Pre-treatment optimization to reduce membrane fouling during produced water treatment with an integrated FO-MD system

Muhammad Saqib Nawaz , Sofiane Soukane , Muhammad Bilal Asif , Veerabhadraiah Gudideni , Sultan Alrubaish , Noreddine Ghaffour
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Abstract

During oil exploration, fresh water that is injected into underground reservoirs returns to the surface loaded with hydrocarbons, salts, and other contaminants. This complex solution is typically known as produced water (PW). Generally, different PW streams are generated at a given site, which, after suitable treatment, are sent for re-injection for enhanced oil recovery or to disposal wells. However, there is a potential for water recovery from this hypersaline contaminated stream. Forward osmosis (FO) and membrane distillation (MD) are two low-pressure membrane treatment technologies successfully used in a single hybrid system for PW treatment. During operation, the key foulants on the FO membrane were CaSiO3, CaSO4, and NaCl, while for MD, they were SiO2 and CaSO4 plus emulsified oil, causing pore clogging. Some foulants were tightly bound and not removed by osmotic backwashing or hydraulic flushing, thus requiring pre-treatment. Different pre-treatment techniques, like ion exchange resins and polymeric and ceramic membrane-based ultrafiltration (UF), were assessed in this study. The resins were able to remove bivalent metallic ions successfully from lower concentration streams only and thus caused an increase in FO flux and a reduction in MD flux by disturbing the FO-MD system equilibrium. The higher concentrations of resins and chemicals required for their regeneration make them unsuitable for such applications. On the contrary, PW pre-treated with polymeric and ceramic UF membranes led to increased FO and MD fluxes without any chemical requirement and proved suitable for pre-treatment.
采用集成FO-MD系统对采出水处理过程中的膜污染进行预处理优化
在石油勘探过程中,注入地下储层的淡水带着碳氢化合物、盐和其他污染物返回地表。这种复杂的溶液通常被称为采出水(PW)。一般来说,在给定的地点产生不同的废液流,经过适当的处理后,这些废液流被送去重新注入以提高采收率或进入处置井。然而,从这条高盐污染的河流中有可能回收水。正向渗透(FO)和膜蒸馏(MD)是两种低压膜处理技术,成功应用于单一混合系统中处理PW。在运行过程中,FO膜上的关键杂质是CaSiO3、CaSO4和NaCl,而MD膜上的主要杂质是SiO2和CaSO4 +乳化油,会造成孔隙堵塞。有些污物结合紧密,不能通过渗透反冲洗或液压冲洗去除,因此需要预处理。本研究评估了不同的预处理技术,如离子交换树脂、聚合物和陶瓷膜基超滤(UF)。树脂只能成功地从低浓度流中去除二价金属离子,从而通过扰乱FO-MD系统平衡导致FO通量增加和MD通量减少。其再生所需的较高浓度的树脂和化学物质使其不适合此类应用。相反,用聚合物和陶瓷UF膜预处理的PW在不需要任何化学反应的情况下增加了FO和MD的通量,证明了预处理是合适的。
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