V. Mavrov et al., Spent process water desalination and organic removal by membranes for water reuse in the food industry, DESALINATN, 138(1-3), 2001, pp. 65-74
In this study, it could be shown that, drinking water consumption in the fo
od industry could be drastically reduced by water reuse. Boiler make-up wat
er or warm cleaning water could be economically produced from low contamina
ted process water (electrical conductivity below 3000 muS/cm and COD below
700mgO(2)/l) by membrane desalination and organic removal. Due to varying c
oncentrations in impurities in the different types of spent process water (
milk processing and meat processing) experiments were performed with differ
ent pre-treatment steps and main membrane treatment stage. The post-treatme
nt stage guarantees that the requirements for residual inorganic and organi
c concentration in the water are maintained and keeps microorganism concent
ration below limit values. A demonstration plant, consisting of the followi
ng stages, was set up: (a) pretreatment: belt filtration, cartridge filtrat
ion (two stages) and UV predisinfection; (b) main treatment: first stage, n
anofiltration with sprial wound modules; (c) post-treatment: second stage,
nanofiltration with sprial wound modules and (d) UV disinfection. It was sh
own that it was possible to obtain, from the spent process water streams, w
ater for reuse e.g. boiler make-up water (electrical conductivity of < 40 m
uS/cm at 25 degreesC; Ca2+<0.4mg/l; COD < 10mg O-2/l etc.) or warm cleaning
water (el. conductivity below 200 muS/cm, Ca2+< 1mg/l, TOC < 4mg/l etc.).