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首页> 外文期刊>Desalination: The International Journal on the Science and Technology of Desalting and Water Purification >Alternative design to dual stage NF seawater desalination using high rejection brackish water membranes
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Alternative design to dual stage NF seawater desalination using high rejection brackish water membranes

机译:使用高排阻微咸水膜进行双级NF海水淡化的替代设计

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摘要

Dual stage NF membrane desalination process was proposed as an alternative approach to RO seawater desalination. Despite of being cheaper than RO desalination, dual stage NF process is not commercially applied yet due to the low overall recovery rate. In an attempt to increase the process recovery rate and to reduce the operation complicity, brackish water RO membrane was used instead of NF in the second stage. ROSA software was used in this study to verify the applicability and cost-effectiveness of the NF-BW dual stage desalination process. Similarly to dual stage NF desalination process, an NF membrane was used in the first stage and BW membrane in the second stage. Permeate from NF membrane was used as a feed into the BW membranes. The effect of membrane type and seawater salinity on the process performance was investigated. For any given recovery rate and seawater salinity, the simulation results showed that the overall cost of NF-NF was slightly lower than the NF-BW process but that was on the cost of higher permeate TDS. For instance, at 43,000 mg/1 feed salinity the difference in the specific power consumption between NF-NF and NF-BW process was 0.38 kWh/m~3. The permeate TDS was 125 mg/1 for NF-BW and 1030 mg/1 for NF-NF process. The difference in the permeate TDS between NF-NF and NF-BW process increased with increasing the feed salinity. In dual stage NF process, a low permeate was achieved at low recovery rate. For example, at 43,000 mg/1 feed salinity the permeate TDS from dual stage NF process was 359 mg/1 when the overall recovery rate was 22%. It was also found that the effect of BW membrane type on the process efficiency was insignificant. Finally, the energy requirements of NF-NF and NF-BW were compared to a single stage RO desalination process. The specific power consumption at 43,000 mg/1 feed salinity was 4.58 kWh/m~3, 4.2 kWh/m~3 and 3.86 kWh/m~3 for RO, NF-BW and NF-NF process respectively.
机译:提出了双级NF膜脱盐工艺作为RO海水淡化的替代方法。尽管比RO脱盐便宜,但由于总回收率低,双级NF工艺尚未在商业上应用。为了提高工艺回收率并减少操作复杂性,在第二阶段中使用微咸水RO膜代替NF。在这项研究中,使用了ROSA软件来验证NF-BW双级淡化工艺的适用性和成本效益。类似于双阶段NF脱盐工艺,在第一阶段使用NF膜,在第二阶段使用BW膜。来自NF膜的渗透物用作BW膜的进料。研究了膜类型和海水盐度对工艺性能的影响。对于任何给定的回收率和海水盐度,模拟结果均表明,NF-NF的总成本略低于NF-BW工艺,但其代价是较高的渗透性TDS。例如,在43,000 mg / 1的饲料盐度下,NF-NF和NF-BW工艺之间的比功率消耗差异为0.38 kWh / m〜3。对于NF-BW,渗透物TDS为125 mg / 1,对于NF-NF工艺,渗透物TDS为1030 mg / 1。 NF-NF和NF-BW工艺之间的渗透TDS的差异随着饲料盐度的增加而增加。在双阶段NF工艺中,以低回收率实现了低渗透。例如,当总回收率为22%时,在43,000 mg / 1的进料盐度下,来自双阶段NF工艺的渗透物TDS为359 mg / 1。还发现,BW膜类型对工艺效率的影响微不足道。最后,将NF-NF和NF-BW的能量需求与单级反渗透淡化工艺进行了比较。 RO,NF-BW和NF-NF工艺在43,000 mg / 1进料盐度下的单位能耗分别为4.58 kWh / m〜3、4.2 kWh / m〜3和3.86 kWh / m〜3。

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