WO2011021473A1 - Dispositif de production d'un carburant en émulsion - Google Patents

Dispositif de production d'un carburant en émulsion Download PDF

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Publication number
WO2011021473A1
WO2011021473A1 PCT/JP2010/062348 JP2010062348W WO2011021473A1 WO 2011021473 A1 WO2011021473 A1 WO 2011021473A1 JP 2010062348 W JP2010062348 W JP 2010062348W WO 2011021473 A1 WO2011021473 A1 WO 2011021473A1
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WO
WIPO (PCT)
Prior art keywords
water
oil
emulsion fuel
flow path
mixer
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PCT/JP2010/062348
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English (en)
Japanese (ja)
Inventor
義忠 曽根
薫 廣瀬
Original Assignee
株式会社フォーライフ
有限会社三星機工
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Filing date
Publication date
Application filed by 株式会社フォーライフ, 有限会社三星機工 filed Critical 株式会社フォーライフ
Publication of WO2011021473A1 publication Critical patent/WO2011021473A1/fr

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/328—Oil emulsions containing water or any other hydrophilic phase
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/05—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste oils
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23K—FEEDING FUEL TO COMBUSTION APPARATUS
    • F23K5/00—Feeding or distributing other fuel to combustion apparatus
    • F23K5/02—Liquid fuel
    • F23K5/08—Preparation of fuel
    • F23K5/10—Mixing with other fluids
    • F23K5/12—Preparing emulsions

Definitions

  • the present invention relates to an apparatus for producing emulsion fuel by mixing water and waste oil with fuel oil such as heavy oil.
  • This “emulsion fuel production device” includes a static mixer that mixes water, fuel oil, and an emulsifier, a magnetic cascade pump that further mixes a liquid mixture from the static mixer and supplies emulsion fuel to the combustion device, and a magnetic cascade pump. And a feedback unit that recirculates part of the emulsion fuel from the downstream side to the upstream side.
  • the emulsion fuel produced by the “emulsion fuel production apparatus” described in Patent Document 1 has poor ignitability, when used in a combustion apparatus such as a heavy oil boiler, it is ignited using only A heavy oil at the start, After about several seconds, it is necessary to switch to emulsion fuel. Therefore, when used in a combustion device operated based on the ON-OFF control method, not only when the combustion device starts operating, but also every time it is restarted after stopping operation, an ignition operation using only A heavy oil and the subsequent emulsion Switching to fuel must be performed. For this reason, a new fuel switching mechanism, a complicated control method, etc. are needed, and it cannot be denied that the possibility of an ignition mistake at the time of re-ignition occurs.
  • the problem to be solved by the present invention is to provide an emulsion fuel production apparatus that has an extremely small and simple structure and can efficiently produce an emulsion fuel with good ignitability without using an emulsifier. is there.
  • the emulsion fuel production apparatus of the present invention comprises a mixer for mixing fuel oil, waste oil and water, a static mixer for emulsifying the mixture liquid fed from the mixer, and an emulsion flowing out from the static mixer A pump for sending fuel to a combustion device, and at least a pair of magnets facing each other across the axis of the static mixer is disposed on the outer periphery of the static mixer, and a part of the emulsion fuel sent from the pump A return flow path for flowing into the mixer is provided.
  • the fuel oil, waste oil and water mixture formed in the mixer is vigorously stirred and mixed by the internal elements in the process of flowing in the static mixer, and opposed to each other. Since the molecules are refined by passing through the magnetic field between the magnets formed, emulsification proceeds rapidly. Part of the emulsion fuel generated by flowing in the static mixer passes through the return flow path and flows into the mixer, and then emulsifies by passing through the circulation flow path passing through the static mixer and pump again. Progresses dramatically. Therefore, an emulsion fuel with good ignitability can be efficiently produced without using an emulsifier.
  • the circulation flow path formed by providing the return flow path is utilized, the emulsification proceeds while the mixed liquid of fuel oil, waste oil and water is circulated between the mixer, the static mixer and the pump.
  • a large-scale mixing device, a stirring device, a large-capacity storage tank or the like is not necessary, and an extremely small and simple structure can be achieved.
  • a fuel oil or kerosene can be used as the fuel oil, and edible oil waste oil, machine oil waste oil, or the like can be used as the waste oil.
  • the mixer includes a combined flow path in which a liquid can flow in one direction, a fuel oil inflow path and a waste oil inflow path for individually supplying fuel oil, waste oil, and water that are continuously supplied to the combined flow path. And a water inflow channel.
  • the fuel oil inflow path, the waste oil inflow path, and the water inflow path are arranged so as to communicate obliquely with respect to the combined flow path.
  • the fuel oil inflow path, the waste oil inflow path, and the water inflow path are communicated in this order from the upstream side to the downstream side of the combined flow path.
  • an emulsion fuel production apparatus that has an extremely small and simple structure and can efficiently produce an emulsion fuel having good ignitability without using an emulsifier.
  • FIG. 1 It is the schematic which shows the structure of the emulsion fuel manufacturing apparatus which is embodiment of this invention. It is a partial cross section figure of the water tank which comprises the emulsion fuel manufacturing apparatus shown in FIG. It is sectional drawing of the mixer which comprises the emulsion fuel manufacturing apparatus shown in FIG. FIG. 2 is a partially omitted perspective view of a static mixer constituting the emulsion fuel production apparatus shown in FIG. 1.
  • A) is a cross-sectional view taken along line AA in FIG. 4, and
  • (b) is a cross-sectional view taken along line BB in (a).
  • FIG. 1 shows a cross-sectional view taken along line AA in FIG. 4
  • Emulsion fuel manufacturing apparatus 11 Water tank 12 Heavy oil tank 13 Waste oil tank 11a, 12a, 13a Drain valve 14, 15 Mixer 14a, 15a Combined flow path 16 Static mixer main body 16x, 16y, 16z Static mixer 16a Casing 16b, 16c Opening 16d Right element 16e Left element 17 Main flow path 18 Combustion device 19 Return flow path 20 Solenoid valve 21 Check valve 22 Waste oil flow path 22p Waste oil inflow path 23 Water flow path 23p Water inflow path 24, 24a, 24b Heavy oil flow path 24ap, 24bp Heavy oil inflow Path 25 On-off valve 26 Supply flow path 31 Water supply pipe 31a, 32a, 34a Opening 32 Oil supply pipe 33 Spherical body 34 Guide pipe 35 Filter 36 Mounting member 37 Mounting hole F Heavy oil M Magnet S Liquid surface W Water X Shaft center
  • the emulsion fuel production apparatus 10 of the present embodiment includes a water tank 11 that stores water supplied via a water supply pipe 31, and a heavy oil that stores heavy oil supplied via an oil supply pipe 32.
  • Three pairs of magnets M are arranged on the outer periphery of the static mixers 16x, 16y, and 16z along the respective longitudinal directions.
  • Solenoid valve 20 and check valve 21 are arranged in this order in water flow path 23 and heavy oil flow paths 24, 24 a and 24 b from water tank 11 and heavy oil tank 12 to mixers 14 and 15, respectively, and mixed with waste oil tank 13.
  • a waste oil passage 22 is provided between the container 14 and the container 14.
  • drain valves 11a, 12a, and 13a are provided below the water tank 11, the heavy oil tank 12, and the waste oil tank 13, respectively.
  • the main flow path 17 on the downstream side of the pump P is provided with an on-off valve 25 for supplying and stopping the emulsion fuel to the combustion device 18.
  • the internal structure of the water tank 11 and the heavy oil tank 12 is the same, and the opening part 31a (32a) of the lower end of the water supply pipe 31 (oil supply pipe 32) is in the water tank 11 (heavy oil tank 12). It is piped so as to be positioned above, and a guide tube 34 is connected to the outer periphery of the opening 31a (32a).
  • a spherical body 33 that opens and closes an opening 31 a (32 a) of the water supply pipe 31 (oil supply pipe 32) is housed in the guide pipe 34 so as to be movable up and down, and the opening 34 a at the lower end of the guide pipe 34 has water permeability (permeability).
  • An oily filter 35 is provided.
  • the spherical body 33 moves up and down in the guide tube 34 in accordance with the elevation of the liquid level S of the water W (heavy oil F) in the water tank 11 (heavy oil tank 12). By doing so, the opening part 31a (32a) of the lower end of the water supply pipe 31 (oil supply pipe 32) is opened and closed. That is, when the level S of the water W (heavy oil F) in the water tank 11 (heavy oil tank 12) falls, the spherical body 33 descends and the opening 31a (32a) at the lower end of the water supply pipe 31 (oil supply pipe 32) is formed.
  • water W (heavy oil F) is supplied from the water supply pipe 31 (oil supply pipe 32) into the water tank 11 (heavy oil tank 12), and the liquid of the water W (heavy oil F) in the water tank 11 (heavy oil tank 12).
  • the surface S rises to a predetermined position, the spherical body 33 rises, the opening 31a (32a) at the lower end of the water supply pipe 31 (oil supply pipe 32) is closed, and the water tank 11 (heavy oil) from the water supply pipe 31 (oil supply pipe 32).
  • the supply of water W (heavy oil F) into the tank 12) is stopped. Thereby, the liquid level S of the water W (heavy oil F) in the water tank 11 (heavy oil tank 12) is maintained at a constant height.
  • the mixers 14 and 15 are arranged in series in this order from upstream to downstream of the main flow path 17.
  • a heavy oil passage 24a is connected to the upstream side of the mixer 14, and a waste oil passage 22 is connected to the downstream side.
  • a heavy oil passage 24b is connected to the upstream side of the mixer 15, and a water passage 23 is connected to the downstream side.
  • straight tubular joint channels 14 a and 15 a connected in series to the main channel 17 are provided in the mixers 14 and 15, respectively.
  • a heavy oil inflow passage 24ap and a waste oil inflow passage 22p are formed in the mixer 14 so as to communicate the heavy oil passage 24a, the waste oil passage 22 and the combined flow passage 14a.
  • 24b, a heavy oil inflow passage 24bp and a water inflow passage 23p are formed to communicate the water passage 23 and the combined passage 15a.
  • the heavy oil flow path 24a communicates with the upstream side of the combined flow path 14a
  • the waste oil flow path 22 communicates with the downstream side of the combined flow path 14a
  • the heavy oil flow path 24b communicates with the upstream side of the combined flow path 15a
  • the combined flow path 15a communicates with the water channel 23.
  • the heavy oil flow path 24p, the waste oil flow path 22p, the heavy oil flow path 24p, and the water flow path 23p communicate with each other in an inclined state of about 75 degrees (acute angle) with respect to the axial center of the combined flow paths 14a and 15a. That is, the downstream sides of the heavy oil inflow passage 24ap, the waste oil inflow passage 22p, the heavy oil inflow passage 24bp, and the water inflow passage 23p are inclined in the direction of going to the downstream side of the main flow passage 17, respectively. Since the inclination angle is not limited, it can be changed within a range of about 80 to 70 degrees according to the use conditions.
  • the heavy oil inflow path 24ap the waste oil inflow path 22p, the heavy oil inflow path 24bp, and the water inflow path 23p
  • the heavy oil inflow path 24ap, the waste oil inflow path 22p, and the heavy oil inflow path 24bp have substantially the same inner diameter, but the water flow path 23p. Is set smaller than the inner diameters of the oil inflow passage 24ap, the waste oil inflow passage 22p, and the heavy oil inflow passage 24bp.
  • the static mixers 16x, 16y, and 16z will be described with reference to FIGS.
  • the static mixers 16x, 16y, and 16z are arranged in series along the flow of the main flow path 17 in this order.
  • the static mixers 16x and 16z have a structure in which three pairs of magnets M are arranged along the longitudinal direction of the outer periphery of the static mixer main body 16 shown in FIG. 6, and the static mixer 16y has a structure as shown in FIG. It consists only of the static mixer body 16.
  • the static mixer body 16 includes two types of right elements 16d, having different twist directions along the axial direction in a cylindrical casing 16a having openings 16b, 16c at both ends.
  • the left elements 16e are alternately arranged.
  • Each of the right element 16d and the left element 16e has a shape in which a rectangular plate material is twisted 180 degrees, and the directions of twist are left-handed and right-handed respectively.
  • the static mixers 16x and 16z in the static mixers 16x and 16z, three pairs of magnets M facing each other with the axis X of the static mixer body 16 therebetween are arranged on the outer periphery of the static mixer body 16.
  • the three pairs of magnets M are arranged along the longitudinal direction (axial center X direction) of the static mixer body 16, and each magnet M is arranged on the same straight line parallel to the axial center X.
  • the opposing magnets M are arranged such that different polarities (N pole and S pole) face each other across the axis X.
  • the opposing magnets M can be arranged so that the same poles (N poles or S poles) face each other.
  • the three pairs of magnets M in the static mixers 16x and 16z are fixed via a pair of attachment members 36, respectively.
  • the flat mounting member 36 is provided with three mounting holes 37, and magnets M are fitted into the three mounting holes 37, respectively.
  • the two attachment members 36 into which the magnets M are fitted are arranged so as to be parallel to each other with the static mixer body 16 interposed therebetween, and are fixed by winding an adhesive tape (not shown) around them.
  • the fixing means is not limited to this.
  • the attachment member 36 is made of a wood material, but other materials that do not affect the magnetic lines of force of the magnet M (for example, a synthetic resin material, a paper material, an inorganic material, etc.) can also be employed.
  • the mixture of heavy oil, waste oil and water formed in the mixers 14 and 15 flows in order in the static mixers 16x, 16y and 16z.
  • the mixed liquid flowing from the opening 16b toward the other opening 16c is vigorously stirred and mixed by the dividing action, the converting action and the reversing action of the right element 16d and the left element 16e in the casing 16a, and the emulsification proceeds.
  • the static mixers 16x and 16z when the mixed solution passes through the magnetic field between the magnets M arranged opposite to each other with the axis X interposed therebetween, the emulsification rapidly proceeds and passes through the last static mixer 16z.
  • the pump P When the emulsion fuel production apparatus 10 is operated, the pump P is operated with the on-off valve 25 disposed at the most downstream side of the main flow path 17 closed, and the solenoid valve 20 and the check valve 21 are opened.
  • the water passes through the solenoid valve 20 and the check valve 21 along the water flow path 23 and is fed into the mixer 15.
  • the heavy oil in the heavy oil tank 12 flows into the solenoid valve 20 along the heavy oil flow path 24, passes through the solenoid valve 20, is divided into two heavy oil flow paths 24 a and 24 b, and flows into the check valve 21. After passing through the check valve 21, it is fed into the mixers 14 and 15 via the heavy oil passages 24a and 24b, respectively. Waste oil in the waste oil tank 13 is sent to the mixer 14 via the waste oil passage 22.
  • the on-off valve 25 shown in FIG. 1 when the on-off valve 25 shown in FIG. 1 is opened, the emulsion fuel formed through the static mixer 16z flows out to the supply flow path 26, is sent to the combustion device 18 such as a boiler, and is used for combustion. . Since the emulsion fuel produced by the emulsion fuel production apparatus 10 has good ignitability, the operation of the combustion apparatus 18 can be started without using A heavy oil alone as the ignition fuel. Therefore, when the combustion device 18 is operated by ON-OFF control, a fuel switching mechanism, a complicated control method, and the like are not required.
  • a part of the emulsion fuel formed by passing through the mixers 14, 15, the static mixers 16 x, 16 y, 16 z and the pump P passes through the return flow path 19.
  • a circulation flow path is formed which again flows into the mixers 14 and 15 and passes through the static mixer 16 and the pump P.
  • the emulsion of the mixed solution jumps by passing through the static mixer 16 and the pump P a plurality of times. Therefore, the emulsion fuel can be efficiently produced without using an emulsifier.
  • the mixed liquid of fuel oil, waste oil and water is transferred between the mixers 14, 15, the static mixers 16 x, 16 y, 16 z and the pump P.
  • Emulsification is progressed while circulating in the tank, so that a large-scale mixing device, a stirring device or a large-capacity storage tank is not required, and an extremely small and simple structure can be achieved. Therefore, the existing heavy oil boiler, for example, a combustion apparatus such as a heating boiler for an agricultural vinyl house, can be easily used without newly remodeling or providing a large installation space.
  • the mixers 14 and 15 are combined oil flow channels 14a and 15a in which the liquid can flow in one direction, and heavy oil inflow for individually supplying continuously supplied fuel oil, waste oil and water to the combined flow channels 14a and 15a, respectively. Since the paths 24ap, 24bp, the waste oil inflow path 22p, and the water inflow path 23p are provided, the fuel oil, waste oil, and water can be mixed efficiently while avoiding the complexity of the structure.
  • the heavy oil inflow passages 24ap, 24bp, the waste oil inflow passage 22p, and the water inflow passage 23p are arranged so as to communicate obliquely with the combined flow paths 14a, 15a, so that the liquid flowing in the combined flow paths 14a, 15a in one direction. Fuel oil, waste oil, and water can be efficiently flowed into the combined flow paths 14a and 15a using the suction force generated by (mixed liquid).
  • the heavy oil inflow path 24ap, the waste oil inflow path 22p, the heavy oil inflow path 24bp, and the water inflow path 23p are communicated in order from the upstream side to the downstream side of the combined flow paths 14a and 15a, the specific gravity and viscosity are different. Three kinds of liquids (fuel oil, waste oil and water) can be easily mixed.
  • the emulsion fuel production apparatus 10 can produce an emulsion fuel of about 25 to 30 liters per minute while being an extremely small apparatus having a width of 450 mm ⁇ depth of 450 mm ⁇ height of 400 mm.
  • a check valve 21 is disposed on the downstream side of the solenoid valve 20 of the water flow path 23 and heavy oil flow paths 24, 24a and 24b from the heavy oil tank 12 to the mixers 14 and 15, respectively. Therefore, the mixed liquid and emulsion fuel passing through the mixers 14 and 15 do not flow back into the tanks 11, 12 and 13.
  • the emulsion fuel production apparatus 10 includes three static mixers 16x, 16y, and 16z, and three pairs of magnets M are arranged in each of the two static mixers 16x and 16z.
  • the present invention can be widely used as an apparatus for producing emulsion fuel that can be used in a combustion apparatus such as a boiler using fuel oil, waste oil and water as raw materials.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Feeding And Controlling Fuel (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

L'invention porte sur un dispositif de production d'un carburant en émulsion qui présente une structure extrêmement petite et simple et qui peut produire efficacement un carburant en émulsion qui possède une excellente propriété d'allumage sans utiliser d'agent émulsifiant. Un dispositif de production de carburant en émulsion (10) est composé d'une cuve à eau (11), d'une cuve à huile lourde (12) et d'une cuve à huile usée (13), qui contiennent respectivement de l'eau, de l'huile lourde et de l'huile usée ; une pluralité de mélangeurs (14, 15), agencés en série dans un passage principal (17) pour mélanger l'eau, l'huile lourde et l'huile usée fournies par les réservoirs (11, 12, 13) ; une pluralité de mélangeurs statiques (16x, 16y, 16z) qui sont agencés en série dans le passage principal (17) en aval du mélangeur (15) pour émulsifier un liquide mélangé formé par les mélangeurs (14, 15) ; et une pompe (P) qui fournit le carburant en émulsion formé par les mélangeurs statiques (16x, 16y, 16z), à un dispositif de combustion (18), et un passage de retour (19). Trois paires d'aimants (M) sont agencées sur la périphérie extérieure de chaque mélangeur statique (16x, 16y, 16z).
PCT/JP2010/062348 2009-08-19 2010-07-22 Dispositif de production d'un carburant en émulsion WO2011021473A1 (fr)

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JP2009-190445 2009-08-19
JP2009190445A JP4757335B2 (ja) 2009-08-19 2009-08-19 エマルジョン燃料製造装置

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015198231A1 (fr) * 2014-06-25 2015-12-30 Advanced Financial Services S.A. Dispositif et procédé pour obtenir des émulsions d'eau dans du fioul
US11015126B2 (en) 2016-12-30 2021-05-25 Eme International Limited Apparatus and method for producing biomass derived liquid, bio-fuel and bio-material
US11084004B2 (en) 2014-11-10 2021-08-10 Eme International Lux S.A. Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion
WO2023115113A1 (fr) * 2021-12-21 2023-06-29 Manuel Barreiro Système de conditionnement de combustible

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07144122A (ja) * 1993-11-26 1995-06-06 Mitsui Petrochem Ind Ltd 二液混合装置
JP2000329333A (ja) * 1999-05-14 2000-11-30 Kankyo Gijutsu Kenkyusho:Kk 合成燃料油生成装置
JP3111006U (ja) * 2005-04-04 2005-07-07 鐵夫 杉岡 燃料原液改質システム

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH03111006A (ja) * 1989-09-26 1991-05-10 Bon:Kk 額縁用枠材の開閉機構

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH07144122A (ja) * 1993-11-26 1995-06-06 Mitsui Petrochem Ind Ltd 二液混合装置
JP2000329333A (ja) * 1999-05-14 2000-11-30 Kankyo Gijutsu Kenkyusho:Kk 合成燃料油生成装置
JP3111006U (ja) * 2005-04-04 2005-07-07 鐵夫 杉岡 燃料原液改質システム

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015198231A1 (fr) * 2014-06-25 2015-12-30 Advanced Financial Services S.A. Dispositif et procédé pour obtenir des émulsions d'eau dans du fioul
US11084004B2 (en) 2014-11-10 2021-08-10 Eme International Lux S.A. Device for mixing water and diesel oil, apparatus and process for producing a water/diesel oil micro-emulsion
US11015126B2 (en) 2016-12-30 2021-05-25 Eme International Limited Apparatus and method for producing biomass derived liquid, bio-fuel and bio-material
WO2023115113A1 (fr) * 2021-12-21 2023-06-29 Manuel Barreiro Système de conditionnement de combustible

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JP2011079869A (ja) 2011-04-21
JP4757335B2 (ja) 2011-08-24

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