地沟油是各类劣质废油脂的统称,此类油脂具有较深的颜色和明显的酸败味道,不仅营养价值低下,还含有多种对人体有害的成分。近年来,广西的餐饮行业发展迅速,而包括地沟油在内的餐饮废弃物产量也逐年增加。据统计,当前桂林市区废弃食用油脂日产量超过20 吨,这些地沟油若不加以回收利用,不但浪费宝贵的自然资源,还会对水体等自然环境造成二次污染,并可能对人民群众的身心健康造成巨大威胁[1-2]。当前,对地沟油的资源化利用的主要途径包括将地沟油转化为生物柴油[3-6]、润滑剂[7-8]、醇酸树脂[9]和洗涤用品[10-11]等。在具有完善餐饮废弃物回收利用体系的地区,以地沟油为原料生产生物柴油已经被市场证明为地沟油资源化利用的有效方式。由于地沟油原料本身的低成本,基于地沟油的生物柴油比其他植物基生物柴油更加经济[13-16],同时生产过程能耗更低,并且能减少温室气体排放[17-19]。然而,在资金欠缺和基础设施不够完善的地区,多种因素阻碍了地沟油基生物柴油的大规模商业化生产:(1)生物柴油属于大宗商品,生产需要大量稳定的地沟油原料供应,而经济欠发达地区的餐饮废油产出单位规模小且分散,同时缺乏强有力的回收网络体系支持,难以形成稳定的地沟油原料供应链[20-21];(2)生物柴油生产对地沟油原料有较高的要求,
包括较少的游离脂肪酸含量和特定的脂肪酸组成,即并不是所有的地沟油都适合生物柴油生产。同时由于地沟油杂质含量多,成分不稳定,造成作为生物柴油原料的地沟油需要繁琐的预处理步骤(如脱色、除臭、脱胶、脱盐、脱水等),这不仅增加了生产和设备投资成本,而且也会影响产品的质量[22-26];(3)大规模生物柴油生产需要催化剂,通常催化剂价格昂贵且生产工艺复杂,会进一步提高生物柴油的成本[27-28]。因此,在如广西等我国经济欠发达地区,若要实现地沟油充分、高效的资源化利用,需要在生物柴油途径之外探索更多的有效补充途
径。这些途径最好具有步骤简单、生产灵活、投资成本低的特点,并能够利用质量较低的地沟油。
植物蜡是一种绿色环保健康的自然资源,主要由长链脂肪酸、长链脂肪醇和蜡酯构成[29]。对比从石油中提炼出来的石蜡,以大豆蜡为代表的植物蜡制备的蜡烛点燃时黑烟少、污染小、安全环保,可以广泛用于高端的艺术蜡烛、精油蜡烛、蜡像、蜡笔的生产。同时,基于其绿色环保的的特性,植物蜡还可能在食品添加剂[30-32]、可食用涂膜[33-35]、化妆品[36-37]和涂料领域[38]获得应用。和生物柴油相比,植物蜡市场份额相对较小,但单位产品的附加值相对较高,如用于制备精油蜡烛的大豆蜡,其市场售价30 元/kg以上,利润率超过100%,是石蜡的2-3倍。此外,相比生物柴油,蜡材料生产设备投资相对较小,生产控制比较灵活[39-40]。当前我国地沟油的主要来源是大豆油、菜籽油等油脂,有一定可能作为蜡材料的原料的。结合植物蜡材料在产品附加值和生产方面的优势,将地沟油转化为植物蜡材料有希望成为地沟油回收利用的一种有效方式。不过,优质的植物蜡必须具有浅色、无味的特征,需要有一定的硬度和熔点,其产品如蜡烛等应具有足够的燃烧时间。而地沟油成分复杂,主要含有一定量双键的混合甘油三酯以及多种有色或有气味的有机杂质,这对制备实用的蜡材料带来巨大困难。首先,混合甘油三酯中大量的不饱和双键会导致松散的分子排列,造成地沟油本身熔点低,硬度极差,一般在室温下无法成型;其次,地沟油中含有的大量深色和酸败气味的有机杂质,会导致蜡产品色泽深,异味重,对消费者健康不利。因此,若不采用特定的处理手段,地沟油很难作为蜡的优质原料。目前,国内外对地沟油基蜡的研究基本处于空白状态。
当前,主流市场植物蜡的制备主要有两种途径:(1)以物理手段提取植物蜡。如亚麻籽蜡可以将粉碎的亚麻油油渣加石油醚和乙醇混合溶剂回流提取,提取物经过除灰、除脂和脱色后制得,其收率约为0.09 %。通常,提取法产率较低,流程复杂,存在二次污染可能性,主要用于高价值的特殊植物蜡制备[41];(2)氢化法制备植物蜡。如制备市场常见的大豆蜡,可将大豆油毛油加热到 150~170 ℃,在0.29~0.39 MPa 氢气压力下,以雷尼镍为催化剂,进行氢化反应,反应结束后,获得的半固态蜡加入丙酮精制,干燥后获得大豆蜡产品[42]。但对于地沟油而言,若以氢化法制备蜡,首先无法忽略脱色、除臭等预处理步骤,其次较高的温度和气体压力将导致额外的安全措施,同时需要昂贵的催化剂[43-46],以上问题都将大幅度提高投资和生产成本,因此氢化法也不适合地沟油基蜡的商业化生产。
我们在前期研究中注意到,环氧化也是一种有效的油脂改性的方法[47-49]。该方法可在温和反应条件(<100 ℃和大气压)下进行,一些常用的环氧化试剂如过氧乙酸(通过过氧化氢和冰醋酸反应制备)是一种强氧化剂,会使地沟油中的各种有色、恶臭有机杂质发生过氧化降解,消除酸败味,降低地沟油油品色泽。其次,地沟油中的不饱和双键被环氧化形成环氧基。与地沟油中含有双键的甘油三酯相比,环氧化的环氧甘油三酯可以形成更规则的颗粒。因此,环氧地沟油显示出比地沟油更高的熔点和硬度,可以在室温或初始燃烧阶段保持其形状。此外,环氧地沟油颜色相对较浅且无气味,可以作为实用地沟油基蜡的中间体,在要求不高的条件下,甚至可以直接作为蜡材料使用[50]。
不过,前期实验结果表明,环氧地沟油的颜色仍然比一般的大豆蜡深,不完全符合国家标准要求。此外,由于环氧地沟油是一类枝状分子,无法形成太规整的排列和坚固的晶格网络,因此其熔点和硬度低于商用大豆蜡,在燃烧过程中蜡烛会变软,燃烧时间很短。因此,有必要进一步对其进行化学改性。长链脂肪酸及其与高级脂肪醇形成的酯,属于直链棒状分子,容易形成较大长棒状晶体颗粒,构筑稳定的三维交联网络。我们最近的研究结果表明,令环氧地沟油在适当条
件下发生水解反应,可获得具有直链分子构型的混合脂肪酸(主要为饱和脂肪酸和羟基脂肪酸的混合物)[51]。可以预见,将所得地沟油基混合脂肪酸再进一步酯化,可以生成地沟油基脂肪酸脂肪醇酯,从而有效提高蜡材料的熔点和硬度,增加蜡烛的燃烧时间,并令蜡材料获得细腻光滑的外表。另一方面,在酯化反应同时,若加入少量活性白土等脱色剂脱色,有望进一步降低地沟油基蜡的色泽,从而获得具有实用价值的地沟油基蜡材料。
综上,基于当前植物蜡价格较高,而地沟油回收利用问题未能得到有效解决的现状,我们拟将植物蜡与地沟油的回收利用相结合。以地沟油为合成原料,通过环氧化后制备环氧地沟油,并进一步对其进行分子设计改性,制备高附加值、低成本(生产成本在 6 元/千克以下,不高于商品大豆蜡成本的 1/2),能够替代商品大豆蜡材料的地沟油基蜡材料,并将其加工成商业化的蜡产品(如蜡烛)等,对所得蜡的性能指标进行深入研究,并探讨其商业化的可行性。通过该项目的研究,可以获得一类以地沟油为原料的新型蜡材料,这类地沟油基蜡相比市场同类植物蜡产品,具有价格低廉,加工方便,产品附加值高,市场竞争力强的优势,能够为地沟油资源化利用和低成本蜡材料的开发提供新途径,具有重要的科研、经济和社会价值。
参考文献:
[1] 李臣, 周洪星, 石骏, 林向阳. 地沟油的特点及其危害[J]. 农产品加工, 2010, (06), 69-70.
[2] 国务院办公厅. 国务院办公厅关于加强地沟油整治和餐厨废弃物管理的意见[N]. 国办发〔2010〕36 号, 2010-7-13.
[3] J. C. C. Santana, A. C. Miranda, L. Souza, C. L. K. Yamamura, D.
F. Coelho, E. B. Tambourgi, F. T. Berssaneti and L. L. Ho, Clean Production of Biofuel from Waste Cooking Oil to Reduce Emissions, Fuel Cost, and Respiratory Disease Hospitalizations[J]. Sustainability, 2021, 13, 9185.
[4] V. C. Ravelo and J. S. Rodriguez., Biodiesel production as a solution to waste cooking oil (WCO) disposal. Will any type of WCO do for a transesterification process? A quality assessment[J]. Journal of Environmental Management, 2018, 228, 117-129.
[5] T. K. Sahu, S. Sarkar and P. C. Shukla, Combustion investigation of waste cooking oil (WCO) with varying compression ratio in a single cylinder CI engine[J]. Fuel, 2021, 283, 119262.
[6] H. H. Bandbafha, C. Li, X. Chen, W. Peng, M. Aghbashlo, S. S. Lam and M. Tabatabaei, Managing the hazardous waste cooking oil by conversion into bioenergy through the application of waste-derived green catalysts: A review[J]. Journal of Hazardous Materials, 2021, 127636.
[7] W. Zhang, H. Ji, Y. Song, S. Ma, W. Xiong, C. Chen, B. Chen and X. Zhang, Green preparation of branched biolubricant by chemically modifying waste cooking oil with lipase and ionic liquid[J]. Journal of Cleaner Production, 2020, 274, 122918.
[8] R. Z. K. Hussein, N. K. Attia, K. F. Mai and S. T. Elsheltawy, Experimental investigation and process simulation of biolubricant production from waste cooking oil[J]. Biomass and Bioenergy, 2021, 144, 105850.
[9] L. M. Orozco, S. Cardona, C. Gomez, H. Inciarte, Y. Villada and L. Rios, Evaluation of KHSO4 as a recyclable catalyst in the production of dehydrated castor oil to be applied in alkyd resins[J]. Progress in Organic Coatings, 2021, 161, 106467.
[10] K. Sharma, S. S. Toor, J. Brando, T. H. Pedersen and L. A. Rosendahl, Optimized conversion of waste cooking oil into ecofriendly bio-based polymeric surfactant- A solution for enhanced oil recovery and green fuel compatibility[J]. Journal of Cleaner Production, 2021, 294, 126214.
[11] A. Pospisilova, I. Novackova and R. Prikryl, Isolation of poly(3-hydroxybutyrate) from bacterial biomass using soap made of waste cooking oil[J]. Bioresource Technology, 2021, 326, 124683.
[12] B. H. H. Goh, C. T. Chong, Y. Ge, H. C. Ong, J. H. Ng, B. Tian, V. Ashokkumar, S. Lim, T. Seljak, and V. Jozsa, in utilisation of waste cooking oil for sustainable biodiesel and biojet fuel production[J]. Energy Conversion and Management, 2020, 223, 113296.
[13] B. Changmai, C. Vanlalveni, A. P. Ingle, T. Noor, R. Bhagat and S. L. Rokhum, Widely used catalysts in biodiesel production: a review[J]. RSC Advances, 2020, 10, 41625.
[14] D. Singh, D. Sharma, S. L. Soni, C. S. Inda, S. Sharma P. K., Sharma and A. Jhalani, A comprehensive review of biodiesel production from waste cooking oil and its use as fuel in compression ignition engines: 3rd generation cleaner feedstock[J]. Journal of Cleaner Production, 2021, 307, 127299.
[15] R. S. Nursal, A. Khalid, I. S. Abdullah, N. Jaat, N. Darlis and H. Koten, Autoignition behavior and emission of biodiesel from palm oil, waste cooking oil, tyre pyrolysis oil, algae and jatropha[J]. Fuel, 2021, 306, 121695.
[16] I. S. Abdullah, A. Khalid, N. Jaat, R. S. Nursal, H. Koten and Y. Karagoz, A study of ignition delay, combustion process and emissions in a high ambient temperature of diesel combustion[J]. Fuel, 2021, 297, 120706.
[17] M. Mohadesi, B. Aghel, M. Maleki and A. Ansari, The use of KOH/Clinoptilolite catalyst in pilot of microreactor for biodiesel production from waste cooking oil[J]. Fuel, 2020, 263, 116659.
[18] B. Panchal, Z. Zhu, S. Qin, T. Chang, Q. Zhao, Y. Sun, C. Zhao, J. Wang, K. Bian and S. Rankhamb, The current state applications of ethyl carbonate with ionic liquid in sustainable biodiesel production: A review[J]. Renewable Energy, 2022, 181, 341-354.
[19] N. F. Sulaiman, N. I. Ramly, M. H. A. Mubinc and S. L. Lee, Transition metal oxide (NiO, CuO, ZnO)-doped calcium oxide catalysts derived from eggshells for the transesterification of refined waste cooking oil[J]. RSC Advances, 2021, 11, 21781.
[20] J. Yang and H. Shan, The willingness of submitting waste cooking oil (WCO) to biofuel companies in China: An evolutionary analysis in catering networks[J]. Journal of Cleaner Production, 2021, 282, 125331 .
[21] Y. Zhao, C. Wang, L. Zhang, Y. Chang and Y. Hao, Converting waste cooking oil to biodiesel in China: Environmental impacts and economic feasibility[J]. Renewable and Sustainable Energy Reviews, 2021, 140, 110661.
[22] P. Sharma, M. Usman, E. S. Salama, M. Redina, N. Thakur, and X. Li, Evaluation of various waste cooking oils for biodiesel production: A comprehensive analysis of feedstock[J]. Waste Management, 2021, 136, 219-229.
[23] A. S.Yusuff, A. O. Gbadamosi and L. T. Popoola, Biodiesel production from transesterified waste cooking oil by zinc-modified anthill catalyst: Parametric optimization and biodiesel properties improvement[J]. Journal of Environmental Chemical Engineering, 2021, 9, 104955.
[24] W. H. Foo, W. Y. Chia, D. Y. Y. Tang, S. S. N. Koay, S. S. Lim and K. W. Chew, The conundrum of waste cooking oil: Transforming hazard into energy[J]. Journal of Hazardous Materials, 2021, 417, 126129.
[25] H. M. Khan, T. Iqbal, C. H. Ali, A. Javaid and I. I. Cheema, Sustainable biodiesel production from waste cooking oil utilizing waste ostrich (Struthio camelus) bones derived heterogeneous catalyst[J]. Fuel, 2020, 277, 118091.
[26] A. R. Mohammed and C. Bandari, Optimization of biodiesel production from waste cooking oil using static mixer technology in Vietnam[J]. Biofuels, 2018, 9, 567-574.
[27] A. Gouran, B. Aghel, and F. Nasirmanesh, Biodiesel production from waste cooking oil using wheat bran ash as a sustainable biomass[J]. Fuel, 2021, 295, 120542.
[28] J. Patchimpet, B. K. Simpson, K. Sangkharak, and S. Klomklao, Optimization of process variables for the production of biodiesel by transesterification of used cooking oil using lipase from Nile tilapia viscera[J]. Renewable Energy, 2020, 153, 861-869.
[29] 何丽兵, 王森, 植物蜡的综合利用研究进展[J]. 粮食和油脂, 2020, 33, 14-16.
[30] 许仁溥. 米糠蜡制备和开发[J]. 粮食与油脂, 2005, 4, 35-37. [31] C. D. Doan, I. Tavernier, P. K. Okuro and K. Dewettinck, Internal and external factors affecting the crystallization, gelation and applicability of wax-based oleogels in food industry[J]. Innovative Food Science & Emerging Technologies, 2018, 45, 42-52.
[32] A. R. Patel, M. Babaahmadi, A. Lesaffer and K. Dewettinck, Profiling of organogels prepared at critical gelling concentrations of natural waxes in a triacylglycerol solvent[J]. Journal of Agricultural and Food Chemistry, 2015, 63, 4862-4869.
[33] G. D. S. Pereira, F. L. D. C. Machado and J. M. C. D. Costa, Quality of 'Delta Valencia' orange grown in semiarid climate and stored under refrigeration after coating with wax[J]. Food Science and Technology, 2013, 33, 276-281.
[34] S. Singh, P. Khemariya, A. Rai, A.C. Rai, T. K. Koley and B. Singh, Carnauba waxbased edible coating enhances shelf-life and retain quality of eggplant (Solanum melongena) fruits[J]. LWT-Food Science and Technology, 2016, 74, 420-426.
[35] E. Oregel-Zamudio, M. V. Angoa-Pérez, G. Oyoque-Salcedo, C. N. Aguilar-González and H. G. Mena-Violante, Effect of candelilla wax edible coatings combined with biocontrol bacteria on strawberry quality during the shelf-life[J]. Scientia Horticulturae, 2017, 214, 273-279.
[36] 彭东洲, 吴喜光. 尿囊素唇膏的研制与临床疗效[J]. 西北药学杂志, 2003, 18, 265-266.
[37] 王洪云. 漆蜡(油)的成分及其综合利用价值[J]. 中国民族民间医药, 2013, 22, 3,5.
[38] A. Lozhechnikova, H. Bellanger, B. Michen, I. Burgert and S. Österberg, Surfactant-free carnauba wax dispersion and its use for layer-bylayer assembled protective surface coatings on wood[J]. Applied Surface Science, 2017, 396: 1273-1281.
[39] K. Rezaei, W. Tong and L. A. Johnson, Hydrogenated vegetable oils as candle wax[J]. Journal of the American Oil Chemists Society, 2002, 79, 1241-1247.
[40] T. Fei, K. Ren and T. Wang, The Friction and Wear Behaviors of Vegetable Oil-Based Waxes, Natural Beeswax, and Petroleum Paraffin Wax[J]. Journal of the American Oil Chemists Society, 2020, 97, 1141-1150.
[41] 李明媛, 王振爽, 张丰, 欧娜, 李舒然, 吴梧桐. 亚麻油油渣中植物蜡的提取、纯化与基本性质[J]. 药物生物技术, 2011, 18, 526-529.
[42] 夏剑秋, 王延春, 张瑾, 苏晓雪. 天然植物性大豆蜡的研发[J]. 中国油脂, 2005, 30, 41-42.
[43] R. X. Chen and W. C. Wang, The production of renewable aviation fuel from waste cooking oil. Part I: Bio-alkane conversion through hydro-processing of oil[J]. Renewable energy, 2019, 135, 819-835.
[44] P. Dujjanutat and P. Kaewkannetra, Production of bio-hydrogenated kerosene by catalytic hydrocracking from refined bleached deodorised palm/ palm kernel oils[J]. Renewable Energy, 2020, 147, 464-472.
[45] P. Ji, Z. Fan, M. Niu, L. Pan, G. Jing, R. Tian, and W. Li, Study on the co-hydrogenation of coal tar and kitchen waste oil over Co–Mo/γ–Al2O3[J]. Reaction Kinetics, Mechanisms and Catalysis, 2021, 132, 751–769.
[46] H. Iida, K. Takahashi, A. Yanagisawa, H. Hashimoto, and A. Igarashi, Reduction of trans fatty acids in hydrogenated soybean oil using Ni/TiO2 catalysts[J]. Food Chemistry, 2021, 340, 127927.
[47] P. T. Wai, P. Jiang, Y. Shen, P. Zhang, Q. Gu and Y. Leng, Catalytic developments in the epoxidation of vegetable oils and the analysis methods of epoxidized products[J]. RSC Advances, 2019, 9, 38119.
[48] P. D. Jadhav, A. V. Patwardhan and R. D. Kulkarni, Kinetic study of in situ epoxidation of mustard oil[J]. Molecular Catalysis, 2021, 511, 111748.
[49] M. J. Jalil, A. Hadi and I. S. Azmi, Catalytic epoxidation of palm oleic acid using in situ generated performic acid – Optimization and kinetic studies[J]. Materials Chemistry and Physics, 2021, 270, 124754.
[50] Y. Liu, M. Y. Liu, Y. X. Qi, X. Y. Jin, H. R. Xu, Y. X. Chen, S. P. Chen, H. P. Su, Synthesis and properties of wax based on waste cooking oil[J]. RSC advance, 2022, 12, 3365-3371.
[51] Y. Liu, X. G. Fan, M. Y. Liu, L. Wang, P. Y. Wang, H. R. Xu, Y. X. Chen and S. P. Chen, Fatty acid wax from epoxidation and hydrolysis treatments of waste cooking oil: Synthesis and properties, RSC advance, 2022, 12, 36018-36027