JP2015172197A - Additive for water-addition biofuel, water-addition biofuel, and production method thereof - Google Patents
Additive for water-addition biofuel, water-addition biofuel, and production method thereof Download PDFInfo
- Publication number
- JP2015172197A JP2015172197A JP2015086031A JP2015086031A JP2015172197A JP 2015172197 A JP2015172197 A JP 2015172197A JP 2015086031 A JP2015086031 A JP 2015086031A JP 2015086031 A JP2015086031 A JP 2015086031A JP 2015172197 A JP2015172197 A JP 2015172197A
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- Prior art keywords
- water
- weight
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- acid
- additive
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- Granted
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- 239000000654 additive Substances 0.000 title claims abstract description 61
- 230000000996 additive effect Effects 0.000 title claims abstract description 61
- 239000002551 biofuel Substances 0.000 title claims abstract description 57
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- 239000000295 fuel oil Substances 0.000 claims abstract description 103
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 88
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 49
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims abstract description 38
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 37
- 238000002156 mixing Methods 0.000 claims abstract description 34
- 239000004094 surface-active agent Substances 0.000 claims abstract description 26
- 239000002245 particle Substances 0.000 claims abstract description 24
- 239000002028 Biomass Substances 0.000 claims abstract description 23
- 235000014113 dietary fatty acids Nutrition 0.000 claims abstract description 14
- 229930195729 fatty acid Natural products 0.000 claims abstract description 14
- 239000000194 fatty acid Substances 0.000 claims abstract description 14
- 150000004665 fatty acids Chemical class 0.000 claims abstract description 14
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 13
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 12
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 claims abstract description 11
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims abstract description 8
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims abstract description 4
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 28
- 239000000243 solution Substances 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 17
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 14
- 125000004432 carbon atom Chemical group C* 0.000 claims description 11
- 239000003921 oil Substances 0.000 claims description 10
- 235000019198 oils Nutrition 0.000 claims description 10
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 9
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 8
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 8
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 8
- 239000005642 Oleic acid Substances 0.000 claims description 8
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 8
- 239000002253 acid Substances 0.000 claims description 8
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 8
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 8
- 239000003350 kerosene Substances 0.000 claims description 7
- YZXBAPSDXZZRGB-DOFZRALJSA-N arachidonic acid Chemical compound CCCCC\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O YZXBAPSDXZZRGB-DOFZRALJSA-N 0.000 claims description 6
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 claims description 6
- KEMQGTRYUADPNZ-UHFFFAOYSA-N heptadecanoic acid Chemical compound CCCCCCCCCCCCCCCCC(O)=O KEMQGTRYUADPNZ-UHFFFAOYSA-N 0.000 claims description 6
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 claims description 6
- UTOPWMOLSKOLTQ-UHFFFAOYSA-N octacosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCC(O)=O UTOPWMOLSKOLTQ-UHFFFAOYSA-N 0.000 claims description 6
- SECPZKHBENQXJG-FPLPWBNLSA-N palmitoleic acid Chemical compound CCCCCC\C=C/CCCCCCCC(O)=O SECPZKHBENQXJG-FPLPWBNLSA-N 0.000 claims description 6
- BEOUGZFCUMNGOU-UHFFFAOYSA-N tuberculostearic acid Chemical compound CCCCCCCCC(C)CCCCCCCCC(O)=O BEOUGZFCUMNGOU-UHFFFAOYSA-N 0.000 claims description 6
- 239000003225 biodiesel Substances 0.000 claims description 5
- -1 glycol alcohols Chemical class 0.000 claims description 4
- VKOBVWXKNCXXDE-UHFFFAOYSA-N icosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCC(O)=O VKOBVWXKNCXXDE-UHFFFAOYSA-N 0.000 claims description 4
- VHOCUJPBKOZGJD-UHFFFAOYSA-N triacontanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCCCCCCCCCC(O)=O VHOCUJPBKOZGJD-UHFFFAOYSA-N 0.000 claims description 4
- 235000015112 vegetable and seed oil Nutrition 0.000 claims description 4
- 239000008158 vegetable oil Substances 0.000 claims description 4
- GWHCXVQVJPWHRF-KTKRTIGZSA-N (15Z)-tetracosenoic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCCCC(O)=O GWHCXVQVJPWHRF-KTKRTIGZSA-N 0.000 claims description 3
- CUXYLFPMQMFGPL-UHFFFAOYSA-N (9Z,11E,13E)-9,11,13-Octadecatrienoic acid Natural products CCCCC=CC=CC=CCCCCCCCC(O)=O CUXYLFPMQMFGPL-UHFFFAOYSA-N 0.000 claims description 3
- OYHQOLUKZRVURQ-NTGFUMLPSA-N (9Z,12Z)-9,10,12,13-tetratritiooctadeca-9,12-dienoic acid Chemical compound C(CCCCCCC\C(=C(/C\C(=C(/CCCCC)\[3H])\[3H])\[3H])\[3H])(=O)O OYHQOLUKZRVURQ-NTGFUMLPSA-N 0.000 claims description 3
- 235000021357 Behenic acid Nutrition 0.000 claims description 3
- 235000021353 Lignoceric acid Nutrition 0.000 claims description 3
- CQXMAMUUWHYSIY-UHFFFAOYSA-N Lignoceric acid Natural products CCCCCCCCCCCCCCCCCCCCCCCC(=O)OCCC1=CC=C(O)C=C1 CQXMAMUUWHYSIY-UHFFFAOYSA-N 0.000 claims description 3
- XJXROGWVRIJYMO-SJDLZYGOSA-N Nervonic acid Natural products O=C(O)[C@@H](/C=C/CCCCCCCC)CCCCCCCCCCCC XJXROGWVRIJYMO-SJDLZYGOSA-N 0.000 claims description 3
- 235000021314 Palmitic acid Nutrition 0.000 claims description 3
- 235000021319 Palmitoleic acid Nutrition 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 235000021355 Stearic acid Nutrition 0.000 claims description 3
- CUXYLFPMQMFGPL-SUTYWZMXSA-N all-trans-octadeca-9,11,13-trienoic acid Chemical compound CCCC\C=C\C=C\C=C\CCCCCCCC(O)=O CUXYLFPMQMFGPL-SUTYWZMXSA-N 0.000 claims description 3
- DTOSIQBPPRVQHS-PDBXOOCHSA-N alpha-linolenic acid Chemical compound CC\C=C/C\C=C/C\C=C/CCCCCCCC(O)=O DTOSIQBPPRVQHS-PDBXOOCHSA-N 0.000 claims description 3
- 235000020661 alpha-linolenic acid Nutrition 0.000 claims description 3
- 229940114079 arachidonic acid Drugs 0.000 claims description 3
- 235000021342 arachidonic acid Nutrition 0.000 claims description 3
- 229940116226 behenic acid Drugs 0.000 claims description 3
- SECPZKHBENQXJG-UHFFFAOYSA-N cis-palmitoleic acid Natural products CCCCCCC=CCCCCCCCC(O)=O SECPZKHBENQXJG-UHFFFAOYSA-N 0.000 claims description 3
- GWHCXVQVJPWHRF-UHFFFAOYSA-N cis-tetracosenoic acid Natural products CCCCCCCCC=CCCCCCCCCCCCCCC(O)=O GWHCXVQVJPWHRF-UHFFFAOYSA-N 0.000 claims description 3
- FARYTWBWLZAXNK-WAYWQWQTSA-N ethyl (z)-3-(methylamino)but-2-enoate Chemical compound CCOC(=O)\C=C(\C)NC FARYTWBWLZAXNK-WAYWQWQTSA-N 0.000 claims description 3
- 239000003502 gasoline Substances 0.000 claims description 3
- 229960004488 linolenic acid Drugs 0.000 claims description 3
- KQQKGWQCNNTQJW-UHFFFAOYSA-N linolenic acid Natural products CC=CCCC=CCC=CCCCCCCCC(O)=O KQQKGWQCNNTQJW-UHFFFAOYSA-N 0.000 claims description 3
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 claims description 3
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 3
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 239000008117 stearic acid Substances 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 2
- 229910052799 carbon Inorganic materials 0.000 abstract description 2
- 238000002485 combustion reaction Methods 0.000 description 32
- 239000000446 fuel Substances 0.000 description 29
- 238000000034 method Methods 0.000 description 13
- 239000000839 emulsion Substances 0.000 description 12
- 235000011114 ammonium hydroxide Nutrition 0.000 description 11
- 239000002994 raw material Substances 0.000 description 9
- 239000003344 environmental pollutant Substances 0.000 description 8
- 239000005431 greenhouse gas Substances 0.000 description 7
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- 230000000052 comparative effect Effects 0.000 description 6
- 238000002407 reforming Methods 0.000 description 5
- 230000003381 solubilizing effect Effects 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- 150000001298 alcohols Chemical class 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 230000036571 hydration Effects 0.000 description 2
- 238000006703 hydration reaction Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000006386 neutralization reaction Methods 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 230000007928 solubilization Effects 0.000 description 2
- 238000005063 solubilization Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- 238000004448 titration Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 241000221089 Jatropha Species 0.000 description 1
- 239000004909 Moisturizer Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- XKMRRTOUMJRJIA-UHFFFAOYSA-N ammonia nh3 Chemical compound N.N XKMRRTOUMJRJIA-UHFFFAOYSA-N 0.000 description 1
- 239000010775 animal oil Substances 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000008162 cooking oil Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 230000005183 environmental health Effects 0.000 description 1
- OCLXJTCGWSSVOE-UHFFFAOYSA-N ethanol etoh Chemical compound CCO.CCO OCLXJTCGWSSVOE-UHFFFAOYSA-N 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
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- 239000008233 hard water Substances 0.000 description 1
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- 229930195733 hydrocarbon Natural products 0.000 description 1
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- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 230000009967 tasteless effect Effects 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
Classifications
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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
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
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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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
- C10L1/125—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
-
- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1266—Inorganic compounds nitrogen containing compounds, (e.g. NH3)
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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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
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- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1826—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms poly-hydroxy
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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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
- C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
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- 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
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
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- 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
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
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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
- C10L2200/00—Components of fuel compositions
- C10L2200/04—Organic compounds
- C10L2200/0407—Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
- C10L2200/0415—Light distillates, e.g. LPG, naphtha
- C10L2200/0423—Gasoline
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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
- C10L2200/00—Components of fuel compositions
- C10L2200/04—Organic compounds
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- C10L2200/043—Kerosene, jet fuel
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- C10L2200/00—Components of fuel compositions
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Abstract
Description
本国際出願は、2010年10月14日に日本国特許庁に出願された日本国特許出願第2010−231862号に基づく優先権を主張するものであり、日本国特許出願第2010−231862号の全内容を本国際出願に援用する。 This international application claims priority based on Japanese Patent Application No. 2010-231862 filed with the Japan Patent Office on October 14, 2010, and is based on Japanese Patent Application No. 2010-231862. The entire contents are incorporated into this international application.
本発明は、加水バイオ燃料用添加剤、それを使用した加水バイオ燃料及びその製造方法に関する。 TECHNICAL FIELD The present invention relates to an additive for hydrated biofuel, a hydrated biofuel using the same, and a method for producing the same.
近年、原油価格の高騰や地球資源である化石燃料の枯渇問題、また、それを使用する際に排出され、地球の環境破壊につながるCO2等の温室効果ガスや環境汚染物質の低減化の観点から、燃料油に適量の水を混合した燃料、いわゆるエマルジョン燃料の研究が盛んに行われている。 In recent years, crude oil prices have risen and fossil fuels, which are global resources, are depleted, and CO 2 and other greenhouse gases and environmental pollutants that are emitted when they are used and lead to the destruction of the environment Therefore, research on a fuel in which an appropriate amount of water is mixed with fuel oil, so-called emulsion fuel, has been actively conducted.
エマルジョン燃料は、一般には燃料油(重油や灯油、軽油、廃油等)に水と界面活性剤を添加し、機械的に撹拌して燃料油中に水を分散させた燃料であり、燃料の使用量の削減やそれに伴う環境汚染物質の低減化に、ある程度有効な燃料として公知である。このようなエマルジョン燃料としては、例えば特許文献1から5を始めとした様々なものがある。 Emulsion fuel is generally a fuel in which water and surfactant are added to fuel oil (heavy oil, kerosene, light oil, waste oil, etc.) and mechanically stirred to disperse water in the fuel oil. It is known as a fuel that is effective to some extent for reducing the amount and environmental pollutants associated therewith. As such an emulsion fuel, for example, there are various ones including Patent Documents 1 to 5.
上述したように、エマルジョン燃料に関しては、長年にわたり研究、開発が行われており、一部で試験的に運用されている。
しかしながら、前記従来のエマルジョン燃料においては、製造後に比較的短時間で燃料油と水が分離し、上層に油分の多くが移動し下層に水分の多くが移動して二層化することがある。このような二層化による使用上のトラブルや、貯蔵(備蓄)と輸送の困難性及び含水の影響による燃焼効率や燃焼カロリーの低下、熱効率の低下による燃費の低下及び燃焼室の腐食等、様々な欠点や問題点を有していた。
As described above, emulsion fuel has been researched and developed for many years, and is partly operated on a trial basis.
However, in the conventional emulsion fuel, fuel oil and water may be separated in a relatively short time after production, and a large amount of oil may move to the upper layer and a large amount of water may move to the lower layer, resulting in two layers. Various problems such as troubles in use due to such double layering, difficulty in storage (stockpile) and transportation and reduction of combustion efficiency and combustion calories due to the effect of water content, reduction of fuel efficiency and combustion chamber corrosion due to reduction of thermal efficiency, etc. It had various drawbacks and problems.
したがって、エマルジョン燃料においては、これらの要因が重なり、一部で試験的に運用されている例はあるものの、市場での十分な普及には至っていないのが現状である。
(本発明の目的)
本発明は、水の粒子を細かくし、燃料油全体に均一に分散させ、乳化を抑制して可溶化することができる加水バイオ燃料用添加剤及びその製造方法を提供することを目的とする。
Therefore, in the emulsion fuel, these factors are overlapped, and although there are examples in which some of them are operated on a trial basis, the current situation is that they have not been sufficiently spread in the market.
(Object of the present invention)
It is an object of the present invention to provide an additive for hydrobiofuel that can make water particles finely dispersed uniformly throughout the fuel oil, suppress emulsification and solubilize, and a method for producing the same.
本発明の他の目的は、燃料油と水が分離したり二層化したりすることを抑制して、製造後、品質を低下させることなく長期にわたる貯蔵と、輸送ができる加水バイオ燃料およびその製造方法を提供することである。本発明のさらなる目的は、通常の燃料と比較して、燃焼効率及び燃焼カロリーの向上を図ると共に、CO2等の温室効果ガスや環境汚染物質の排出を低減することができる加水バイオ燃料及びその製造方法を提供することである。 Another object of the present invention is to provide a biofuel that can be stored and transported for a long period of time without degrading the quality of the fuel oil and water by separating and separating the fuel oil and water from each other and manufacturing the same. Is to provide a method. A further object of the present invention is to improve the combustion efficiency and combustion calorie as compared with ordinary fuels, as well as a hydrobiofuel capable of reducing emissions of greenhouse gases such as CO 2 and environmental pollutants, and its It is to provide a manufacturing method.
上記課題を解決するために成された本発明は、次のとおりである。
本発明の加水バイオ燃料用添加剤は、
界面活性剤と、グリコール系アルコールと、バイオマスから合成できるアルコールと、アンモニアとを含む。
The present invention made to solve the above problems is as follows.
The additive for hydrobiofuel of the present invention is
A surfactant, a glycol-based alcohol, an alcohol that can be synthesized from biomass, and ammonia are included.
本発明の加水バイオ燃料用添加剤においては、
前記アンモニアは、アンモニア水であり、
当該加水バイオ燃料用添加剤の組成が、前記界面活性剤55〜70重量部、前記グリコール系アルコール10〜15重量部、前記バイオマスから合成できるアルコール15〜25重量部、及び前記アンモニア水(25%溶液)5.5〜8.8重量部であってもよい。
In the additive for hydrobiofuel of the present invention,
The ammonia is aqueous ammonia,
The composition of the additive for hydrobiofuel is 55 to 70 parts by weight of the surfactant, 10 to 15 parts by weight of the glycol alcohol, 15 to 25 parts by weight of alcohol that can be synthesized from the biomass, and the aqueous ammonia (25% The solution may be 5.5 to 8.8 parts by weight.
本発明の加水バイオ燃料用添加剤においては、
当該加水バイオ燃料用添加剤の組成が、前記界面活性剤55〜70重量部、前記グリコール系アルコール10〜15重量部、前記バイオマスから合成できるアルコール15〜25重量部を混合した溶液に、該溶液100g当たり、前記アンモニアを1.25〜2.0リットル溶解させたものであってもよい。
In the additive for hydrobiofuel of the present invention,
The composition of the additive for hydrobiofuel is a solution prepared by mixing 55 to 70 parts by weight of the surfactant, 10 to 15 parts by weight of the glycol alcohol, and 15 to 25 parts by weight of alcohol that can be synthesized from the biomass. 1.25-2.0 liters of the ammonia may be dissolved per 100 g.
本発明の加水バイオ燃料用添加剤においては、
前記界面活性剤が、炭素数16以上の脂肪酸から選ばれる1種類又は複数種類の界面活性剤であってもよい。
In the additive for hydrobiofuel of the present invention,
The surfactant may be one or more surfactants selected from fatty acids having 16 or more carbon atoms.
また、前記炭素数が16以上の脂肪酸が、パルミチン酸、パルミトレイン酸、マルガリン酸、ステアリン酸、オレイン酸、パクセン酸、リノール酸、リノレン酸、エレオステアリン酸、ツベルクロステアリン酸、アラキジン酸、アラキドン酸、ベヘン酸、リグノセリン酸、ネルボン酸、セロチン酸、モンタン酸又はメリシン酸からなる群から選択されてもよい。 The fatty acid having 16 or more carbon atoms is palmitic acid, palmitoleic acid, margaric acid, stearic acid, oleic acid, paxenoic acid, linoleic acid, linolenic acid, eleostearic acid, tuberculostearic acid, arachidonic acid, arachidone. It may be selected from the group consisting of acids, behenic acid, lignoceric acid, nervonic acid, serotic acid, montanic acid or melissic acid.
本発明の加水バイオ燃料用添加剤においては、
前記グリコール系アルコールが、エチレングリコール、プロピレングリコール、ジエチレングリコール、ポリエチレングリコールからなる群から選ばれる1種類または複数種類のグリコール系アルコールであってもよい。
In the additive for hydrobiofuel of the present invention,
The glycol alcohol may be one or more glycol alcohols selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, and polyethylene glycol.
本発明の加水バイオ燃料用添加剤においては、
前記バイオマスから合成できるアルコールが、エタノール、メタノール、プロパノール、ブタノールからなる群から選ばれる1種類または複数種類のバイオマスから合成可能なアルコールであってもよい。
In the additive for hydrobiofuel of the present invention,
The alcohol that can be synthesized from the biomass may be an alcohol that can be synthesized from one or more types of biomass selected from the group consisting of ethanol, methanol, propanol, and butanol.
本発明の加水バイオ燃料用添加剤の製造方法は、
界面活性剤55〜70重量部、グリコール系アルコール10〜15重量部、バイオマスから合成できるアルコール15〜25重量部を混合し撹拌する工程と、得られた混合液にアンモニア水(25%溶液)5.5〜8.8重量部を加え、更に撹拌および混合する工程と、を含む。
The method for producing the additive for hydrobiofuel of the present invention comprises:
A step of mixing and stirring 55 to 70 parts by weight of a surfactant, 10 to 15 parts by weight of a glycol-based alcohol, and 15 to 25 parts by weight of an alcohol that can be synthesized from biomass, and aqueous ammonia (25% solution) 5 in the resulting mixed solution Adding 5 to 8.8 parts by weight, and further stirring and mixing.
本発明の加水バイオ燃料は、
燃料油に、水と、本発明の加水バイオ燃料用添加剤とを配合し、前記燃料油に対して水の粒子を細かくして分散し可溶化したものである。
The hydrobiofuel of the present invention is
The fuel oil is blended with water and the additive for a hydrobiofuel of the present invention, and water particles are finely dispersed and solubilized in the fuel oil.
本発明の加水バイオ燃料においては、
前記燃料油が、A重油、ガソリン、軽油、灯油、ケロシン、植物油、バイオディーゼル燃料からなる群から選ばれる一種類の燃料油であってもよい。
In the hydrous biofuel of the present invention,
The fuel oil may be one kind of fuel oil selected from the group consisting of A heavy oil, gasoline, light oil, kerosene, kerosene, vegetable oil, and biodiesel fuel.
本発明の加水バイオ燃料においては、
当該加水バイオ燃料の組成が、前記燃料油58〜62重量部、前記加水バイオ燃料用添加剤15〜20重量部、前記水18〜27重量部であってもよい。
In the hydrous biofuel of the present invention,
The composition of the hydrated biofuel may be 58 to 62 parts by weight of the fuel oil, 15 to 20 parts by weight of the additive for hydrated biofuel, and 18 to 27 parts by weight of the water.
本発明の加水バイオ燃料の製造方法は、
燃料油58〜62重量部と、請求項1から7の何れか1項に記載の加水バイオ燃料用添加剤15〜20重量部とを混合し撹拌する工程と、得られた混合液に水18〜27重量部を加え、撹拌および混合して、前記燃料油に水を可溶化させる工程と、を含む。
The method for producing the hydrous biofuel of the present invention comprises:
A step of mixing and stirring 58 to 62 parts by weight of fuel oil and 15 to 20 parts by weight of the additive for hydrobiofuel according to any one of claims 1 to 7, and water 18 Adding ~ 27 parts by weight, stirring and mixing to solubilize water in the fuel oil.
本発明は、水の粒子を細かくし、燃料油全体に均一に分散させ、乳化を抑制して可溶化することができる加水バイオ燃料用添加剤及びその製造方法を提供することができる。
また、本発明は、燃料油と水が分離したり二層化したりすることを抑制して、製造後、品質を低下させることなく長期にわたる貯蔵と、輸送ができると共に、通常の燃料と比較して、燃焼効率及び燃焼カロリーの向上を図ると共に、CO2等の温室効果ガスや環境汚染物質の排出を低減することができる加水バイオ燃料及びその製造方法を提供することができる。
INDUSTRIAL APPLICABILITY The present invention can provide an additive for a hydrobiofuel that can make water particles fine, uniformly disperse it throughout the fuel oil, suppress solubilization and solubilize, and a method for producing the same.
In addition, the present invention suppresses separation and two-layered separation of fuel oil and water, and can be stored and transported for a long time without degradation in quality after production. Thus, it is possible to provide a hydrobiofuel capable of improving combustion efficiency and calorie calorie and reducing emission of greenhouse gases such as CO 2 and environmental pollutants, and a method for producing the same.
本発明に係る加水バイオ燃料用添加剤及びそれを使用した加水バイオ燃料について説明する。
本明細書及び特許請求の範囲において、「可溶化」の用語は、水などの溶媒に本来は溶けないか又は溶けにくい物質が、界面活性剤の存在下で、その溶媒に溶けるようになるという意味を含むものである。
The additive for hydrobiofuel according to the present invention and the hydrobiofuel using the same will be described.
In the present specification and claims, the term “solubilization” means that a substance that is inherently insoluble or difficult to dissolve in a solvent such as water becomes soluble in that solvent in the presence of a surfactant. It has meaning.
本発明に係る加水バイオ燃料用添加剤及び加水バイオ燃料の原料又は成分の主な性質を以下に簡単に説明する。
前記原料又は成分は、いずれも一般市場で様々な用途に使用されているものであり、流通量も多く比較的安価なものであるため入手が容易である。
The main properties of the additive for hydrobiofuel and the raw material or components of hydrobiofuel according to the present invention will be briefly described below.
All of the raw materials or components are used in various applications in the general market, and are easy to obtain because they have a large amount of distribution and are relatively inexpensive.
界面活性剤には多くの種類があるが、本発明においては脂肪酸を使用する。脂肪酸には炭素数が4から30まで様々な種類があり、本発明者が試行及び実験を重ねた結果、炭素数が16以上の脂肪酸が特に有効であることが分かった。 There are many types of surfactants, but fatty acids are used in the present invention. There are various types of fatty acids having 4 to 30 carbon atoms. As a result of repeated trials and experiments by the present inventors, it has been found that fatty acids having 16 or more carbon atoms are particularly effective.
炭素数16以上の脂肪酸としては、例えばパルミチン酸、パルミトレイン酸、マルガリン酸、ステアリン酸、オレイン酸、パクセン酸、リノール酸、リノレン酸、エレオステアリン酸、ツベルクロステアリン酸、アラキジン酸、アラキドン酸、ベヘン酸、リグノセリン酸、ネルボン酸、セロチン酸、モンタン酸、メリシン酸等があげられる。これらの炭素数16以上の脂肪酸の中でも、特に流通量、価格等の観点から入手及び使用に有利と思われるオレイン酸を使用することが好ましい。本発明では、これらの炭素数16以上の脂肪酸からなる群から選ばれる一種類の界面活性剤を使用してもよいし、これらの炭素数16以上の脂肪酸からなる群から選ばれる複数種類の界面活性剤を混合して使用してもよい。 Examples of fatty acids having 16 or more carbon atoms include palmitic acid, palmitoleic acid, margaric acid, stearic acid, oleic acid, paxenoic acid, linoleic acid, linolenic acid, eleostearic acid, tuberculostearic acid, arachidic acid, arachidonic acid, Examples include behenic acid, lignoceric acid, nervonic acid, serotic acid, montanic acid, melicic acid and the like. Among these fatty acids having 16 or more carbon atoms, it is preferable to use oleic acid, which is considered advantageous for acquisition and use, particularly from the viewpoint of the distribution amount, price, and the like. In the present invention, one type of surfactant selected from the group consisting of these fatty acids having 16 or more carbon atoms may be used, or a plurality of types of interfaces selected from the group consisting of these fatty acids having 16 or more carbon atoms. You may mix and use an active agent.
グリコール系アルコールとしては、エチレングリコール、プロピレングリコール、ジエチレングリコール、ポリエチレングリコール等があげられる。これらのグリコール系アルコールの中でも、特に流通量、価格等の観点から入手及び使用に有利と思われるプロピレングリコールを使用することが好ましい。本発明では、ここで例示したグリコール系アルコールの中から一種類を選択して使用してもよいし、ここで例示したグリコール系アルコールの中から複数種類を選択して混合して使用してもよい。 Examples of the glycol alcohol include ethylene glycol, propylene glycol, diethylene glycol, polyethylene glycol and the like. Among these glycol-based alcohols, it is preferable to use propylene glycol, which is considered advantageous for acquisition and use, particularly from the viewpoint of distribution amount, price, and the like. In the present invention, one of the glycol alcohols exemplified here may be selected and used, or plural kinds of glycol alcohols exemplified here may be selected and mixed for use. Good.
また、バイオマスから合成可能なアルコールとしては、エタノール、メタノール、プロパノール、ブタノール等があげられる。これらのバイオマスから合成可能なアルコールの中でも、特に流通量、価格等の観点から入手及び使用に有利と思われるエタノールを使用することが好ましい。本発明では、ここで例示したバイオマスから合成可能なアルコールの中から一種類を選択して使用してもよいし、ここで例示したバイオマスから合成可能なアルコールの中から複数種類を選択して混合して使用してもよい。 Examples of alcohols that can be synthesized from biomass include ethanol, methanol, propanol, and butanol. Among these alcohols that can be synthesized from biomass, it is preferable to use ethanol that is considered advantageous for acquisition and use, particularly from the viewpoint of the distribution amount, price, and the like. In the present invention, one kind of alcohol that can be synthesized from the biomass exemplified here may be selected and used, or plural kinds of alcohols that can be synthesized from the biomass exemplified here may be selected and mixed. May be used.
オレイン酸(oleic Acid)は、浅黄色もしくは黄褐色をした液体であり、例えばラードのような動植物油に含まれる脂肪酸である。水には溶けず、有機溶剤に溶ける。本発明に係る加水バイオ燃料用添加剤の主成分であるが、完成した添加剤の凝固点を勘案して凝固点8℃以下のものを採用するのが好ましい。 Oleic acid is a light yellow or tan liquid, and is a fatty acid contained in animal and vegetable oils such as lard. Not soluble in water but soluble in organic solvents. Although it is the main component of the additive for hydrobiofuel according to the present invention, it is preferable to adopt one having a freezing point of 8 ° C. or lower in consideration of the freezing point of the completed additive.
プロピレングリコール(propylene glycol)は、無色、無味、無臭で吸湿性のある液体である。保湿剤、潤滑剤、乳化剤、不凍液などとして用いられる。
エタノール(ethanol)は、一般的なアルコールの性質を持つものであり、水を始めとする極性溶媒や炭化水素を含む各種有機溶剤など、様々な溶媒と混和することができる。殺菌、消毒の用途で用いられる。
Propylene glycol is a colorless, tasteless, odorless and hygroscopic liquid. Used as a moisturizer, lubricant, emulsifier, antifreeze, etc.
Ethanol (ethanol) has general alcohol properties, and can be mixed with various solvents such as polar solvents including water and various organic solvents including hydrocarbons. Used for sterilization and disinfection.
アンモニア(Ammonia)は、常温常圧では無色の気体で、特有の強い刺激臭を持つ。水によく溶けるため、水溶液(アンモニア水)として使用されることも多い。
次に、加水バイオ燃料用添加剤の各成分の作用(役割)について説明する。
Ammonia (Ammonia) is a colorless gas at normal temperature and pressure, and has a unique strong irritating odor. Since it dissolves well in water, it is often used as an aqueous solution (aqueous ammonia).
Next, the action (role) of each component of the additive for hydrobiofuel will be described.
燃料油の表面張力は比較的小さく(弱く)、これに対し水の表面張力は比較的大きい(強い)。界面活性剤は、燃料油と水の双方の表面張力をより小さくし、撹拌混合することで、乳化状態になりやすいようにする働きをする。 The surface tension of fuel oil is relatively small (weak), while the surface tension of water is relatively large (strong). The surfactant acts to make it easier to become an emulsified state by reducing the surface tension of both the fuel oil and water and stirring and mixing them.
プロピレングリコールは、水の表面張力の大きさを燃料油の表面張力に近づける改質作用を促進する働きをする。
エタノールは、プロピレングリコールとは反対に燃料油の表面張力の大きさを水の表面張力に近づける改質作用を促進する働きをする。
Propylene glycol serves to promote a reforming action that brings the surface tension of water closer to the surface tension of the fuel oil.
In contrast to propylene glycol, ethanol serves to promote a reforming action that brings the surface tension of fuel oil closer to the surface tension of water.
また、アンモニア(アンモニア水)は、水の粒子を細かくして燃料油と水を結合させ、水を可溶化し燃料油に包含させる働きをする。
加水バイオ燃料用添加剤の製造にあたり、界面活性剤の配合割合が70重量部を超えると、燃料油と水の表面張力を小さくする作用の進行は鈍化し、他の成分の機能を抑制する傾向がある。また、界面活性剤の配合割合が55重量部に満たないと、燃料油と水の表面張力を十分に小さくすることができなくなる傾向がある。これにより、いずれの場合も加水バイオ燃料用添加剤を使用した加水バイオ燃料が乳化しやすくなる。
Ammonia (ammonia water) works to make water particles fine and combine fuel oil and water to solubilize water and include it in fuel oil.
In the production of the additive for hydrobiofuel, when the blending ratio of the surfactant exceeds 70 parts by weight, the progress of the action of reducing the surface tension of the fuel oil and water is slowed, and the function of other components tends to be suppressed. There is. Further, when the blending ratio of the surfactant is less than 55 parts by weight, the surface tension of the fuel oil and water tends not to be sufficiently reduced. Thereby, in any case, the hydrated biofuel using the hydrated biofuel additive is easily emulsified.
プロピレングリコールの配合割合が15重量部を超えると、前記水の表面張力の大きさを燃料油の表面張力に近づける改質作用が鈍化する傾向がある。また、プロピレングリコールの配合割合が10重量部に満たないと、前記改質作用が不十分となる傾向がある。これにより、いずれの場合も加水バイオ燃料用添加剤を使用した加水バイオ燃料が乳化しやすくなる。 When the proportion of propylene glycol exceeds 15 parts by weight, the reforming action of bringing the surface tension of water close to the surface tension of the fuel oil tends to slow down. Moreover, when the blending ratio of propylene glycol is less than 10 parts by weight, the modifying action tends to be insufficient. Thereby, in any case, the hydrated biofuel using the hydrated biofuel additive is easily emulsified.
エタノールの配合割合が25重量部を超えると、前記燃料油の表面張力の大きさを水の表面張力に近づける改質作用が鈍化する傾向がある。また、エタノールの配合割合が15重量部に満たないと、前記改質作用が不十分となる傾向がある。これにより、いずれの場合も加水バイオ燃料用添加剤を使用した加水バイオ燃料が乳化しやすくなる。 When the blending ratio of ethanol exceeds 25 parts by weight, the reforming action that brings the surface tension of the fuel oil close to the surface tension of water tends to be slowed. Moreover, if the blending ratio of ethanol is less than 15 parts by weight, the reforming action tends to be insufficient. Thereby, in any case, the hydrated biofuel using the hydrated biofuel additive is easily emulsified.
アンモニアは、次のような性質を有する。アンモニア水(25%溶液)の場合は、8.8重量部を超えると、前記水の粒子を細かくして燃料油と水を結合させ、水を可溶化し燃料油に包含させる作用が鈍化する傾向がある。また、アンモニアの場合は、界面活性剤、グリコール系アルコール、バイオマスから合成できるアルコールを混合した溶液100g当たりの溶解量が2.0リットルを超えると、前記水の粒子を細かくして燃料油と水を結合させ、水を可溶化し燃料油に包含させる作用が鈍化する傾向がある。さらに、アンモニア水(25%溶液)の場合は、5.5重量部に満たないと、前記水を可溶化し燃料油に包含させる作用が不十分となる傾向がある。また、アンモニアの場合は、界面活性剤、グリコール系アルコール、バイオマスから合成できるアルコールを混合した溶液100g当たりの溶解量が1.25リットルに満たないと、前記水を可溶化し燃料油に包含させる作用が不十分となる傾向がある。また、これにより、いずれの場合も加水バイオ燃料用添加剤を使用した加水バイオ燃料が乳化しやすくなる。 Ammonia has the following properties. In the case of ammonia water (25% solution), when the amount exceeds 8.8 parts by weight, the action of making the water particles finer, combining the fuel oil and water, solubilizing the water and including it in the fuel oil slows down. Tend. In the case of ammonia, if the amount of solution per 100 g of a mixture of a surfactant, glycol alcohol, and alcohol synthesized from biomass exceeds 2.0 liters, the water particles are made finer and fuel oil and water The action of solubilizing water and solubilizing water and including it in fuel oil tends to slow down. Furthermore, in the case of aqueous ammonia (25% solution), if it is less than 5.5 parts by weight, the action of solubilizing the water and including it in the fuel oil tends to be insufficient. In the case of ammonia, the water is solubilized and included in the fuel oil if the dissolved amount per 100 g of a solution in which a surfactant, glycol alcohol, and alcohol that can be synthesized from biomass are mixed is less than 1.25 liters. There is a tendency for the action to be insufficient. This also makes it easier to emulsify the hydrated biofuel using the hydrated biofuel additive in any case.
加水バイオ燃料の製造にあたり、燃料油の配合割合が58重量部に満たないと、十分な燃焼効率と燃焼カロリーが得られない傾向がある。また、燃料油の配合割合が62重量部を超えると、地球の環境破壊につながるCO2等の温室効果ガスや環境汚染物質の排出が増加する傾向がある。 In the production of the hydrous biofuel, if the blending ratio of the fuel oil is less than 58 parts by weight, there is a tendency that sufficient combustion efficiency and combustion calories cannot be obtained. In addition, when the blending ratio of the fuel oil exceeds 62 parts by weight, the emission of greenhouse gases such as CO 2 and environmental pollutants that lead to environmental destruction of the earth tends to increase.
加水バイオ燃料の製造に使用する燃料油は、A重油、ガソリン、軽油、灯油、ケロシン(ジェット燃料として利用される場合がある)、植物油、バイオディーゼル燃料から選択することができる。A重油とは、重油の一種であり、動粘度によりJIS規格で分類されたものである。また、バイオディーゼル燃料は、BDF(登録商標)とも呼ばれ、生物由来油から作られるディーゼルエンジン用燃料の総称である。バイオディーゼル燃料は、バイオマスエネルギーの1つであり、原料となるパーム、ジャトロファ、廃食油などの油脂からグリセリンをエステル交換により取り除くなどして化学処理を施し、ディーゼルエンジンとして使用できるようにしたものである。 The fuel oil used for the production of the hydrated biofuel can be selected from A heavy oil, gasoline, light oil, kerosene, kerosene (which may be used as jet fuel), vegetable oil, and biodiesel fuel. A heavy oil is a kind of heavy oil and is classified according to JIS standards by kinematic viscosity. Biodiesel fuel is also called BDF (registered trademark), and is a general term for diesel engine fuel made from biological oil. Biodiesel fuel is one of the biomass energies, and it can be used as a diesel engine by chemical treatment by removing glycerin from the oils and fats such as palm, jatropha, and waste cooking oil by transesterification. is there.
水の配合割合が27重量部を超えると、十分な燃焼効率と燃焼カロリーが得られない傾向がある。また、水の配合割合が18重量部に満たないと、地球の環境破壊につながるCO2等の温室効果ガスや環境汚染物質の排出が増加する傾向がある。 When the mixing ratio of water exceeds 27 parts by weight, there is a tendency that sufficient combustion efficiency and combustion calories cannot be obtained. Moreover, if the mixing ratio of water is less than 18 parts by weight, the emission of greenhouse gases such as CO 2 and environmental pollutants that lead to environmental destruction of the earth tends to increase.
加水バイオ燃料用添加剤の配合割合が15重量部に満たないと、水の粒子を細かくして燃料油と水を結合させることにより水を可溶化し燃料油に包含させることができなくなる傾向がある。また、加水バイオ燃料用添加剤の配合割合が20重量部を超えると、水を可溶化し燃料油に包含させることはできても、燃料油の配合割合が相対的に減るため十分な燃焼効率と燃焼カロリーが得られない傾向がある。 If the blending ratio of the additive for hydro-biofuel is less than 15 parts by weight, water tends to be solubilized by making the water particles fine and combining the fuel oil and water so that they cannot be included in the fuel oil. is there. Moreover, if the blending ratio of the additive for hydrobiofuel exceeds 20 parts by weight, water can be solubilized and included in the fuel oil, but the blending ratio of the fuel oil is relatively reduced, so that sufficient combustion efficiency is achieved. And there is a tendency not to obtain calories burned.
加水バイオ燃料用添加剤の製造は、撹拌機に界面活性剤55〜70重量部、グリコール系アルコール10〜15重量部、バイオマスから合成できるアルコール15〜25重量部を混合し撹拌する工程と、その後、アンモニア水(25%溶液)5.5〜8.8重量部を混合し、所要時間撹拌して反応させる工程を経て行われる。また、アンモニア水ではなく、アンモニア(アンモニアガス)を使用する場合は、界面活性剤、グリコール系アルコール、バイオマスから合成できるアルコールを混合した溶液100g当たり、1.25〜2.0リットルを溶解させる。なお、アンモニア水又はアンモニアを混合した後の反応については、溶液に気泡状のものが発生し、溶液の温度が40〜55℃位まで上昇することで確認ができる。 Production of the additive for hydrobiofuel is carried out by mixing and stirring 55 to 70 parts by weight of a surfactant, 10 to 15 parts by weight of a glycol-based alcohol, and 15 to 25 parts by weight of an alcohol that can be synthesized from biomass. Then, 5.5 to 8.8 parts by weight of aqueous ammonia (25% solution) is mixed and stirred for a required time to react. When ammonia (ammonia gas) is used instead of ammonia water, 1.25 to 2.0 liters are dissolved per 100 g of a solution in which a surfactant, glycol alcohol, and alcohol synthesized from biomass are mixed. In addition, about the reaction after mixing ammonia water or ammonia, a bubble-like thing generate | occur | produces in a solution and it can confirm by the temperature of a solution rising to about 40-55 degreeC.
加水バイオ燃料は、燃料油と前記加水バイオ燃料用添加剤及び水の配合割合が、燃料油58〜62重量部、加水バイオ燃料用添加剤15〜20重量部、水18〜27重量部である。加水バイオ燃料の製造は、燃料油58〜62重量部と加水バイオ燃料用添加剤15〜20重量部を混合し、所要時間撹拌する工程と、得られた混合液に水18〜27重量部を加えながら撹拌・混合し、水を可溶化し包含させる工程を経て行われる。
(作用)
まず、燃料油と水を界面活性剤の存在下で混合した後、燃料油と水が分離したり二層化したりする最大の要因は、燃料油と水の表面張力が大きく違うためである。
In the water-added biofuel, the blending ratio of the fuel oil and the water-added biofuel additive and water is 58 to 62 parts by weight of the fuel oil, 15 to 20 parts by weight of the water-added biofuel additive, and 18 to 27 parts by weight of water. . In the production of the hydrobiofuel, 58 to 62 parts by weight of fuel oil and 15 to 20 parts by weight of the additive for hydrobiofuel are mixed and stirred for the required time, and 18 to 27 parts by weight of water is added to the resulting mixture. Stirring and mixing while adding, solubilizing and including water.
(Function)
First, after the fuel oil and water are mixed in the presence of the surfactant, the greatest factor that causes the fuel oil and water to separate or form two layers is that the surface tension of the fuel oil and water is greatly different.
本発明に係る加水バイオ燃料用添加剤を使用して加水バイオ燃料を製造した場合、燃料油と水の表面張力の大きさが同等又は同等にきわめて近くなることにより、燃料油の粒子の中に水の粒子を細かくして均一に分散させ、可溶化・包含させることができると思われる。この理由は明らかではないが、仮に、前記理由が正しくないとしても、本発明の成立にいささかの影響も与えるものではない。 When the hydrobiofuel is produced using the hydrobiofuel additive according to the present invention, the size of the surface tension of the fuel oil and water becomes equal or very close to each other, so that It seems that water particles can be finely dispersed uniformly and solubilized and included. The reason for this is not clear, but even if the reason is not correct, it does not have any effect on the establishment of the present invention.
本発明に係る加水バイオ燃料は、加水バイオ燃料用添加剤の存在下で水の粒子が細かくなって燃料油に可溶化していると思われるので、エマルジョン化(乳化)することがなく、燃料油そのものと同等の透明度を有しており、時間の経過と共に燃料油と水が分離したり二層化したりすることもない。したがって、製造後、数年経過したものも分離したり二層化したりせず透き通った状態、すなわち水の粒子が燃料油に可溶化した状態を保つことができる。 The hydrobiofuel according to the present invention is considered to be solubilized in the fuel oil because the water particles become fine in the presence of the hydrobiofuel additive. It has the same transparency as the oil itself, and the fuel oil and water do not separate or stratify over time. Therefore, it is possible to maintain a transparent state without separation or double-layering even after several years from manufacture, that is, a state where water particles are solubilized in fuel oil.
また、加水バイオ燃料の燃焼時には、一般に使用される燃料油そのものを燃料とした場合と比較して、より完全燃焼に近い状態で燃焼するので、燃焼効率や燃焼カロリーが向上すると共に、CO2等温室効果ガスや環境汚染物質の発生も抑制することができる。このことは、後述する取得データはもとより、試験施設である炉内の煤の色、量からも確認することができる。 In addition, when the biofuel is burned, it is burned in a state close to complete combustion as compared with a case where fuel oil itself that is generally used is used as fuel, so that combustion efficiency and combustion calories are improved, and CO 2 etc. Generation of greenhouse gases and environmental pollutants can also be suppressed. This can be confirmed not only from the acquired data described later, but also from the color and amount of soot in the furnace as the test facility.
以下、本発明の一実施例について説明する。但し、本発明はこれに限定されるものではない。 Hereinafter, an embodiment of the present invention will be described. However, the present invention is not limited to this.
〔加水バイオ燃料用添加剤の製造方法〕
本実施例においては、炭素数16以上の脂肪酸としてオレイン酸を使用し、グリコール系アルコールとしてプロピレングリコールを使用し、バイオマスから合成可能なアルコールとしてエタノールを使用した。
[Method for producing additive for hydro-biofuel]
In this example, oleic acid was used as a fatty acid having 16 or more carbon atoms, propylene glycol was used as a glycol alcohol, and ethanol was used as an alcohol that can be synthesized from biomass.
加水バイオ燃料用添加剤は、まず、撹拌機の撹拌槽に、界面活性剤であるオレイン酸1.30kg(65重量部)、プロピレングリコール0.24kg(12重量部)、エタノール0.34kg(17重量部)、を投入して混合し、5分間撹拌する。なお、この撹拌時間は、前記各成分の配合割合や量の違いで適宜調整することができる。この攪拌時間は、例えば、5〜10分間としてもよい。 First, the additive for hydrobiofuel was added to a stirring tank of a stirrer, 1.30 kg (65 parts by weight) of oleic acid as a surfactant, 0.24 kg (12 parts by weight) of propylene glycol, 0.34 kg of ethanol (17 parts). Parts by weight), and mix for 5 minutes. In addition, this stirring time can be suitably adjusted with the difference in the mixture ratio and quantity of each said component. This stirring time may be, for example, 5 to 10 minutes.
前記のようにオレイン酸、プロピレングリコール及びエタノールを混合した後、撹拌槽にアンモニア水(25%溶液)0.12kg(6重量部)を加えながら、10分間撹拌・混合する。この攪拌時間は、例えば、5〜10分間としてもよい。 After mixing oleic acid, propylene glycol and ethanol as described above, the mixture is stirred and mixed for 10 minutes while adding 0.12 kg (6 parts by weight) of aqueous ammonia (25% solution) to the stirring tank. This stirring time may be, for example, 5 to 10 minutes.
その後、前記混合物である溶液に気泡状物質が発生し、溶液の温度が反応熱の発生により、40〜55℃位まで徐々に上昇する。なお、温度については外気温などの条件によって前記温度範囲から逸脱することがあってもよい。 Thereafter, a bubble-like substance is generated in the solution as the mixture, and the temperature of the solution gradually rises to about 40 to 55 ° C. due to generation of reaction heat. In addition, about temperature, it may deviate from the said temperature range by conditions, such as external temperature.
前記のような溶液中の気泡状物質の発生と溶液の温度の上昇は、化学反応の進行を意味していると思われるが、そのメカニズムについては明らかではない。そして、そのまましばらく撹拌を続けると、この気泡状物質が徐々に消滅していき、溶液の温度も元の温度に戻るので、これが反応の終了を意味すると思われる。このようにして、加水バイオ燃料用添加剤2.0kgを製造することができた。 The generation of the bubble substance in the solution and the increase in the temperature of the solution seem to mean the progress of the chemical reaction, but the mechanism is not clear. Then, if stirring is continued for a while, this bubble-like substance gradually disappears, and the temperature of the solution also returns to the original temperature. This seems to mean the end of the reaction. In this way, 2.0 kg of the additive for hydrobiofuel could be produced.
前記製造方法で使用する撹拌機は、任意・公知のものが使用される。撹拌方法については、アジテータ、循環ポンプ、ラインミキサーなど、様々な方法があるが、本発明に係る製造方法においては、市販の循環ポンプにより循環させるだけの簡単な方法で撹拌を行った。循環ポンプの吐量など、撹拌の強さについて特に限定するものではないが、気泡が発生するような激しい撹拌を行う必要はない。
〔加水バイオ燃料の製造方法〕
次に、前記のようにして製造された加水バイオ燃料用添加剤を用いた加水バイオ燃料を製造する方法について説明する。
As the stirrer used in the production method, any known one can be used. As for the stirring method, there are various methods such as an agitator, a circulation pump, and a line mixer. In the production method according to the present invention, stirring was performed by a simple method of circulating by a commercially available circulation pump. Although there is no particular limitation on the strength of stirring, such as the discharge amount of the circulation pump, it is not necessary to perform vigorous stirring that generates bubbles.
[Method for producing hydro-biofuel]
Next, a method for producing a hydrated biofuel using the hydrated biofuel additive produced as described above will be described.
撹拌機を使用し、燃料油であるA重油6.0kg(60重量部)と前記のようにして製造された加水バイオ燃料用添加剤2.0kg(20重量部)を混合し、5分間撹拌する。撹拌時間はこれに限定するものではなく、前記原料の配合割合や量の違いで適宜調整することができる。この攪拌時間は、例えば、5〜10分間としてもよい。 Using a stirrer, 6.0 kg (60 parts by weight) of fuel oil A heavy oil and 2.0 kg (20 parts by weight) of the additive for hydrobiofuel produced as described above are mixed and stirred for 5 minutes. To do. The stirring time is not limited to this, and can be appropriately adjusted depending on the mixing ratio and amount of the raw materials. This stirring time may be, for example, 5 to 10 minutes.
前記撹拌作業によって十分に撹拌することにより、燃料油の中に加水バイオ燃料用添加剤を満遍なく均一に混合することが重要である。満遍なく均一に混合することで、この後加えられる水を燃料油の中に均一に分散し、可溶化・包含させることが可能になる。 It is important to uniformly and uniformly mix the additive for hydrobiofuel into the fuel oil by sufficiently stirring by the stirring operation. By mixing evenly and uniformly, the water added thereafter can be uniformly dispersed in the fuel oil, solubilized and included.
次に、燃料油に加水バイオ燃料用添加剤が加えられ撹拌された溶液に、水2.0kg(20重量部)を加えながら、さらに撹拌する。この撹拌時間は本実施例では10分間であるが、撹拌時間はこれに限定するものではなく、各原料の配合割合や量の違いで適宜調整することができる。この攪拌時間は、例えば、5〜10分間としてもよい。 Next, the mixture is further stirred while adding 2.0 kg (20 parts by weight) of water to the stirred solution obtained by adding the additive for hydrobiofuel to the fuel oil. This stirring time is 10 minutes in this embodiment, but the stirring time is not limited to this, and can be appropriately adjusted depending on the blending ratio and amount of each raw material. This stirring time may be, for example, 5 to 10 minutes.
このような工程を経ることで、燃料油中には水の粒子が細かくなって均等に分散し、可溶化・包含されたものと思われ、乳化することなく、原料の燃料油であるA重油そのものと同等の透明度を有する加水バイオ燃料10.0kgを製造することができた。 Through these steps, it is considered that the water particles are finely dispersed and evenly dispersed in the fuel oil, solubilized and included, and the fuel oil A is the raw fuel oil without being emulsified. It was possible to produce 10.0 kg of hydrated biofuel having transparency equivalent to itself.
なお、加水バイオ燃料を製造する際に各成分を混合する順序は、燃料油に加水バイオ燃料用添加剤を入れた後、水を入れるのが重要である。加水バイオ燃料用添加剤と水を直接混合するとドロドロの粘性を有する状態となるため、混合する順序に間違いがないようにする。 In addition, it is important to add water after adding the additive for hydration biofuels to fuel oil as the order which mixes each component when manufacturing a hydration biofuel. When the additive for water-added biofuel and water are mixed directly, it will have a muddy viscosity, so the order of mixing should be correct.
また、加水バイオ燃料の製造に使用する撹拌機は、本実施例ではラインミキサーであるが、他の撹拌機を使用することもできる。また、本実施例に係る加水バイオ燃料用添加剤を使用した加水バイオ燃料は、原料である水の種類について特に限定することなく使用することができる。つまり、いわゆる硬水でも軟水でも使用することができ、普通の水道水や井戸水を使用することもできる。 Moreover, although the stirrer used for manufacture of hydrated biofuel is a line mixer in a present Example, another stirrer can also be used. Moreover, the hydrated biofuel which uses the additive for hydrated biofuel which concerns on a present Example can be used without specifically limiting about the kind of water which is a raw material. That is, so-called hard water or soft water can be used, and ordinary tap water or well water can also be used.
本実施例に係る加水バイオ燃料の外観を経時的に観察した結果について以下に説明する。
比較対象となる燃料としては、本実施例の加水バイオ燃料の原料であり、漁船の燃料として使用しているものと同等のA重油を使用した。
The results of observing the appearance of the hydrobiofuel according to this example over time will be described below.
As a fuel to be compared, A heavy oil equivalent to that used as a fuel for fishing boats was used as a raw material for the hydrobiofuel of this example.
表1は、A重油と、本実施例に係る加水バイオ燃料の製造後における経過時間の異なるサンプルS1、S2の外観を示すデータである。 Table 1 is the data which shows the external appearance of sample S1 and S2 from which elapsed time after manufacture of the A heavy oil and the hydrobiofuel which concerns on a present Example differs.
〔考察〕
表1から分かるように、製造直後のサンプルS1は、原料の燃料油であるA重油そのものとそれ程違わない透明度を有しており、更に、製造後878日(約二年五ヶ月)が経過したサンプルS2もサンプルS1に比べれば色濃くなったが透明度を有する状態を維持していた。また、サンプルS1、S2共に燃料油であるA重油と水の分離も二層化も認められなかった。このように、本実施例に係る加水バイオ燃料は、製造後、長期にわたって燃料油と水の分離及び二層化が起こらない状態を維持できることがわかった。
〔燃焼試験〕
本実施例に係る加水バイオ燃料の燃焼試験の結果について以下に説明する。
[Discussion]
As can be seen from Table 1, the sample S1 immediately after production has a transparency that is not so different from the A fuel oil itself, which is the raw fuel oil, and 878 days (about 2 years and 5 months) have passed since the production. Sample S2 was also darker than sample S1, but maintained a state of transparency. In addition, neither sample S1 nor sample S2 was separated into a fuel oil A fuel oil and water, nor was it layered. Thus, it was found that the hydrobiofuel according to this example can maintain a state in which separation and bilayering of fuel oil and water do not occur over a long period of time after production.
[Combustion test]
The result of the combustion test of the hydrous biofuel according to this example will be described below.
比較対象となる燃料としては、本実施例の加水バイオ燃料の原料であり、漁船の燃料として使用しているものと同等のA重油を使用した。
また、A重油と本実施例に係る加水バイオ燃料との燃焼試験は、バーナーボイラーを使用して行った。データの測定は、環境衛生科学研究所において、オルザット法、円形ろ紙法、化学発光法、中和滴定法など、JIS規格に沿った測定方法で測定した。
As a fuel to be compared, A heavy oil equivalent to that used as a fuel for fishing boats was used as a raw material for the hydrobiofuel of this example.
Moreover, the combustion test of A heavy oil and the hydrated biofuel which concerns on a present Example was done using the burner boiler. Data was measured at the Institute of Environmental Health Sciences using a measuring method in accordance with JIS standards such as the Orsat method, circular filter paper method, chemiluminescence method, and neutralization titration method.
具体的には、CO2等の排出ガス組成をオルザット法、煤塵濃度を円形ろ紙法、窒素酸化物濃度を化学発光法、硫黄酸化物濃度を中和滴定法、水分量を吸湿管法、酸素濃度をジルコニア式で測定した。 Specifically, the exhaust gas composition such as CO 2 is the Orzat method, the dust concentration is the circular filter paper method, the nitrogen oxide concentration is the chemiluminescence method, the sulfur oxide concentration is the neutralization titration method, the moisture content is the moisture absorption tube method, oxygen The concentration was measured by the zirconia method.
なお、使用したバーナーボイラーは、三州社製のビニールハウス暖房機SK−200KM−DFであり、使用した循環ポンプは、荏原製作所社製の15GPE6.4型であり、ラインミキサーは、OHR社製のスタティクミキサーF型を使用した。 The burner boiler used was a greenhouse SK-200KM-DF manufactured by Sanshu Co., Ltd., the circulation pump used was 15GPE 6.4 model manufactured by Ebara Seisakusho, and the line mixer was manufactured by OHR. The static mixer F type was used.
表2は、A重油と、本実施例に係る加水バイオ燃料の製造後における経過時間の異なるサンプルS1、S2の燃焼性能を比較したデータである。 Table 2 shows data comparing the combustion performance of Samples S1 and S2 having different elapsed times after the manufacture of the heavy fuel oil A and the hydrobiofuel according to this example.
〔考察〕
表2から、本実施例に係る加水バイオ燃料は、A重油と比較して燃焼温度がやや向上することが認められた。また、加水バイオ燃料は、温室効果ガスであるCO2を始めとする
煤塵、窒素酸化物、硫黄酸化物等の各種環境汚染物質の排出量が大幅に低減することがわかった。しかも、加水バイオ燃料の製造後における経過時間に関わらず、サンプルS1、S2は、ほぼ同等の値を示した。
[Discussion]
From Table 2, it was recognized that the combustion biofuel which concerns on a present Example raises a combustion temperature a little compared with A heavy oil. Also, hydrolytic biofuel was found to dust including CO 2, a greenhouse gas, nitrogen oxides emissions of various environmental pollutants such as sulfur oxides is greatly reduced. Moreover, the samples S1 and S2 showed almost the same value regardless of the elapsed time after the production of the hydrobiofuel.
また、前記燃焼試験の結果から、一応次のようにまとめることができる。
すなわち、バーナーボイラーでの加水バイオ燃料の燃焼は、燃料油であるA重油滴の燃焼であり、A重油滴の表面に物理的現象により気化したA重油と空気中の酸素が混合気を形成して燃焼が進行するようである。そして、加水バイオ燃料に含まれている水の粒子がこの燃焼により輻射熱を受けて加熱され、沸点に達して次々とミクロ爆発を起こし、周囲のA重油滴を飛散させることによりA重油の二次微粒化が起こるものと考えられる。
Moreover, it can be summarized as follows from the result of the combustion test.
That is, the combustion of the hydro-biofuel in the burner boiler is the combustion of A heavy oil droplets that are fuel oil, and the A heavy oil vaporized by the physical phenomenon and the oxygen in the air form a mixture on the surface of the A heavy oil droplets. It seems that combustion proceeds. The water particles contained in the hydro-biofuel are heated by receiving radiant heat from this combustion, reach the boiling point, cause micro explosions one after another, and scatter secondary A heavy oil droplets by scattering the surrounding A heavy oil droplets. It is thought that atomization occurs.
このように、燃料油であるA重油が瞬時に細かくなる(超微粒化する)ことにより、空気との接触面積が増大し、急速に完全燃焼が行なわれ、燃焼排ガス中の煤煙や未燃炭素の発生を抑えると思われる。また、この接触面積の増大は、燃焼に必要な空気量が過剰になることを抑え、排気ガスによる熱の持ち去りを低く抑えることができるので、省エネルギー効果が大きくなる。 As described above, the fuel oil A, which is instantly fine (ultra-fine), increases the contact area with the air and rapidly complete combustion, soot and unburned carbon in the combustion exhaust gas. It seems to suppress the occurrence of. Further, the increase in the contact area can suppress an excessive amount of air necessary for combustion, and can suppress the removal of heat by the exhaust gas, so that the energy saving effect is increased.
この条件を満たすためには、燃料油の粒子の中に水の粒子を細かくして均一に分散・包含させることが最も重要であるが、通常、水の粒子は表面張力が比較的大きいため、例えば20〜40ナノメートルまで細かくすることは困難であり、従来のエマルジョン燃料はこの水の粒子を細かくすることが十分にできていないために乳化した状態となっていた。 In order to satisfy this condition, it is most important to finely and uniformly disperse and include water particles in the fuel oil particles. However, since water particles usually have a relatively large surface tension, For example, it is difficult to reduce the fineness to 20 to 40 nanometers, and conventional emulsion fuels are in an emulsified state because the water particles are not sufficiently fine.
表3は、本実施例の加水バイオ燃料と従来のエマルジョン燃料の特徴の比較を示したものである。エマルジョン燃料については、日本国内だけでも数多くの会社が実験、研究を行っており、容易に入手することができる。ここでは、その中の1つのエマルジョン燃料を比較例として使用した。 Table 3 shows a comparison of the characteristics of the hydrated biofuel of this example and the conventional emulsion fuel. With regard to emulsion fuel, many companies in Japan are conducting experiments and research and can easily obtain them. Here, one of the emulsion fuels was used as a comparative example.
本実施例に係る加水バイオ燃料用添加剤は、燃料油に混合される水の粒径を20〜40ナノメートルまで細かくすることが可能であると思われる。水の粒径がナノメートル単位であることは、水がA重油に可溶化し、乳化することなく、透明度がA重油とそれ程変わらないことで証明することができる。これにより、加水バイオ燃料を単なる燃料油・水の混合ではなく、燃料油であるA重油の粒子の中に細かくなった水の粒子が均一に分散した可溶化・包含状態とすることができる。 It seems that the additive for hydrobiofuel according to the present example can make the particle size of water mixed with fuel oil finer to 20 to 40 nanometers. The fact that the particle size of water is in nanometer units can be proved by the fact that water is solubilized in A heavy oil and does not emulsify and the transparency is not so different from that of A heavy oil. Thus, the hydrobiofuel can be brought into a solubilized / included state in which finely divided water particles are dispersed uniformly in the particles of the A fuel oil, which is fuel oil, instead of simply mixing fuel oil and water.
なお、エマルジョン燃料に含まれる水の粒子の大きさはマイクロメートル単位であり、ナノメートル単位まで細かくすることができないために乳化した状態となる。
このように、本実施例に係る加水バイオ燃料は、エマルジョン燃料と比較して、燃焼温度・燃焼効率及び燃焼カロリーが高く燃費が低下しない。また、燃料油と水が乳化することなく透き通った包含状態となっているために分離したり二層化することがない。したがって、長期にわたる貯蔵と、輸送をすることが可能であり、装置の腐食等、燃焼機関への影響も低減できる。
〔発電機出力試験〕
続いて、本実施例に係る加水バイオ燃料の発電機出力試験の結果について以下に説明する。この試験では、発電機として、西鉄テクノサービス株式会社建設機械事業部の福岡営業所にある型式DCA90SPH(発電機容量90KVA/220V/60Hz/236A/力率0.8)の発電機を使用し、また、負荷装置として同営業所の型式LE−125の装置を使用した。
In addition, since the size of the water particles contained in the emulsion fuel is in a micrometer unit and cannot be reduced to a nanometer unit, it is in an emulsified state.
Thus, the hydrobiofuel according to the present embodiment has a high combustion temperature / combustion efficiency and combustion calorie as compared with the emulsion fuel, and the fuel consumption does not decrease. Further, since the fuel oil and water are in a transparent inclusion state without being emulsified, they are not separated or double-layered. Therefore, it can be stored and transported for a long time, and the influence on the combustion engine such as corrosion of the apparatus can be reduced.
[Generator output test]
Then, the result of the generator output test of the water biofuel which concerns on a present Example is demonstrated below. In this test, a generator of type DCA90SPH (generator capacity 90KVA / 220V / 60Hz / 236A / power factor 0.8) located in the Fukuoka office of the construction machinery division of Nishitetsu Techno Service Co., Ltd. is used as the generator. Moreover, the apparatus of the type LE-125 of the same sales office was used as a load apparatus.
比較対象となる燃料としては、本実施例の加水バイオ燃料の原料であり、漁船の燃料として使用しているものと同等のA重油を使用した。
その結果を、以下の表4に示す。
As a fuel to be compared, A heavy oil equivalent to that used as a fuel for fishing boats was used as a raw material for the hydrobiofuel of this example.
The results are shown in Table 4 below.
表4に示すように、負荷率100%の場合には、実施例Aは比較例aと比べてやや回転数の低下が確認された。しかし、電流値は、発電機に設けられた自動電圧調整器によって定格電流を発生させることで、実施例Aと比較例aとの間で差は認められなかった。 As shown in Table 4, when the load factor was 100%, it was confirmed that the rotational speed of Example A was slightly lower than that of Comparative Example a. However, no difference was found between Example A and Comparative Example a in terms of current value by generating a rated current with an automatic voltage regulator provided in the generator.
さらに、上記の試験に使用した加水バイオ燃料中のA重油の代わりに軽油を使用して製造した加水バイオ燃料についても、上記と同様の発電機出力試験を行った。ここでは、比較対象となる燃料として、当該加水バイオ燃料の原料である軽油を使用した。 Furthermore, the generator output test similar to the above was conducted also about the hydrobiofuel manufactured using light oil instead of the heavy oil A in the hydrobiofuel used for said test. Here, the light oil which is the raw material of the said hydrobiofuel was used as a fuel used as a comparison object.
その結果を、以下の表5に示す。 The results are shown in Table 5 below.
表5に示すように、負荷率100%の場合には、実施例Bは比較例bと比べてやや回転数の低下が確認された。しかし、電流値は、発電機に設けられた自動電圧調整器によって定格電流を発生させることで、実施例Bと比較例bとの間で差は認められなかった。 As shown in Table 5, when the load factor was 100%, the rotational speed of Example B was confirmed to be slightly lower than that of Comparative Example b. However, as for the current value, no difference was observed between Example B and Comparative Example b by generating a rated current with an automatic voltage regulator provided in the generator.
以上より、発電機出力試験では、本発明に加水バイオ燃料(実施例AおよびB)とJIS燃料(比較例aおよびb)との間で同等の出力が得られることが確認された。
以上、本発明について説明したが、本発明は上記実施形態だけに限定されるものではない。上記実施形態は例示であり、本発明の特許請求の範囲に記載された技術的思想と実質的に同一な構成を有し同様な作用効果を奏するものは、いかなるものであっても本発明の技術範囲に包含される。
From the above, in the generator output test, it was confirmed that the present invention can obtain an equivalent output between the hydrated biofuel (Examples A and B) and the JIS fuel (Comparative Examples a and b).
As mentioned above, although this invention was demonstrated, this invention is not limited only to the said embodiment. The above-described embodiment is an exemplification, and any device that has substantially the same configuration as the technical idea described in the claims of the present invention and has the same operational effects can be used. Included in the technical scope.
Claims (12)
加水バイオ燃料用添加剤。 A surfactant, a glycol-based alcohol, an alcohol that can be synthesized from biomass, and ammonia;
Additive for hydro-biofuel.
当該加水バイオ燃料用添加剤の組成が、前記界面活性剤55〜70重量部、前記グリコール系アルコール10〜15重量部、前記バイオマスから合成できるアルコール15〜25重量部、及び前記アンモニア水(25%溶液)5.5〜8.8重量部である、
請求項1に記載の加水バイオ燃料用添加剤。 The ammonia is aqueous ammonia,
The composition of the additive for hydrobiofuel is 55 to 70 parts by weight of the surfactant, 10 to 15 parts by weight of the glycol alcohol, 15 to 25 parts by weight of alcohol that can be synthesized from the biomass, and the aqueous ammonia (25% Solution) 5.5 to 8.8 parts by weight,
The additive for hydrobiofuel according to claim 1.
請求項1に記載の加水バイオ燃料用添加剤。 The composition of the additive for hydrobiofuel is a solution prepared by mixing 55 to 70 parts by weight of the surfactant, 10 to 15 parts by weight of the glycol alcohol, and 15 to 25 parts by weight of alcohol that can be synthesized from the biomass. 1.25 to 2.0 liters of the ammonia was dissolved per 100 g.
The additive for hydrobiofuel according to claim 1.
請求項1から3の何れか1項に記載の加水バイオ燃料用添加剤。 The surfactant is one or more surfactants selected from fatty acids having 16 or more carbon atoms,
The additive for hydrobiofuel according to any one of claims 1 to 3.
請求項4に記載の加水バイオ燃料用添加剤。 The fatty acid having 16 or more carbon atoms is palmitic acid, palmitoleic acid, margaric acid, stearic acid, oleic acid, paxenoic acid, linoleic acid, linolenic acid, eleostearic acid, tuberculostearic acid, arachidic acid, arachidonic acid, Selected from the group consisting of behenic acid, lignoceric acid, nervonic acid, serotic acid, montanic acid or melissic acid,
The additive for hydrobiofuel according to claim 4.
請求項1から5の何れか1項に記載の加水バイオ燃料用添加剤。 The glycol alcohol is one or more glycol alcohols selected from the group consisting of ethylene glycol, propylene glycol, diethylene glycol, and polyethylene glycol.
The additive for hydrobiofuel according to any one of claims 1 to 5.
請求項1から6の何れか1項に記載の加水バイオ燃料用添加剤。 The alcohol that can be synthesized from the biomass is an alcohol that can be synthesized from one or more types of biomass selected from the group consisting of ethanol, methanol, propanol, and butanol.
The additive for hydrobiofuel according to any one of claims 1 to 6.
加水バイオ燃料用添加剤の製造方法。 A step of mixing and stirring 55 to 70 parts by weight of a surfactant, 10 to 15 parts by weight of a glycol-based alcohol, and 15 to 25 parts by weight of an alcohol that can be synthesized from biomass, and aqueous ammonia (25% solution) 5 in the resulting mixed solution Adding 5 to 8.8 parts by weight, and further stirring and mixing. A method for producing an additive for a hydrobiofuel.
加水バイオ燃料。 The fuel oil is blended with water and the additive for a hydrobiofuel according to any one of claims 1 to 7, and water particles are finely dispersed and solubilized in the fuel oil.
Water biofuel.
請求項9に記載の加水バイオ燃料。 The fuel oil is one kind of fuel oil selected from the group consisting of A heavy oil, gasoline, light oil, kerosene, kerosene, vegetable oil, biodiesel fuel,
The hydrated biofuel according to claim 9.
請求項9又は10に記載の加水バイオ燃料。 The composition of the hydrated biofuel is 58 to 62 parts by weight of the fuel oil, 15 to 20 parts by weight of the additive for hydrated biofuel, and 18 to 27 parts by weight of the water.
The water-added biofuel according to claim 9 or 10.
加水バイオ燃料の製造方法。 A step of mixing and stirring 58 to 62 parts by weight of fuel oil and 15 to 20 parts by weight of the additive for hydrobiofuel according to any one of claims 1 to 7, and water 18 Adding ~ 27 parts by weight, stirring and mixing to solubilize water in the fuel oil,
A method for producing a hydrated biofuel.
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US5004479A (en) * | 1986-06-09 | 1991-04-02 | Arco Chemical Technology, Inc. | Methanol as cosurfactant for microemulsions |
JP2010095683A (en) * | 2008-10-20 | 2010-04-30 | Kazuyuki Umemura | Water-mixed fuel, additive adjusted fuel oil, additive, and method for producing them |
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JP2930909B2 (en) * | 1996-08-01 | 1999-08-09 | 五郎 石田 | Emulsion fuel generation method and apparatus, and emulsion fuel combustion apparatus |
BR9915587A (en) * | 1998-11-23 | 2001-08-07 | Pure Energy Corp | Fuel composition |
JP2001011477A (en) * | 1999-06-30 | 2001-01-16 | Goro Ishida | Surface active agent composition and emulsified fuel containing the same |
US20080086934A1 (en) * | 2006-10-16 | 2008-04-17 | Cunningham Lawrence J | Protecting fuel delivery systems in engines combusting ethanol-containing fuels |
JP2008255208A (en) * | 2007-04-04 | 2008-10-23 | Masayuki Furuno | Additive for water-solubilized oil, method for producing the same additive, and method for producing water-solubilized oil by using the same additive |
US20090260280A1 (en) * | 2008-04-17 | 2009-10-22 | Klausmeier William H | Method of formulating a fuel composition for use in internal-combustion engines |
US20090260278A1 (en) * | 2008-04-17 | 2009-10-22 | Klausmeier William H | Fuel compositions |
US20090260279A1 (en) * | 2008-04-17 | 2009-10-22 | Klausmeier William H | Biodiesel and diesel compositions |
US8450536B2 (en) * | 2008-07-17 | 2013-05-28 | Pioneer Energy, Inc. | Methods of higher alcohol synthesis |
JP2011184569A (en) * | 2010-03-09 | 2011-09-22 | Yoshida Takeyoshi | Glycerine-blended fuel and method for producing the same |
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US5004479A (en) * | 1986-06-09 | 1991-04-02 | Arco Chemical Technology, Inc. | Methanol as cosurfactant for microemulsions |
JP2010095683A (en) * | 2008-10-20 | 2010-04-30 | Kazuyuki Umemura | Water-mixed fuel, additive adjusted fuel oil, additive, and method for producing them |
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US20130291429A1 (en) | 2013-11-07 |
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