Water Treatment Reverse Osmosis Facility to Produce Fully Demineralized Water for Slovak Refinery
Turning Danube water into pure process water: The reverse osmosis facility at the Slovnaft oil refinery in Slovakia utilises 630 Lewabrane RO B400 HR membrane elements for water treatment. Read how this plant performs.
Cologne/Germany – The raw water for the plant is sourced from the Danube. It contains between 320 and 400 mg/l dissolved solids with seasonally fluctuating organic fractions, and it displays an electric conductivity of up to 580 μS/cm. During treatment, it first undergoes chemical pretreatment (coagulation, flocculation) and ultra-filtration, before continuing on to the reverse osmosis (RO) system, which is divided into five separate lines, each equipped with 126 membrane elements. The three-stage demineralization facility can turn out up to 135 cubic meters of permeate per hour and line, and the maximum conductivity falls far below the target value stipulated by the operator of 15 μS/cm. The system has a permeate yield of up to 85 percent. In the subsequent cleaning stage, also mixed bed ion exchange resins from Lanxess' Lewatit line are used to remove any remaining ionic compounds. The facility produces fully demineralized water that is available as boiler feed water for water-steam circuits and other technical purposes.
Calculations with the LewaPlus design software, developed specifically for Lewabrane and Lewatit products, already showed in the planning phase that permeate conductivities of less than 10 μS/cm could be expected. Accordingly, this meant less of a burden on the mixed bed ion exchange resins. “We met all these expectations, and that makes us very optimistic about easily fulfilling all the performance guarantees we granted to the customer,” confirmed Alexander Scheffler, Director Membrane Business in the Lanxess Liquid Purification Technologies business unit.
Extended Dwell Times
Compared to the other membrane elements used in previous years, the new system displays significantly longer dwell times. “We used to have to go through the cleaning regimen every four to six weeks, but the magnitude of pressure decline and the conductivity did not increase with the elements from LANXESS until after four months. After cleaning, the elements were back up to the same performance level as when they went into operation,” said Peter Šrámek, head of Slovnaft refinery.
Overall, the longer intervals between cleanings reduced the consumption of cleaning chemicals and increased the availability of the RO lines. Similarly, the low salt content of the permeate extends the regeneration intervals of the mixed bed ion exchange system, further cutting costs.