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Inhibition and Interaction between Iron Sulphide,Zinc Sulphide and LeadSulphide

机译:硫化铁,硫化锌和铅硫化铁之间的抑制作用

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Iron sulphide (FeS),zinc sulphide (ZnS) and lead sulphide (PbS) scales have been observed in many souroil and gas wells.Sulphide scales often form alongside other scales such as calcium carbonate and bariumsulphate and such scales can be removed using chemicals like hydrochloric acid (HCl) and chelating agents.However,there are several drawbacks associated with the removal of sulphide scales,for example,HClacid,which outperforms other dissolvers has a high corrosion rate and generates hydrogen sulphide (H2S)gas as a byproduct.Other dissolvers,including chelating agents,have very low dissolution rates.Therefore,FeS inhibition is much preferred to its removal,if this can be achieved efficiently and economically.The objective of this paper is to investigate the inhibition efficiency of inhibitors/dispersants forpreventing FeS,ZnS and PbS scales.Different scale inhibitor chemistries have been examined over a widerange of parameters,including temperature,salinity,pH and concentrations of Fe,Zn,Pb and sulphide.Static formation and inhibition experiments were conducted and the progress of the reaction was monitoredby ion tracking using inductively coupled plasma (ICP) analysis and pH monitoring.Also,filter-blockinginhibition tests were carried out to examine the impact of scale inhibitor concentration on the scaling time.Polymeric scale inhibitors showed a high inhibition efficiency for ZnS while no inhibition was observedfor phosophonate based scale inhibitors.Unlike ZnS,none of the tested scale inhibitors inhibited FeS.Highmolecular weight scale inhibitors performed well even at high temperature and salinity and maintainedthe particles suspended in solution for several days.However,high scale inhibitor concentrations wererequired to prevent the deposition of FeS,particularly when the iron concentration was raised to 100 ppmand above.In SI-1 solutions,it was easier to inhibit PbS and ZnS when they formed concurrently rather thanforming PbS followed by ZnS.These results are in line with the difference in the MIC (Minimum InhibitorConcentration) observed in SI-2 solutions.Based on these results,the tested polymeric scale inhibitors managed to inhibit ZnS and PbS but failedagainst FeS under the same conditions despite the fact that the solubility of ZnS and PbS is less than FeS.Itwas also found that,cation displacement and the sequence of the scale formation had a significant impacton the inhibition efficiency.The size of scale particles was dependent on the type of scale inhibitor andconcentration and this was reflected in the scaling time in the dynamic inhibition tests.
机译:在许多源极和气体井中已经观察到硫化铁(FES),硫化锌(ZnS)和铅硫化铅(PBS)尺度。普通鳞片通常形成其他鳞片,例如碳酸钙和钡氧化钙,并且可以使用化学品除去这种鳞片盐酸(HCl)和螯合剂。然而,随着硫化物鳞片的除去有几个缺点,例如Hclacid,其优于其他溶解器具有高腐蚀速率并产生作为副产品的硫化氢(H2S)气体。其他溶剂包括螯合剂,包括螯合剂的溶解率具有非常低的溶解率。因此,如果可以有效且经济地实现,FES抑制是较多的。本文的目的是探讨抑制剂/分散剂的抑制效率,如图所示, ZnS和PBS尺度。已经在参数较宽的参数上进行了种不同的比例抑制剂化学物质,包括温度,盐度,pH和Fe的浓度,Zn,Pb和硫化物。进行了静态形成和抑制实验,使用电感耦合等离子体(ICP)分析和pH监测来监测反应的进展。进行过滤阻塞抑制试验以检查影响缩放抑制剂浓度对缩放时间。聚合物测量抑制剂对ZnS显示出高抑制效率,同时不观察到基于偶磷酸盐的测量抑制剂的抑制。诸如测试的水垢抑制剂没有抑制FES。即使在高温下,高分分子的重量抑制剂也表现良好和盐度并将颗粒维持在溶液中悬浮几天。然而,高尺度抑制剂浓度无序以防止FES的沉积,特别是当将铁浓度升至100 ppmand时。在Si-1溶液中,抑制PBS更容易抑制PBS当它们同时形成而不是形成PBS后,ZnS是ZnS。结果AR E符合在Si-2溶液中观察到的MIC(最小抑制剂浓度)的差异。基于这些结果,测试的聚合物抑制剂抑制ZnS和PBS抑制ZnS和PBS,但在相同的条件下,难以使得陷入困境的情况ZNS和PBS小于FES.ITWA也发现,阳离子位移和刻度形成的序列具有显着的抗撞击官,抑制效率。规模粒子的大小取决于规模抑制剂和浓度的类型,这反映在动态抑制试验中的缩放时间。

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