共查询到19条相似文献,搜索用时 64 毫秒
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以高温高盐油藏为切入点,从提高表面活性剂体系的抗温抗盐性等实际应用出发,介绍了氧乙基数为3、烷基碳数为8,10,12,14,16的五种APES系列表面活性剂的合成方法。同时对该系列表面活性剂与新疆漠北002脱气原油的动态界面张力进行评价;并对该系列表面活性剂的抗盐性进行深入研究。实验表明阴-非离子表面活性剂APES具有较好的耐盐性,十分适合在高盐油藏使用。 相似文献
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悬浮聚合分散剂的分散能力和保胶能力 总被引:1,自引:3,他引:1
本文采用振荡法。以三氯乙烯模拟氯乙烯测定氯乙烯悬浮聚合常用的分散剂(明胶、聚乙烯醇、纤维素醚类等)的分散能力和保胶能力,研究分散剂的品种,规格及浓度等对分散保胶能力的影响规律,可供合理选用分散剂参考。 相似文献
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表面活性剂中的非离子型产品,具有优良独特的洗涤、渗透、乳化、增溶、润湿、分散等能力.它在水中溶解时不发生电离作用,在酸、碱和盐水溶液中是稳定的,并有极高的抗热性,因而被广泛用于洗涤、纺织、印染、农药、化妆品、食品、皮革、橡胶、涂料、金属加工和石油开采和加工各个领域,做为合纤工业的整理剂(又称油剂)中的集束剂、平滑剂、抱合剂均采用非离子表面活性剂,我国每年有万吨消耗量,产值高、利税大,但由于质量要求严格,使许多生产厂家可望而不可及. 相似文献
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以某油田作为油相,研究了不同浓度的碱(苛性碱与碳酸钠)与阴-非离子表面活性剂(AEC、AES)复配体系在55℃时与原油油水界面张力行为。首先通过阴-非离子表面活性剂与地层水的配伍性实验筛选合适的阴-非离子表面活性剂;然后通过碱与筛选出来的表面活性剂复配,研究不同浓度下碱对该表面活性剂的界面张力的影响效果。研究结果表明:0.01%~1.20%Na OH分别与0.1%AES和0.3%AEC组成的复配体系体系以及0.01%~1.20%Na2CO3分别与0.1%AES和0.3%AEC组成的复配体系体系能够产生一定的协同效应,使得油水界面张力逐渐降低,最终都能达到10-3m N/m的超低界面张力,而且在相同浓度的Na OH、Na2CO3下,含AES的复配体系要比含AEC的复配体系所得到界面张力低。考虑到碱耗以及对储集层伤害的影响,选择0.6%~1.2%Na2CO3与0.1%AES复配体系能更好的达到降低油水界面张力、提高油田采收率的目的。 相似文献
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以黄铜片为基体进行化学镀铜,基础镀液组成和工艺条件为:CuSO4.5H2O10g/L,EDTA-2Na40g/L,NaOH12g/L,HCHO10mL/L,pH13.0,温度35°C,时间10min。研究了非离子型表面活性剂OP-10、曲拉通X-100和吐温-80对起镀时间、沉积速率、铜镀层韧性和晶粒细化的影响。结果表明,3种表面活性剂都会降低铜的沉积速率。质量浓度为1~9mg/L时,曲拉通X-100和OP-10都能使铜镀层的韧性改善和晶粒细化,同时延长起镀时间;吐温-80会显著降低铜的沉积速率,但对铜镀层韧性的影响不大。与曲拉通X-100和吐温-80相比,OP-10是较理想的沉铜韧性改善剂。 相似文献
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添加剂对非离子表面活性剂浊点的影响 总被引:1,自引:0,他引:1
研究了醇类、聚合物、离子型表面活性剂、有机复配物等添加剂对非离子表面活性剂浊点的影响,总结出几类添加剂对非离子表面活性剂浊点的影响规律。结果表明,有机醇对浊点的影响比较复杂,聚合物随着分子链的长短对浊点的影响而不同,离子型表面活性剂的加入会有效提高非离子表面活性剂的浊点。 相似文献
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分别从表面活性剂的亲油性和亲水性的二种性能 ,研究了复配型表面活性剂的性能及规律。在表面活性剂同系物复配的研究中 ,得出相对分子质量分布窄的表面活性剂不能与原油形成低的界面张力 ,但两种以上相对分子质量分布窄的表面活性剂按一定比例混合后 ,则可以与大庆原油形成超低界面张力。形成超低界面张力的表面活性剂平均当量范围为 410~ 430 ,相对分子质量、碱浓度和界面张力三者之间有一定规律 ,即表面活性剂平均相对分子质量增加 ,界面张力曲线向低浓度碱方向移动 ;平均相对分子质量降低 ,界面张力曲线向高浓度碱方向移动。相对分子质量分布是影响界面张力的又一因素 ,表面活性剂相对分子质量分布、原油中的碳数分布和界面张力可能存在某种特定联系。支链对降低界面张力方面比直链有更好的效果 ,表面活性剂相对分子质量越高 ,则油砂对其吸附量越大 相似文献
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Effects of polymerization temperature, conversions, and nonionic surfactant on the particle properties of suspension poly(vinyl chloride) (PVC) resins were investigated. It was shown that polymerization temperature has no significant influences on the mean particle size of PVC resin, and that the cold plasticiser absorption (CPA) of resin decreases linearly with the increase of polymerization temperature. Agglomeration of VCM droplets finishes before 20% conversion, and the mean particle size keeps almost constant at later stages of the polymerization process, but the CPA continues decreasing with the increase of conversion. Scanning Electron Microscopy (SEM) micrographs show that the degree of agglomeration of primary particles increases with polymerization temperature and conversion. Addition of nonionic surfactant to the VCM suspension system, as a secondary suspending agent, has a great influence on the particle properties of PVC resin. The particle size and CPA increase as the concentration of nonionic surfactant increases. The nonionic surfactant with a greater HLB value is more effective in raising the mean particle size, but is less effective in raising the CPA. It is considered that the added nonionic surfactant would be absorbed faster on the VCM/water interface than the poly(vinyl alcohol) (PVA), which was used as the primary suspending agent. Because the colloid protection ability of the nonionic surfactant is less than that of PVA, droplets become less resistant to coalescence, and the mean particle size of the final PVC resin increases consequently. The increase of porosity is caused by the combined effects of increased coalescence of VCM droplets and the nonionic surfactant's steric effect inside the droplets. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 85: 1544–1552, 2002 相似文献
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Effects of individual and composed poly(vinyl alcohol) (PVA) suspending agents on the particle morphology of poly(vinyl chloride) (PVC) resins were investigated and discussed in the view of PVA absorption at the oil/water interface and interfacial behavior. It was shown that the percentage and surface coverage of PVA at the oil/water interface decreased with the increase of the degree of hydrolysis (DH) of PVA in the DH range of 70–98 mol %, while the interfacial tension of VC/PVA aqueous solution increased linearly with the increase of DH of PVA. PVC resin with more regular particle shape, increased agglomeration and fusion of primary particles, lower porosity and higher bulk density, was prepared by using PVA with a higher DH as a suspending agent. This was caused by the occurrence of drop coalescence at the very early stage of VC polymerization, the increase of particle shrinkage, and the lower colloidal protection to primary particles. It was also shown that the interfacial tension of VC/water in the presence of composed PVA suspending agents varied linearly with the weight composition of the composed PVA suspending agents. The particle properties of PVC resin prepared by using the composed PVC suspending agents were usually situated in between the properties of PVC resins prepared by using the corresponding individual PVA suspending agent. The particle morphology and properties of PVC resin could be controlled by the suitable choice of the composed PVA suspending agents. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 90: 3848–3855, 2003 相似文献
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研究了二甘醇双(α-磺酸钠)烷基羧酸酯(DMES-n)、十二烷基二甲基胺乙内酯(BS-12)两类表面活性剂与原油的界面张力,并考察了表面活性剂的耐温抗盐性。实验结果表明,DMES-n能将油水界面张力降低至10-2mN/m数量级,但是抗盐性不如BS-12;将两者复配后,在NaCl浓度为30 000~100 000 mg/L、MgCl2和CaCl2浓度为10 000 mg/L的条件下,DMES-14/BS-12和DMES-16/BS-12复配体系都能将油水界面张力降低至10-3mN/m数量级,表明复配体系既具有更好的降低界面张力的能力,同时还具有良好的抗高盐、高钙镁性能以及良好的耐温性。 相似文献
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