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随着三元复合驱采油技术的大面积推广,三元复合驱采出液的化学破乳作为重要的配套技术也开始成为人们必须关注的问题。在对三元复合驱采出液化学破乳的室内研究中,受工作时间和条件的限制,不可能以不同的采出阶段的油田的实际采出液作为研究客体进行实验。因此,本文考虑以杏1- 4-23和杏2-2-试采出液上层乳化油和下层游离水按一定比例混合后均质制得模拟乳化体。考察了影响模拟乳化体性状的因素,并与实际采出液的性质作对比。 相似文献
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周广玲 《中国石油和化工标准与质量》2012,33(15):48
三元复合驱技术迅速发展,在矿场试验中取得了较好的增油降水效果,但是采出液中残余的聚合物、碱、表活剂使采出液乳化严重,导致油水分离困难。本文进行三种破乳剂对两口三元井采出液室内破乳评价室验,通过破乳效果分析,筛选出一种适合三元复合驱采出液的破乳剂,并进行了现场实验,取得了较好效果。 相似文献
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由于三元复合驱采出液中表活剂、聚合物以及天然乳化剂的多重作用,致使采出液油水分离困难。通过对聚酰胺-胺(PAMAM)进行季铵化改性,使其端基带有正电荷,提高了其对三元复合驱采出水的破乳性能,试验结果表明,破乳剂PA01对三元驱污水具有较好的破乳效果:在温度45℃、沉降时间90min条件下,投加PA01120mg.L-1,破乳后初始含油量为5000mg.L-1降至195mg.L-1,脱油率为96.1%;初始含油量为1500mg.L-1降至214mg.L-1,脱油率为85.6%。 相似文献
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自20世纪90年代开始,国内研究人员在聚合物驱采出液性质和破乳方法方面开展了大量研究和试验工作,发现与水驱采出液相比,聚合物驱采出液水相粘度和携砂量大,油水分离速率低,乳化原油导电性强,造成游离水脱除器和电脱水器内淤积严重,电脱水器运行电流升高甚至频繁垮电场。 相似文献
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油水分离剂在低驱油剂含量三元复合驱采出液处理中的应用 总被引:5,自引:0,他引:5
通过室内和现场试验评价了针对聚合物驱采出液研制的油水分离剂SP1003处理大庆油田杏二中试验区低驱油剂含量(NaOH388mg/L,重烷基苯磺酸盐表面活性剂25mg/L,部分水解聚丙烯酰胺108mg/L)三元复合驱采出液的可行性。现场试验过程中在SP1003加药量为30mg/L的情况下,游离水脱除器放水和水处理设施进水含油量分别由试验前的平均40030mg/L和1547mg/L降低到858mg/L和197mg/L,降低幅度分别为97.9%和87.3%。试验过程中还发现杏二中试验站游离水脱除器前的离心脱水泵造成采出液严重二次乳化,二次乳化后的采出液在脱水泵至游离水脱除器间管道内的停留时间过短使得采出液中的油珠聚并不充分,以及采出液处理设施运行不平稳都对杏二中试验区三元复合驱采出液和采出水处理有非常严重的不良影响。 相似文献
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弱碱三元复合驱采出液乳化严重,油水分离的速度及程度,影响其经济效益.采用恒温静沉分离、多重光散射仪、脱水率等手段,研究了加热条件下清水型、聚醚型、多乙烯多胺型破乳剂对大庆油田某弱碱三元复合驱乳状液的破乳效果.结果 表明,在加热条件下,3类破乳剂对弱碱三元复合驱均有不同程度的破乳效果,3类破乳剂中100#(聚醚型)破乳剂的破乳脱水速率较快.温度越高,破乳速率越高,乳状液的分离效果越好,温度升高至55℃时,出现极值温度点,乳状液的破乳效果最好,温度继续升高,乳状液反而出现乳化现象.10#聚醚型破乳剂在10mg· L-1油相、水相具有良好的破乳效果,适合大庆油田某区块弱碱三元复合驱采出液破乳. 相似文献
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乙烯酮(双乙烯酮)是十分重要的化工中间体,其下游产品较多。江苏某化工厂开发生产乙烯酮(双乙烯酮)下游产品三十多个,年生产规模三万多吨,是国内以乙烯酮(双乙烯酮)为中间体生产精细化学品的综合骨干企业。针对乙烯酮(双乙烯酮)下游产品废水特点,该厂结合企业实际,开展了产品优化,结构调整,清洁生产,资源循环利用,节水降耗等工作,从源头削减了污染物的生产。同时投资二千多万元新建预处理装置三套,6000m3/d废水生化处理装置一套,使全厂乙烯酮(双乙烯酮)下游产品的废水得到了有效的治理。 相似文献
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D. G. Gordeev L. F. Gudarenko M. V. Zhernokletov V. G. Kudel’kin M. A. Mochalov 《Combustion, Explosion, and Shock Waves》2008,44(2):177-189
A semi-empirical equation of state for metals is described. Its capabilities are demonstrated by the example of the equation
of state for aluminum. New experimental data are presented on the location of the isentrope of aluminum for unloading from
the state at p = 229.71 GPa on the shock adiabat to an aerogel (SiO2) of density 0.08 g/cm3.
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Translated from Fizika Goreniya i Vzryva, Vol. 44, No. 2, pp. 61–75, March–April, 2008. 相似文献
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Jorge Marcelo Romero Soledad Bustillo Hugo Enrique Ramirez Maisuls Nelly Lidia Jorge Manuel Eduardo Gómez Vara Eduardo Alberto Castro Alicia H. Jubert 《International journal of molecular sciences》2007,8(7):688-694
A thermochemical rather simple experimental technique is applied to determine the enthalpy of formation of Diperoxide of ciclohexanone. The study is complemented with suitable theoretical calculations at the semiempirical and ab initio levels. A particular satisfactory agreement between both ways is found for the ab initio calculation at the 6–311G basis This set level. Some possible extensions of the present procedure are pointed out. 相似文献
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A perturbation viscometer is a differential capillary viscometer that measures the logarithmic viscosity gradient of the viscosity-composition curve for gas mixtures. Measurements are made at different gas mixture compositions. Integration of the logarithmic viscosity gradients measured over the full composition range gives the mixture viscosity relative to the viscosity of one of the pure components of the gas mixture. This method is attractive because, for measurements of equal precision, integration of the gradients is potentially an order of magnitude more precise than measurement of the viscosities directly. It can also work at high and low temperatures and perhaps high pressures.The perturbation viscometer has been used to make measurements on ideal gas mixtures at ambient and elevated temperatures. The situation is more complicated when the gas mixtures are non-ideal. Extra effects due to density differences, molar volume change on mixing and differential thermal expansion may be measured in addition to the desired viscosity change producing systematic errors in the results. Thus, a more sophisticated apparatus is required. The standard perturbation viscometer has been modified to separate out the extra effects to permit measurement of the true change in viscosity. In addition, the theoretical operation of the modified apparatus has been revised to account for the design changes to permit calculation of the viscosity-composition profiles from the results.The apparatus has been tested using helium-HFC-125 mixtures and two new viscosity-composition profiles are presented for these mixtures at 23 and . Internal consistency tests have been used to confirm that the data produced are of high quality with an estimated uncertainty in the viscosity ratio data at of 0.9% and at of 1.5%. 相似文献
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塔设备改造选型的分析 总被引:2,自引:0,他引:2
就当前扩产增容中塔设备设计和改造时板式塔和填料塔的选型问题加以分析。在评述目前国内常用的几种塔板和新型填料之后,着重介绍一种新型塔板(导向梯形浮阀塔板)和一种新型填料(波环填料——乾隆帕克)。 相似文献