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通过真空膜蒸馏随后结晶从页岩气采出水回收水和盐。

Water and salt recovery from shale gas produced water by vacuum membrane distillation followed by crystallization.

作者信息

Qiu Boya, Liu Jingyun, Liu Yicai, Wang Yinan, Xiao Zeyi, Fan Senqing

机构信息

School of Chemical Engineering, Sichuan University, No. 24 South Section 1, Yihuan Road, 610065 Chengdu, China.

School of Chemical Engineering, Sichuan University, No. 24 South Section 1, Yihuan Road, 610065 Chengdu, China.

出版信息

J Environ Manage. 2023 Dec 1;347:119094. doi: 10.1016/j.jenvman.2023.119094. Epub 2023 Sep 28.

Abstract

A vacuum membrane distillation (VMD) followed by crystallization (VMD-C) was developed for the recovery of water and salts from shale gas produced water (SGPW). Before VMD, the pretreatment of SGPW with Fenton oxidation-flocculation is applied, with the chemical oxygen demand (COD) concentration reduction of 75% and the total removal of the total suspended solids (TSS), Ca, and Mg in SGPW. The pretreatment of SGPW mitigated the membrane fouling in the VMD and effectively prevented the reduction of membrane flux over time. The average flux of the PTFE membrane reached 12.1 kg m h during the separation of the pretreated SGPW at a feed flux of 40 L h and a feed temperature of 40 °C. The rejection rate of the membrane to TDS in SGPW was over 99%. Fresh water with a conductivity of below 20 μs cm was produced by VMD-C. The salts concentrated upstream of the membrane were recovered by a stirring crystallization process. The VMD-C system resulted in a 61% cost savings compared to conventional SGPW treatment.

摘要

开发了一种先进行真空膜蒸馏(VMD)再进行结晶(VMD-C)的工艺,用于从页岩气采出水(SGPW)中回收水和盐分。在进行VMD之前,采用芬顿氧化-絮凝对SGPW进行预处理,化学需氧量(COD)浓度降低75%,SGPW中的总悬浮固体(TSS)、钙和镁被完全去除。SGPW的预处理减轻了VMD中的膜污染,并有效防止了膜通量随时间的降低。在进料通量为40 L/h、进料温度为40°C的条件下,对预处理后的SGPW进行分离时,聚四氟乙烯(PTFE)膜的平均通量达到12.1 kg·m⁻²·h⁻¹。该膜对SGPW中总溶解固体(TDS)的截留率超过99%。VMD-C工艺产出了电导率低于20 μs/cm的淡水。膜上游浓缩的盐分通过搅拌结晶工艺回收。与传统的SGPW处理方法相比,VMD-C系统节省了61%的成本。

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