Distillery Wastewater Research Articles

Performance enhancement with powdered activated carbon (PAC) addition in a membrane bioreactor (MBR) treating distillery effluent

This work investigated the effect of powdered activated carbon (PAC) addition on the operation of a membrane bioreactor (MBR) treating sugarcane molasses based distillery wastewater (spentwash). The 8 L reactor was equipped with a submerged 30 μm nylon mesh filter with 0.05 m 2 filtration area. Detailed characterization of the commercial wood charcoal based PAC was performed before using it in the MBR. The MBR was operated over 200 days at organic loading rates (OLRs) varying from 4.2 to 6.9 kg m −3 d −1. PAC addition controlled the reactor foaming during start up and enhanced the critical flux by around 23%; it also prolonged the duration between filter cleaning. Operation at higher loading rates was possible and for a given OLR, the chemical oxygen demand (COD) removal was higher with PAC addition. However, biodegradation in the reactor was limited and the high molecular weight compounds were not affected by PAC supplementation. The functional groups on PAC appear to interact with the polysaccharide portion of the sludge, which may reduce its propensity to interact with the nylon mesh.

Investigation of soluble microbial products in a full-scale UASB reactor running at low organic loading rate

Investigation on a full-scale UASB treating industrial wastewater at a low organic loading rate (OLR) was conducted. Excellent treatment performance was achieved when treating the evaporator condensate of distillery wastewater at the OLR of less than 1 kg COD/m 3 d. Anaerobic effluent could be discharged without further treatment, which saved energy and running cost considerably. GC–MS analysis showed that the soluble microbial products (SMPs) were decreased to a low level at the low OLR. The main SMP in the anaerobic effluent were long chain carbohydrates and esters, accounting for 55–65% of the total organic matters. Anaerobic SMP was more complex than the aerobic ones. Soluble COD, protein and polysaccharide showed an obvious decrease at the sludge layer from 10 to 15 m despite the low MLSS/MLVSS content. Methanogens were found to be predominant in this layer, which indicated that the methanogens might be the main consumers of the SMP in anaerobic reactors. Economic comparison confirmed that the anaerobic treatment at low OLR could be a good option.

Nitrogen Removal from Biomethanated Spentwash Using Hydroponic Treatment Followed by Fungal Decolorization

A two-stage sequential treatment for anaerobically digested wastewater from a cane molasses-based distillery is proposed. In the first step, the wastewater was treated in a hydroponic based system using two plant species (Vetiveria zizanioides and Phragmites kharka) to reduce the high nitrogen (total Kjeldahl nitrogen) content of the effluent. Roots of these plants showed profuse growth on effluent. Nitrogen removal to the tune of 84% was achieved. When this hydroponically treated effluent was subjected for treatment by fungal isolates, 86.33% decolorization was obtained with Pleurotus florida Eger EM1303 followed by Aspergillus flavus TERIDB9 (74.67%), with significant reduction in chemical oxygen demand (COD) as well. The suggested method is thus important from the point of treating distillery wastewaters without the need of high dilutions and addition of supplementary carbon sources.

Decreased activity of a propionate degrading community in a UASB reactor fed with synthetic medium without molybdenum, tungsten and selenium

The composition and dynamics of the propionate degrading community in a propionate-fed upflow anaerobic sludge bed (UASB) reactor with sludge originating from an alcohol distillery wastewater treating UASB reactor was studied. The rather stable propionate degrading microbial community comprised relatives of propionate degrading Syntrophobacter spp., the hydrogen and formate consuming Methanospirillum hungatei and the acetate consuming Methanosaeta concilii. The effect of the long-term absence of molybdenum, tungsten and selenium from the feed to the UASB reactor on microbial community dynamics and activity was examined. Measurements for metal concentrations of the sludge and specific methanogenic activity tests with supplied molybdenum, tungsten and selenium were found to be unsuitable to detect the potential limitation of the microbial activity of the UASB sludge by these trace metals. During a long-term absence of molybdenum, tungsten and selenium from the feed to the UASB reactor, the methanogenic activity decreased while relatives of Smithella propionica and Pelotomaculum spp . competed with Syntrophobacter spp. for propionate consumption.

Utilization and biodegradation of starch stillage (distillery wastewater)

Stillage (distillery wastewater) is the main by-product originating in distilleries, and its volume is approximately 10 times that of ethanol produced. It is not surprising that the utilization of the stillage raises serious problems, and that many attempts have been made all over the world to solve them. In Poland most of the ethanol (about 90%) is produced from starch-based feedstocks, i.e. grains and potatoes. Starch feedstocks are widely used for spirit production also in other European countries, as well as outside Europe. The manuscript provides an overview of global fuel ethanol production and information on methods used for starch-based stillage biodegradation and utilization. The methods presented in this paper have been classified into two major groups. One of these includes the mode of utilizing starch stillage, the other one comprises methods, both aerobic and anaerobic, by which the stillage can be biodegraded.

Utilization and biodegradation of starch stillage (distillery wastewater)

Utilization and biodegradation of starch stillage (distillery wastewater)

Thermo- and mesophilic aerobic batch biodegradation of high-strength distillery wastewater (potato stillage) – Utilisation of main carbon sources

The aim of the study was to ascertain the extent to which temperature influences the utilisation of main carbon sources (reducing substances determined before and after hydrolysis, glycerol and organic acids) by a mixed culture of thermo- and mesophilic bacteria of the genus Bacillus in the course of aerobic batch biodegradation of potato stillage, a high-strength distillery effluent (COD = 51.88 g O 2/l). The experiments were performed at 20, 30, 35, 40, 45, 50, 55, 60 and 63 °C, at pH 7, in a 5 l working volume stirred-tank bioreactor (Biostat ®B, B. Braun Biotech International) with a stirrer speed of 550 rpm and aeration at 1.6 vvm. Particular consideration was given to the following issues: (1) the sequence in which the main carbon sources in the stillage were assimilated and (2) the extent of their assimilation achieved under these conditions.

Isolation and characterization of aerobic bacteria capable of the degradation of synthetic and natural melanoidins from distillery effluent

Melanoidins, complex biopolymer of amino-carbonyl compounds are the major coloring and polluting constituents of distillery wastewaters. In this study, three aerobic melanoidin-degrading bacteria (RNBS1, RNBS3 and RNBS4) were isolated from soil contaminated with distillery effluent and characterized as Bacillus licheniformis (RNBS1), Bacillus sp. (RNBS3) and Alcaligenes sp. (RNBS4) by biochemical tests and 16S rRNA gene sequence analysis. The degradation of synthetic and natural melanoidins was studied by using the axenic and mixed bacterial consortium. Results have revealed that the mixed consortium was more effective compared to axenic culture decolorizing 73.79 and 69.83% synthetic and natural melanoidins whereas axenic cultures RNBS1, RNBS3 and RNBS4 decolorized 65.88, 62.56 and 66.10% synthetic and 52.69, 48.92 and 59.64% natural melanoidins, respectively. The HPLC analysis of degraded samples has shown reduction in peak areas compared to controls, suggesting that decrease in color intensity might be largely attributed to the degradation of melanoidins by isolated bacteria.

Decolorization of anaerobically digested molasses spent wash by Pseudomonas putida

The distillery wastewater (spent wash) contains dark-brown colored recalcitrant organic compounds that are not amenable to conventional biological treatment. The characteristic recalcitrance to decolorization is due to the presence of brown melanoidin polymers. In the present study, feasibility of using Pseudomonas putida strain U for decolorization of spent wash was demonstrated. Batch cultures of P. putida decolourized spent wash by 24%, 2- fold higher decolorization was achieved following immobilization in calcium alginate beads. Glucose concentration was critical for decolourization and improved color removal efficiency was obtained by periodic replenishment of glucose. Decolourization was also observed with lactose or whey as alternative carbon sources. The results of our study suggest that P. putida could be used for biological decolorization of molasses spent washes and that supplementation with whey (a by-product from cheese industry) can offer economical viability to the process.

Pilot Testing Results of a Two-Stage Anaerobic System Treating Distillery Wastewater

Pilot Testing Results of a Two-Stage Anaerobic System Treating Distillery Wastewater

Treatment and phosphorus removal from high-concentration organic wastewater by the yeast Hansenula anomala J224 PAWA

A flocculent yeast, Hansenula anomala J224 PAWA, bred in this study, accumulated twice as much phosphorus as the wild type. Over a 30-d period, PAWA removed 70–80% of dissolved total phosphorus from sweet-potato and barley shochu wastewaters (alcoholic distillery wastewaters) while the wild type removed only 30%. Waste sludge was easily separated from effluent wastewater because PAWA cells made large flocks that rapidly settled. Component analysis suggested that PAWA sludge could be used as a protein source for feedstuff and as a phosphorus source for fertilizer. Under anaerobic conditions, denitrification was rapid, resulting in the removal of large amounts of nitrogen from barley shochu wastewater. These results suggest that small shochu manufacturers could benefit from using PAWA to remove phosphorus and organic compounds and then by using a combination of the upflow anaerobic sludge blanket and the downflow hanging sponge method (UASB-DHS method) for nitrification/denitrification.

Electrocoagulation Studies on Treatment of Biodigester Effluent using Aluminum Electrodes

In the present paper, electrocoagulation (EC) has been employed for the reduction of chemical oxygen demand (COD) reduction of a distillery wastewater (biodigester effluent) in a batch EC reactor using aluminum electrode. The individual and interactive effects of the four main independent parameters have been studied on the COD removal efficiency using a central composite experimental design. The parameters studied are current density (j): 44.65–223.25 A/m2; initial pH (pH 0): 2–8; inter-electrode distance (g): 1–3 cm; and electrolysis time (t): 30–150 min. Pareto analysis of variance of the results showed a high coefficient of determination value (R 2 = 0.9693) and satisfactory prediction for second-order regression model. Maximum COD removal efficiency of 52.23% was obtained with j = 120 A/m2, pH 0 = 6.0, g = 1 cm, and t = 150 min.

Electrochemical treatment of a distillery wastewater: Parametric and residue disposal study

Most of the distilleries in India and the world over employ bio-methanation of molasses spent wash in a bio-digester plant followed by two-stage aerobic treatment as a treatment strategy. The bio-digester effluent (BDE) generated after this treatment strategy still has a high chemical oxygen demand (COD) and dark brown color, and cannot be directly discharged into a water body. In the present study, electrocoagulation (EC) has been employed for the COD and color removal of a BDE in a batch EC reactor using stainless steel (SS) electrode. A central composite (CC) experimental design has been employed to evaluate the individual and interactive effects of four independent parameters namely initial pH (pH0: 3.5–9.5), current density (j: 39.06–195.31 A m−2), inter-electrode distance (g: 1–2 cm) and electrolysis time (t: 30–150 min) on the COD and color removal efficiency. Pareto analysis of variance (ANOVA) showed a high coefficient of determination value for COD (R2 = 0.9144) and color (R2 = 0.7650) between the experimental values and the predicted values by a second-order regression model. Maximum COD and color removal of 61.6 and 98.4%, respectively, were observed at optimum conditions. Detailed physico-chemical analysis of electrode and residues (scum and sludge) of the EC process has also been carried out. A strategy for the disposal of EC residues has been proposed.

Submerged membrane bioreactor using fly ash filters: trials with distillery wastewater

This work presents preliminary results for distillery wastewater treatment in a MBR equipped with filters prepared from waste fly ash. The system was fabricated locally and employed submerged membranes in the 2-8 microm pore-size range. Distillery wastewater, after anaerobic digestion, was used as the feed and the bioreactor was inoculated with sludge obtained from a local distillery unit. The MBR was operated for around 250 days. The wastewater quality was monitored in terms of COD (chemical oxygen demand), colour, phenol, and MLSS (mixed liquor suspended solids) concentration. An average COD and phenol removal of 36% and 60% respectively was obtained. The maximum suspended solids retention by the ash filter was as high as 98%. The results were encouraging and further trials are currently underway to improve the performance.

Robust Control of Volatile Fatty Acids in Anaerobic Digestion Processes

This paper is focused on the experimental implementation of a robust control scheme for the regulation of volatile fatty acids (VFA) in continuous anaerobic digestion processes. The robust scheme is made of an output feedback control, and an extended Luenberger observer is used to estimate the uncertain terms of the process (i.e., influent concentration and process kinetics). The control scheme is implemented in a pilot plant up-flow fixed-bed reactor that is treating industrial wine distillery wastewater. The performance of the robust scheme is tested over a period of 36 days, under different set-point values and several uncertain scenarios, including model mismatch, badly known parameters, and load disturbances. Experimental results show that the VFA concentration can be effectively regulated over a wide range of operating conditions. In addition, it is shown that the control scheme has a structure that improves its performance in the presence of noisy measurements and control input saturations.

Adsorption-;Desorption Process Using Wood-Based Activated Carbon for Recovery of Biosurfactant from Fermented Distillery Wastewater

Methods used for biosurfactant recovery include solvent extraction, precipitation, crystallization, centrifugation and foam fractionation. These methods cannot be used when distillery wastewater (DW) is used as the nutrient medium for biosurfactant production by Pseudomonas aeruginosa strain BS2, because recovery of biosurfactant by any of these methods imparts color to the biosurfactant. The biosurfactant has a nonaesthetic appearance with lowered surface active properties. These methods cannot be used for continuous recovery of biosurfactant during cultivation. Hence, a new downstream technique for biosurfactant recovery from fermented DW comprised of adsorption-desorption processes using wood-based activated carbon (WAC) was developed. This study involves batch experiments to standardize the factors affecting the rate of biosurfactant adsorption onto WAC. WAC was the most efficient adsorbent among various ones tested (i.e., silica gel, activated alumina and zeolite). The WAC (1% w v(-1)), equilibrium time (90 min), pH range of 5-10 and temperature of 40 degrees C were optimum to achieve 99.5% adsorption efficiency. Adsorption kinetics and intraparticle diffusion studies revealed the involvement of both boundary layer diffusion and intraparticle diffusion. The Langmuir adsorption isotherm of WAC indicated the formation of a monolayer coverage of the biosurfactant over a homogeneous carbon surface, while the Freundlich isotherm showed high adsorption at strong solute concentrations and low adsorption at dilute solute concentrations. WAC concentration of 4% w v(-1) facilitated complete removal of the biosurfactant from collapsed foam (contained 5-fold higher concentration of biosurfactant than was present in fermented DW). Biosurfactant adsorption was of chemisorption type. Acetone (polar solvent) was a specific viable eluant screened among various ones tested because it selectively facilitated maximum recovery, i.e., 89% biosurfactant from WAC. By acetone treatment, complete regeneration of WAC was feasible and WAC can be reused for biosurfactant recovery up to 3 cycles. The recovered biosurfactant showed improved surface-active property (i.e., much lower critical micelle concentration value of 0.013 verses 0.028 mg mL(-1) for biosurfactant recovered by classical methods). The reuse potential of WAC was assessed and results suggest that the carbon can be reused for three consecutive cycles for biosurfactant adsorption from fermented wastewater without any decrease in adsorption efficiency. Thus, this process forms a basis for continuous recovery of biosurfactant from fermented DW and concentrated foam. This process reduces the use of high cost solvent, avoids end product inhibition and minimizes product degradation.

ASSESSMENT OF A MICROALGAE POND FOR POST‐TREATMENT OF THE EFFLUENT FROM AN ANAEROBIC FIXED BED REACTOR TREATING DISTILLERY WASTEWATER

An evaluation of the performance of a laboratory‐scale microalgae pond treating effluent from an anaerobic fixed bed reactor digesting distillery wastewater was carried out. The microalgae pond operated with an effluent recycling (R) of 10:1 with respect to the influent and at surface organic loading rates of 418 kg COD ha−1 day−1 and 92 kg BOD5 ha−1 day−1. During the experiment total chemical oxygen demand (COD), biochemical oxygen demand (BOD5), total solids (TS), total suspended solids (TSS), volatile suspended solids (VSS), total nitrogen, ammonia, total phosphorus, orthophosphate, total chlorophyll (C T) and chlorophyll a (C a ) concentrations were monitored. Overall COD and BOD5 removal efficiencies of 98.2 % and 98.8 % were obtained. The global solids removal efficiencies were of 93.2%, 92.6 % and 97.6 % for TS, TSS and VSS, respectively. The removal efficiencies obtained for organic nitrogen and ammonia were 90.2% and 84.1%, respectively. Finally, the removals for total phosphorus and orthophosphate were 85.5% and 87.3%, respectively. It was demonstrated that microalgae grew in this waste by determination of the total chlorophyll and chlorophyll a in the effluent.

Tertiary treatment of distillery wastewater by nanofiltration

Tertiary treatment of aerobically treated distillery wastewater by nanofiltration was carried out in a spiral wound nanofiltration membrane module under different operating conditions. The results show that the percentage separation of organic and inorganic compounds was quite high, as reflected by the reduction of chemical oxygen demand (COD) and total dissolved solids (TDS) in the range of 96–99.5%, and 85–95% respectively. The color removal was in the range of 98–99.5%. The results of the effect of variation of the inlet concentration, feed circulation rate and pH conform to the mechanism of gel layer formation. Gel layer formation and Concentration polarization was found to play a major role in the treatment of distillery waste using nanofiltration (NF) membrane. It was observed that as concentration of feed solution increases the permeate flux was reduced. This change was higher compared to the separation of COD and TDS. The result indicates that the NF membrane showed very high performance efficiency for organic components (96–99.5%), as indicated by COD removal. In comparison, the separation of inorganic compounds was found to be in the range of 25–90% as estimated from relative separation of COD and TDS. The present study shows that nanofiltration is a promising technique for recovery of water from distillery waste, which could be used to achieve zero discharge status and solve a major environmental problem.

Treatment Methods for Wine-Related and Distillery Wastewaters: A Review

ABSTRACT A large and increasing volume of wastewater is produced globally by the winery and distillery industries. These wastewaters are generally acidic, high in chemical oxygen demand (COD) and color, and may contain phenolic compounds that can inhibit biological treatment systems. Treatment of distillery and phenolic compound–rich wastewaters by physicochemical, aerobic biological systems and hybrid treatment methods are discussed, as well as products derived from fungal treatment. White-rot fungi have been shown to exhibit unique biodegradation capabilities, primarily due to their production of extracellular and broad substrate range enzymes that are capable of mineralizing lignin, a recalcitrant biopolymer. One of these enzymes, laccase, catalyses the oxidation of various organic compounds with the subsequent reduction of molecular oxygen to water. Laccase synthesis, induction, and inhibition are discussed with the utilization of waste residues for laccase production and the enzyme's potential industrial applications. Distillery wastewaters offer a unique, presterilized, potential growth substrate for the production of lignolytic enzymes such as laccase. Compounds may be utilized for enzyme and biomass production resulting in remediation by the growing fungus.

Treatment of distillery effluent in a membrane bioreactor (MBR) equipped with mesh filter

This work investigates operation of a laboratory scale membrane bioreactor (MBR) in the continuous mode for distillery wastewater (spentwash) treatment using submerged 30 μm nylon mesh filters. The inoculum was municipal activated sludge, which was first acclimatized in a fed-batch reactor over a period of 102 days, before initiating continuous operation. Critical flux for this wastewater–filter combination was measured by flux stepping method, and the MBR was operated under subcritical flux conditions. Organic loading rates ranging from 3 to 5.71 kg m −3 day −1 were investigated and the performance was analyzed in terms of COD removal and biomass growth in the reactor. Up to 41% COD removal was obtained over 245 days of reactor operation. The molecular weight profiles of the untreated and treated effluent suggested that the degradation of low molecular weight compounds occurred in the reactor while the high molecular weight compounds comprising the colour imparting melanoidins remained unaffected. Up to 100% suspended solid retention (average 87%) was obtained and the system could be operated up to 2 weeks without significant flux drop.