JP5750708B2 - Hydrolyzed fuel and additive-adjusted fuel oil and additive and method for producing them - Google Patents
Hydrolyzed fuel and additive-adjusted fuel oil and additive and method for producing them Download PDFInfo
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- JP5750708B2 JP5750708B2 JP2010071293A JP2010071293A JP5750708B2 JP 5750708 B2 JP5750708 B2 JP 5750708B2 JP 2010071293 A JP2010071293 A JP 2010071293A JP 2010071293 A JP2010071293 A JP 2010071293A JP 5750708 B2 JP5750708 B2 JP 5750708B2
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- 239000000295 fuel oil Substances 0.000 title claims description 60
- 239000000446 fuel Substances 0.000 title claims description 54
- 230000000996 additive effect Effects 0.000 title claims description 45
- 238000004519 manufacturing process Methods 0.000 title claims description 36
- 239000002816 fuel additive Substances 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 56
- 239000000654 additive Substances 0.000 claims description 51
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 26
- 239000003921 oil Substances 0.000 claims description 26
- 235000019198 oils Nutrition 0.000 claims description 26
- POULHZVOKOAJMA-UHFFFAOYSA-N dodecanoic acid Chemical compound CCCCCCCCCCCC(O)=O POULHZVOKOAJMA-UHFFFAOYSA-N 0.000 claims description 24
- QGZKDVFQNNGYKY-UHFFFAOYSA-N ammonia Natural products N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 22
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 21
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 21
- 150000001298 alcohols Chemical class 0.000 claims description 20
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 19
- 229930195729 fatty acid Natural products 0.000 claims description 19
- 239000000194 fatty acid Substances 0.000 claims description 19
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims description 18
- 150000004665 fatty acids Chemical class 0.000 claims description 18
- 238000002156 mixing Methods 0.000 claims description 16
- 239000000203 mixture Substances 0.000 claims description 16
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 14
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 12
- MBMBGCFOFBJSGT-KUBAVDMBSA-N all-cis-docosa-4,7,10,13,16,19-hexaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCC(O)=O MBMBGCFOFBJSGT-KUBAVDMBSA-N 0.000 claims description 12
- 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 12
- 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 12
- GHVNFZFCNZKVNT-UHFFFAOYSA-N decanoic acid Chemical compound CCCCCCCCCC(O)=O GHVNFZFCNZKVNT-UHFFFAOYSA-N 0.000 claims description 12
- UKMSUNONTOPOIO-UHFFFAOYSA-N docosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCCCC(O)=O UKMSUNONTOPOIO-UHFFFAOYSA-N 0.000 claims description 12
- IPCSVZSSVZVIGE-UHFFFAOYSA-N hexadecanoic acid Chemical compound CCCCCCCCCCCCCCCC(O)=O IPCSVZSSVZVIGE-UHFFFAOYSA-N 0.000 claims description 12
- VKOBVWXKNCXXDE-UHFFFAOYSA-N icosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCC(O)=O VKOBVWXKNCXXDE-UHFFFAOYSA-N 0.000 claims description 12
- WWZKQHOCKIZLMA-UHFFFAOYSA-N octanoic acid Chemical compound CCCCCCCC(O)=O WWZKQHOCKIZLMA-UHFFFAOYSA-N 0.000 claims description 12
- 239000002994 raw material Substances 0.000 claims description 11
- 239000003350 kerosene Substances 0.000 claims description 8
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims description 7
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims description 7
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims description 7
- 239000005642 Oleic acid Substances 0.000 claims description 7
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims description 7
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims description 7
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims description 7
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 claims description 7
- HOBAELRKJCKHQD-UHFFFAOYSA-N (8Z,11Z,14Z)-8,11,14-eicosatrienoic acid Natural products CCCCCC=CCC=CCC=CCCCCCCC(O)=O HOBAELRKJCKHQD-UHFFFAOYSA-N 0.000 claims description 6
- 235000021357 Behenic acid Nutrition 0.000 claims description 6
- 239000005632 Capric acid (CAS 334-48-5) Substances 0.000 claims description 6
- 239000005635 Caprylic acid (CAS 124-07-2) Substances 0.000 claims description 6
- 235000021298 Dihomo-γ-linolenic acid Nutrition 0.000 claims description 6
- OPGOLNDOMSBSCW-CLNHMMGSSA-N Fursultiamine hydrochloride Chemical compound Cl.C1CCOC1CSSC(\CCO)=C(/C)N(C=O)CC1=CN=C(C)N=C1N OPGOLNDOMSBSCW-CLNHMMGSSA-N 0.000 claims description 6
- 239000005639 Lauric acid Substances 0.000 claims description 6
- 235000021353 Lignoceric acid Nutrition 0.000 claims description 6
- CQXMAMUUWHYSIY-UHFFFAOYSA-N Lignoceric acid Natural products CCCCCCCCCCCCCCCCCCCCCCCC(=O)OCCC1=CC=C(O)C=C1 CQXMAMUUWHYSIY-UHFFFAOYSA-N 0.000 claims description 6
- 235000021314 Palmitic acid Nutrition 0.000 claims description 6
- 235000021355 Stearic acid Nutrition 0.000 claims description 6
- 235000020661 alpha-linolenic acid Nutrition 0.000 claims description 6
- 235000021342 arachidonic acid Nutrition 0.000 claims description 6
- 229940114079 arachidonic acid Drugs 0.000 claims description 6
- 229940116226 behenic acid Drugs 0.000 claims description 6
- HOBAELRKJCKHQD-QNEBEIHSSA-N dihomo-γ-linolenic acid Chemical compound CCCCC\C=C/C\C=C/C\C=C/CCCCCCC(O)=O HOBAELRKJCKHQD-QNEBEIHSSA-N 0.000 claims description 6
- 235000020669 docosahexaenoic acid Nutrition 0.000 claims description 6
- 229940090949 docosahexaenoic acid Drugs 0.000 claims description 6
- 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 6
- VZCCETWTMQHEPK-UHFFFAOYSA-N gamma-Linolensaeure Natural products CCCCCC=CCC=CCC=CCCCCC(O)=O VZCCETWTMQHEPK-UHFFFAOYSA-N 0.000 claims description 6
- VZCCETWTMQHEPK-QNEBEIHSSA-N gamma-linolenic acid Chemical compound CCCCC\C=C/C\C=C/C\C=C/CCCCC(O)=O VZCCETWTMQHEPK-QNEBEIHSSA-N 0.000 claims description 6
- 235000020664 gamma-linolenic acid Nutrition 0.000 claims description 6
- 229960002733 gamolenic acid Drugs 0.000 claims description 6
- 235000011187 glycerol Nutrition 0.000 claims description 6
- 239000013067 intermediate product Substances 0.000 claims description 6
- 229960004488 linolenic acid Drugs 0.000 claims description 6
- WQEPLUUGTLDZJY-UHFFFAOYSA-N n-Pentadecanoic acid Natural products CCCCCCCCCCCCCCC(O)=O WQEPLUUGTLDZJY-UHFFFAOYSA-N 0.000 claims description 6
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims description 6
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims description 6
- 229960002446 octanoic acid Drugs 0.000 claims description 6
- 229960002969 oleic acid Drugs 0.000 claims description 6
- 235000021313 oleic acid Nutrition 0.000 claims description 6
- 238000000926 separation method Methods 0.000 claims description 6
- 239000008117 stearic acid Substances 0.000 claims description 6
- JIWBIWFOSCKQMA-UHFFFAOYSA-N stearidonic acid Natural products CCC=CCC=CCC=CCC=CCCCCC(O)=O JIWBIWFOSCKQMA-UHFFFAOYSA-N 0.000 claims description 6
- TUNFSRHWOTWDNC-HKGQFRNVSA-N tetradecanoic acid Chemical compound CCCCCCCCCCCCC[14C](O)=O TUNFSRHWOTWDNC-HKGQFRNVSA-N 0.000 claims description 6
- 239000002699 waste material Substances 0.000 claims description 6
- JAZBEHYOTPTENJ-JLNKQSITSA-N all-cis-5,8,11,14,17-icosapentaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCCC(O)=O JAZBEHYOTPTENJ-JLNKQSITSA-N 0.000 claims description 5
- 235000020673 eicosapentaenoic acid Nutrition 0.000 claims description 5
- JAZBEHYOTPTENJ-UHFFFAOYSA-N eicosapentaenoic acid Natural products CCC=CCC=CCC=CCC=CCC=CCCCC(O)=O JAZBEHYOTPTENJ-UHFFFAOYSA-N 0.000 claims description 5
- 229960005135 eicosapentaenoic acid Drugs 0.000 claims description 5
- 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 4
- 239000010775 animal oil Substances 0.000 claims description 4
- 230000001143 conditioned effect Effects 0.000 claims description 4
- 239000003502 gasoline Substances 0.000 claims description 4
- 230000036571 hydration Effects 0.000 claims description 4
- 238000006703 hydration reaction Methods 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
- 239000002253 acid Substances 0.000 claims description 3
- 239000010779 crude oil Substances 0.000 claims description 3
- 239000002351 wastewater Substances 0.000 claims description 2
- DPUOLQHDNGRHBS-UHFFFAOYSA-N Brassidinsaeure Natural products CCCCCCCCC=CCCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-UHFFFAOYSA-N 0.000 claims 4
- URXZXNYJPAJJOQ-UHFFFAOYSA-N Erucic acid Natural products CCCCCCC=CCCCCCCCCCCCC(O)=O URXZXNYJPAJJOQ-UHFFFAOYSA-N 0.000 claims 4
- DPUOLQHDNGRHBS-KTKRTIGZSA-N erucic acid Chemical compound CCCCCCCC\C=C/CCCCCCCCCCCC(O)=O DPUOLQHDNGRHBS-KTKRTIGZSA-N 0.000 claims 4
- 150000007513 acids Chemical class 0.000 claims 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 10
- 238000003756 stirring Methods 0.000 description 10
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 8
- 239000000839 emulsion Substances 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 5
- 239000006185 dispersion Substances 0.000 description 5
- FERIUCNNQQJTOY-UHFFFAOYSA-N Butyric acid Chemical compound CCCC(O)=O FERIUCNNQQJTOY-UHFFFAOYSA-N 0.000 description 4
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 4
- -1 amine compound Chemical class 0.000 description 4
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 4
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 4
- FUZZWVXGSFPDMH-UHFFFAOYSA-N hexanoic acid Chemical compound CCCCCC(O)=O FUZZWVXGSFPDMH-UHFFFAOYSA-N 0.000 description 4
- 239000004094 surface-active agent Substances 0.000 description 4
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 description 4
- 239000000499 gel Substances 0.000 description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 3
- XFRVVPUIAFSTFO-UHFFFAOYSA-N 1-Tridecanol Chemical compound CCCCCCCCCCCCCO XFRVVPUIAFSTFO-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000001530 fumaric acid Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- KJIOQYGWTQBHNH-UHFFFAOYSA-N undecanol Chemical compound CCCCCCCCCCCO KJIOQYGWTQBHNH-UHFFFAOYSA-N 0.000 description 2
- 229940005605 valeric acid Drugs 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- ZVWHEFMEBWIIII-UHFFFAOYSA-N C(C=C/C(=O)O)(=O)O.C(CCCCCCCCCCCC=C/CCCCCCCC)(=O)O Chemical compound C(C=C/C(=O)O)(=O)O.C(CCCCCCCCCCCC=C/CCCCCCCC)(=O)O ZVWHEFMEBWIIII-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
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- 150000002148 esters Chemical class 0.000 description 1
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- 239000010419 fine particle Substances 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 229940098895 maleic acid Drugs 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
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- 150000003384 small molecules Chemical class 0.000 description 1
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- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
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Description
本発明は、加水燃料と、加水により加水燃料になり得る加水前の調整燃料油と、それに加える添加剤、並びに、それらの製造方法に関する。 The present invention relates to a hydrated fuel, a conditioned fuel oil that can be converted into a hydrated fuel by hydration, an additive to be added thereto, and a production method thereof.
石油資源の枯渇や、石油使用に伴う環境問題などにより、燃料油に水を混合させた加水燃料が注目を浴びている。加水燃料は、燃料油のみを燃焼させた場合と同等の燃焼効率を得ることは既に公知であり、各種のものが提案されている。
従来の加水燃料に関する技術には、例えば特許文献1〜4がある。
Due to the depletion of petroleum resources and environmental problems associated with the use of oil, water-mixed fuels that contain water and fuel oil are attracting attention. It has been already known that a hydrous fuel has a combustion efficiency equivalent to that obtained when only fuel oil is burned, and various fuels have been proposed.
For example, there are Patent Documents 1 to 4 as techniques related to conventional water-added fuel.
しかし、従来の加水燃料は、燃焼の安定性に欠ける点や、油水が分離するなど長期の安定性にかける点、油水の均一性に欠ける点などの問題があり、十分実用化に耐えるものではなかった。 However, conventional hydrofuels have problems such as lack of combustion stability, long-term stability such as separation of oil and water, and lack of uniformity of oil and water. There wasn't.
そこで、本発明は、油水の均一な分散を実現して燃焼効率を向上させると共に、その油水の均一な分散を長期に安定させられる添加剤と、その添加によって得られる添加剤調整燃料油及び加水燃料、並びに、それらの製造方法を提供することを課題とする。
特に、界面活性剤を用いなくてもよい手段を提供することを課題とする。
Therefore, the present invention achieves uniform dispersion of oil water to improve combustion efficiency, and an additive that can stabilize the uniform dispersion of oil water for a long period of time, and an additive-adjusted fuel oil and water solution obtained by the addition. It is an object of the present invention to provide a fuel and a manufacturing method thereof.
In particular, it is an object to provide a means that does not require the use of a surfactant.
上記課題を解決するために、本発明の添加剤の製造方法は、次の構成を備える。すなわち、燃料油に添加して、加水燃料、または、その加水前の調整燃料油を生成するために用いる添加剤の製造方法であって、脂肪酸類または比較的分子量の大きなアルコール類に、比較的分子量の小さなアルコール類を溶解させて、中間生成物1を生成するステップと、中間生成物1にアンモニア水またはアンモニアガスを加えて、所望の添加剤を生成するステップと、を有することを特徴とする。 In order to solve the above problems, the method for producing an additive of the present invention comprises the following configuration. That is, it is a method for producing an additive used to produce a hydrated fuel or a conditioned fuel oil prior to its addition to a fuel oil, which is relatively free from fatty acids or relatively high molecular weight alcohols. And a step of dissolving an alcohol having a low molecular weight to produce an intermediate product 1 and a step of adding ammonia water or ammonia gas to the intermediate product 1 to produce a desired additive. To do.
ここで、燃料油としては、ガソリン、灯油、軽油、A重油、B重油、C重油、原油 植物油、動物油、廃油 製紙排水黒液が利用できる。 Here, as fuel oil, gasoline, kerosene, light oil, A heavy oil, B heavy oil, C heavy oil, crude vegetable oil, animal oil, waste oil and paper wastewater black liquor can be used.
脂肪酸類としては、酪酸、吉草酸、カプロン酸、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α−リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ-リノレン酸、ジホモ−γ−リノレン酸、アラキドン酸、オレイン酸、エルカ酸マレイン酸、フマール酸、ドデカン酸のいずれか、または、そのエステルが好適である。 Fatty acids include butyric acid, valeric acid, caproic acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid, eicosapentaene Any of acid, docosahexaenoic acid, linoleic acid, γ-linolenic acid, dihomo-γ-linolenic acid, arachidonic acid, oleic acid, maleic acid erucate, fumaric acid, dodecanoic acid, or an ester thereof is suitable.
比較的分子量の大きなアルコール類としては、ペンタノール、ヘキサノール、ペンタノール、ウンデカノール、ドデカノール、トリデカノールが好適である。 As alcohols having a relatively large molecular weight, pentanol, hexanol, pentanol, undecanol, dodecanol, and tridecanol are suitable.
比較的分子量の小さなアルコール類としては、メタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンもしくはその混合物が好適である。 As the alcohol having a relatively small molecular weight, methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin or a mixture thereof is preferable.
脂肪酸類または比較的分子量の大きなアルコール類、比較的分子量の小さなアルコール類、アンモニア水またはアンモニアガスの混合比としては、1:1.0〜2.5:0.001〜0.7(mol濃度)、より好ましくは、1:1.1〜2.2:0.003〜0.2(mol濃度)が好適である。 The mixing ratio of fatty acids or relatively high molecular weight alcohols, relatively low molecular weight alcohols, ammonia water or ammonia gas is 1: 1.0 to 2.5: 0.001 to 0.7 (mol concentration). ), More preferably 1: 1.1 to 2.2: 0.003 to 0.2 (mol concentration).
本発明の添加剤は、上述の製造方法によって製造された添加剤であって、原料として少なくとも、脂肪酸類または比較的分子量の大きなアルコール類、比較的分子量の小さなアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有することを特徴とする。 The additive of the present invention is an additive produced by the above-described production method, and includes, as a raw material, at least fatty acids or relatively high molecular weight alcohols, relatively low molecular weight alcohols or mixtures thereof, aqueous ammonia or It has an ammonia gas.
本発明の添加剤調整燃料油の製造方法は、加水により加水燃料になり得る加水前の調整燃料油の製造方法であって、前記の添加剤を燃料油に加えて、所望の添加剤調整燃料油を生成するステップを有することを特徴とする。 The method for producing an additive-adjusted fuel oil according to the present invention is a method for producing an adjusted fuel oil prior to addition that can be converted to a water-added fuel by addition of water. It has the step which produces | generates oil, It is characterized by the above-mentioned.
添加剤、燃料油の混合比としては、0.03〜1:1(容積)、より好ましくは、0.10〜0.75:1(容積)が好適である。 The mixing ratio of the additive and the fuel oil is preferably 0.03 to 1: 1 (volume), more preferably 0.10 to 0.75: 1 (volume).
本発明の添加剤調整燃料油は、上述の製造方法によって製造された添加剤調整燃料油であって、添加剤の原料として少なくとも、脂肪酸類または比較的分子量の大きなアルコール類、比較的分子量の小さなアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有することを特徴とする。 The additive-adjusted fuel oil of the present invention is an additive-adjusted fuel oil produced by the above-described production method, and includes at least fatty acids or relatively high molecular weight alcohols and relatively low molecular weights as raw materials for the additives. It has an alcohol or a mixture thereof, aqueous ammonia or ammonia gas.
本発明の加水燃料の製造方法は、前記の添加剤調整燃料油に水を加えて、所望の加水燃料を生成するステップを有することを特徴とする。 The method for producing a hydrolyzed fuel according to the present invention includes a step of adding water to the additive-adjusted fuel oil to produce a desired hydrolyzed fuel.
水、添加剤調整燃料油の混合比としては、0.1〜1:1(容積)、より好ましくは、0.2〜0.6:1(容積)が好適である。 The mixing ratio of water and additive-adjusted fuel oil is preferably 0.1 to 1: 1 (volume), more preferably 0.2 to 0.6: 1 (volume).
本発明の加水燃料は、上述の製造方法によって製造された加水燃料であって、添加剤の原料として少なくとも、脂肪酸類または比較的分子量の大きなアルコール類、比較的分子量の小さなアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有することを特徴とする。 The water fuel of the present invention is a water fuel produced by the above-described production method, and at least as a raw material for the additive, at least fatty acids or relatively high molecular weight alcohols, relatively low molecular weight alcohols or mixtures thereof, It has ammonia water or ammonia gas.
本発明によって得られる加水燃料は、適切な添加剤の添加によって、油水の均一な分散が実現して燃焼効率が向上すると共に、その油水の均一な分散が長期に安定するので、加水前の調整燃料油としても運搬や保管もでき利便性が高い。
また、界面活性剤を用いなくてもよく、製造のステップも少なくて済む。
The water-added fuel obtained by the present invention achieves a uniform dispersion of oil and water by adding appropriate additives to improve combustion efficiency, and the uniform dispersion of the oil and water is stable over a long period of time. It can be transported and stored as fuel oil and is highly convenient.
Further, it is not necessary to use a surfactant, and the number of manufacturing steps can be reduced.
以下に、本発明の実施形態を、図面に示す実施例を基に説明する。なお、実施形態は下記の例示に限らず、本発明の趣旨から逸脱しない範囲で、前記特許文献など従来公知の技術を用いて適宜設計変更可能である。 Hereinafter, embodiments of the present invention will be described based on examples shown in the drawings. The embodiment is not limited to the following examples, and the design can be changed as appropriate using a conventionally known technique such as the above-mentioned patent document without departing from the gist of the present invention.
本発明者は、特定の添加剤を燃料油に加えることで、加水燃料における油水の均一な分散とその長期安定化が達成される知見を得て、特願2008−270038に「加水燃料及び添加剤調整燃料油及び添加剤とそれらの製造方法」を出願している。
なお、燃料油とは、ガソリン、灯油、軽油、A重油、B重油、C重油、原油、植物油、動物油、廃油、製紙工場廃油(黒液)等の可燃油一般を指す。そして、本発明の加水燃料は、その燃料油に所定量の水と本発明による添加剤を混合されたものである。
The present inventor has obtained the knowledge that a uniform dispersion of oil water in the hydrofuel and a long-term stabilization thereof can be achieved by adding a specific additive to the fuel oil. For the preparation of the fuel for adjusting the fuel and additives and the process for producing them.
Fuel oil generally refers to combustible oils such as gasoline, kerosene, light oil, A heavy oil, B heavy oil, C heavy oil, crude oil, vegetable oil, animal oil, waste oil, and paper mill waste oil (black liquor). And the water-added fuel of this invention mixes the predetermined amount of water and the additive by this invention with the fuel oil.
その研究の延長として、本発明者は、界面活性剤を用いなくても、加水燃料用の添加剤を生成できる知見を得て、本発明に至った。特願2008−270038と比較すると、更にアミン化合物も加えなくてもよく、製造のステップが大幅に簡素化される方法である。 As an extension of that research, the present inventor has obtained the knowledge that an additive for a hydrolyzed fuel can be produced without using a surfactant, and has reached the present invention. Compared with Japanese Patent Application No. 2008-270038, it is not necessary to add an amine compound, and this is a method that greatly simplifies the production steps.
図1は、加水燃料を生成する流れを示す説明図である。
添加剤の製造方法は次の通りである。
まず、脂肪酸類または比較的分子量の大きなアルコール類に、比較的分子量の小さなアルコール類を溶解させて、中間生成物1を生成する。
なお、脂肪酸類は、脂肪酸のみでなく脂肪酸エステルとの混合物としてもよい。
FIG. 1 is an explanatory diagram showing a flow of generating water fuel.
The method for producing the additive is as follows.
First, an intermediate product 1 is produced by dissolving relatively small molecular weight alcohols in fatty acids or relatively large molecular weight alcohols.
In addition, fatty acids are good not only as a fatty acid but as a mixture with fatty acid ester.
ここで、比較的分子量の大きなアルコール類とは、大きなアルキル基を有する液体で、例えばペンタノール、ヘキサノール、ペンタノール、ウンデカノール、ドデカノール、トリデカノール等を指す。イソ化合物など、側鎖を有するアルコールでもよい。 Here, alcohols having a relatively large molecular weight are liquids having a large alkyl group, such as pentanol, hexanol, pentanol, undecanol, dodecanol, tridecanol, and the like. Alcohol having a side chain such as an iso compound may be used.
また、比較的分子量の小さなアルコール類とは、小さなアルキル基を有する液体で、例えばメタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンもしくはその混合物等を指す。 The alcohol having a relatively small molecular weight is a liquid having a small alkyl group, and refers to, for example, methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin or a mixture thereof.
また、脂肪酸類とは、例えば酪酸、吉草酸、カプロン酸、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α-リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ-リノレン酸、ジホモ-γ-リノレン酸、アラキドン酸、オレイン酸、エルカ酸マレイン酸、フマール酸、ドデカン酸など、1〜多価の脂肪酸でメタノールまたはエタノール、プロパノールなど比較的分子量の小さなアルコール類に溶融しうるものを指す。 Examples of fatty acids include butyric acid, valeric acid, caproic acid, caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid , Eicosapentaenoic acid, docosahexaenoic acid, linoleic acid, γ-linolenic acid, dihomo-γ-linolenic acid, arachidonic acid, oleic acid, erucic acid maleic acid, fumaric acid, dodecanoic acid, etc. This refers to those that can be melted into alcohols having a relatively low molecular weight such as ethanol and propanol.
次に、上記の中間生成物1にアンモニア水またはアンモニアガスを加え、よく攪拌し一定の条件に整えて、本発明の添加剤を生成する。
アンモニアガスを過剰に加えると、添加剤がゲル化するので、量を調整することが好ましい。アンモニア水を加える場合には、水が既に存在するためにゲル化する。
生成時における反応温度は30〜40℃が好ましく、攪拌の条件は、空気の混入が少ない範囲での攪拌が好ましい。生成時には、発熱を起こすので反応が均一となるように十分に攪拌することが好ましい。
Next, ammonia water or ammonia gas is added to the intermediate product 1, and the mixture is stirred well and adjusted to a certain condition to produce the additive of the present invention.
If the ammonia gas is added excessively, the additive gels, so it is preferable to adjust the amount. When ammonia water is added, it gels because water already exists.
The reaction temperature at the time of production is preferably 30 to 40 ° C., and the stirring conditions are preferably stirring in a range where there is little air contamination. It is preferable to sufficiently stir the reaction so that the reaction becomes uniform because it generates heat during the production.
原料の混合にはさまざまな組み合わせがあるため最適な比率は原料によって異なるが、大まかな比率としては下記の値が目安として利用できる。
脂肪酸類または比較的分子量の大きなアルコール類:比較的分子量の小さなアルコール類もしくはその混合物:アンモニア水またはアンモニアガス=1:1.0〜2.5:0.001〜0.7(mol濃度)、
より好ましくは、脂肪酸類または比較的分子量の大きなアルコール類:比較的分子量の小さなアルコール類もしくはその混合物:アンモニア水またはアンモニアガス=1:1.1〜2.2:0.003〜0.2(mol濃度)である。
Since there are various combinations in mixing raw materials, the optimum ratio varies depending on the raw materials, but the following values can be used as a rough guideline.
Fatty acids or relatively high molecular weight alcohols: relatively low molecular weight alcohols or mixtures thereof: ammonia water or ammonia gas = 1: 1.0-2.5: 0.001-0.7 (mol concentration)
More preferably, fatty acids or relatively high molecular weight alcohols: relatively low molecular weight alcohols or mixtures thereof: ammonia water or ammonia gas = 1: 1.1 to 2.2: 0.003 to 0.2 ( mol concentration).
(実施例)
添加剤を製造した実施例は次の通りである。
図2のように、オレイン酸2.50molにメタノール3.94molとエチレングリコール0.55molの混合液を攪拌し、アンモニアガス0.01molを順次混合攪拌することで、添加剤が製造できた。
(Example)
Examples of manufacturing the additive are as follows.
As shown in FIG. 2, an additive could be produced by stirring a mixed solution of 3.94 mol of methanol and 0.55 mol of ethylene glycol to 2.50 mol of oleic acid, and sequentially mixing and stirring 0.01 mol of ammonia gas.
添加剤による燃料油の調整方法は次の通りである。
本発明による前述の添加剤を、ガソリン、灯油、軽油、A重油、B重油、C重油、原油、植物油、動物油、廃油、製紙工場廃油(黒液)等の燃料油に混合させ攪拌することで、添加剤調整燃料油を生成する。
この添加剤調整燃料油の状態で保存しておき、使用時に加水して加水燃料を生成してもよい。
The method for adjusting the fuel oil with the additive is as follows.
By mixing and stirring the aforementioned additives according to the present invention in fuel oil such as gasoline, kerosene, light oil, A heavy oil, B heavy oil, C heavy oil, crude oil, vegetable oil, animal oil, waste oil, paper mill waste oil (black liquor), etc. To produce additive-adjusted fuel oil.
You may preserve | save in the state of this additive adjustment fuel oil, and it may add water at the time of use, and may produce | generate a water fuel.
添加剤の原料となる脂肪酸などの種類は、添加対象の燃料油の種類によって適宜対応させて調整することで、後述の加水量も最適化することが可能となる。 It is possible to optimize the amount of water to be described later by adjusting the type of the fatty acid as the raw material of the additive as appropriate according to the type of fuel oil to be added.
添加剤の必要量は、燃料油の種類や、比較的小さな分子のアルコール類の種類およびアンモニアガス・アンモニア水の添加量にて異なるが、大まかな比率としては下記の値が目安として利用できる。
添加剤:燃料油=0.1〜1:1(容積)、
より好ましくは、添加剤:燃料油=0.2〜0.6:1(容積)である。
The required amount of additive varies depending on the type of fuel oil, the type of alcohol with relatively small molecules, and the amount of ammonia gas / ammonia water added, but the following values can be used as rough guidelines.
Additive: Fuel oil = 0.1 to 1: 1 (volume)
More preferably, additive: fuel oil = 0.2 to 0.6: 1 (volume).
(実施例)
添加剤調整燃料油を製造した実施例は次の通りである。
図3のように、軽油10リットル(容積77%)に添加剤5リットル(容積23%)を混合攪拌することで、添加剤調整燃料油が製造できた。
(Example)
Examples of producing additive-adjusted fuel oil are as follows.
As shown in FIG. 3, an additive-adjusted fuel oil could be produced by mixing and stirring 5 liters (volume 23%) of additive with 10 liters (volume 77%) of diesel oil.
添加剤調整燃料油による加水燃料の調整方法は次の通りである。
本発明による前述の添加剤調整燃料油に、水を混合させ攪拌することで、加水燃料を生成する。
攪拌時に空気が混入すると、爆発混合気を発する危惧があるので、空気の混入の皆無な攪拌が好ましい。
The adjustment method of the water-added fuel with the additive-adjusted fuel oil is as follows.
Water is mixed with the above-described additive-adjusted fuel oil according to the present invention and stirred to produce a hydrolyzed fuel.
If air is mixed at the time of stirring, there is a risk of generating an explosive air-fuel mixture, so stirring without any air mixing is preferable.
水の比率によって、生成燃料が液化したりゲル化したりする。また、水の比率が高すぎると、燃焼温度や燃焼カロリーの低下を生じる。例えば、ガスタービン用の燃料とする場合には、加水はボイラー用給水とすることが好ましい。
なお、添加剤の原料の混合比が十分適切でなかった場合や、添加剤の反応が十分に促進しなかった場合、反応温度によっては、加水後に白い沈殿物が生じることがあるが、燃焼には支障ない。
Depending on the ratio of water, the produced fuel liquefies or gels. Moreover, when the ratio of water is too high, the combustion temperature and the calorie calories are reduced. For example, when the fuel is used for a gas turbine, it is preferable that the water is supplied to the boiler.
If the mixing ratio of the raw materials for the additive is not adequate or if the reaction of the additive is not sufficiently accelerated, a white precipitate may be formed after addition depending on the reaction temperature. Is no problem.
加水量は、燃焼効率や経済効率の点では、大まかな比率としては下記の値が目安として利用できる。
水:添加剤調整燃料油=0.1〜0.8:1(容積)、
より好ましくは、水:添加剤調整燃料油=0.2〜0.6:1(容積)である。
As for the amount of water added, the following values can be used as a rough standard as a rough ratio in terms of combustion efficiency and economic efficiency.
Water: Additive-adjusted fuel oil = 0.1-0.8: 1 (volume)
More preferably, water: additive-adjusted fuel oil = 0.2 to 0.6: 1 (volume).
(実施例)
加水燃料を製造した実施例は次の通りである。
図4のように、軽油と添加剤の混合液13リットル(容積72%)に水5リットル(容積28%)を混合攪拌することで、加水燃料が製造できた。
(Example)
The example which manufactured the water fuel is as follows.
As shown in FIG. 4, the water fuel was produced by mixing and stirring 5 liters (volume 28%) of water in 13 liters (volume 72%) of the mixture of light oil and additive.
図5は、加水燃料の均一度を示す実験結果の写真である。
製造した加水燃料における灯油と添加剤と水の比率は、灯油:添加剤:水=50%:25%:25%であり、左は製造から3ヶ月経過後、右は6ヶ月経過後の状態である。
いずれの時間経過後の加水燃料も、白濁や、2層分離や、粒状の分離もなく、透明度が高く、油水が均一な混合状態が保たれた。また、この均一状態は、長期間安定して維持された。
FIG. 5 is a photograph of the experimental results showing the uniformity of the water fuel.
The ratio of kerosene / additive / water in the produced hydrofuel is kerosene: additive: water = 50%: 25%: 25%, the left is the state after 3 months from the production, the right is the state after 6 months It is.
The hydrated fuel after any lapse of time did not have white turbidity, two-layer separation, or granular separation, and had high transparency and a uniform mixed state of oil and water. This uniform state was stably maintained for a long time.
図6も、加水燃料の均一度を示す実験結果の写真である。
左側ほど、添加剤の割合が高く、灯油と添加剤と水の比率は、それぞれ、
灯油:添加剤:水=50%:25%:25%、
60%:20%:20%、
70%:15%:15%、
80%:10%:10%、
90%:5%:5%であり、
3ヶ月経過後の状態である。
いずれの混合比率の加水燃料も、白濁や、2層分離や、粒状の分離もなく、透明度が高く、油水が均一な混合状態が保たれた。また、この均一状態は、長期間安定して維持された。
FIG. 6 is also a photograph of the experimental results showing the uniformity of the water fuel.
On the left side, the ratio of the additive is high, and the ratio of kerosene, additive, and water is
Kerosene: Additive: Water = 50%: 25%: 25%
60%: 20%: 20%,
70%: 15%: 15%,
80%: 10%: 10%,
90%: 5%: 5%,
This is the state after 3 months.
The mixed fuels of any mixing ratio were not cloudy, separated into two layers, or separated into particles, and had high transparency and a uniform mixed state of oil and water. This uniform state was stably maintained for a long time.
一般に、油水の混合率や添加剤の添加率に応じて、加水燃料の様相が変化する。しかし、本発明による加水燃料では、加水の割合によって白濁が進行して透過度が減少するが、2層に分離したり、粒状の分離もなく、油水が均一な混合状態が保たれた。また、この均一状態は、長期間安定して維持され、例えば0℃の環境でも安定性が保たれた。 In general, the aspect of the water fuel changes depending on the mixing ratio of oil and water and the adding ratio of additives. However, in the water-added fuel according to the present invention, white turbidity progresses depending on the ratio of water addition and the permeability decreases. However, the oil-water is kept in a uniform mixed state without separation into two layers or granular separation. Further, this uniform state was stably maintained for a long time, and stability was maintained even in an environment of 0 ° C., for example.
加水燃料の用途は、環境問題を叫ばれる昨今需要が増えている。本発明によると、添加剤調整燃料への加水を施すことにより、明らかなCO2 、NOx、SOx、燃焼粉塵の減少などが見られる。また、アンモニウム型界面活性剤やアミン化合物を利用しないため、NOxを大幅に減らせる。
さまざまな燃料、例えば、温風ボイラー、温水ボイラー、蒸気ボイラーなどの各種ボイラーや、発電機、農業機械、自動車、船舶などのディーゼルエンジンの燃料として実用的であり、環境対策、燃料不足対策、経済上からも産業上利用価値が高い。
As for the use of water fuel, demand is increasing recently as the environmental problem is called out. According to the present invention, the reduction of CO 2 , NO x, SO x, combustion dust and the like is observed by adding water to the additive-adjusted fuel. In addition, since no ammonium type surfactant or amine compound is used, NOx can be greatly reduced.
It is practical as a fuel for various fuels, such as various types of boilers such as hot air boilers, hot water boilers, steam boilers, and diesel engines for generators, agricultural machinery, automobiles, ships, etc. From the top, the industrial utility value is high.
Claims (9)
カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α-リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ -リノレン酸、ジホモ-γ -リノレン酸、アラキドン酸、オレイン酸、エルカ酸、ドデカン酸の群から選択される脂肪酸類に、メタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンの群から選択されるアルコール類もしくはその混合物を溶解させて、中間生成物1を生成するステップと、
最後に、中間生成物1にアンモニア水またはアンモニアガスを加えて、所望の添加剤を生成するステップを有し、
脂肪酸類、アルコール類、アンモニアガスの混合比を、1:1.0〜2.5:0.001〜0.7(mol濃度)とする
ことを特徴とする添加剤の製造方法。 A method for producing an additive that is added to a fuel oil and used to produce a transparent hydrated fuel in a uniform mixed state without separation of oil or water, or a conditioned fuel oil before the hydration,
Caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid, eicosapentaenoic acid, docosahexaenoic acid, linoleic acid, γ-linolenic acid, Fatty acids selected from the group of dihomo-γ-linolenic acid, arachidonic acid, oleic acid, erucic acid , dodecanoic acid, alcohols selected from the group of methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin or Dissolving the mixture to produce intermediate product 1;
Finally, adding aqueous ammonia or ammonia gas to the intermediate product 1 to produce the desired additive,
Fatty acids, alcohols, a mixture ratio of ammonia gas, 1: 1.0~2.5: 0.001~0.7 (mol concentration) and method for producing the additive, characterized by.
請求項1に記載の添加剤の製造方法。 The method for producing an additive according to claim 1, wherein the fuel oil is any one of gasoline, kerosene, light oil, A heavy oil, B heavy oil, C heavy oil, crude oil, vegetable oil, animal oil, waste oil, and paper wastewater black liquor.
原料として少なくとも、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α-リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ -リノレン酸、ジホモ-γ -リノレン酸、アラキドン酸、オレイン酸、エルカ酸、ドデカン酸の群から選択される脂肪酸類、メタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンの群から選択されるアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有する
ことを特徴とする添加剤。 An additive produced by the production method according to claim 1 or 2,
As raw materials, at least caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid, eicosapentaenoic acid, docosahexaenoic acid, linoleic acid, γ -Linolenic acid, dihomo-γ-linolenic acid, arachidonic acid, oleic acid, erucic acid , fatty acid selected from the group of dodecanoic acid, selected from the group of methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin An additive comprising alcohols or a mixture thereof, aqueous ammonia or ammonia gas.
請求項3に記載の添加剤を燃料油に加えて、所望の添加剤調整燃料油を生成するステップを有する
ことを特徴とする添加剤調整燃料油の製造方法。 A method for producing a conditioned fuel oil prior to hydration that can be hydrated by hydration,
A method for producing an additive-adjusted fuel oil, comprising the step of adding the additive according to claim 3 to the fuel oil to produce a desired additive-adjusted fuel oil.
0.03〜1:1(容積)である
請求項4に記載の添加剤調整燃料油の製造方法。 The mixing ratio of additive and fuel oil is
It is 0.03-1: 1 (volume). The manufacturing method of the additive adjustment fuel oil of Claim 4.
添加剤の原料として少なくとも、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α-リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ -リノレン酸、ジホモ-γ -リノレン酸、アラキドン酸、オレイン酸、エルカ酸、ドデカン酸の群から選択される脂肪酸類、メタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンの群から選択されるアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有する
ことを特徴とする添加剤調整燃料油。 An additive-adjusted fuel oil produced by the production method according to claim 4 or 5,
As raw materials for additives, at least caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid, eicosapentaenoic acid, docosahexaenoic acid, linol Fatty acids selected from the group of acids, γ-linolenic acid, dihomo-γ-linolenic acid, arachidonic acid, oleic acid, erucic acid , dodecanoic acid, methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin An additive-adjusted fuel oil comprising an alcohol or a mixture thereof, aqueous ammonia or ammonia gas.
請求項6に記載の添加剤調整燃料油に水を加えて、所望の加水燃料を生成するステップを有する
ことを特徴とする加水燃料の製造方法。 A method for producing water-containing fuel,
A method for producing a hydrolyzed fuel, comprising: adding water to the additive-adjusted fuel oil according to claim 6 to produce a desired hydrolyzed fuel.
0.1〜1:1(容積)である
請求項7に記載の加水燃料の製造方法。 The mixing ratio of water and additive-adjusted fuel oil is
It is 0.1-1: 1 (volume) The manufacturing method of the water-containing fuel of Claim 7.
添加剤の原料として少なくとも、カプリル酸、カプリン酸、ラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、アラキジン酸、ベヘン酸、リグノセリン酸、α-リノレン酸、ステアリドン酸、エイコサペンタエン酸、ドコサヘキサエン酸、リノール酸、γ -リノレン酸、ジホモ-γ -リノレン酸、アラキドン酸、オレイン酸、エルカ酸、ドデカン酸の群から選択される脂肪酸類、メタノール、エタノール、プロパノール、エチレングリコール、プロピレングリコール、グリセリンの群から選択されるアルコール類もしくはその混合物、アンモニア水またはアンモニアガスを有する
ことを特徴とする加水燃料。 A hydrofuel produced by the production method according to claim 7 or 8,
As raw materials for additives, at least caprylic acid, capric acid, lauric acid, myristic acid, palmitic acid, stearic acid, arachidic acid, behenic acid, lignoceric acid, α-linolenic acid, stearidonic acid, eicosapentaenoic acid, docosahexaenoic acid, linol Fatty acids selected from the group of acids, γ-linolenic acid, dihomo-γ-linolenic acid, arachidonic acid, oleic acid, erucic acid , dodecanoic acid, methanol, ethanol, propanol, ethylene glycol, propylene glycol, glycerin A water-containing fuel characterized by having an alcohol or a mixture thereof, aqueous ammonia or ammonia gas.
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