CN106833762A - 一种低冰点燃料及其制备方法 - Google Patents
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- 230000008014 freezing Effects 0.000 title claims abstract description 45
- 238000007710 freezing Methods 0.000 title claims abstract description 45
- 239000000446 fuel Substances 0.000 title claims abstract description 39
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 claims abstract description 59
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000007788 liquid Substances 0.000 claims abstract description 25
- 238000003756 stirring Methods 0.000 claims abstract description 14
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 claims abstract description 11
- 229960003540 oxyquinoline Drugs 0.000 claims abstract description 11
- MCJGNVYPOGVAJF-UHFFFAOYSA-N quinolin-8-ol Chemical compound C1=CN=C2C(O)=CC=CC2=C1 MCJGNVYPOGVAJF-UHFFFAOYSA-N 0.000 claims abstract description 11
- 235000002906 tartaric acid Nutrition 0.000 claims abstract description 11
- 239000011975 tartaric acid Substances 0.000 claims abstract description 11
- 238000002156 mixing Methods 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims abstract description 7
- 239000005725 8-Hydroxyquinoline Substances 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 6
- 230000008901 benefit Effects 0.000 abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract description 3
- 238000009826 distribution Methods 0.000 abstract description 3
- 239000002920 hazardous waste Substances 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000000567 combustion gas Substances 0.000 abstract description 2
- 239000003380 propellant Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- 239000007800 oxidant agent Substances 0.000 description 4
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- WFPZPJSADLPSON-UHFFFAOYSA-N dinitrogen tetraoxide Chemical compound [O-][N+](=O)[N+]([O-])=O WFPZPJSADLPSON-UHFFFAOYSA-N 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- -1 peroxide hydrogen Chemical class 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
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- C10L1/00—Liquid carbonaceous fuels
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- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
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Abstract
本发明涉及一种低冰点燃料及其制备方法,该低冰点燃料包括以下重量份含量的组分:过氧化氢60~95,乙醇40~5,酒石酸0.01~0.2,8‑羟基喹啉0.01~0.2;上述产品通过以下方法制备而成:将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;将8‑羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体。再将第一液体和第二液体混合搅拌均匀,即得到目的产物。与现有技术相比,本发明具有低温不结冰,低温适应性好,稳定性好,腐蚀性小,燃气洁净不结垢、不积碳,生产过程无危险性废液生成等优点。
Description
技术领域
本发明涉及一种燃料,尤其是涉及一种低冰点燃料及其制备方法。
背景技术
过氧化氢的使用历史已经超过100多年,它在航空航天、国防等工业领域得到极其广泛的应用。在军事上它最初由于应用于火箭技术和国防武器而得到重视和发展,特别是在二战期间及冷战初期。随着航天运载费用、推进剂长期可贮存性、安全性、无毒无污染、可重复使用、快速发射等要求越来越高,高浓度过氧化氢在推进领域又重新受到了越来越广泛的关注。
目前,过氧化氢推进技术在美、英等国各机构得到广泛研究,如:NASA、美国空军、波音、Aerojet、轨道技术公司、轨道科学公司、普渡大学、Surrey卫星技术公司等。而且,火箭推进领域推进剂的发展方向之一是减少肼、四氧化二氮的使用,所以过氧化氢将会是目前和将来推进领域的研究开发重点之一。
过氧化氢具有高密度比冲、绿色环保、常温可贮存、操作安全方便、可单组元分解和可自燃等优点,非常适合作为现代火箭发动机的推进剂。过氧化氢作为液体推进剂具有以下几个显著的优良特性:
(1)无毒、无污染。
(2)可在地面或空间的常温条件下长期贮存。
(3)密度及密度比冲高。
(4)既可作为双组元推进剂的氧化剂,又可以作为单组元推进剂。
(5)良好的热物性。
(6)多用途。
但是过氧化氢推进剂的冰点,如85%过氧化氢为-15℃,95%过氧化氢为-5℃,容易结冰的劣势限制了广泛应用,采取保温措施增加了***重量和复杂性,使用环境温度的要求使其优势无法得到体现。
发明内容
本发明的目的就是为了克服上述现有技术存在的缺陷而提供一种具有低温适应性好,腐蚀性小,燃气洁净不结垢、不积碳,生产过程无危险性废液生成等优点的低冰点燃料及其制备方法,该燃料可应用于航空发动机、航天发动机、车辆、机器人、气体发生装置、能量发生装置、二氧化碳发生装置及其他特种动力设备。
本发明的目的可以通过以下技术方案来实现:
一种低冰点燃料,包括以下重量份含量的组分:
各组分均为试剂级原料。
优选地,其冰点为-60~-10℃。
优选地,该低冰点燃料包括以下重量份含量的组分:
优选地,其冰点为-60~-50℃。
该低冰点燃料的制备方法,包括以下步骤:
(1)按配比将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;
(2)按配比将8-羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体;
(3)将第一液体和第二液体混合并搅拌均匀即得到所述的低冰点燃料。
优选地,各步骤搅拌过程中转速为60~4000转/分钟,搅拌时间为60~200分钟,温度控制在-20℃~50℃。
本发明通过在过氧化氢中加入冰点较低的乙醇(冰点低于-100℃),来降低过氧化氢的冰点,乙醇廉价易得,与过氧化氢互溶,能有效降低其冰点,使得过氧化氢的冰点在较大的范围内可调,同时乙醇也可以作为燃料,燃料氧化剂混合相容性良好,包含双组元和单组元燃料优势。
由于过氧化氢具有氧化性,贮存及在航天器使用过程中,外界环境变化多端,过氧化氢不稳定,容易分解,少量的酒石酸和8-羟基喹啉作为稳定剂,来稳定过氧化氢,防止过氧化氢的分解。酒石酸和8-羟基喹啉通过络合反应来稳定过氧化氢,酒石酸是一种良好的过氧化氢稳定剂,同时呈酸性,这增大了8-羟基喹啉的溶解量。制备过程中,分别将酒石酸加入过氧化氢中,以及将8-羟基喹啉加入乙醇中,利用了物质之间的相容性,使不容易直接溶解在过氧化氢中的8-羟基喹啉通过先溶解在乙醇中,再与过氧化氢混合,使之溶解在体系中。
与现有技术相比,本发明具有以下有益效果:
(1)低冰点:由于采用了科学的配比,该燃料产品的冰点比单一过氧化氢的冰点降低5~20℃,达到-60~-10℃,可以在低温环境条件下正常使用。
(2)稳定性好,可以在室温条件下长期保存该燃料产品。
(3)本发明的燃料毒性小、腐蚀性小,环保,燃烧后产物洁净不结垢、不积碳,生产过程无危险性废液生成。
(4)燃料氧化剂混合相容性良好,包含双组元和单组元燃料优势。
具体实施方式
下面结合具体实施例对本发明进行详细说明。
实施例1
一种低冰点燃料,包括以下重量份含量的组分:
该低冰点燃料的制备方法,包括以下步骤:
(1)按配比将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;
(2)按配比将8-羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体;
(3)将第一液体和第二液体混合并搅拌均匀即得到所述的低冰点燃料。
各步骤搅拌过程中转速为60~4000转/分钟,搅拌时间为60~200分钟,控制在常温下进行。
实施例2
一种低冰点燃料,包括以下重量份含量的组分:
该低冰点燃料的制备方法,包括以下步骤:
(1)按配比将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;
(2)按配比将8-羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体;
(3)将第一液体和第二液体混合并搅拌均匀即得到所述的低冰点燃料。
各步骤搅拌过程中转速为60~4000转/分钟,搅拌时间为60~200分钟,控制在常温下进行。
实施例3
一种低冰点燃料,包括以下重量份含量的组分:
该低冰点燃料的制备方法,包括以下步骤:
(1)按配比将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;
(2)按配比将8-羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体;
(3)将第一液体和第二液体混合并搅拌均匀即得到所述的低冰点燃料。
各步骤搅拌过程中转速为60~4000转/分钟,搅拌时间为60~200分钟,控制在常温下进行。
实施例4
本实施与实施例1基本相同,不同之处在于,本实施例制备过程中控制温度在0℃。
实施例5
本实施与实施例1基本相同,不同之处在于,本实施例制备过程中控制温度在-20℃。
实施例6
本实施与实施例1基本相同,不同之处在于,本实施例制备过程中控制温度在50℃。
对比例1
将过氧化氢与乙醇按照30:70的质量比搅拌均匀。
对比例2
95%过氧化氢。
将上述对比例1~2的过氧化氢混合物和实施例1~3的低冰点燃料进行检测,结果见表1。
表1
由上表可知,本发明所生产的耐低温、燃料氧化剂混合相容性良好、包含双组元和单组元燃料优势的低冰点燃料产品具有良好的低冰点、高稳定性的优点,根据对它的性能测试与实践运用,该燃料产品的冰点比单一过氧化氢的冰点降低5~20℃,达到-60~-10℃,可以在低温环境条件下正常使用,可以在室温条件下长期保存该燃料产品。适用于航空发动机、航天发动机、车辆、机器人、气体发生装置、能量发生装置、二氧化碳发生装置、其他特种动力设备、军工、科研等高端领域的使用。
Claims (6)
1.一种低冰点燃料,其特征在于,包括以下重量份含量的组分:
2.根据权利要求1所述的一种低冰点燃料,其特征在于,其冰点为-60~-10℃。
3.根据权利要求1所述的一种低冰点燃料,其特征在于,包括以下重量份含量的组分:
4.根据权利要求3所述的一种低冰点燃料,其特征在于,其冰点为-60~-50℃。
5.根据权利要求1所述的一种低冰点燃料的制备方法,其特征在于,包括以下步骤:
(1)按配比将酒石酸加入过氧化氢中,并搅拌均匀,得到第一液体;
(2)按配比将8-羟基喹啉加入乙醇中,并搅拌均匀,得到第二液体;
(3)将第一液体和第二液体混合并搅拌均匀即得到所述的低冰点燃料。
6.根据权利要求5所述的一种低冰点燃料的制备方法,其特征在于,各步骤搅拌过程中转速为60~4000转/分钟,搅拌时间为60~200分钟,温度控制在-20℃~50℃。
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