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RPSEA Project 07122-12 TECHNICAL ASSESSMENT OF PRODUCED WATER TREATMENT TECHNOLOGIES 1st Edition Figure 29. A schematic of a vertical-tube, falling-film MVC evaporator (Source: [129]). Figure 30. The vertical-tube, falling-film MVC evaporation system for produced water treatment and steam production (Source: [129]). De-oiled produced water enters a feed tank where the pH is adjusted. The wastewater is pumped to a heat exchanger that raises its temperature to a boiling point. Hot, de-aerated feed enters the evaporator sump, where it combines with the recirculating brine slurry. The slurry is pumped to the top of a bundle of heat transfer tubes. As the brine flows down the tubes, a small portion evaporates and the rest falls into the sump to be recirculated (Figure 29). The vapor travels down the tubes with the brine and is drawn up through specially designed mist eliminators on its way to the vapor compressor. Compressed vapor flows to the outside of the heat transfer tubes, where its latent heat is given up to the cooler brine slurry falling inside. As the vapor loses heat, it condenses as distilled water. The distillate is pumped back through the heat exchanger, where it gives up sensible heat to the incoming wastewater. A small amount of the brine slurry is continuously blowdown from the evaporator to control density [129]. 88PDF Image | TECHNICAL ASSESSMENT OF PRODUCED WATER TREATMENT TECHNOLOGIES
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