CN115505405A - Chlorinated hydrocarbon solubilizing emulsion material based on waste grease and preparation method thereof - Google Patents
Chlorinated hydrocarbon solubilizing emulsion material based on waste grease and preparation method thereof Download PDFInfo
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- 239000000839 emulsion Substances 0.000 title claims abstract description 73
- 239000000463 material Substances 0.000 title claims abstract description 44
- 150000008280 chlorinated hydrocarbons Chemical class 0.000 title claims abstract description 41
- 239000002699 waste material Substances 0.000 title claims abstract description 39
- 230000003381 solubilizing effect Effects 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 16
- 239000004519 grease Substances 0.000 title claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 62
- 239000003921 oil Substances 0.000 claims abstract description 60
- FCBUKWWQSZQDDI-UHFFFAOYSA-N rhamnolipid Chemical compound CCCCCCCC(CC(O)=O)OC(=O)CC(CCCCCCC)OC1OC(C)C(O)C(O)C1OC1C(O)C(O)C(O)C(C)O1 FCBUKWWQSZQDDI-UHFFFAOYSA-N 0.000 claims abstract description 24
- 239000013504 Triton X-100 Substances 0.000 claims abstract description 23
- 229920004890 Triton X-100 Polymers 0.000 claims abstract description 23
- 239000010806 kitchen waste Substances 0.000 claims abstract description 7
- 239000012071 phase Substances 0.000 claims description 69
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- 239000008346 aqueous phase Substances 0.000 claims description 7
- 239000003945 anionic surfactant Substances 0.000 claims description 6
- 239000008162 cooking oil Substances 0.000 claims description 6
- 239000002736 nonionic surfactant Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 4
- 229910021641 deionized water Inorganic materials 0.000 claims description 4
- 239000003513 alkali Substances 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims 1
- 238000005067 remediation Methods 0.000 abstract description 20
- XSTXAVWGXDQKEL-UHFFFAOYSA-N Trichloroethylene Chemical group ClC=C(Cl)Cl XSTXAVWGXDQKEL-UHFFFAOYSA-N 0.000 abstract description 19
- 239000003673 groundwater Substances 0.000 abstract description 17
- 239000003344 environmental pollutant Substances 0.000 abstract description 14
- 231100000719 pollutant Toxicity 0.000 abstract description 14
- 239000004094 surface-active agent Substances 0.000 abstract description 11
- 238000011065 in-situ storage Methods 0.000 abstract description 9
- 239000003876 biosurfactant Substances 0.000 abstract description 8
- 239000002957 persistent organic pollutant Substances 0.000 abstract description 7
- 150000001875 compounds Chemical class 0.000 abstract description 4
- 238000004090 dissolution Methods 0.000 abstract description 3
- 239000002689 soil Substances 0.000 abstract description 3
- 230000007935 neutral effect Effects 0.000 abstract description 2
- 238000003756 stirring Methods 0.000 abstract description 2
- 239000002352 surface water Substances 0.000 abstract description 2
- 238000013329 compounding Methods 0.000 abstract 1
- 239000008157 edible vegetable oil Substances 0.000 abstract 1
- 238000005063 solubilization Methods 0.000 description 25
- 230000007928 solubilization Effects 0.000 description 25
- 239000000243 solution Substances 0.000 description 13
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 12
- 239000002245 particle Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 6
- UBOXGVDOUJQMTN-UHFFFAOYSA-N trichloroethylene Natural products ClCC(Cl)Cl UBOXGVDOUJQMTN-UHFFFAOYSA-N 0.000 description 6
- 230000007613 environmental effect Effects 0.000 description 5
- 230000015556 catabolic process Effects 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 239000000693 micelle Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 230000005012 migration Effects 0.000 description 3
- 238000013508 migration Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 238000003933 environmental pollution control Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- UOCLXMDMGBRAIB-UHFFFAOYSA-N 1,1,1-trichloroethane Chemical compound CC(Cl)(Cl)Cl UOCLXMDMGBRAIB-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000315 carcinogenic Toxicity 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005238 degreasing Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011066 ex-situ storage Methods 0.000 description 1
- 238000000855 fermentation Methods 0.000 description 1
- 230000004151 fermentation Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004530 micro-emulsion Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- -1 mixed evenly Substances 0.000 description 1
- 231100000219 mutagenic Toxicity 0.000 description 1
- 230000003505 mutagenic effect Effects 0.000 description 1
- ZPIRTVJRHUMMOI-UHFFFAOYSA-N octoxybenzene Chemical compound CCCCCCCCOC1=CC=CC=C1 ZPIRTVJRHUMMOI-UHFFFAOYSA-N 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 235000010482 polyoxyethylene sorbitan monooleate Nutrition 0.000 description 1
- 229920000053 polysorbate 80 Polymers 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000008439 repair process Effects 0.000 description 1
- 230000002441 reversible effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 231100000378 teratogenic Toxicity 0.000 description 1
- 230000003390 teratogenic effect Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- C09K23/00—Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
- C09K23/42—Ethers, e.g. polyglycol ethers of alcohols or phenols
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- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F1/00—Treatment of water, waste water, or sewage
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- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
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- C02F2101/30—Organic compounds
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Abstract
本发明涉及一种基于废弃油脂的氯代烃增溶乳液材料及其制备方法。该乳液材料由轻质油相与水相组成,其中油相为厨余食用油,而水相为复配表面活性剂溶液包括0.45%~0.9%的鼠李糖脂和0.05%~0.1%的Triton X‑100,油相与水相体积比为0.25~0.5。制备方法是将两种表面活性剂溶解于水中获得水相溶液,在搅拌水相过程中逐步加入油相使两者混合。本发明通过复配生物表面活性剂联合废弃油脂制备乳液材料,能够将三氯乙烯在水相的溶解效率提高880倍,并且乳液材料具有较好的pH稳定性,可以在中性至碱性环境中用于增溶氯代有机污染物,本发明有望应用于土壤、地下水、地表水中污染物原位修复领域。
The invention relates to a chlorinated hydrocarbon solubilizing emulsion material based on waste oil and a preparation method thereof. The emulsion material is composed of a light oil phase and a water phase, wherein the oil phase is kitchen waste edible oil, and the water phase is a compound surfactant solution including 0.45%~0.9% rhamnolipid and 0.05%~0.1% For Triton X-100, the volume ratio of oil phase to water phase is 0.25~0.5. The preparation method is to dissolve two surfactants in water to obtain a water phase solution, and gradually add an oil phase to mix the two during the stirring of the water phase. The invention prepares the emulsion material by compounding biosurfactant and waste oil, which can increase the dissolution efficiency of trichlorethylene in the water phase by 880 times, and the emulsion material has good pH stability, and can be used in neutral to alkaline environments. The invention is used to solubilize chlorinated organic pollutants, and the invention is expected to be applied to the field of in-situ remediation of pollutants in soil, groundwater and surface water.
Description
技术领域technical field
本发明属于环境工程技术领域,具体涉及一种对氯代有机污染物有增溶能力的废弃油脂-生物表面活性剂乳液及其制备方法,即一种基于废弃油脂的氯代烃增溶乳液材料及其制备方法。The invention belongs to the technical field of environmental engineering, and specifically relates to a waste oil-biological surfactant emulsion capable of solubilizing chlorinated organic pollutants and a preparation method thereof, that is, a chlorinated hydrocarbon solubilizing emulsion material based on waste oil and its preparation method.
背景技术Background technique
氯代烃是一种重要的化工原料,广泛应用于工业洗涤、衣服脱脂、有机合成中间体等领域,具有致癌、致畸、致突变的毒性,危害人体健康及生态安全,常见的地下水污染物包括三氯乙烯(TCE)、1,1,1-三氯乙烷等。由于氯代烃密度高于水且难溶于水,因此一旦进入地下水环境中往往垂直向下迁移进入低渗透区,形成自由相态的重非水相液体,长期存在从而造成污染。Chlorinated hydrocarbons are an important chemical raw material widely used in industrial washing, degreasing of clothes, organic synthesis intermediates and other fields. They have carcinogenic, teratogenic and mutagenic toxicity, endanger human health and ecological safety, and are common groundwater pollutants. Including trichloroethylene (TCE), 1,1,1-trichloroethane, etc. Since chlorinated hydrocarbons have a higher density than water and are insoluble in water, once they enter the groundwater environment, they tend to migrate vertically downward into the low-permeability zone, forming a free-phase heavy non-aqueous phase liquid, which exists for a long time and causes pollution.
地下水污染物的修复方法分异位修复(抽出)与原位修复两种。近年来,原位修复以其低扰动、修复成本相对低廉等优势,成为氯代烃等典型有机污染场地修复的优选及发展趋势。国内土壤及地下水修复行业发展也逐渐转向长效的原位治理,修复过程需兼顾污染物的降解效率与环境影响,发展绿色、高效的增溶材料将有助于原位修复技术在实际场地中的应用。There are two methods of remediation of groundwater pollutants: ex-situ remediation (extraction) and in-situ remediation. In recent years, in-situ remediation has become the preferred choice and development trend for the remediation of typical organic contaminated sites such as chlorinated hydrocarbons due to its advantages of low disturbance and relatively low remediation cost. The development of the domestic soil and groundwater remediation industry is also gradually turning to long-term in-situ treatment. The remediation process needs to take into account both the degradation efficiency of pollutants and the environmental impact. The development of green and efficient solubilizing materials will help in-situ remediation technology in actual sites. Applications.
限制氯代烃原位降解的重要因素之一是其有效性。氯代烃在地下水中主要有气相、自由相、残留相与溶解相四种赋存状态。溶解相的氯代烃比较少,但是直接影响人类生活及健康,而自由相的氯代烃是地下水中的主要污染源,会不断地向地下水中溶解污染物而影响地下水质量安全。在原位修复中,一般是将修复材料注入地下水中,利用自然的水力梯度促进修复材料与污染接触而提高降解,因此污染物与修复药剂主要在水相中进行反应,污染物不易进入水相而降低了其修复效率,尤其是在低渗透场地中,污染物与修复药剂均存在扩散困难的问题,要提高污染物的去除率,需增强氯代烃的水相溶解及流动性。One of the important factors limiting the in situ degradation of chlorinated hydrocarbons is their availability. Chlorinated hydrocarbons mainly exist in four states: gas phase, free phase, residual phase and dissolved phase in groundwater. The chlorinated hydrocarbons in the dissolved phase are relatively small, but they directly affect human life and health, while the free phase chlorinated hydrocarbons are the main source of pollution in groundwater, which will continuously dissolve pollutants in groundwater and affect the quality and safety of groundwater. In in-situ remediation, the remediation material is generally injected into groundwater, and the natural hydraulic gradient is used to promote the contact between the remediation material and the pollution to improve degradation. Therefore, the pollutants and the remediation agent mainly react in the water phase, and the pollutants are not easy to enter the water phase. However, the remediation efficiency is reduced, especially in low-permeability sites, where both pollutants and remediation agents are difficult to diffuse. To improve the removal rate of pollutants, it is necessary to enhance the aqueous phase solubility and fluidity of chlorinated hydrocarbons.
表面活性剂是一种同时带亲水基团及亲油基团的化合物,其在水溶液中达到一定的浓度时,能够自发形成胶束(外部亲水内部亲油)或者反胶束(外部亲油内部亲水),降低水-油界面张力,促进污染物的溶解。当油相液体进入表面活性剂胶束的内部后,将均匀地分散在水中而形成不透明的乳液,能够促进氯代烃在地下水中的迁移。表面活性剂结合轻质油制备乳液增溶氯代烃,通过非极性相之间的互溶,一方面可以为氯代烃溶解进入水中提供更大的容量;另一方面,能够降低氯代烃的密度,将含水层底板中的氯代烃带入水相,从而有利于氯代烃在地下水中的迁移及降解。Surfactant is a compound with both hydrophilic and lipophilic groups. When it reaches a certain concentration in aqueous solution, it can spontaneously form micelles (external hydrophilic and internal lipophilic) or reverse micelles (external hydrophilic and internal). Hydrophilic inside the oil), reduce the water-oil interfacial tension, and promote the dissolution of pollutants. When the oil phase liquid enters the interior of the surfactant micelles, it will be uniformly dispersed in water to form an opaque emulsion, which can promote the migration of chlorinated hydrocarbons in groundwater. Surfactants are combined with light oil to prepare emulsions to solubilize chlorinated hydrocarbons. Through mutual solubility between non-polar phases, on the one hand, it can provide greater capacity for chlorinated hydrocarbons to dissolve into water; on the other hand, it can reduce the amount of chlorinated hydrocarbons. density, bringing the chlorinated hydrocarbons in the aquifer floor into the water phase, thus facilitating the migration and degradation of chlorinated hydrocarbons in groundwater.
增溶乳液材料目前主要用于化妆品、炼油驱油等领域,近些年才逐渐应用于环境修复领域。常用的污染物增溶的材料以Tween 80、十二烷基硫酸钠(SDS)等化学表面活性剂为主,采用正辛烷、正己烷等化合物作为轻质油相制备乳液或者微乳液,在多相抽提或地下水抽出处理时能显著增强污染物修复效率,但在原位修复时,注入地下水中的修复药剂难以回收。因此,使用易降解环境友好的增溶乳液材料变得更为重要。Solubilizing emulsion materials are currently mainly used in the fields of cosmetics, oil refining and flooding, and have only been gradually applied in the field of environmental restoration in recent years. Commonly used pollutant solubilizing materials are mainly chemical surfactants such as Tween 80 and sodium dodecyl sulfate (SDS), and compounds such as n-octane and n-hexane are used as light oil phases to prepare emulsions or microemulsions. Multiphase extraction or groundwater pumping treatment can significantly enhance the efficiency of pollutant remediation, but in situ remediation, the remediation agents injected into groundwater are difficult to recover. Therefore, it is more important to use easily degradable and environmentally friendly solubilized emulsion materials.
发明内容Contents of the invention
本发明的目的在于提供一种以废弃油脂为轻质油相、以生物表面活性剂为水相的用于氯代烃增溶的基于废弃油脂的氯代烃增溶乳液材料及其制备方法,以克服生物表面活性剂增溶效率低、化学表面活性剂存在的潜在环境风险等问题,通过添加少量的废弃油脂提高生物表面活性剂对氯代有机污染物的增溶,实现环境污染物治理的同时减少二次污染、促进废弃物资源的循环利用。The object of the present invention is to provide a kind of chlorinated hydrocarbon solubilizing emulsion material based on waste oil and its preparation method for chlorinated hydrocarbon solubilization with waste oil as light oil phase and biosurfactant as water phase, In order to overcome the low solubilization efficiency of biosurfactants and the potential environmental risks of chemical surfactants, the solubilization of chlorinated organic pollutants by biosurfactants can be improved by adding a small amount of waste oil, so as to realize the goal of environmental pollution control. At the same time reduce secondary pollution and promote recycling of waste resources.
本发明的目的是通过以下技术方案实现的:The purpose of the present invention is achieved through the following technical solutions:
一种基于废弃油脂的氯代烃增溶乳液材料,由油相与水相组成;其中,所述的油相为废弃油脂;所述的水相包括阴离子型表面活性剂和非离子型表面活性剂,两者在水相中的质量比例分别为0.05% ~ 0.9%、0.01% ~ 0.25%;所述的油相与水相的体积比为0.25 ~4。A chlorinated hydrocarbon solubilizing emulsion material based on waste oil, consisting of an oil phase and a water phase; wherein, the oil phase is waste oil; the water phase includes an anionic surfactant and a nonionic surfactant agent, the mass ratio of the two in the water phase is 0.05% ~ 0.9%, 0.01% ~ 0.25% respectively; the volume ratio of the oil phase to the water phase is 0.25 ~ 4.
进一步地,所述的油相为厨余食用油;所述的阴离子表面活性剂为鼠李糖脂,所述的非离子型表面活性剂为Triton X-100,亦即,所述的水相中的表面活性剂为阴离子型表面活性剂鼠李糖脂与非离子型表面活性剂Triton X-100(聚乙二醇辛基苯基醚),两者的复配溶液。Further, the oil phase is kitchen waste cooking oil; the anionic surfactant is rhamnolipid, and the nonionic surfactant is Triton X-100, that is, the water phase The surfactant in the mixture is a compound solution of anionic surfactant rhamnolipid and nonionic surfactant Triton X-100 (polyethylene glycol octyl phenyl ether).
进一步地,鼠李糖脂在水相中的质量比例为0.45% ~ 0.9%,Triton X-100在水相中的质量比例为0.05% ~ 0.1%;油相与水相的体积比为0.25 ~ 0.5。Further, the mass proportion of rhamnolipid in the water phase is 0.45% ~ 0.9%, the mass proportion of Triton X-100 in the water phase is 0.05% ~ 0.1%; the volume ratio of the oil phase to the water phase is 0.25 ~ 0.5.
更进一步地,鼠李糖脂在水相中的质量比例为0.45%,Triton X-100在水相中的质量比例为0.05%;油相与水相的体积比为0.25。Furthermore, the mass proportion of rhamnolipid in the water phase is 0.45%, the mass proportion of Triton X-100 in the water phase is 0.05%; the volume ratio of the oil phase to the water phase is 0.25.
上述基于废弃油脂的氯代烃增溶乳液材料的制备方法,包括以下步骤:The preparation method of the above-mentioned chlorinated hydrocarbon solubilizing emulsion material based on waste oil comprises the following steps:
A、根据乳液中各组分的质量百分比,分别称取0.05% ~ 0.9%的鼠李糖脂、0.01% ~0.5%的Triton X-100,溶解于去离子水中,混合均匀,加入碱(NaOH)调节溶液pH至10~13,获得水相;A. According to the mass percentage of each component in the emulsion, weigh 0.05% ~ 0.9% rhamnolipid and 0.01% ~ 0.5% Triton X-100 respectively, dissolve them in deionized water, mix well, add alkali (NaOH ) adjusting the pH of the solution to 10-13 to obtain an aqueous phase;
B、将上述水相溶液不断地搅拌,按油-水体积比0.25 ~ 4缓慢加入废弃油脂,混合均匀后得到乳液材料。B. Stir the above water phase solution continuously, slowly add waste oil according to the oil-water volume ratio of 0.25 ~ 4, and mix well to obtain the emulsion material.
与现有技术相比,本发明的有益效果在于:Compared with prior art, the beneficial effect of the present invention is:
1、本发明制备乳液的方法简单易行、可生物降解,操作方便,易于工业化生产。1. The method for preparing the emulsion of the present invention is simple, biodegradable, easy to operate, and easy to industrialized production.
2、本发明中增溶乳液由可自然降解的鼠李糖脂与废弃油脂构成,对环境影响较小,不易产生二次污染。2. The solubilizing emulsion in the present invention is composed of naturally degradable rhamnolipids and waste oils, which has less impact on the environment and is less prone to secondary pollution.
3、本发明乳液制备所用到鼠李糖脂可由微生物发酵产生,轻质油相为厨余食用油,制备乳液的材料均来自于废弃物资源,实现了废弃资源的循环利用。3. The rhamnolipid used in the preparation of the emulsion of the present invention can be produced by microbial fermentation, and the light oil phase is kitchen waste cooking oil. The materials for preparing the emulsion are all from waste resources, realizing the recycling of waste resources.
4、本发明所制得的增溶乳液对氯代烃有良好的增溶效果,比水中溶解相的氯代烃的增溶效率提高125~880倍左右,通过添加废弃油脂能够显著增加氯代有机污染物在的水相的溶解性,同时轻质油相(废弃油脂厨余食用油)与氯代烃的互溶可以降低氯代烃的密度,促进其在水相中的迁移。4. The solubilized emulsion prepared by the present invention has a good solubilizing effect on chlorinated hydrocarbons, and the solubilization efficiency of chlorinated hydrocarbons in the dissolved phase in water is increased by about 125 to 880 times, and the addition of waste oil can significantly increase the solubilization efficiency of chlorinated hydrocarbons. The solubility of organic pollutants in the water phase, and the mutual solubility of the light oil phase (waste grease, kitchen waste cooking oil) and chlorinated hydrocarbons can reduce the density of chlorinated hydrocarbons and promote their migration in the water phase.
5、本发明提供了一种增溶乳液的制备方法,通过合适的鼠李糖脂、Triton X-100与废弃油脂配比,制得不透明乳液状材料用于地下水氯代烃的增溶修复。5. The present invention provides a method for preparing a solubilized emulsion. Through a suitable ratio of rhamnolipid, Triton X-100 and waste oil, an opaque emulsion-like material is prepared for the solubilization and repair of groundwater chlorinated hydrocarbons.
6、本发明的用于地下水氯代烃增溶的生物表面活性剂乳液材料及其制备方法,通过使用生物表面活性剂鼠李糖脂与化学表面活性剂Triton X-100复配及添加少量的废弃油脂,提高了生物表面活性剂对氯代有机污染物的增溶,克服了生物表面活性剂增溶效率低、化学表面活性剂存在的潜在环境风险等问题,实现了环境污染物治理的同时减少二次污染、促进废弃物资源的循环利用。6. The biosurfactant emulsion material and preparation method thereof for groundwater chlorinated hydrocarbon solubilization of the present invention is compounded by using biosurfactant rhamnolipid and chemical surfactant Triton X-100 and adding a small amount of Waste oil improves the solubilization of chlorinated organic pollutants by biosurfactants, overcomes the problems of low solubilization efficiency of biosurfactants and potential environmental risks of chemical surfactants, and realizes environmental pollution control while Reduce secondary pollution and promote recycling of waste resources.
7、本发明制得的增溶乳液材料具有较好的pH稳定性,可以在中性至碱性环境中用于增溶氯代有机污染物,该增溶乳液材料有望应用于土壤、地下水、地表水中污染物原位修复领域。7. The solubilized emulsion material prepared by the present invention has good pH stability, and can be used for solubilizing chlorinated organic pollutants in a neutral to alkaline environment. The solubilized emulsion material is expected to be applied to soil, groundwater, In situ remediation of pollutants in surface water.
附图说明Description of drawings
图1为乳液微粒的粒径分布图;Fig. 1 is the particle size distribution figure of emulsion particle;
图2为乳液的zeta电位图;Fig. 2 is the zeta potential figure of emulsion;
图3为废弃油脂乳液与正辛烷乳液对氯代烃增溶能力的差异图;Fig. 3 is the difference diagram of waste oil emulsion and n-octane emulsion to chlorinated hydrocarbon solubilizing ability;
图4为不同pH下乳液对三氯乙烯的增溶能力图。Fig. 4 is a graph showing the solubilization ability of the emulsion to trichlorethylene at different pHs.
具体实施方式detailed description
以下通过具体实施例和附图对本发明作进一步的说明。下述具体实施方式不以任何形式限制本发明的技术方案,凡是采用等同替换或等效变换的方式所获得的技术方案均落在本发明的保护范围内。The present invention will be further described below through specific embodiments and accompanying drawings. The following specific embodiments do not limit the technical solutions of the present invention in any form, and all technical solutions obtained by means of equivalent replacement or equivalent transformation fall within the protection scope of the present invention.
实施例1Example 1
一种基于废弃油脂的氯代烃增溶乳液材料,由油相与水相组成,其中,油相为厨余食用油,水相包括阴离子型表面活性剂鼠李糖脂(在水相中的质量比例为0.05% ~ 0.9%)与非离子型表面活性剂Triton X-100(在水相中的质量比例为0.01% ~ 0.25%);所述的油相与水相的体积比为0.25 ~ 4。A chlorinated hydrocarbon solubilizing emulsion material based on waste oil, consisting of an oil phase and a water phase, wherein the oil phase is kitchen waste cooking oil, and the water phase includes an anionic surfactant rhamnolipid (in the water phase The mass ratio is 0.05% ~ 0.9%) and the non-ionic surfactant Triton X-100 (the mass ratio in the water phase is 0.01% ~ 0.25%); the volume ratio of the oil phase to the water phase is 0.25 ~ 4.
所述基于废弃油脂的氯代烃增溶乳液材料的制备方法,包括以下步骤:The preparation method of the chlorinated hydrocarbon solubilizing emulsion material based on waste oil, comprises the following steps:
A、根据乳液中各组分间不同的比例,称取适量的鼠李糖脂(在水相中的质量比例为0.05% ~ 0.9%)、Triton X-100(在水相中的质量比例为0.01% ~ 0.25%)溶解于去离子水中,混合均匀,加入碱(NaOH)调节溶液pH 至10~13,获得水相溶液。A. According to the different proportions of the components in the emulsion, weigh an appropriate amount of rhamnolipid (the mass ratio in the water phase is 0.05% ~ 0.9%), Triton X-100 (the mass ratio in the water phase is 0.01% ~ 0.25%) was dissolved in deionized water, mixed evenly, and alkali (NaOH) was added to adjust the pH of the solution to 10~13 to obtain an aqueous phase solution.
B、将上述获得的水相溶液不断搅拌,按一定比例(油-水体积比0.25 ~ 4)同时缓慢加入轻质油相,继续搅拌,待油、水两相混匀后即得到增溶的乳液材料。B. Stir the aqueous phase solution obtained above continuously, and slowly add the light oil phase according to a certain proportion (oil-water volume ratio 0.25 ~ 4) at the same time, continue stirring, and the solubilized solution will be obtained after the oil and water phases are mixed evenly. Emulsion material.
按表1中的不同配比(鼠李糖脂浓度、Triton X-100浓度及油相-水相体积比不同)制成不同的乳液材料备用。According to the different proportions in Table 1 (the concentration of rhamnolipid, the concentration of Triton X-100 and the volume ratio of oil phase to water phase are different), different emulsion materials are prepared for use.
实施例2Example 2
乳液材料对氯代烃的增溶能力测试Solubilization Ability Test of Emulsion Materials to Chlorinated Hydrocarbons
以三氯乙烯(TCE)代表氯代有机污染物,取1 ml TCE于40 mL硼硅酸样品瓶中,另加入5 mL实施例1中的乳液材料,室温振荡2h,振荡结束后用正己烷萃取乳液中的三氯乙烯,带ECD检测器的安捷伦气相色谱(7890A)测定正己烷中三氯乙烯的含量。Take trichlorethylene (TCE) as a representative of chlorinated organic pollutants, take 1 ml of TCE in a 40 mL borosilicate sample bottle, add 5 mL of the emulsion material in Example 1, shake at room temperature for 2 hours, and wash with n-hexane after shaking Trichlorethylene in emulsion was extracted, and Agilent gas chromatography (7890A) with ECD detector was used to determine the content of trichlorethylene in n-hexane.
对比乳液材料对TCE的增溶倍数(相较于纯水中溶解的三氯乙烯260 mg/L),结果见表1,其中,当鼠李糖脂为0.45%、Triton X-100为0.05%且油水比为0.25的乳液对三氯乙烯增溶量(溶解量和增溶倍数)较高,而乳液体系中的Triton X-100的含量达0.25%时,乳液对三氯乙烯的增溶能力下降。Comparing the solubilization ratio of emulsion materials to TCE (compared to 260 mg/L of trichlorethylene dissolved in pure water), the results are shown in Table 1. Among them, when rhamnolipid is 0.45%, Triton X-100 is 0.05% And the emulsion with an oil-water ratio of 0.25 has a higher solubilization capacity (dissolution amount and solubilization ratio) for trichlorethylene, and when the content of Triton X-100 in the emulsion system reaches 0.25%, the solubilization ability of the emulsion for trichlorethylene decline.
表1 不同配比的乳液材料对三氯乙烯的增溶能力Table 1 Solubilization ability of emulsion materials with different ratios to trichlorethylene
实施例3Example 3
根据实施例2中的结果,选择0.45%鼠李糖脂、0.05%Triton X-100以及油-水相比0.25,测定乳液中微粒粒径及zeta电位。According to the results in Example 2, 0.45% rhamnolipid, 0.05% Triton X-100 and oil-water ratio of 0.25 were selected to measure the particle size and zeta potential of the emulsion.
将样品置于比色皿中,用纳米粒度与zeta电位仪(Malvern Zetasizer NanoZS90)测定乳液的粒径及zeta电位,常温检测。乳液粒径的测试结果如图1所示,其平均粒径为230 nm;乳液的zeta电位为-58.2 mV(结果如图2所示),一般认为体系的zeta电位小于-30 mV时可以形成稳定的悬浊液,因此制备的乳液胶束粒径分布均匀、性质稳定。The sample was placed in a cuvette, and the particle size and zeta potential of the emulsion were measured with a nanometer particle size and zeta potential meter (Malvern Zetasizer NanoZS90), and detected at room temperature. The test results of the particle size of the emulsion are shown in Figure 1, and the average particle size is 230 nm; the zeta potential of the emulsion is -58.2 mV (the result is shown in Figure 2), and it is generally believed that when the zeta potential of the system is less than -30 mV, it can form Stable suspension, so the prepared emulsion micelles have uniform particle size distribution and stable properties.
实施例4Example 4
将轻质油相以正辛烷代替废弃油脂(厨余食用油)制备乳液材料,对比两种不同轻质油相生成的乳液对氯代烃增溶效果的差异。The light oil phase was replaced by n-octane waste oil (kitchen waste cooking oil) to prepare emulsion materials, and the difference in the solubilization effect of chlorinated hydrocarbons was compared between the emulsions formed by two different light oil phases.
按0.45%鼠李糖脂、0.05%Triton X-100配制水相溶液,分别以废弃油脂和正辛烷为轻质油相(油-水体积比0.25)制备两种不同的乳液材料(正辛烷乳液材料及废弃油脂乳液材料),制备方法同实施例1。The water phase solution was prepared according to 0.45% rhamnolipid and 0.05% Triton X-100, and two different emulsion materials (n-octane Emulsion material and waste oil emulsion material), the preparation method is the same as embodiment 1.
取10 ul的TCE、5mL正辛烷/废弃油脂乳液于样品瓶中,测定两种乳液材料对TCE的增溶能力差异,具体方法同实施例2。结果如图3所示,相比较而言,废弃油脂形成的乳液对TCE的增溶效果优于正辛烷形成的乳液。Take 10 ul of TCE and 5 mL of n-octane/waste grease emulsion in a sample bottle, and measure the difference in the solubilization ability of the two emulsion materials to TCE, the specific method is the same as in Example 2. The results are shown in Figure 3. In comparison, the solubilization effect of the emulsion formed by waste oil on TCE is better than that formed by n-octane.
实施例5Example 5
不同pH条件下的乳液对氯代烃增溶能力的影响Effects of Emulsions Under Different pH Conditions on Solubilization Ability of Chlorinated Hydrocarbons
称取适量的鼠李糖脂、Triton X-100加水溶解,用NaOH调节溶液至pH 10-14,制得终浓度0.45%鼠李糖脂、0.05%Triton X-100,pH分别为10、11、12、13、14的五种水相溶液。以油-水体积比0.25配制不同pH下的乳液材料,乳液的具体的配制过程同实施例1。Weigh an appropriate amount of rhamnolipid and Triton X-100 to dissolve in water, and adjust the solution to pH 10-14 with NaOH to obtain a final concentration of 0.45% rhamnolipid and 0.05% Triton X-100, with pHs of 10 and 11 respectively. , 12, 13, 14 five aqueous phase solutions. Emulsion materials at different pHs were prepared with an oil-water volume ratio of 0.25, and the specific preparation process of the emulsion was the same as in Example 1.
用气相色谱法测定不同pH条件下乳液对三氯乙烯的增溶,结果如图4所示,在pH10~13的范围内乳液对三氯乙烯的增溶能力保持较好的增溶能力,当pH达13.5时,乳液对污染物的增溶能力显著下降,说明由鼠李糖脂、Triton X-100、废弃油脂构成的乳液材料具有较好的pH稳定性。Gas chromatography was used to measure the solubilization of trichlorethylene by emulsion under different pH conditions. As shown in Figure 4, the solubilization ability of emulsion to trichlorethylene in the range of pH 10-13 maintained a good solubilization ability. When the pH reached 13.5, the solubilization ability of the emulsion to pollutants decreased significantly, indicating that the emulsion material composed of rhamnolipid, Triton X-100, and waste oil had good pH stability.
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