海水脱硫-优化水垢处理和降低运营成本和资本支出

S. Baraka-Lokmane, N. Lesage, A. Fayed, M. Jungas, S. Heng, M. Jacob, P. Pedenaud
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摘要

为了能够生产出同样数量的石油,必须向储层注入一桶海水。为了避免酸化和/或与储层水不相容的问题,注入脱硫海水。在本文中,我们完全重新考虑了脱硫过程,目标是产生更多的水,同时优化阻垢剂的数量和类型,优先考虑绿色化学品。自1992年以来建立的脱硫工艺从未修改过。我们的新理念适应了野外生活的限制。考虑到基于流体力学、电中性和材料转移的参数和物理定律,对膜(极化层)上垢沉积的风险进行了理论和模拟研究。膜的行为和沉积风险取决于温度、压力、通量、切向流量、膜和间隔层上潜在的水垢积聚;已经使用了现场和实验室试点。为了选择阻垢剂,进行了堵管试验。结果表明,在阻垢剂的帮助下,可以实现80%以上的采收率。83%的回收率似乎是最大限度。在不使用阻垢剂的情况下,在某些情况下可以获得75%的回收率。这些结果使我们能够就道达尔的业务领域、正在开发的项目和我们未来的项目提出业务建议。增加回收率和/或降低阻垢剂浓度将减少(通过精矿)排放到海洋的化学物质。此外,阻垢剂的选择允许选择几种可生物降解的产品,比目前使用的产品效率更高。在测试的11种产品中,有4种已被选中。降低运营成本:在某些操作条件下,阻垢剂的用量可以降低2 - 3,甚至可以抑制。选择试验使我们能够从技术、经济和环境友好的角度选择最合适的化学品。减少资本支出:回收率的提高使我们能够减少纳滤整个预处理的规模,因为流量是影响水处理厂成本最大的参数。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Sea Water Desulphation – Optimisation of Scale Treatment and Reduction of OPEX & CAPEX
One barrel of seawater has to be injected into the reservoir in order to be able to produce the same amount of oil. In order to avoid problems of souring and/or incompatibility with reservoir water, desulphated seawater is injected. In this paper, we have completely reconsidered the desulphation process with the objective of producing more water while optimising the quantity and type of scale inhibitors, with a priority given to green chemicals. The desulphation process established since 1992 has not been modified since. Our new philosophy adapts to the constraints of the field life. Theoretical and simulations studies have been carried out on risks of scale deposition on the membrane (polarisation layer) taking into account parameters and physical laws based on fluid mechanics, electroneutrality and material transfer. The behavior of membrane and risk of deposition depends on temperature, pressure, flux, tangential flow, potential accumulation of scale on the membrane and spacer; site and laboratory pilots have been used. Tube blocking tests have been carried out in order to select the scale inhibitors. Results showed that it is possible to operate beyond 80% of recovery with the help of a scale inhibitor. 83% recovery appears to be a maximum limit. Without the use of a scale inhibitor it is possible to obtain 75% of recovery under certain circumstances. These results have enabled us to issue operational recommendations on TOTAL operating fields, on projects under development and on our future projects. The increase of the recovery and / or decrease in the concentration of scale inhibitor will conduct to less chemical discharged to the sea (via the concentrate). In addition, the selection of scale inhibitors has allowed selection of several biodegradable products, with better efficiency than currently used products. Of the 11 products tested, four have been selected. Reduction of OPEX: The consumption of scale inhibitor could be reduced by 2 or 3 and even suppressed for certain operating conditions. Selection tests have allowed us to choose most appropriate chemical from a technical, economic and environmental friendly point of view. Reduction of CAPEX: The increase of recovery has allowed us to reduce the dimensioning of the whole pretreatment of the nanofiltration as the flowrate is the parameter that influences the most the cost of a water treatment plant.
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