油泥清洗工艺中的药剂化学研究
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摘要
为了实现热化学洗涤法净化油泥、回收石油资源,选取某油田落地油泥,采过标准筛、粒度测量等方法进行成分分析,将分析结果作为确定该含油污泥的清洗工艺的必要参数。
     以清洗后泥砂中的残油率为指标,分别考察了工艺运行中温度、搅拌时间、pH、搅拌强度、泥水比等参数的变化对落地油泥清洗效率的影响,来确定最佳工艺条件。在最佳工艺条件下,选取十一种化学药剂,进行了药剂筛选实验。用筛选出来的清洗药剂进行药剂复配实验,确定了最佳清洗剂的配方。对配方中影响效果最大的硅酸钠进行了清洗条件实验。
     (1)成分分析结果,研究所用含油污泥样品的固体成分含量较大,颗粒粒径主要在0.125~0.250mm范围内。含油率为17.5%,主要为可萃取油,水含量较少。含油污泥分段灼烧实验可知,350~500℃时灼烧的油分最多。根据含油污泥的组成成分,研究选取了热化学清洗工艺处理该含油污泥。
     (2)油泥清洗工艺参数实验,确定最佳工艺条件,温度70℃,搅拌时间30min,搅拌强度36.3s~(-1),pH=9,泥水比1:5。
     (3)药剂筛选实验中,阴离子表面活性剂AEO-9,NP-10及分散剂硅酸钠的清洗效果较好,洗后的残油率都在2%以下。
     (4)用筛选出来的阴离子表面活性剂AEO-9,NP-10及分散剂硅酸钠进行药剂复配实验,确定了最佳清洗剂的配方,①3(AEO-9):1(NP-10):6(Na_2SiO_3);②1(AEO-9):3(NP-10):6(Na_2SiO_3)。以上两种配方均可使洗出泥残油率可降至0.4%以下,且混合药剂中的硅酸钠对药剂的清洗效果影响较大。
     (5)影响硅酸钠清洗效率实验。实验结果,硅酸钠的最佳清洗条件为温度60℃,搅拌时间40min,搅拌强度40s~(-1),pH=9,浓度2g/L,泥水比对硅酸钠的清洗效果影响较小。
     含油污泥的清洗是一个复杂的动力学多相流过程,工艺参数和化学药剂是两大重点和难点。清洗化学药剂的筛选涉及物料运移和分离等方面因素,在药剂筛选时应依据现场工艺条件,以实现污泥净化和石油回收两方面最大程度的兼顾。
For the purpose of oily sludge detergency and recovery of oil content using chemical heat washing process, the research chooses oily sludge and analyses the ingredient of them by standard griddle, microgram measurement etc. Then according to the result we choose the proper process of oily sludge treatment.
    Using the residual oil percentage of treated sludge, the study investigates the influence factors including agitate temperature, agitate time, pH, agitate intensity, solid-liquid ratio, reagent concentration etc. on the efficiency of oily sludge washing and conducts to optimize the process parameters. In these optimize parameters we selected surfactant from 11 chemistry doses. By a mixture surfactant from above selected surfactants, a serious of experiments were conducted to determine the optimal ratio of each component. Then we did optimize parameter experiment to Na_2SiO_3 which dominates the washing efficiency of mixture surfactant.
    (1)According to the analyses of ingredient, the oily sludge used in the experiment contain a lot of solid. And the main granule size is 0.125-0.250mm. Oil concentration is 17.5%. The most ingredient of the oil in the oily sludge is extractable oil. There is little water in the oily sludge. According to the oven drying experiment, the burned oil is the most in 350-500℃. Based on the ingredient of oily sludge we chose the hot water washing process as the process of oily sludge treatment.
    (2)The oily sludge washing experiment indicated that the optimal efficiency of oily sludge washing was achieved when agitate temperature was at 70℃, agitate time 30min, agitate intensity 36.3s~(-1), pH=9 and solid liquid ratio 1:5.
    (3)The washing effect of anion surfactant AEO-9, NP-10 and dispersant Na_2SiO_3 was better than others. By using above chemistry dose the oil concentration in treated sludge would less than 2%.
    (4) By a mixture surfactant from above three components, a serious of experiments were conducted to determine the optimal ratio of each component, and results supported two surfactant dispensing (1)3 (AEO-9) : 1 (NP-10) : 6 (Na_2SiO_3); (2)1 (AEO-9) : 3 (NP-10) : 6 (Na_2SiO_3). Under this condition, the residual oil percentage of treated oily sludge may be less than 0.3%. And the Na_2SiO_3 dominates the washing efficiency of mixture surfactant.
引文
[1] 刘天齐.石油化工环境保护手册.烃加工出版社,1990.
    [2] 费庆志.O/W型乳化废液的混凝及絮渣处理.大连铁道学院学报.2001,22(3):101-104.
    [3] 尹先清.含油污水处理技术研究.工业水处理,2000,20(3):29-31.
    [4] 李凡修.含油污泥无害化处理及综合利用的途径.油气田环境保护,1998,8(3):42-44.
    [5] 李凡修,肖遥.含油污泥混凝处理实验研究.石油与天然气化工,2000,29(4):211-213.
    [6] 李凡修.含油污泥脱水性能实验.环境污染与防治,2001,(3):105-106.
    [7] 陆斌,陆晓千.一种含油乳化液废水处理技术的工程应用.环境工程,2001,19(3):12-13.
    [8] 王毓仁,陈家伟,孙晓兰.国外炼油厂含油污泥处理技术.炼油设计,1999,29(9):51-56.
    [9] 宫晖.乌石化炼油厂污泥处理技术现状.石油化工环境保护,2003,26(3):38-41.
    [10] Hollman E. R. Seperation Scheme for Cleaning Oil Waste. CIM/ASOTRA, 31-37.
    [11] Reis. R. C. An Overview of the Environmental Issues Facing the Upstream Petroleum Industry. SPE 26366,1993.
    [12] F.E.帕诺夫等箸,裴德禄等译.石油与天然气工业企业的环境保护[M].北京:石油工业出版社,1992,52-58.
    [13] 孟相民,郝以专,刘红梅.含油污泥浓缩工艺技术的研究与应用.油气田地面工程,2001,20(3):33-34.
    [14] 刘新华.土壤油类污染治理的水力冲洗和表面活性剂冲洗技术初步实验研究.环境科学学报,1996,16(4):24-26.
    [15] 周高华.含油污泥脱水设备与技术.化工机械,2003,30(5):306-311.
    [16] Ramin Abrishamian. Oil Gas J, 1992, 90(44):51-56.
    [17] 郑远扬.石油污染生化治理的进展.国外环境科学技术,1993,(3):46-50.
    [18] Oil &Gas Journal. 1994,8(5) :92-95.
    [19] Oil &Gas Journal., 1992, 11(2) :51-55.
    [20] 李增强.用固-液旋流工艺处理油田集输泵站含油泥砂.化工环保,2005,25(5):386-389.
    [21] Schutte, Robert. Process for reducing sludge accumulation in the hot water extraction process for oil sands, USA, US 5492628, 1996.
    [22] 李新盛.油泥分离与处理的研究:(硕士学位论文).沈阳:东北大学,2004.
    [23] 谢宏明.从废弃油泥中提取原油的工艺方法.中国,CN 1195017A,1995.
    [24] 王国柱.从石油土中提取石油的方法.中国,CN 90107638.4,1990.
    [25] 贾茂郎,贾中军.油泥分离方法及设备.中国,CN 90104444.x,1990.
    [26] 国家环境保护总局科技标准司著.危险废物污染与防治技术指南.北京:中国环境科学出版社.
    [27] 国家环保局编.石油化学工业固体废物治理.北京:环境科学出版社.
    [28] Richard J Ayen, et al. Environmental Progress, 1992,11(2):127-133.
    [29] Solomon M Jacob, et al. Liquid Sludge Disposal Process. USA, US 4786401, 1987.
    [30] Numrich. Method and apparatus for the purification of oil-containing and water-containing ro11 scale sludge. USA, US 5964045, 1999.
    [31] Hydrocarbon Processing, Aug. 1995, 55-60.
    [32] 尤俊洪.一种处理污泥的方法.中国,CN 816001176,1986.
    [33] Stephen C. Paspek, Jr., North Royalton et al. Novel Technique for Rendering Oily Sludges Environmentally Acceptable. USA, US 4842715, 1987.
    [34] 张秀霞,耿春香,冯成武.溶剂萃取-蒸汽蒸馏法处理含油污泥.上海环境科学,2000,19(5):228-229.
    [35] 孙向东,李美蓉,李然.溶剂提取法资源化处理集输罐底高含油污泥.承德石油高等专科学校学报,2006,8(2):12-15.
    [36] 杨国清主编.固体废弃物处理工程.北京:科学出版社.
    [37] 薛涛.含油污泥无害处理与资源回用技术研究:(硕士学位论文).西安:长安大学,2003.
    [38] 陈家伟,孙晓兰,王毓仁.国外炼厂污泥无害化处理实践和发展方向.石油化工环境保护,1996.
    [39] 陈书林,邵涛.油泥、油砂生物综合处理技术研究及应用.石油天然气学报,2005,27(2):427-430.
    [40] 郭雄华,黄煦.孤东油区含油泥砂现状及处理途径探索.河南石油,2005,19(6):81-82.
    [41] 曹方起,曾庆辉,何国安.临盘油田含油泥砂处理技术研究.石油天然气学报,2005,27(3):572-574.
    [42] Kuriakose A P, et al. Liquid Sludge Disposal Process. USA, US4786401, 1987
    [43] Sandeep Versa, V.V. Kumar. Relationship between oil-water interfacial tension and oily soil removal in mixed surfactant systems. Journal of colloid and interface science, 1998, 207:1-10.
    [44] 常致成.脂肪酰胺和脂肪酯类非离子表面活性的开发和应用.表面活性剂工业,2000(2):5-8.
    [45] Daradicsl, Palinkas. Synthesis and analysis of fatty acid-acylated polypeptides. Tenside Surf Det, 1999, 36(5): 309-313.
    [46] 王军,葛虹.烷基葡糖酰胺的合成和性能.日用化学工业,2002,32(3):54-57.
    [47] Warwels. Polymers and surfactants on the basis of renewable resources .Chemosphere, 2001,43:39-48.
    [48] 袁少明,周庚生,牛金平,等.脂肪酸甲酯的喷射磺化工艺研究.日用化学工业,2003,33(4):225-227.
    [49] 王军.从天然可再生资源制备表面活性剂的研究进展.精细与专用化学品,2002(15):4-5.
    [50] Cohenl, Trujillof. Performance of sulfoxylated fatty acid methyl esters. Surfactants Deterg, 1999,2(3): 363-365.
    [51] Cohenl, Sotof, Lunams. Sulfoxylated methyl esters as potential components of liquid formulations. Surfactants Deterg, 2001, 4 (2): 147-150.
    [52] 王斌,张敏,颜连学,等.脂肪酸酰胺类阴离子表面活性剂的合成、性能和应用.南京大学学报(自然科学),2001,37(2):262-265.
    [53] Crudden JJ, Lemery Roland J. Use of lauroyl ED3A chelating surfactants with detergent enzymes. Cahn Arno. Proc world conf deterg: Strategies 21st century[C]. Nashua: AOCS, 1998.311-316.
    [54] Beck, Roland. The properties and industrial applications of N-acyl ED3A chelating surfactants. Spec Publ-R Soc Chem, 1999, 230: 117-129.
    [55] Brain A Parker. The commercia lsynthesis and characterization of novel multifunction surfactant chelates. CESIO. 4th world surfactants conference[C]. Barcelona: CESICO, 1996. 446-460.
    [56] Joe Crudden. N-acyl ED3A chelating surfactants: properties and application in detergency. Floyd E, Frriedl I. Detergency of speciality surfactants[C]. NewYork: Marcel Dekker I NC, 2001.104.
    [57] 黄智,李成海,梁宁宁,等.N-N′-双月桂酰基乙二胺二乙酸钠的合成.精细化工,2001,18(12):687-690.
    [58] 黄智,李成海,梁宁宁,等.N-N′-双月桂酰基乙二胺二乙酸钠合成方法的改进.精细化工,2002,19(1):1-3.
    [59] 陈燕妮,卢云,吴昊,等.N-酰基氨基酸系列表面活性剂的合成和应用.化学研究与应 用,2001,13(2):192-195.
    [60] Ishizuka Tatsushi, Matsumoto Kotaro. Preparation of high-purity N-(long-chainacyl) amino acid. JP: 96038, 2003-04-03.
    [61] Ishizuka Tatsushi, Matsumoto Kotaro. Preparation of high-purity N-(long-chainacyl) amino acid salt. JP: 96039, 2003-04-03.
    [62] Hattori Tatsuya, Kitamuran, Yamaton, et al. Amidation method for preparing N-long-chain-acyl neutral amino acid surfactants. EP: 1314717, 2003-03-28.
    [63] 韦异,朱海洋,李华山等.-脂肪酰基谷氨酸系表面活性剂在日用化学品中的应用.日用化学品科学,2003,26(4):20-23.
    [64] 岳可芬,周春生,史真.咪唑啉还原开环反应在表面活性剂合成中的应用.日用化学工业,2000,30(5):34-36.
    [65] Olenick A JJ, Imperante John. Glyceryl phosphobetaine compounds for surfactants in personal care products. US: 6180806, 2001-01-30.
    [66] Wang Shi-fa, Furuno Takeshi, Cheng Zhi. Synthesis of new betaine-type amphoteric surfactants from tall oil fatty acid. Journa of Wood Science, 2002, 48(5): 419-424.
    [67] Fujii Tamotsu, Ito Tamotsu. Development of the novl amphoteric surfactant and application to cosmetics. Fragrance Journal, 2002, 30(6): 99-105.
    [68] Leidreiter H I, Gruning B, Kasebornd. Amphoteric surfactants-processing, product composition and properties. Sofw2000, 126(5): 2, 4-6, 8-10.
    [69] 岳可芬,周春生,史真等.新型咪唑啉两性表面活性剂的合成及性能测定.西北大学学报,2002,32(3):258.
    [70] Wang Shi-fa, Furuno Takeshi, Cheng Zhi. Synthesis of new amino acid-type surfactants from tall oil fatty acid. Journal of Wood Sci, 2001, 47(6): 470-475.
    [71] 付冀峰,杨建新,徐宝财.二聚表面活性剂的制备、性质和应用.精细化工,2001,18(1):14-17.
    [72] Gao C, Millqvist-fureby A, Whitcombe MJ, et al. Regioselective synthesis of dimeric (Gemini) and trimeric sugar-based surfactants. SurfDet, 1999, 2: 293-302.
    [73] Clapes Saboritpere, Piera Vilar Eulalia, Urgell Joan B. Enzymic synthesis of geminal cationic surfactants of the type N~α, N~ω-bis (N-acylarginine) α, ω-alkanediamide dihydrochlorides in solutions with low content of water. ES: 2163352, 2002-01-16.
    [74] Perez Lourdes, Garcia MT, Ribosa Isabel, et al. Biological properties of arginine-based Gemini cationic surfactants. Environm-ental Toxicology and Chemistry, 2002, 21(6): 1279-1285.
    [75] Perezl, Pinazoa, Vinardellp, et al. Synthesis and biological properties of dicationic arginine-diglycerides. New Journal of Chemistry, 2002, 26(9): 1221-1227.
    [76] Camilleri Patrick, Kirby AJ, Perrin Chirstele, et al. Preparation of diaminodicarboxylic acid: Peptide Gemini surfactant compounds. WO: 0250100, 2002-06-27.
    [77] Alami E, Holmberg K. Heteroge mini surfactants based on fatty acid synthesis and interracial properties. Colloid and Interface Science, 2001(239):230-240.
    [78] 肖稳发.原油破乳剂的研究进展.精细与专用化学品,2004,12(24):18-20.
    [79] 何泽能,李振山,籍国东.油田污染土壤中石油回收的模拟研究.应用基础与工程科学学报,2005,13(2):136-145
    [80] Reis. R. C. An Overview of the Environmental Issues Facing the Upstream Petroleum Industry. SPE 26366, 1993
    [81] 艾宏荣.水基型稠油清洗剂的研究与开发.日用化学工业,1999,6:20-23