CN114657022A - Deodorization method for improving quality of microalgae oil rich in DHA - Google Patents
Deodorization method for improving quality of microalgae oil rich in DHA Download PDFInfo
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- 238000004332 deodorization Methods 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000001301 oxygen Substances 0.000 claims abstract description 8
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 8
- 238000009835 boiling Methods 0.000 claims abstract description 4
- 239000007789 gas Substances 0.000 claims abstract description 4
- 241000222480 Schizophyllum Species 0.000 claims abstract description 3
- 230000006037 cell lysis Effects 0.000 claims abstract description 3
- 238000005119 centrifugation Methods 0.000 claims abstract description 3
- 239000003921 oil Substances 0.000 claims description 48
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 10
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 229910052757 nitrogen Inorganic materials 0.000 claims description 5
- 238000007670 refining Methods 0.000 claims description 4
- 239000002781 deodorant agent Substances 0.000 claims description 3
- 238000004061 bleaching Methods 0.000 claims description 2
- 239000010779 crude oil Substances 0.000 claims description 2
- 235000011121 sodium hydroxide Nutrition 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims 1
- BHAAPTBBJKJZER-UHFFFAOYSA-N p-anisidine Chemical compound COC1=CC=C(N)C=C1 BHAAPTBBJKJZER-UHFFFAOYSA-N 0.000 abstract description 2
- 150000002978 peroxides Chemical class 0.000 abstract description 2
- 238000000605 extraction Methods 0.000 abstract 1
- MBMBGCFOFBJSGT-KUBAVDMBSA-N docosahexaenoic acid Natural products 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 description 23
- 235000020669 docosahexaenoic acid Nutrition 0.000 description 22
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 238000004042 decolorization Methods 0.000 description 3
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 3
- YYGNTYWPHWGJRM-UHFFFAOYSA-N (6E,10E,14E,18E)-2,6,10,15,19,23-hexamethyltetracosa-2,6,10,14,18,22-hexaene Chemical compound CC(C)=CCCC(C)=CCCC(C)=CCCC=C(C)CCC=C(C)CCC=C(C)C YYGNTYWPHWGJRM-UHFFFAOYSA-N 0.000 description 2
- BHEOSNUKNHRBNM-UHFFFAOYSA-N Tetramethylsqualene Natural products CC(=C)C(C)CCC(=C)C(C)CCC(C)=CCCC=C(C)CCC(C)C(=C)CCC(C)C(C)=C BHEOSNUKNHRBNM-UHFFFAOYSA-N 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- PRAKJMSDJKAYCZ-UHFFFAOYSA-N dodecahydrosqualene Natural products CC(C)CCCC(C)CCCC(C)CCCCC(C)CCCC(C)CCCC(C)C PRAKJMSDJKAYCZ-UHFFFAOYSA-N 0.000 description 2
- 150000002576 ketones Chemical class 0.000 description 2
- 235000016709 nutrition Nutrition 0.000 description 2
- 229940031439 squalene Drugs 0.000 description 2
- TUHBEKDERLKLEC-UHFFFAOYSA-N squalene Natural products CC(=CCCC(=CCCC(=CCCC=C(/C)CCC=C(/C)CC=C(C)C)C)C)C TUHBEKDERLKLEC-UHFFFAOYSA-N 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 238000006392 deoxygenation reaction Methods 0.000 description 1
- 229940090949 docosahexaenoic acid Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000010685 fatty oil Substances 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 150000002432 hydroperoxides Chemical class 0.000 description 1
- 125000003473 lipid group Chemical group 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 235000020978 long-chain polyunsaturated fatty acids Nutrition 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B3/00—Refining fats or fatty oils
- C11B3/12—Refining fats or fatty oils by distillation
- C11B3/14—Refining fats or fatty oils by distillation with the use of indifferent gases or vapours, e.g. steam
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Microbiology (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
Abstract
本发明涉及油脂萃取领域,公开了一种提高富含DHA的微藻油质量的脱臭方法。该脱臭方法如下:首先通过裂褶菌发酵DHA,再通过细胞裂解和离心获得富含DHA的油,进行预精制,得到脱色油。对脱色油进行脱臭处理,其中脱臭所用离子水,先加热至沸腾,排出从水中分离出来的气体和蒸汽后再泵入蒸汽发生器。预除氧水进一步加热形成蒸汽。之后再进行脱臭。该方法通过减少氧气的负面影响来有效降低油脂的过氧化值和对茴香胺值,最终得到满足市场需求的高质量产品。The invention relates to the field of oil and fat extraction, and discloses a deodorization method for improving the quality of DHA-rich microalgae oil. The deodorization method is as follows: firstly, DHA is fermented by Schizophyllum, and then DHA-rich oil is obtained by cell lysis and centrifugation, and pre-refined to obtain decolorized oil. The deodorized oil is deodorized, wherein the ionized water used for deodorization is heated to boiling first, and the gas and steam separated from the water are discharged and then pumped into the steam generator. The pre-deoxygenated water is further heated to form steam. Then deodorize. The method effectively reduces the peroxide value and p-anisidine value of the oil by reducing the negative influence of oxygen, and finally obtains a high-quality product that meets the market demand.
Description
技术领域technical field
本发明涉及微藻油加工技术领域,主要涉及一种提高富含DHA的微藻油的质量的脱臭方法。The invention relates to the technical field of microalgal oil processing, and mainly relates to a deodorization method for improving the quality of DHA-rich microalgal oil.
背景技术Background technique
二十二碳六烯酸(DHA,22:6n-3)是一种重要的长链多不饱和脂肪酸(PUFA),对人类健康起着重要作用。传统上,海洋鱼类是DHA的主要来源,但由于海洋资源日益稀缺,富含DHA的微藻油受到了广泛关注。Docosahexaenoic acid (DHA, 22:6n-3) is an important long-chain polyunsaturated fatty acid (PUFA) that plays an important role in human health. Traditionally, marine fish have been the main source of DHA, but due to the increasing scarcity of marine resources, DHA-rich microalgal oils have received extensive attention.
市场上应用富含DHA的油的主要问题之一在于其强烈的不愉快味道。富含DHA的微藻油含有近70%的多不饱和脂肪酸,多不饱和脂肪酸比例高的油在加工和储存过程中容易氧化,形成氢过氧化物(一级氧化产物)和气味成分,如醛和酮(二级氧化产物)。One of the main problems with the use of DHA-enriched oils on the market is their strong unpleasant taste. DHA-rich microalgal oil contains nearly 70% polyunsaturated fatty acids, and oils with a high proportion of polyunsaturated fatty acids are easily oxidized during processing and storage to form hydroperoxides (primary oxidation products) and odor components such as Aldehydes and ketones (secondary oxidation products).
炼油过程通常用于改善油品质量,而脱臭通常是分解氧化物和去除异味成分的最后和关键过程,而氧气是油酸败的重要原因,因为它是氧化的起始物,能够生成过氧化氢。因此,如果油在脱臭过程中与氧气接触,富含DHA的油的质量和稳定性也会受到不利影响。现有的脱臭过程中给使用的水蒸气脱臭中,会导致酸败,影响油脂质量。本研究开发了一种有效的除臭方法,通过减少氧气的负面影响,开发一种有效且简单的方法,用于去除富含DHA的微藻油的异味并提高其质量。本研究中提供的方法为油的除臭提供了一种简单的方法,为富含DHA的微藻油的除臭提供了一种替代方法,从而生产出满足市场需求的高品质最终产品。Oil refining process is usually used to improve oil quality, and deodorization is usually the last and key process to break down oxides and remove odorous components, and oxygen is an important cause of oil rancidity because it is the starting material of oxidation, which can generate hydrogen peroxide . Therefore, the quality and stability of DHA-enriched oils can also be adversely affected if the oils come into contact with oxygen during deodorization. The water vapor used in the existing deodorization process will cause rancidity and affect the quality of the oil. This study developed an effective deodorization method by reducing the negative effects of oxygen, developing an effective and simple method for deodorizing and improving the quality of DHA-enriched microalgal oil. The method presented in this study provides a simple method for the deodorization of oils and an alternative to the deodorization of DHA-enriched microalgal oils, resulting in high-quality final products that meet market demands.
发明内容SUMMARY OF THE INVENTION
本发明提供一种微藻油高效脱臭方法,用于解决上述背景技术中提到的技术问题。The present invention provides a high-efficiency deodorization method for microalgae oil, which is used to solve the technical problems mentioned in the above background art.
为实现上述目的,本发明提供如下技术方案:一种富含DHA的微藻油的脱臭方法,包括以下步骤:To achieve the above object, the present invention provides the following technical solutions: a deodorization method of DHA-rich microalgal oil, comprising the following steps:
(1)富含DHA微藻油的预精制工艺(1) Pre-refining process of DHA-rich microalgal oil
通过裂褶菌发酵DHA后,通过细胞裂解和离心获得富含DHA的油。通过冲洗、烧碱精制和漂白对原油进行预精制,所得脱色油用于下一道除臭工序。After fermentation of DHA by Schizophyllum, DHA-enriched oil was obtained by cell lysis and centrifugation. The crude oil is pre-refined by washing, caustic soda refining and bleaching, and the resulting decolorized oil is used in the next deodorization process.
(2)油脱臭工艺(2) Oil deodorization process
对富含DHA的微藻油进行除臭。设备包括蒸汽发生器、冷却罐和真空泵。真空由与除臭器相连的真空泵。Deodorizes DHA-enriched microalgal oil. Equipment includes steam generators, cooling tanks and vacuum pumps. Vacuum is provided by a vacuum pump connected to the deodorizer.
①将脱色后获得的约60kg富含DHA的油送入除臭剂中。真空保持在100kPa。① Send about 60kg of DHA-rich oil obtained after decolorization into the deodorant. The vacuum was maintained at 100 kPa.
②使用导热油将试验箱加热至180℃,并在此温度下保持4小时。②Use heat transfer oil to heat the test box to 180℃ and keep it at this temperature for 4 hours.
③整个脱臭过程中的汽提蒸汽总消耗量调整为约9L。③ The total consumption of stripping steam in the whole deodorization process is adjusted to about 9L.
④脱臭后,油被用纯N2推入冷却罐,并在N2保护下通过冷水循环冷却。④After deodorization, the oil is pushed into the cooling tank with pure N2 , and cooled by cold water circulation under the protection of N2 .
⑤首先将去离子水加热至沸腾,排出从水中分离出来的气体和蒸汽,并将预除氧水泵入蒸汽发生器。⑤ First, heat the deionized water to boiling, discharge the gas and steam separated from the water, and pump the pre-deoxygenated water into the steam generator.
⑥预除氧水进一步加热形成蒸汽,用于除臭。⑥ The pre-deoxygenated water is further heated to form steam for deodorization.
与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:
1.由于脱色过程的高温,油中产生了许多过氧化氢的次级产品。一级氧化产物过氧化氢在室温下是稳定的。但在高温条件下,如180℃脱臭过程,易分解为醛类、酮类、酸类等,为二级氧化产物,具有强烈的不良气味。降低氧气水平可以大大减少二次脂质氧化产物的形成。1. Due to the high temperature of the decolorization process, many secondary products of hydrogen peroxide are produced in the oil. The primary oxidation product, hydrogen peroxide, is stable at room temperature. However, under high temperature conditions, such as the deodorization process at 180 °C, it is easily decomposed into aldehydes, ketones, acids, etc., which are secondary oxidation products and have a strong bad odor. Reducing oxygen levels can greatly reduce the formation of secondary lipid oxidation products.
2.不皂化脂质角鲨烯可通过除臭过程去除。然而,在这项研究中,我们没有观察到角鲨烯的明显去除。使用除氧蒸汽的除臭过程并未影响油中的DHA含量,从而保留了微藻油的营养价值并使其可供食用。2. The unsaponifiable lipid squalene can be removed by the deodorization process. However, in this study, we did not observe significant removal of squalene. The deodorization process using deoxygenated steam did not affect the DHA content in the oil, thereby preserving the nutritional value of the microalgal oil and making it edible.
3.根据TBARS测试,使用策略I的脱色油和脱臭油在7天后显示出比使用策略II的脱臭油更高的值。3. The decolorized and deodorized oils using strategy I showed higher values after 7 days than the deodorized oils using strategy II according to the TBARS test.
4.这项工作提供了一个简单的策略来提高富含DHA的油脱臭过程的效率,强调了用于产生脱臭蒸汽的水的预除氧的重要性。使用该策略,可获得高质量的富含DHA的微藻油,其过氧化值为零,对茴香胺值非常低,能够满足市场的高质量要求。脱臭过程后,油和DHA的损失分别约为6%和3%。分别为30%,这并没有显著降低富含DHA的微藻油的营养价值。此外,作者还提出了其他除氧方法,如氮气置换或膜处理,以去除蒸汽中的氧气。4. This work provides a simple strategy to improve the efficiency of the DHA-enriched oil deodorization process, emphasizing the importance of pre-deoxygenation of water used to generate deodorized steam. Using this strategy, high-quality DHA-rich microalgal oil with zero peroxide value and very low p-anisidine value can be obtained, which can meet the high-quality requirements of the market. After the deodorization process, the losses of oil and DHA were about 6% and 3%, respectively. 30%, respectively, which did not significantly reduce the nutritional value of DHA-enriched microalgal oil. In addition, the authors propose other oxygen removal methods, such as nitrogen replacement or membrane treatment, to remove oxygen from the steam.
具体实施方式:Detailed ways:
具体实施方式一:Specific implementation one:
对富含DHA的微藻油进行脱臭处理,设备包括蒸汽发生器、冷却罐和真空泵。真空由与除臭器相连的罗茨真空泵提供。将脱色后约60kg左右的脱色油送入除臭剂中。真空保持在100kpa。使用导热油将试验箱加热至180℃,并在此温度下保持4小时。整个脱臭过程中汽提蒸汽消耗总量调整为9L左右,Deodorization of DHA-enriched microalgal oil with steam generators, cooling tanks and vacuum pumps. Vacuum is provided by a Roots vacuum pump connected to the deodorizer. About 60kg of decolorized oil after decolorization is sent to the deodorant. The vacuum is kept at 100kpa. Heat the test chamber to 180°C using heat transfer oil and keep it at this temperature for 4 hours. During the whole deodorization process, the total consumption of stripping steam is adjusted to about 9L,
具体实施方式二:Specific implementation two:
脱臭后,将油用纯氮气推入冷却罐,在氮气保护下通过冷水循环冷却:将室温下的去离子水注入蒸汽发生器,将水加热形成蒸汽,用于除臭。After deodorization, the oil is pushed into the cooling tank with pure nitrogen, and cooled by cold water circulation under nitrogen protection: deionized water at room temperature is injected into the steam generator, and the water is heated to form steam for deodorization.
具体实施方式三:Specific implementation three:
本实施方式与具体实施方式二的不同点在于首先将去离子水加热至沸腾,排出从水中分离出来的气体和蒸汽,并将预脱氧水泵入蒸汽发生器。预除氧水进一步加热形成蒸汽,用于除臭。其它步骤与具体实施方式二相同。具体实施方式四:The difference between this embodiment and the second embodiment is that the deionized water is first heated to boiling, the gas and steam separated from the water are discharged, and the pre-deoxygenated water is pumped into the steam generator. The pre-deoxygenated water is further heated to form steam for deodorization. Other steps are the same as in the second embodiment. Specific implementation four:
每种除臭方法重复三次。Each deodorization method was repeated three times.
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CN104263510A (en) * | 2014-10-09 | 2015-01-07 | 重庆大学 | Deodorization process for preparation of low-acidity vegetable insulating oil |
CN108753458A (en) * | 2018-08-03 | 2018-11-06 | 梁云 | Improve the refinery practice of microbial grease stability and safety |
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CN104263510A (en) * | 2014-10-09 | 2015-01-07 | 重庆大学 | Deodorization process for preparation of low-acidity vegetable insulating oil |
CN108753458A (en) * | 2018-08-03 | 2018-11-06 | 梁云 | Improve the refinery practice of microbial grease stability and safety |
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