US2010186288A1PendingUtilityA1

Method for production of emulsion fuel and apparatus for production of the fuel

39
Assignee: NANOMIZER INCPriority: Sep 1, 2006Filed: Aug 31, 2007Published: Jul 29, 2010
Est. expirySep 1, 2026(~0.1 yrs left)· nominal 20-yr term from priority
B01F 23/40F23K 5/12C10L 1/32C10L 1/328
39
PatentIndex Score
0
Cited by
0
References
0
Claims

Abstract

Disclosed is an emulsion-type water-mixed fuel which is free from separating between an oil and a water, thereby being excellent in stability, has a high combustion efficiency, and an extremely high energy-saving effect. An emulsion fuel, in which an average diameter of the water or the combustible oil is 1,000 nm or less (more preferably, average diameter is 200 to 700 nm), is formed by finely-dividing and mixing the water and the combustible oil by a finely-dividing and mixing means, while adding 10.0 to 150.0 parts by volume of the water with respect to 100 parts by volume of the combustible oil (more preferably, 25.0 to 120.0 parts by volume of the water with respect to 100 parts by volume of the combustible oil). Further, the water to be used preferably has a reduction potential of −100 my or lower, more preferably −300 my or lower.

Claims

exact text as granted — not AI-modified
1 . A method for production of an emulsion fuel, comprising, while adding 10.0 to 150.0 parts by volume of a water with respect to 100 parts by volume of a combustible oil, finely-dividing and mixing the water and the combustible oil by a finely-dividing and mixing means, to thereby form an emulsion fuel in which an average diameter of the water or the combustible oil is 1,000 nm or less. 
   
   
       2 .- 15 . (canceled) 
   
   
       16 . A method for production of an emulsion fuel according to  claim 1 , wherein the finely-dividing and mixing means comprises an apparatus in which a primary mixture liquid including the water and the combustible oil is subjected to a pressure, and is finely-divided and mixed through a cavitation effect due to turbulence generated at one or two or more of orifices. 
   
   
       17 . A method for production of an emulsion fuel according to  claim 1 , wherein the finely-dividing and mixing means comprises an apparatus in which: a primary mixture liquid including the water and the combustible oil is subjected to a pressure to be caused to flow within a pump at a flow rate of 50 m/s or more; the primary mixture liquid is accelerated to pass into holes of a wall member having multiple holes each having a diameter of 500 μm or less formed therein; and is finely-divided and mixed through a cavitation effect due to turbulence between flows of the liquid. 
   
   
       18 . A method for production of an emulsion fuel according to  claim 1 , wherein the emulsion fuel, in which the average diameter of the water or the combustible oil is 200 to 700 nm, is formed by finely-dividing and mixing the water and the combustible oil by the finely-dividing and mixing means. 
   
   
       19 . A method for production of an emulsion fuel according to  claim 18 , wherein the finely-dividing and mixing means comprises an apparatus in which a primary mixture liquid including the water and the combustible oil is subjected to a pressure, and is finely-divided and mixed through a cavitation effect due to turbulence generated at one or two or more of orifices. 
   
   
       20 . A method for production of an emulsion fuel according to  claim 18 , wherein the finely-dividing and mixing means comprises an apparatus in which: a primary mixture liquid including the water and the combustible oil is subjected to a pressure to be caused to flow within a pump at a flow rate of 50 m/s or more; the primary mixture liquid is accelerated to pass into holes of a wall member having multiple holes each having a diameter of 500 μm or less formed therein; and is finely-divided and mixed through a cavitation effect due to turbulence between flows of the liquid. 
   
   
       21 . A method for production of an emulsion fuel according to  claim 1 , wherein the emulsion fuel, in which the average diameter of the water or the combustible oil is 200 to 700 nm, is formed by adding the combustible oil to the water having a reduction potential of −100 my or lower, and by finely-dividing and mixing the water and the combustible oil by the finely-dividing and mixing means. 
   
   
       22 . A method for production of an emulsion fuel according to  claim 21 , wherein the finely-dividing and mixing means comprises an apparatus in which a primary mixture liquid including the water and the combustible oil is subjected to a pressure, and is finely-divided and mixed through a cavitation effect due to turbulence generated at one or two or more of orifices. 
   
   
       23 . A method for production of an emulsion fuel according to  claim 21 , wherein the finely-dividing and mixing means comprises an apparatus in which: a primary mixture liquid including the water and the combustible oil is subjected to a pressure to be caused to flow within a pump at a flow rate of 50 m/s or more; the primary mixture liquid is accelerated to pass into holes of a wall member having multiple holes each having a diameter of 500 μm or less formed therein; and is finely-divided and mixed through a cavitation effect due to turbulence between flows of the liquid. 
   
   
       24 . A method for production of an emulsion fuel according to  claim 1 , wherein the water is one or two or more selected from a tap water for drinking, a rain water, a domestic waste water, an organic waste water, an industrial waste water, or a stockbreeding waste water. 
   
   
       25 . A method for production of an emulsion fuel according to  claim 1 , wherein the combustible oil is one kind or two or more kinds selected from: petroleum such as a heavy oil, a light oil, a lamp oil, and a volatile oil; an industrial waste oil; and cooking oils such as a tempura oil, a soybean oil, a sesame oil. 
   
   
       26 . A method for production of an emulsion fuel according to  claim 1 , wherein the combustible oil or the water, or the combustible oil and the water comprise(s) PCBs (polychlorinated biphenyl) or dioxins, or PCBs and dioxins. 
   
   
       27 . A method for production of an emulsion fuel according to  claim 26 , wherein the finely-dividing and mixing means comprises an apparatus in which a primary mixture liquid including the water and the combustible oil is subjected to a pressure, and is finely-divided and mixed through a cavitation effect due to turbulence generated at one or two or more of orifices. 
   
   
       28 . A method for production of an emulsion fuel according to  claim 26 , wherein the finely-dividing and mixing means comprises an apparatus in which: a primary mixture liquid including the water and the combustible oil is subjected to a pressure to be caused to flow within a pump at a flow rate of 50 m/s or more; the primary mixture liquid is accelerated to pass into holes of a wall member having multiple holes each having a diameter of 500 μm or less formed therein; and is finely-divided and mixed through a cavitation effect due to turbulence between flows of the liquid. 
   
   
       29 . An apparatus for production of an emulsion fuel, comprising: a water-combustible oil primary mixing means for primarily mixing a water and the combustible oil, while adding 10.0 to 150.0 parts by volume of the water with respect to 100 parts by volume of the combustible oil; and a finely-dividing and mixing means for finely-dividing and mixing a water-combustible oil-based primary mixture liquid obtained by the primary mixing means into a fine particle state, to thereby form an emulsion fuel in which an average diameter of the water or the combustible oil is 1,000 nm or less. 
   
   
       30 . An apparatus for production of an emulsion fuel according to  claim 29 , wherein a reduction potential of the water to be adopted is −100 my or lower. 
   
   
       31 . An apparatus for production of an emulsion fuel according to  claim 29 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to pass through one or two or more of small pores, and finely-divides and mixes through a cavitation effect due to turbulence generated at orifices. 
   
   
       32 . An apparatus for production of an emulsion fuel according to  claim 29 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to flow within a pump at a flow rate of 50 m/s or more; accelerates the water-combustible oil-based primary mixture liquid to pass into holes of a wall member having multiple holes each having a diameter of 200 μm or less formed therein; and finely-divides and mixes the water-combustible oil-based primary mixture liquid by causing a cavitation by turbulence generated by orifices between flows of the liquid. 
   
   
       33 . An apparatus for production of an emulsion fuel according to  claim 29 , wherein the finely-dividing and mixing means finely-divide and mix the water-combustible oil-based mixture obtained by the primary mixing means into the fine particle state, to thereby form an emulsion fuel in which the average diameter of the water or the combustible oil is 200 to 700 nm. 
   
   
       34 . An apparatus for production of an emulsion fuel according to  claim 33 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to pass through one or two or more of small pores, and finely-divides and mixes through a cavitation effect due to turbulence generated at orifices. 
   
   
       35 . An apparatus for production of an emulsion fuel according to  claim 33 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to flow within a pump at a flow rate of 50 m/s or more; accelerates the water-combustible oil-based primary mixture liquid to pass into holes of a wall member having multiple holes each having a diameter of 200 μm or less formed therein; and finely-divides and mixes the water-combustible oil-based primary mixture liquid by causing a cavitation by turbulence generated by orifices between flows of the liquid. 
   
   
       36 . An apparatus for production of an emulsion fuel according to  claim 33 , wherein a reduction potential of the water to be adopted is −100 mv or lower. 
   
   
       37 . An apparatus for production of an emulsion fuel according to  claim 36 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to pass through one or two or more of small pores, and finely-divides and mixes through a cavitation effect due to turbulence generated at orifices. 
   
   
       38 . An apparatus for production of an emulsion fuel according to  claim 36 , wherein the finely-dividing and mixing means pressurizes the water-combustible oil-based primary mixture liquid to cause to flow within a pump at a flow rate of 50 m/s or more; accelerates the water-combustible oil-based primary mixture liquid to pass into holes of a wall member having multiple holes each having a diameter of 200 μm or less formed therein; and finely-divides and mixes the water-combustible oil-based primary mixture liquid by causing a cavitation by turbulence generated by orifices between flows of the liquid. 
   
   
       39 . An emulsion fuel, wherein 10.0 to 150.0 parts by volume of a water is mixed with respect to 100 parts by volume of a combustible oil by the finely-dividing and mixing means, and an average diameter of the combustible oil is 1,000 nm or less. 
   
   
       40 . An emulsion fuel according to  claim 39 , wherein the average diameter of the water or the combustible oil in the emulsion fuel is 200 to 700 nm.

Cited by (0)

No later patents cite this yet.

References (0)

No backward citations on record.