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Closed circuit desalination series no-3: high recovery low energy desalination of brackish water by a new two-mode consecutive sequential method

机译:闭路海水淡化系列No-3:通过新的两模式连续序贯方法对微咸水进行高回收率低能量脱盐

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摘要

A new method for continuous Brackish Water desalinated by a two-mode consecutive sequential process which incorporates closed circuit and plug flow desalination (PFD) techniques is exemplified with a commercial apparatus (named REIM-Ⅱ) comprising 10 modules (8"), each of four elements (ESPA2+), with their inlets and outlets connected in parallel, and with recycled concentrate mixed with fresh pressurized feed admitted at inlet to modules. When the salinity of the recycled concentrate inside the closed circuit manifests the desired system recovery level, the apparatus switches from closed circuit to PFD by valve means until the entire brine in the closed circuit replaced by fresh feed, and thereafter, closed circuit desalination (CCD) resumed. CCD in said apparatus experienced most of the time with the same fixed flow rate of feed and permeate under variable pressure conditions; whereas, PFD takes place briefly only after the system attains its desired recovery level at a predefined pressure in order to enable replacement of brine by fresh feed without stopping desalination. Replacement of brine by fresh feed takes place with enhanced feed flow under reduced pressure with a lower momentary recovery in order to expedite the process and minimize brine energy losses. The new method is exemplified by the commercial operation of the REIM-Ⅱ unit with feed of 6800 μS cm~(-1) according to conditions as followed: CCD Mode: 35 m~3 h~(-1) flow rate of feed and permeate (≈19 lmh); 36 m~3 h~(-1) flow rate of recycled concentrate; 1.1 bar of module pressure difference (Δp); and 17-25 bar of an effective variable pressure range. Plug Flow Desalination Mode: 45 m~3 h~(-1) flow rate of feed; 16 m~3 h~(-1) flow rate of permeate (≈10 lmh); 29 m~3 h~(-1) flow rate of rejected brine; 0.5 bar of module pressure difference (Δp); and 9 bar average pressure. Overall Performance: 30.7 m~3 h~(-1) average flow rate of permeate; 37.04 m~3 h~(-1) average flow rate of feed; 82.9% recovery; 28.83 kW power consumption; 0.94 kWh m~(-3) specific energy with 61.5% efficiency of the high pressure pump; 20 min total sequence duration with 65% of the time experienced with CCD, 20% experienced with PFD, and 15% experienced during transitions between cited modes. The commercial REIM-Ⅱ unit has been operated continuously over the past 20 mo and produced some 400,000 m~3 permeates with 88-80% recovery in the respective feed salinity range 5800-8900 μS cm~(-1).
机译:包含闭路和塞流脱盐(PFD)技术的通过双模式连续顺序过程进行连续咸水淡化的新方法,以商用设备(名为REIM-Ⅱ)为例,该设备包括10个模块(8英寸),每个模块四个元素(ESPA2 +),其入口和出口并联,并在模块的入口处将回收的浓缩物与新鲜的加压进料混合,当闭路内部的回收的浓缩物的盐度显示出所需的系统回收率时,设备通过阀装置从闭路切换到PFD,直到闭路中的全部盐水被新鲜的进料代替,然后恢复闭路淡化(CCD),该装置中的CCD在大多数时间内以相同的固定进料速度进行并在可变压力条件下渗透;而PFD仅在系统在预定的压力下达到所需的回收水平后短暂进行确保在不停止淡化的情况下用新鲜饲料代替盐水。用新鲜饲料代替盐水,可以在减压下以更高的进料流量和较低的瞬时回收率来进行进料,以加快流程并最大程度地降低盐水能量损失。该新方法以REIM-Ⅱ装置的商业运行为例,其进料为6800μScm〜(-1),其条件如下:CCD模式:进料流量为35 m〜3 h〜(-1)渗透(≈19lmh);再生精矿流量36 m〜3 h〜(-1); 1.1 bar的模块压差(Δp);有效压力范围为17-25 bar。塞流脱盐模式:进料流量45 m〜3 h〜(-1); 16 m〜3 h〜(-1)透过水流量(≈10lmh);排盐水的流量为29 m〜3 h〜(-1); 0.5 bar的模块压差(Δp);和9巴的平均压力。总体性能:30.7 m〜3 h〜(-1)平均产水量;进料平均流量37.04 m〜3 h〜(-1);回收率82.9%;功耗28.83 kW; 0.94 kWh m〜(-3)比能,高压泵效率为61.5%;总序列持续时间为20分钟,其中CCD经历65%的时间,PFD经历20%的时间,引用模式之间的转换期间经历15%的时间。商用REIM-Ⅱ装置在过去20个月中已连续运行,在各自的盐度范围5800-8900μScm〜(-1)下,生产了约400,000 m〜3的渗透液,回收率达88-80%。

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