンクTK2を常にフルレベル(満杯状態)とするための装置と方法を示す制御ブロッ
ク図である。原料供給タンクTK2の液面が何らかの状況の変化により低下して、動植物油又は使用済み潤滑油が原料供給タンクTK2からオーバーフローして(溢れ出て)原料貯蔵タンクTK1に至らなくなった場合、
図1に示す原料供給タンクTK2に設置されたレベルセンサーLS2がこれを検知して警報を発
するとともに、
タンクの中位レベルに設置された取出し口から供給燃料流量弁と燃料供給ポンプに至る流路に合流する流路の途中に設置された電磁弁EV4を閉じた状態から開いた状態に切り替えるとともに、原料供給タンク上位レベルに設置された取出し口に設置された電磁弁EV3を開いた状態から閉じた状態に切り替える機能を備えている。
また、これらの動作を行っても液面の低下が続く場合、原料供給タンクTK2の液面がタンクの中位レ
ベルに設置された取出口に至る前に、ボイラー・エンジンを停止する等の燃料供給システムの安全に係わる動作を行う機能を持たせることができる。
(Apparatus and method for securing safety even if the level of the raw material supply tank decreases)
FIG. 3 is a control block diagram showing an apparatus and method for always making the raw material supply tank TK2 full level (full state). When the liquid level of the raw material supply tank TK2 falls due to a change in the situation, and the animal or vegetable oil or the used lubricating oil overflows (overflows) from the raw material supply tank TK2 and does not reach the raw material storage tank TK1,
The level sensor LS2 installed in the raw material supply tank TK2 shown in FIG. 1 detects this and issues an alarm.
Switching from the closed state to the open state of the solenoid valve EV4 installed in the middle of the flow path joining the flow path from the outlet located at the middle level of the tank to the flow path from the supplied fuel flow valve to the fuel supply pump; It has a function to switch from the open state to the closed state of the solenoid valve EV3 installed at the outlet located at the upper level of the raw material supply tank.
In addition, if the liquid level continues to decrease even after these operations, the fuel such as stopping the boiler engine before the liquid level of the raw material supply tank TK2 reaches the outlet set at the middle level of the tank It can have the function of performing the operation related to the safety of the supply system.
 (ボイラー・燃料に供給する燃料の温度を通常よりも低く設定出来るための装置と方法)
動植物油及び使用済み潤滑油の粘度は、通常、ボイラーやディーゼルエンジン用の燃料として使用されている軽油やA重油に比べると約10倍高い(40℃における軽油やA重油の動粘度が4~5 cStに対して、同じ温度における動植物油又は使用済み潤滑油の沿動粘度は40
cSt以上)ため、これを加熱することにより軽油やA重油と同等の粘度まで低下させるためには多くのエネルギーを必要とする。
図3に、ボイラー・燃料に供給する燃料の温度を通常よりも低く設定出来るための装置と方法を示す制御ブロック図を示すとともに、図4に、燃料噴射ポンプの作動を示す概念図を示す。
図4に示すように、ディーゼルエンジンに装備されている燃料噴射ポンプは、周囲を燃料で満たされ、側面に燃料吸入孔を備えたバレル(ポンプハウジング)と、その中を縦方向に摺動するプランジャにより構成されている。プランジャが燃料吸入孔よりも下方へ移動すると燃料が吸入されるが、その吸入率(単位時間あたりの吸入量)は燃料吸入孔の直径と燃料の粘度に比例するが、燃料吸入孔の直径は燃料噴射ポンプの仕様によって決まっている。機関速度が速い(高回転の)エンジンでは高い吸入率が求められるが、燃料の粘度が高いとポンプハウジング内に吸入される燃料の量が不足して機関に不具合を生じる可能性がある。このような理由により、通常、ディーゼルエンジンの燃料として使用されている軽油やA重油よりも高い粘度を持つ動植物油及び使用済み潤滑油は、粘度を低下させるために加熱する必要がある。
(Apparatus and method for setting the temperature of fuel supplied to boiler and fuel lower than usual)
The viscosity of animal and vegetable oils and used lubricating oils is about 10 times higher than that of light oil and heavy oil, which are usually used as fuel for boilers and diesel engines (the dynamic viscosity of light oil and heavy oil at 40 ° C is 4 to For 5 cSt, the kinetic viscosity of animal or vegetable oil or used lubricating oil at the same temperature is 40
Therefore, much energy is required to reduce the viscosity to the same level as light oil or A heavy oil by heating it.
FIG. 3 shows a control block diagram showing an apparatus and method for setting the temperature of fuel supplied to a boiler / fuel lower than usual, and FIG. 4 shows a conceptual diagram showing the operation of a fuel injection pump.
As shown in FIG. 4, the fuel injection pump provided on the diesel engine is fuel-filled around its periphery, and slides longitudinally in a barrel (pump housing) provided with fuel suction holes on its side. It is comprised by the plunger. When the plunger moves below the fuel suction port, fuel is sucked, but the suction rate (the amount of suction per unit time) is proportional to the diameter of the fuel suction port and the viscosity of the fuel, but the diameter of the fuel suction port is It is decided by the specification of the fuel injection pump. High intake rates are required for engines with high engine speeds (high revolutions), but if the viscosity of the fuel is high, the amount of fuel drawn into the pump housing may be insufficient to cause problems with the engine. For this reason, animal and vegetable oils and used lubricating oils that have higher viscosity than diesel oil and diesel oil, which are usually used as diesel engine fuels, need to be heated to reduce their viscosity.
 本装置は、燃料供給ポンプPM2にバイパス流路を設けてその途中に燃料供給ポンプのバイパス燃料流量調整弁CV2を設けることにより、ボイラー・エンジンB&Eに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定することができる。これにより(ボイラー・エンジンの燃料噴射装置に比較的高圧の燃料を供給することにより)、ポンプハウジングの周囲を満たす燃料の圧力が高くなり、プランジャが燃料吸入孔よりも下方に移動した際に燃料を燃料ポンプのポンプハウジング内に圧入することにより、燃料油の粘度をA重油や軽油と同等まで低下させることなく(燃料油温度を上昇させることなく)燃料噴射装置を良好に作動させることが可能となる。 In this system, the fuel supply pump PM2 is provided with a bypass flow path, and the fuel supply pump bypass fuel flow control valve CV2 is provided in the middle thereof, so that the pressure of fuel supplied to the boiler engine B & E is relatively high (for example 0.5). (MPa) can be set. This increases the pressure of the fuel filling the periphery of the pump housing (by supplying a relatively high pressure of fuel to the fuel injection system of the boiler engine) and causes the fuel to move when the plunger moves below the fuel inlet. The fuel injection device can be operated well without lowering the viscosity of the fuel oil to the same level as heavy oil or light oil (without raising the temperature of the fuel oil) by pressing the fuel pump into the pump housing of the fuel pump. It becomes.
具体的には、図1に示す「本実施形態としての動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムの概念図」と、図3に示す「制御ブロック線図」において、圧力センサーPS3によりボイラー・エンジンB&Eに供給される燃料の圧力を検知して、燃料供給ポンプのバイパス流路に設置されたバイパス燃料流量調整弁CV2の開度を調整することにより、ボイラー・エンジンに供給される燃料の圧力を比較的高圧(例えば0.5MPa)に設定することができる。
これにより、燃料噴射ポンプを含む燃料噴射装置の作動を良好にし、燃料油の温度を上昇させることにより動粘度を低下させるのと同様の効果を得ることが可能となる。
Specifically, in the "conceptual view of the fuel manufacturing apparatus and fuel supply system using the animal and vegetable oil and the used lubricating oil as the present embodiment as the raw materials shown in Fig. 1" and the "control block diagram" shown in Fig. 3 The pressure sensor PS3 detects the pressure of fuel supplied to the boiler engine B & E, and adjusts the opening degree of the bypass fuel flow control valve CV2 installed in the bypass flow path of the fuel supply pump, The pressure of the fuel supplied to can be set to a relatively high pressure (e.g. 0.5 MPa).
As a result, it is possible to improve the operation of the fuel injection device including the fuel injection pump, and to obtain the same effect as lowering the kinematic viscosity by raising the temperature of the fuel oil.
 (小規模ボイラー・エンジンの起動時に助燃用燃料や助燃装置を必要としないための装
置と方法)
 動物性燃料や使用済み潤滑油は、濾過、加熱、遠心分離、沈殿及び加圧という物理的手法を用いてその性状及び状態を改善しても、ボイラー・エンジンB&Eの運転開始時、長期間の停止後又は短時間(例えば1時間以上)の停止後の起動時においては、ボイラー・エンジンB&Eの燃料噴射装置は装置が設置されている大気又は室内温度に近いため、通常装置を停止する前、又は起動直前に装置内に滞留する燃料を軽油やA重油などの低粘度の燃料に切り替えるか、助燃剤等を加える等の処置を行う必要がある。
 しかし本装置には、ボイラー・エンジンB&Eの燃料噴射装置出口又はボイラー・エンジンの燃料噴射装置直前から燃料供給ポンプPM2の吸入側に導かれて、消費燃料流量計FM3から燃料供給ポンプPM2に至る流路と合流する燃料循環流路CL2と、燃料循環流路CL2の途中に燃料循環弁FCVが設置されているため、ボイラー・エンジンの起動時に助燃用燃料や助燃装置を必要としない構造と機能を備えている。
(Apparatus and methods to eliminate the need for auxiliary fuel and auxiliary devices when starting small-scale boilers and engines)
Even if animal fuel and used lubricating oil are improved in their properties and conditions using physical methods such as filtration, heating, centrifugation, sedimentation and pressurization, they can be used for a long time at the start of operation of the boiler engine B & E. At start-up after stopping or for a short time (for example, one hour or more), since the fuel injection device of the boiler engine B & E is close to the atmosphere or room temperature where the device is installed, usually before stopping the device Alternatively, it is necessary to perform a treatment such as switching the fuel retained in the apparatus to a low viscosity fuel such as light oil or A heavy oil immediately before start-up, or adding a combustion improver or the like.
However, in this device, the flow is led from the fuel injection device outlet of the boiler engine B & E or directly before the fuel injection device of the boiler engine to the suction side of the fuel supply pump PM2, and flows from the fuel consumption flow meter FM3 to the fuel supply pump PM2. Since the fuel circulation passage CL2 joining the passage and the fuel circulation valve FCV are installed in the middle of the fuel circulation passage CL2, the structure and function do not require any auxiliary fuel or auxiliary device at startup of the boiler engine. Have.
 具体的には、通常の運転時には燃料循環弁FCVを閉じておくことにより燃料循環流路CL2に燃料は流れず、原料供給タンクTK2の上位レベルに設置された取出口から流出して、消費燃料流量計FM3、燃料供給ポンプPM2、燃料加熱器TH2、燃料濾過装置FL3を経て(燃料供給流路FSLにより)ボイラー・エンジンB&Eに供給された動植物性油又は使用済み潤滑油は全てボイラー・エンジンにおいて消
費される。
しかしこの供給システムでは、例え短時間でも、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムが設置された場所の外気温度又は室内の温度が低い場合、燃料加熱器HT2からボイラー・エンジンに至る流路に残留した燃料は外気温度又は室内の温度に近づき(又は同等となり)、燃料の性状は保持できても燃料の状態(粘度)はボイラー・エンジンに適合できなくなる。
 そこで本システムは、装置の停止又は何らかの原因により燃料供給流路FSLの温度が低下して流路内に滞留する(流路内を流れる)燃料の温度が低下して燃料の粘度がボイラー・エンジンB&Eの燃料噴射装置に適さなくなった場合、燃料循環流路CL2に設置された燃料循環弁FCVを開くことにより、
燃料供給流路FSL内に滞留する(流路内を流れる)燃料はボイラー・エンジンB&Eの燃料噴射装置出口又はボイラー・エンジンの燃料噴射装置直前から燃料供給ポンプPM2の吸入側に導かれて、消費燃料流量計FM3から燃料供給ポンプPM2に至る流路と合流する燃料循環流路CL2を形成する。
燃料噴射ポンプPM2に吸入された燃料は、燃料噴射ポンプで加圧された後、燃料加熱器HT2で加熱され燃料濾過装置FL3を経てボイラー・エンジンの燃料噴射装置(又は燃料噴射装置の直前)に至り、再び燃料循環流路CL2を経て燃料供給ポンプPM2に吸入されることにより、
ボイラー・エンジンが停止している状態においても燃料の温度(粘度)をボイラー・エンジンの燃料噴射装置に適した温度(粘度)まで上昇させ、ボイラー・エンジンの起動時において助燃用燃料や助燃装置を必要としない構造と機能を備えている。
Specifically, during normal operation, the fuel circulation valve FCV is closed so that the fuel does not flow into the fuel circulation channel CL2, but flows out from the outlet provided at the upper level of the raw material supply tank TK2 and consumed fuel All animal and vegetable oils or used lubricating oils supplied to the boiler engine B & E (through the fuel supply flow path FSL) through the flow meter FM3, fuel supply pump PM2, fuel heater TH2 and fuel filter FL3 are all boiler engines It is consumed.
However, in this supply system, even if the outside air temperature or the temperature in the room where the fuel supply system and fuel supply system using animal and vegetable oil and used lubricating oil are installed is short, even for a short time, fuel heater HT2 The fuel remaining in the flow path leading to the boiler engine approaches (or becomes equivalent to) the outside air temperature or the temperature in the room, and although the fuel properties can be maintained, the fuel state (viscosity) becomes incompatible with the boiler engine.
Therefore, in the present system, the temperature of the fuel supply channel FSL is lowered due to the shutdown of the apparatus or for some reason, the temperature of the fuel stagnated in the channel (flows in the channel) is lowered, and the viscosity of the fuel is If it becomes unsuitable for the B & E fuel injection system, by opening the fuel circulation valve FCV installed in the fuel circulation channel CL2,
The fuel staying in the fuel supply flow path FSL (flowing in the flow path) is led to the suction side of the fuel supply pump PM2 from immediately before the fuel injection device outlet of the boiler engine B & E or the fuel injection device of the boiler engine A fuel circulation channel CL2 is formed which merges with the flow channel from the fuel flow meter FM3 to the fuel supply pump PM2.
The fuel drawn into the fuel injection pump PM2 is pressurized by the fuel injection pump and then heated by the fuel heater HT2 and passes through the fuel filter FL3 to the fuel injection device of the boiler engine (or just before the fuel injection device) As a result, the fuel is again drawn into the fuel supply pump PM2 through the fuel circulation channel CL2.
Even when the boiler engine is stopped, the temperature (viscosity) of the fuel is raised to the temperature (viscosity) suitable for the fuel injection device of the boiler engine, and the auxiliary fuel and auxiliary device are activated when the boiler engine starts. It has structures and functions that you do not need.
TK1 原料貯蔵タンク
TK2 原料供給タンク
HT1 原料加熱器
HT2 燃料加熱器 
CSP 遠心分離機
FL1 濾過器
FL2 原料濾過装置
FL3 燃料濾過装置
CTR コントローラ
PM1 原料循環ポンプ
PM2 燃料供給ポンプ
FM1 原料流量計
FM2 循環原料流量計
FM3 消費燃料流量計
CV1 循環原料流量調整弁
CV2 バイパス燃料流量調整弁
FCV 燃料循環弁
CSV 遠心分離機バイパス弁
EV1 原料濾過装置出口用電磁弁
EV2 燃料濾過装置入口用電磁弁
EV3 原料供給タンク高位電磁弁
EV4 原料供給タンク中位電磁弁
DV1 原料貯蔵タンクドレン弁
DV2 原料供給タンクドレン弁
PS1 原料濾過装置出口圧力センサー
PS2 燃料濾過装置入口圧力センサー
PS3 燃料濾過装置出口圧力センサー
LS1 燃料貯蔵タンクレベルセンサー
LS2 燃料供給タンクレベルセンサー
CL1-1 原料供給流路
CL1-2, CL1 原料循環流路
FSL 燃料供給流路
CL2 燃料循環流路
B&E ボイラー・エンジン
TK1 Raw material storage tank
TK2 Raw material supply tank
HT1 Raw material heater
HT2 fuel heater
CSP centrifuge
FL1 filter
FL2 Raw material filter
FL3 fuel filter
CTR controller
PM1 Raw material circulation pump
PM2 fuel supply pump
FM1 Raw material flow meter
FM2 circulating material flow meter
FM3 Fuel Consumption Flowmeter
CV1 Circulating material flow control valve
CV2 bypass fuel flow control valve
FCV fuel circulation valve
CSV centrifuge bypass valve
EV1 Solenoid valve for outlet of raw material filter
EV2 Solenoid valve for fuel filter inlet
EV3 Raw material supply tank high level solenoid valve
EV4 material supply tank middle solenoid valve
DV1 Raw material storage tank drain valve
DV2 Raw material supply tank drain valve
PS1 Raw material filter outlet pressure sensor
PS2 fuel filter inlet pressure sensor
PS3 fuel filter outlet pressure sensor
LS1 Fuel Storage Tank Level Sensor
LS2 Fuel supply tank level sensor
CL1-1 Raw material supply flow path
CL1-2, CL1 Raw material circulation channel
FSL fuel supply channel
CL2 Fuel circulation channel
B & E boiler engine

Claims (6)

  1.  再生可能エネルギーである動植物性油やリサイクルエネルギーである使用済み潤滑油を原料として、濾過、加熱、遠心分離、沈殿及び加圧という物理的手法のみを用いて燃料化する燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法であって、
    濾過器を備え保温された原料貯蔵タンクと、それに隣接されて原料貯蔵タンクへのオーバーフロー機構を備えるとともに保温された原料供給タンク、濾過装置、加熱器、遠心分離機、沈殿システム、コントローラ及びそれらの機器の間に設置されたポンプ、流量計、流量調整弁、電磁弁、ドレン弁、レベルセンサー及び圧力センサーから構成され、
    濾過器を経て原料貯蔵タンク内に貯蔵された動植物油又は使用済み潤滑油は、原料貯蔵タンクの下位レベルに設置された取出口から流出し、原料濾過装置、原料循環ポンプ、原料加熱器、遠心分離機、原料流量計を経て原料供給タンク内に設置された導入管により原料供給タンク内の下部位置に導かれて流出した後、
    その一部は、原料供給タンクの下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれて、原料濾過装置から原料循環ポンプに至る流路と合流して、原料循環ポンプ,原料加熱器、遠心分離機、原料流量計を経て再び原料供給タンクに戻る原料循環経路を形成することにより連続して加熱、遠心分離、沈殿を繰り返し、
    その一部は、原料供給タンクからオーバーフローして(溢れ出て)原料貯蔵タンクに流入することにより、原料供給タンクは常にフルレベル(満杯)の状態に保たれ、原料加熱器によって加熱された原料が原料貯蔵タンクと原料供給タンクに連続的に供給されることにより、保温されたそれぞれのタンクは加熱装置を必要としなくなるとともに、
    残りは、原料供給タンクの上位レベルに設置された取出口から流出して、消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに供給され、
    燃料供給ポンプにバイパス流路を設けてその途中に燃料供給ポンプのバイパス燃料流量調整弁を設けることにより、ボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定できるという構造と機能を持つとともに、
    ボイラー・エンジンの燃料噴射装置出口又はその直前から燃料供給ポンプの吸入側に導かれて、消費燃料流量計から燃料供給ポンプに至る流路と合流する燃料循環流路を設けるとともに、その途中に燃料循環弁を設置することにより、ボイラー・エンジンの起動時に助燃用燃料などを必要としないという構造と機能を持つ、動植物油又は使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法。
    Fuel production equipment and fuel supply system that uses only physical methods such as filtration, heating, centrifugation, sedimentation and pressurization to convert fuel from renewable energy, such as animal and vegetable oil that is renewable energy and used lubricating oil that is recycled energy, as a raw material And a fuel production / supply method using it,
    An insulated raw material storage tank provided with a filter and an overflow mechanism adjacent to it and provided with an overflow mechanism to the raw material storage tank, and an insulated raw material supply tank, a filter, a heater, a centrifuge, a precipitation system, a controller and the like It consists of a pump, flow meter, flow control valve, solenoid valve, drain valve, level sensor and pressure sensor installed between the equipment,
    The animal or vegetable oil or the used lubricating oil stored in the raw material storage tank via the filter flows out from the outlet provided at the lower level of the raw material storage tank, and is used as a raw material filter, raw material circulation pump, raw material heater, centrifugal After being led to the lower position in the raw material supply tank by the introduction pipe installed in the raw material supply tank through the separator and the raw material flow meter, it flows out,
    Part of it flows out from the outlet installed at the lower level of the feed tank, is led to the suction side of the feed circulation pump through the circulating feed flow meter and the circulation feed flow control valve, and the feed is circulated from the feed filtration device. Consecutive heating, centrifugal separation, precipitation by forming a raw material circulation path that joins the flow path leading to the pump, passes through the raw material circulation pump, the raw material heater, the centrifuge, and the raw material flow meter and returns to the raw material supply tank again. Repeat
    The raw material supply tank is always kept at full level (full) by partially overflowing from the raw material supply tank and flowing into the raw material storage tank, the raw material heated by the raw material heater Is continuously supplied to the raw material storage tank and the raw material supply tank, so that each heated tank does not need a heating device.
    The remainder flows out of the outlet installed at the upper level of the feed tank, and is supplied to the boiler engine through the fuel consumption flow meter, the fuel supply pump, the fuel heater, and the fuel filter.
    A structure in which the pressure of fuel supplied to the boiler / engine can be set to a relatively high pressure (for example, 0.5 MPa) by providing a bypass flow passage in the fuel supply pump and providing a bypass fuel flow control valve for the fuel supply pump in the middle thereof. Along with
    A fuel circulation passage is provided which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler or engine or immediately before that, and a fuel circulation passage joining with the passage from the consumed fuel flow meter to the fuel supply pump is provided A fuel production system and fuel supply system using animal and vegetable oil or used lubricating oil as a raw material and having a structure and a function that does not require auxiliary fuel or the like when the boiler or engine starts by installing a circulation valve Fuel production and supply method used.
  2.  原料貯蔵タンクの下位レベルに設置された取出口から流出し、原料濾過装置、原料循環ポンプ、原料加熱器、遠心分離機及び原料流量計を経て原料供給タンクに至る動植物油又は使用済み潤滑油と、
    原料供給タンクの下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれて、原料濾過装置から原料循環ポンプに至る流路と合流した動植物油又は使用済み潤滑油は、
    燃料供給タンク内に設置された導入管によりタンク内の下部位置に導かれて流出し、
     動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は流出口から下方へ向かって移動し、そのほとんどは原料供給タンク下位レベルに設置された取出口から流出し、循環原料流量計、循環原料流量調整弁を経て、原料濾過装置から原料循環ポンプに至る流路と合流するとともに、その一部はタンク底部に滞留し、
     残りは原料供給タンク内を上方に向かって移動し、そのほとんどは原料供給タンクの上位レベルに設置された取出口から流出して消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至るとともに、その一部は原料供給タンクからオーバーフローして原料貯蔵タンクに至るという過程を連続的に繰り返すことにより、原料供給タンクの上位レベルに設置された取出口から流出してボイラー・エンジンに至る
    動植物油又
    は使用済み潤滑油は、原料供給タンクにおいて効果的な沈殿が繰り返し行なわれることによりボイラー・エンジンに使用可能な性状に改質されるとともに、
    動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は原料供給タンク底部に蓄積され、
     原料供給タンク底部に設置されたドレン弁を開けることにより、タンク底部に蓄積された動植物油又は使用済み潤滑油中に含まれる金属や鉱物及び微小な夾雑物等の油分よりも密度が大きな物質や水分は、動植物油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムから除去されるという機能を持つことを特徴とする請求項1記載の動植物性油及び使用済み潤滑油を原料とする燃料製造置及び燃料供給システムとそれを用いた燃料製造・供給方法。
    An animal or vegetable oil or used lubricating oil which flows out from the outlet installed at the lower level of the raw material storage tank, passes through the raw material filter, raw material circulation pump, raw material heater, centrifuge and raw material flow meter to the raw material supply tank. ,
    It flows out from the outlet installed at the lower level of the feed tank, is led to the suction side of the feed circulation pump through the feedthrough flow meter and circulating feed flow control valve, and the flow path from the feed filtration device to the feed circulation pump Animal or vegetable oil or used lubricating oil combined with
    The feed pipe installed in the fuel supply tank leads to the lower position in the tank and flows out,
    Substances and water with a density higher than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils or used lubricating oils, move downward from the outlet, mostly at the lower level of the feed tank. It flows out from the installed outlet, passes through the circulating feed flow meter and circulating feed flow control valve, joins with the flow path from the feed filtration device to the feed circulation pump, and a part of it stays in the bottom of the tank,
    The remainder move upward in the feed tank, and most of them flow out from the outlet located at the upper level of the feed tank, and the fuel consumption flow meter, fuel feed pump, fuel heater and fuel filter As it passes through the boiler engine, part of it overflows from the raw material supply tank and continues to the raw material storage tank, and it flows out from the outlet provided at the upper level of the raw material supply tank. The animal or vegetable oil or the used lubricating oil leading to the boiler engine is reformed into properties usable for the boiler engine by repeated effective precipitation in the feed tank.
    Substances and water with a density greater than oil, such as metals, minerals, and minute contaminants contained in animal and vegetable oils or used lubricating oils, are accumulated at the bottom of the feed tank,
    By opening the drain valve installed at the bottom of the raw material supply tank, substances or materials with a density greater than oil, such as metals, minerals, and minute contaminants contained in the animal and vegetable oil accumulated in the tank bottom or used lubricating oil The animal and vegetable oil and the used lubricating oil according to claim 1, wherein the water has a function of being removed from a fuel production apparatus and a fuel supply system using the animal and vegetable oil and the used lubricating oil as a raw material. Fuel production system and fuel supply system, and fuel production / supply method using the same.
  3. 原料貯蔵タンクの下位レベルに設置された取出口から流出して原料濾過装置を経て原料循環ポンプに至る動植物油又は使用済み潤滑油の流量を、
    原料供給タンクの上位レベルに設置された取出口から流出して、消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至る動植物油又は使用済み潤滑油の流量よりも多く(例えば1.5倍)なるように設定するとともに、
    原料供給タンクの下位レベルに設置された取出口から流出して循環原料流量計、循環原料流量調整弁を経て原料循環ポンプの吸入側に導かれ、原料濾過装置から原料循環ポンプに至る流路と合流する動植物油又は使用済み潤滑油の流量を、
    原料供給タンクの上位レベルに設置された取出口から流出して消費燃料流量計、燃料供給ポンプ、燃料加熱器、燃料濾過装置を経てボイラー・エンジンに至る動植物油又は使用済み潤滑油の流量と等しくなるように設定することにより、
    動植物油又は使用済み潤滑油は原料供給タンクから常時オーバーフローして(溢れ出て)原料貯蔵タンクに至り、原料供給タンクは常にフルレベル(満杯)の状態となるとともに、
    原料加熱器によって加熱された動植物油又は使用済み潤滑油が原料貯蔵タンクと原料供給タンクに連続的に供給されることにより、
    動植物油又は使用済み潤滑油を原料貯蔵タンクから原料供給タンクに移送する際の動力、配管及び原料供給タンクの液面制御を必要としなくなるとともに、
    原料貯蔵タンク及び原料供給タンクを直接加熱することなくその温度を比較的高温(例えば50℃以上)に保持し、これにより両タンクにおける沈殿作用を促進させることができることを特徴とする請求項1又は2記載の動植物性油及び使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法。
    The flow rate of the animal or vegetable oil or the used lubricating oil which flows out from the outlet provided at the lower level of the raw material storage tank, passes through the raw material filter and reaches the raw material circulation pump,
    From the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet installed at the upper level of the raw material supply tank and passes through the consumed fuel flow meter, fuel supply pump, fuel heater, and fuel filter to the boiler engine As well as (for example, 1.5 times)
    It flows out from the outlet installed at the lower level of the raw material supply tank and is led to the suction side of the raw material circulation pump through the circulating raw material flow meter and circulating raw material flow control valve, and the flow path from the raw material filtration device to the raw material circulation pump The flow rate of the combined animal and vegetable oil or used lubricating oil,
    Equal to the flow rate of animal or vegetable oil or used lubricating oil that flows out from the outlet located at the upper level of the feed tank through the consumed fuel flow meter, fuel feed pump, fuel heater, and fuel filter to the boiler engine By setting to be
    The animal or vegetable oil or the used lubricating oil constantly overflows (overflows) from the raw material supply tank and reaches the raw material storage tank, and the raw material supply tank is always at full level (full).
    By continuously supplying the raw material storage tank and the raw material supply tank with the animal and vegetable oil or the used lubricating oil heated by the raw material heater,
    There is no need for motive power for transferring animal and vegetable oil or used lubricating oil from the raw material storage tank to the raw material supply tank, and control of the level of piping and raw material supply tank,
    The raw material storage tank and the raw material supply tank can be maintained at a relatively high temperature (for example, 50 ° C. or higher) without direct heating, whereby the sedimentation in both tanks can be promoted. The fuel manufacturing apparatus and fuel supply system which use the animal and vegetable oil and the used lubricating oil as 2 raw materials as a raw material, and a fuel manufacturing and supply method using the same.
  4.  原料貯蔵タンクの下位レベルに設置された取出口から流出して原料濾過装置を経て原料循環ポンプに至る動植物油又は使用済み潤滑油の流量が、原料供給タンクの上位レベルに設置された取出口から流出してボイラー・エンジンに至る動植物油又は使用済み潤滑油の流量よりも少なくなり、原料供給タンクから原料貯蔵タンクへのオーバーフローが途絶えて、原料供給タンクの油面が低下した場合、
    原料供給タンクに設置したレベルセンサーによりこれを検知して警報を発し、
    原料供給タンク中位レベルに設置された取出口から流出して、消費燃料流量計から燃料供給ポンプに至る流路に合流する流路の途中に設置された電磁弁を、閉じた状態から開いた状態に切り替えるとともに、
    原料供給タンク上位レベルに設置された取出口から流出して、消費燃料流量計に至る流路に設置された電磁弁を、開いた状態から閉じた状態に切り替えることにより、
    原料供給タンクの液面が、原料供給タンク中位レベルに設置された取出口に至る前にボイラー・エンジンを停止する等の燃料供給システムの安全に関する動作を行う機能を持たせることができることを特徴とする、請求項1~3のいずれか1項記載の動植物油又は使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供
    給方法。
    The flow rate of the animal or vegetable oil or used lubricating oil that flows out from the outlet provided at the lower level of the raw material storage tank and passes through the raw material filter to the raw material circulation pump is from the outlet provided at the upper level of the raw material supply tank. When the flow rate of the animal oil or used lubricating oil flowing down to the boiler engine is less than that of the raw material supply tank, the overflow from the raw material supply tank to the raw material storage tank stops, and the oil level of the raw material supply tank decreases.
    This is detected by the level sensor installed in the raw material supply tank and an alarm is issued,
    The solenoid valve installed in the middle of the flow path that flows out from the outlet installed at the medium level of the raw material supply tank and joins the flow path from the consumed fuel flow meter to the fuel supply pump was opened from the closed state While switching to the state,
    By switching from an open state to a closed state a solenoid valve installed in the flow path that flows out of the outlet installed at the upper level of the raw material supply tank and reaches the fuel consumption flow meter.
    It is characterized in that it is possible to have the function of performing safety-related operations of the fuel supply system such as stopping the boiler and engine before the liquid level of the raw material supply tank reaches the outlet set at the medium level of the raw material supply tank. A fuel production apparatus and a fuel supply system using the animal and vegetable oil or the used lubricating oil according to any one of claims 1 to 3 as a raw material, and a fuel production / supply method using the same.
  5. 燃料供給ポンプにバイパス流路を設けてその途中にバイパス燃料流量調整弁を設置し、燃料供給ポンプをバイパスする燃料の流量を調整してボイラー・エンジンに供給する燃料の圧力を比較的高圧(例えば0.5MPa)に設定することにより、
    ボイラー・エンジンの燃料噴射装置に比較的高圧の燃料を供給し、燃料油の粘度をA重油や軽油と同程度まで低下させることなく(燃料油温度を上昇させることなく)燃料噴射装置が良好な作動を行うことができるような機能を備えることを特徴とする、請求項1~4のいずれか1項記載の動植物油又は使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法。
    A fuel supply pump is provided with a bypass flow path, a bypass fuel flow control valve is installed in the middle thereof, the flow rate of fuel bypassing the fuel supply pump is adjusted, and the pressure of fuel supplied to the boiler / engine is relatively high (for example, By setting to 0.5MPa)
    A relatively high-pressure fuel is supplied to the fuel injection device of the boiler engine, and the fuel injection device is good without lowering the viscosity of the fuel oil to the same extent as A heavy oil or light oil (without raising the fuel oil temperature) A fuel production apparatus and fuel supply system using an animal and vegetable oil or a used lubricating oil as claimed in any one of claims 1 to 4, characterized in that it has a function capable of performing operation. Fuel production and supply method used.
  6. ボイラー・エンジンの燃料噴射装置出口又はその直前から燃料供給ポンプの吸入側に導かれて、消費燃料流量計から燃料供給ポンプに至る流路と合流する燃料循環流路を設けるとともに、燃料循環流路に燃料循環弁を設置することにより、
    ボイラー・エンジンの起動時又は停止時における燃料の温度(粘度)を燃料噴射装置に適した状態にするような構造と機能を有し、ボイラー・エンジンの起動時に助燃用燃料や助燃装置を必要としないことを特徴とする、請求項1~5のいずれか1項記載の動植物油又は使用済み潤滑油を原料とする燃料製造装置及び燃料供給システムとそれを用いた燃料製造・供給方法。
    A fuel circulation passage is provided which is led to the suction side of the fuel supply pump from the fuel injection device outlet of the boiler or engine or just before that, and merges with the passage from the consumed fuel flow meter to the fuel supply pump By installing a fuel circulation valve on the
    It has the structure and function to make the temperature (viscosity) of the fuel at the start or stop of the boiler engine suitable for the fuel injection device, and it is necessary to use the auxiliary fuel or auxiliary device at the start of the boiler engine. A fuel production apparatus and a fuel supply system using the animal and vegetable oil or the used lubricating oil according to any one of claims 1 to 5 as a raw material, and a fuel production / supply method using the same.
PCT/JP2018/026221 2017-07-17 2018-07-11 Fuel production apparatus using animal and vegetable oils and used lubricants as raw materials, fuel supply system, and fuel production and supply method using same WO2019017259A1 (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021124443A1 (en) * 2019-12-17 2021-06-24 株式会社Ihi原動機 Power-generation system

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007161974A (en) * 2005-12-13 2007-06-28 Hirokuni Ijuin Method for producing fuel for diesel engines using edible oil, waste edible oil therefrom, or mixture of edible oil or waste edible oil therefrom and waste petroleum lubricating oil and system for obtaining electricity via stable running of diesel generator using the produced fuel
JP2007284511A (en) * 2006-04-14 2007-11-01 Nippon Biodiesel Fuel Co Ltd Method for refining vegetable fat or oil or animal fat or oil into fuel and device for refining the same
JP2011001416A (en) * 2009-06-17 2011-01-06 Bufa Concrete Protection Japan Kk Method and apparatus for treating waste edible oil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007161974A (en) * 2005-12-13 2007-06-28 Hirokuni Ijuin Method for producing fuel for diesel engines using edible oil, waste edible oil therefrom, or mixture of edible oil or waste edible oil therefrom and waste petroleum lubricating oil and system for obtaining electricity via stable running of diesel generator using the produced fuel
JP2007284511A (en) * 2006-04-14 2007-11-01 Nippon Biodiesel Fuel Co Ltd Method for refining vegetable fat or oil or animal fat or oil into fuel and device for refining the same
JP2011001416A (en) * 2009-06-17 2011-01-06 Bufa Concrete Protection Japan Kk Method and apparatus for treating waste edible oil

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2021124443A1 (en) * 2019-12-17 2021-06-24 株式会社Ihi原動機 Power-generation system

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