Industrial resolution

28 January 2013


Simon Judd

Simon Judd

Author Bio

Simon Judd, author of The MBR Book, Watermaths, and Industrial MBRs, offers observations on membrane technology. Contact Simon at simon@juddwater.com.

Awhile back I posted a discussion on LinkedIn asking for wise and worldly comments on what readers regarded as being the most challenging industrial effluent for treatment using an MBR. It was largely ignored (a common enough, and entirely justifiable, happenstance). However, I’ve recently has reason to revisit this.

It is pretty well known that, whilst perhaps not the worst, pharmaceutical wastewaters are not exactly a walk in the park when it comes to reducing the COD content (a bit of a headache, as my other half has wryly observed). Apparently, many such MBR plants – and examples exist of both immersed and sidestream – operate with pure oxygen, which suggests oxygen mass transfer limitations when using conventional fine bubble diffusion. Presumably, simply extending the residence time is not an option since not all industrial sites are replete with space. Indeed, for many it is the spatial limitations that promote the MBR option in the first place. Of course, not everyone is enamoured with the idea of storing liquid oxygen on an industrial site, although it at least gives our fine H&S colleagues something to bleat about, but the alternative is pressurising the bioreactor. This certainly serves to retain the oxygen, but also retains sour gases – CO2 in particular – which then depresses the pH to the point where nitrification may start to drop off and the reactor to resemble an Ibiza foam party.

At this point, it would be great to be able to write: “the simple solution is ..”. But, of course, real life is never that simple. Treating large volumes of high-strength industrial effluent in a confined space is always going to be (a) challenging, and (b) expensive. Given enough space, and the will to reduce both OPEX and waste, it could be argued that high-strength solutions should only ever be treated anaerobically. It is sometimes asked, by the more alert of the students at Cranfield, where the crossover is between aerobic and anaerobic treatment with respect to the COD concentration. As is so often the case, one can confidently and categorically answer: “It depends”. Interestingly, when Nacho Martin applied himself to this very question with reference to a municipal feed and based on MBR technology, he came up with the easily-remembered answer “about 1000 mg/L”. However, the variables, permutations and general uncertainties probably add a fair margin of error to this figure.

So, pure oxygen, pressurisation, anaerobic: a choice veritably heaving with invidiousness. It perhaps is one of the many reasons that academic MBR research leans so heavily towards municipal wastewater treatment. All this industry is too much like hard work.

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Banner image: full treatment plant for pharmaceutical wastewater in Taizhou, Linhai Park, Zhejiang Province, China, including Shanghai MEGAVISION  flat sheet UF membrane modules in two MBR units. Image courtesy of VALORSABIO, Lda.

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