search.noResults

search.searching

saml.title
dataCollection.invalidEmail
note.createNoteMessage

search.noResults

search.searching

orderForm.title

orderForm.productCode
orderForm.description
orderForm.quantity
orderForm.itemPrice
orderForm.price
orderForm.totalPrice
orderForm.deliveryDetails.billingAddress
orderForm.deliveryDetails.deliveryAddress
orderForm.noItems
PC-APR24-PG42.1_Layout 1 10/04/2024 11:27 Page 42


HEAT TRANSFER


EFFECTIVE SEPARATION USING EVAPORATION


Matt Hale, International Sales & Marketing Director, HRS Heat Exchangers, discusses the role of evaporation in treating challenging wastewater and effluent streams


astewater and effluent can take many different forms, from relatively clean water which can safely be discharged to the environment with little or no treatment, to extremely challenging effluent containing high levels of dissolved or suspended solids, chemicals and biological material. Some materials that can be particularly difficult to treat include landfill leachate, and industrial wastewater streams, many of which can no longer be discharged to the environment or even public sewage systems.


W


The exact types of treatment used will vary depending on many factors, including the nature of the wastewater or effluent stream/s, the material’s chemical and biological oxygen demand (COD & BOD), the standard required for the final material, and whether material capture and reuse are required, to name just a few. However, evaporation is becoming increasingly popular as a way of effectively separating the liquid and solid waste streams. Landfill leachate is formed from water which has entered the landfill from external sources (rainfall, surface water and groundwater) as well as the putrefaction of waste materials in the landfill. The composition of landfill leachate will vary with the age of the landfill and the type of waste involved, but typically contains both dissolved and suspended materials, such as organic matter (alcohols, acids and sugars, etc.), cations (sulphates, chloride, iron, etc.), heavy metals (like lead, nickel, cobalt and mercury) and other complex organic molecules like PCBs and dioxins. Where large volumes of building waste or gypsum have been disposed of, hydrogen sulphide may also be an issue. Industrial wastewater streams can include heavy metals, halogen compounds and other potentially harmful nutrients or suspended solids. Most countries or regions around the world have strict rules on the treatment and discharge of such waste streams, including requirements for the ‘zero discharge’ of wastewater.


High levels of dissolved or suspended organic materials can also make effluents very difficult to treat. A few examples include liquid tannery waste, effluent from fish farms, and wastewater streams from abattoirs or even blood- processing laboratories.


Because of this variation in material and 42 APRIL 2024 | PROCESS & CONTROL


treatment situation there are also a wide range of treatment techniques which can be used to treat them. Physical separation options include settlement, submerged aeration filters (SAF), dissolved aeration filters (DAF), and induced air flotation. Other biological treatments (aerobic or anaerobic) and chemical treatments (such as de-salting, alkylation and neutralisation) are also often required. However, the use of evaporation technologies to separate difficult effluents into water and solid waste streams (or highly concentrated sludges) is becoming increasingly common.


Zero liquid discharge (ZLD) is a liquid waste stream treatment which involves transforming liquid waste streams into clean water (which can be reused) and a minimum volume of solid residues. It is particularly suitable for effluents which are hazardous, toxic or difficult to treat using other methods. A well-designed ZLD system will minimise or eliminate liquid waste streams, resulting in clean water for reuse or environmentally-friendly discharge, and a solid residue suitable for further processing or safe disposal.


However, separating the water from the


effluent requires large amounts of energy: it takes roughly six-times more energy to evaporate water (latent heat) at its boiling point then the energy needed to actually bring it to that boiling point (sensible heat). For this reason, the evaporation processes used for ZLD usually include energy optimisation in the form of multistage evaporators, thermal vapour recompression (TVR), or mechanical vapour recompression (MVR).


HRS has installed a number of evaporation systems to treat difficult effluents. Some of these are true ZLD systems (above), while others reduce the volume of liquid as sludges to enable more efficient management or further treatment. The HRS solution Depending on the effluent being processed, HRS can select from a series of technologies for designing the most optimal ZLD process. Energy optimisation methods (multistage, TVR, MVR) can be combined with different heat transfer technologies and the overall process can be separated into three steps:


1. Evaporation/concentration: The product is concentrated to just below its maximum concentration (saturation). The evaporation plant is usually a multistage evaporator set-up.


2. Cooling: if the maximum solubility curve is steep, the product obtained in step 1 is cooled, provoking immediate precipitation of dissolved solids.


3. Crystallisation: Crystallisation/ sedimentation of the solids produced in step 2 occurs in specially designed crystallisation tanks. A supernatant layer of concentrated solution remains after this stage and is returned to step 1 for reprocessing. The coolers and evaporators used in these situations must be designed to work with difficult materials with very high fouling potential. For this reason, a typical HRS evaporator will use Unicus Series scraped surface evaporators (left) that are self- cleaning and maintain optimal evaporation rates. R Series scraped surface coolers are also used for cooling the saturated solutions that are sent to the crystallisation tanks.


HRS Heat Exchangers www.hrs-heatexchangers.com


Page 1  |  Page 2  |  Page 3  |  Page 4  |  Page 5  |  Page 6  |  Page 7  |  Page 8  |  Page 9  |  Page 10  |  Page 11  |  Page 12  |  Page 13  |  Page 14  |  Page 15  |  Page 16  |  Page 17  |  Page 18  |  Page 19  |  Page 20  |  Page 21  |  Page 22  |  Page 23  |  Page 24  |  Page 25  |  Page 26  |  Page 27  |  Page 28  |  Page 29  |  Page 30  |  Page 31  |  Page 32  |  Page 33  |  Page 34  |  Page 35  |  Page 36  |  Page 37  |  Page 38  |  Page 39  |  Page 40  |  Page 41  |  Page 42  |  Page 43  |  Page 44  |  Page 45  |  Page 46  |  Page 47  |  Page 48  |  Page 49  |  Page 50  |  Page 51  |  Page 52  |  Page 53  |  Page 54  |  Page 55  |  Page 56