Coffee wastewater

Coffee wastewater

The unpicked fruit of the coffee tree, known as the coffee cherry, must undergo a long process to make it ready for consumption. This process often entails the usage of massive amounts of water and the production of considerable amounts of both solid and liquid waste. To determine the type of waste stemming from coffee processing, it is important to know how the coffee cherries are processed. The conversion of the cherry to oro[1] or green bean (the dried coffee bean which is ready to be exported) can be achieved through three different processing techniques: dry, semi-washed, and fully washed.

Contents

Dry processing

The coffee cherries are dried immediately after they are harvested through sun drying, solar drying or artificial drying. In sun drying, the coffee cherries are placed on a clean floor and left to dry in the open air. In solar drying, the cherries are placed in a closed cabinet, which has ventilation holes to let moisture out. Artificial drying is used mostly during the wet season, when the low level of sunlight extends the time needed for solar drying and the cherries are prone to mold growth. After being dried, the cherries are hulled. In this process the dried outer layer of the cherry, known as the pericarp, is removed mechanically.

Semi-washed processing

In semi-washed processing, the cherries are de-pulped to remove the pericarp. After this, the removal of the slimy mucilage layer which covers the bean takes place. This is done mechanically by feeding the beans into a cylindrical device which conveys them upward. While the friction and pressure exerted on the beans by this process is enough to remove most of the mucilage, a small amount of it will still remain in the centre cut of the beans. This technique is used in Colombia and Mexico in order to reduce the water consumption from the long fermentation process and the extensive washing. While semi-washed processing requires less time than washed processing and is thus economically advantageous, the quality of the end product is regarded as inferior[citation needed].

In order to reduce the contamination generated by the wet process of coffee fruits, scientists at Cenicafé developed a technology that avoids using water when is not needed and uses the right water when is needed. The technology, called Becolsub after the Spanish initials of ecological wet coffee process with by-products handling, permits controlling more than 90% of the contamination generated by its antecessor. The quality of the coffee processed by this way is the same as the one for coffee processed by natural fermentation.

The Becolsub technology basically consists in pulping without water, mechanical demucilaging and mixing of the by-products (fruit outer-skin and mucilage) in a screw conveyor. The technology also includes a hydromechanical device to remove flouting fruits and light impurities, as well as heavy and hard objects, and a cylindrical screen to remove the fruits whose skin was not separated in the pulping machine. Scientists at Cenicafé discovered that a coffee fruit with mucilage (immature and dry fruits have no mucilage) has enough water inside for the skin and seeds to be separated in conventional pulping machines without water, that the liquid was only required as a conveying means and that pulping with water absence avoids 72% of the potential contamination.

Mucilage removal has been done throughout a fermenting process, which takes between 14 to 18 hours, until the mucilage is degraded and can be easily removed with water. Washing fermented mucilage requires, in the best case, 5,0 L/kg of DPC. Scientists at Cenicafé developed a machine to remove the mucilage covering the coffee seeds. This machine, called Deslim for initials of the Spanish words mechanical demucilager, washer and cleaner, removes more than 98% of the total mucilage (same as a well conducted fermentation) by exerting shear stresses and generating collisions among beans, using only 0,7 L/kg of DPC. The resulting highly concentrated mixture of water, mucilage and impurities is as viscous that can be added to the separated fruit skin in a screw conveyor, obtaining a great retention in the solid. The screw conveyor is as well mixer that the retention is greater than 60%, which means a 20% additional control of the potential contamination.

Until now, the two by-products have been widely used as worms’ substrate to produce natural fertilizers. However, the high concentration of the mucilage obtained from the demucilager leads to the opportunity of industrializing the by-product.

Fully washed processing

This process is mainly used when processing Coffea arabica[2] After de-pulping, the beans are collected in fermentation tanks where bacterial removal of the mucilage takes place over 12 to 36 hours.[3] The fermentation phase is important in the development of the flavour of the coffee, which is partially due to the microbiological processes that take place. The emergence of yeasts and moulds in acidic water can lead to off-flavours like sour coffee and onion-flavour. However, wet processing is believed to yield higher quality coffee than the other processes since small amounts of off-flavors give the coffee its particular taste and "body".[4]

When the fermentation is complete, the beans should be washed thoroughly to remove fermentation residues and any remaining mucilage. If they are not removed, these cause decolouring of the parchment and make the beans susceptible to yeasts. After washing, the beans are dried. When the drying process is not rapid enough earthy and musty taints, like Rio-flavor come up.[5]

Water usage

The amount of water used in processing depends strongly on the type of processing. Wet fully washed processing of the coffee cherries requires the most fresh water, dry processing the least. Sources indicate a wide range in water use. Recycling of water in the de-pulping process can drastically reduce the amount needed. With reuse and improved washing techniques, up to 1 to 6 m³ water per tonne of fresh coffee cherry is achievable; without reuse a consumption of up to 20m³/tonne is possible.

Water use in coffee processing
Country Process Water use m³/tonne cherry Source
India Semi-washed, wet processing 3 Murthy et al., 2004
Kenya Fully washed, reuse of water 4-6 Von Enden and Calvert 2002 [2]
Colombia Fully washed and environmental processing (BECOLSUB) 1-6 Von Enden and Calvert 2002 [2]
Papua New Guinea Fully washed, recycling use of water 4-8 Von Enden and Calvert 2002 [2]
Vietnam Semi wet and fully washed 4-15 Von Enden and Calvert 2002 [2]
Vietnam Traditional, fully washed 20 Von Enden and Calvert 2002 [1]
India Traditional, fully washed 14-17 Deepa et al. (2002)
Brazil Semi-washed, mechanical demucilage 4 De Matos et al. (2001)
Mexico Semi-washed, mechanical demucilage 3.4 Bello-Mendoza and Castillo-Rivera (1998)
Nicaragua Traditional, fully washed 16 Biomat (1992)
Nicaragua Fully washed, reuse of water 11 Grendelman (2006)

Characteristics

When processing coffee using the fully washed principle much wastewater is generated.

General

Water used in processing coffee leaves the coffee processing unit with high levels of pollution. The main component is organic matter, stemming from de-pulping and mucilage removal.[6] The majority of organic material in the wastewater is highly resistant and COD values, the amount oxygen required to stabilize organic matter by using a strong oxidant, make up 80% of the pollution load, with values as high as 50 g/l.[7] The BOD, the amount of oxygen required for the biological decomposition of organic matter under aerobic conditions at a standardized temperature and time of incubation,[8] coming from biodegradable organic material can reach values of 20 g/l.

With a (rough) screening and removal of the pulp COD and BOD values become considerably lower. Values in the range of 3 - 5 g/l for COD and 1.5 – 3 g/l for BOD5[9] were found.[10] Recorded values of 2.5 g/l for COD and 1.5 g/l for BOD5.[11]

A large part of the organic matter, pectins, precipitates as mucilated solids and could be taken out of the water.[12] When these solids are not removed and pH values rise and an increase in COD can be observed.

In order to optimize the anaerobic processing of the wastewater pH values should be between 6.5 and 7.5, instead of the generally present values of pH = 4, which is highly acidic. This is obtained by adding calcium hydroxide (CaOH2) to the wastewater. This resulted in a regained solubility of the pectins, raising COD from an average of 3.7 g/l to an average of 12.7 g/l.

The water is further characterised by the presence of flavonoid compounds, coming from the skin of the cherries. Flavonoid compounds result in dark colouration of the water at a pH = 7 or higher, but they do not add to BOD or COD levels of the wastewater, nor have major environmental impacts. Lower levels of transparency, however, can have a negative impact on photosynthetic processes and growth and nutrient transformations by (especially) rooted water plants. Many efforts in olive and wine processing industries, with relatively large funds for research, have been trying to find a solution for this problem. Calvert mentions research done into the removal of polyphenolics and flavonoid compounds by species of wood digesting fungi (Basidiomycetes) in a submerged solution with aeration using compressed air.[13] These complex processes seemed to be able to remove the colour compounds, but simplified, cheaper techniques using other types of fungi (i.e. Geotrichum, Penicillium, Aspergillus) only thrived in highly diluted wastewaters.

Coffee wastewater is not a constant flow of water with uniform loadings of contamination. The processing of coffee cherries is a batch process and regarding water flows, two processes can be determined: de-pulping and fermentation/washing.

De-pulping

The water used for de-pulping of the cherries is referred to as pulping water. It accounts for just over half of the water used in the process. According to Von Enden and Calvert, "pulping water consists of quickly fermenting sugars from both pulp and mucilage components. Pulp and mucilage consists to a large extent of proteins, sugars and the mucilage in particular of pectins, i.e. polysaccharide carbohydrates.[14] These sugars are fermenting using the enzymes from the bacteria on the cherries. Other components in pulping water are acids and toxic chemicals like polyphenolics (tannins) or alkaloids (caffeine).

Pulping water can be reused during the de-pulping of the harvest of one day. This results in an increase in organic matter and a decrease in pH. Research in Nicaragua showed COD averages rising from 5,400 mg/l up to 8,400 mg/l with most of the pulp removed.[15] The drop in pH can be attributed to the start of fermentation of the pulping water. This drop continues until fermentation is finished and pH levels of around 4 are reached. The nutrient content of the pulping water at the maximum COD load, which was considered to reflect maximum pollution, was determined during this research. Total nitrogen (TN) concentration in the samples ranged from 50 to 110 mg/l with an average over all samples of 90 mg/l. Total phosphorus (TP) concentration in the samples ranged from 8.9 to 15.2 mg/l with an average over all samples of 12.4 mg/l.

Washing

Washing of the fermented beans leads to wastewater containing mainly pectins from the mucilage, proteins and sugars. The fermentation of the sugars (disaccharide carbohydrates) into ethanol and CO2 leads to acid conditions in the washing water. The ethanol is converted in acetic acids after reaction with oxygen, lowering the pH to levels of around 4. The high acidity can negatively affect the treatment efficiency of treatment facilities treating the coffee wastewater like an anaerobic reactor or constructed wetlands and is considered to be detrimental for aquatic life when discharged directly into surface waters.

During the washing process the research in Nicaragua showed a clear decrease in contamination of the wastewater.[15] The COD values drop from an average of 7,200 mg/l to less than 50 mg/l. Despite the fact that wastewater with COD values below 200 mg/l is allowed to be discharged in the natural waterways in Nicaragua it is advisable to redirect all the wastewater to the treatment system. This is because COD levels cannot be determined onsite during the washing process and discharge of the wastewater into surface waters is based on visual inspection. When the water is "clear" it is considered to be clean enough but the COD values measured during the research showed that discharge generally was to soon, resulting in wastewater with higher levels of COD than permitted. Another positive effect of diverting the wastewater to a treatment system is the dilution of the wastewater which enables better treatment by anaerobic bacteria due to more favourable pH values and better post-treatment due to lower concentrations of ammonium.

TN concentration in the samples of wastewater stemming from washing ranged from 40 to 150 mg/l with an average over all samples of 110 mg/l. TP concentration in the samples ranged from 7.8 to 15.8 mg/l with an average over all samples of 10.7 mg/l.

Notes

  1. ^ Stemming from the Spanish word for gold, due to the color of the dried bean
  2. ^ http://www.herbs2000.com/herbs/herbs_coffee.htm
  3. ^ Von Enden, 2002
  4. ^ Calvert, 1998
  5. ^ Calvert, 1999
  6. ^ Von Enden and Calvert 2002
  7. ^ Treagust, 1999 in Von Enden and Calvert, 2002
  8. ^ Droste, 1997
  9. ^ BOD values after 5 days
  10. ^ De Matos et al., 2001
  11. ^ Bello-Mendoza et al., 1995 in Bello-Mendoza and Castillo-Rivera, 1998
  12. ^ Von Enden and Calvert, 2002
  13. ^ Calvert, 1997
  14. ^ Von Enden and Calvert, 2002, pp.4
  15. ^ a b Grendelman, 2006

References

  • Bello-Mendoza, R. and Castillo-Rivera, M.F. 1998. Start-up of an Anaerobic Hybrid UASB⁄Filter Reactor Treating Wastewater from a Coffee Processing Plant. In: Anaerobe Environmental Microbiology vol. 4, pp. 219 – 225.
  • BIOMAT 1992. Estudio y diseño de la Planta de Tratamiento de los Desechos del Café en la finca "San Luis". Alcaldía de Matagalpa and Oficina Biogás y Saneamiento Ambiental. Matagalpa, Nicaragua.
  • Calvert, K.C. 1997. The treatment of Coffee Wastewater. The Biogas Option. A Review and Preliminary Report of Ongoing Research. Coffee Research Report no. 50. Coffee Industry Corporation ltd. Kainantu, Papua New Guinea.
  • Calvert, K.C. 1998. The Microbiology of Coffee Processing, part 1. PNGCRI Coffee Research Newsletter
  • Calvert, K.C. 1999 The Microbiology of Coffee Processing, part 3. PNGCRI Coffee Research Newsletter
  • Deepa, G.B., Chanakya, H.N., de Alwis, A.A.P., Manjunath, G.R. and Devi, V. 2002. Overcoming Pollution of Lakes and Water Bodies Due to Coffee Pulping Activities With Appropriate Technology Solutions. In: Proceedings "Symposium on Conservation, Restoration and Management of Aquatic Ecosystems", paper 4. Centre for Ecological Sciences, Indian Institute of Science (IIS) and the Karnataka Environment Research Foundation [KERF], Bangalore and Commonwealth of Learning, Canada.
  • De Matos, T, A., Lo Monaco, P.A., Pinto, A.B., Fia, R. and Fukunaga, D.C. 2001. Pollutant Potential of Wastewater of the Coffee Fruits Processing. Federal University of Viçosa, Department of Agricultural Engineering, Viçosa-MG, Brazil.
  • Droste, R. L. 1997. Theory and Practice of Water and Wastewater Treatment. John Wiley & Sons, Inc. Hoboken, Canada.
  • Grendelman, E.R. 2006. Tratar las Aguas Mieles. Wageningen University, sub-departments: Irrigation & Water Engineering Group and Environmental Technology. Unpublished internship paper. Wageningen University, Netherlands.
  • Murthy, K.V.N., D’Sa, A. and Kapur, G. 2004. An effluent treatment-cum-electricity generation option at coffee estates: is it financially feasible? Draft version. International Energy Initiative, Bangalore.
  • Von Enden, J.C. 2002. Best practices at wet processing pay financial benefits to farmers and processors. GTZ-PPP Project "Improvement of coffee quality and sustainability of coffee production in Vietnam".
  • Von Enden, J.C. and Calvert, K.C. 2002. Review of Coffee Waste Water Characteristics and Approaches to Treatment.
  • Von Enden, J.C. and Calvert, K.C. 2002. Limit Environmental Damage By Basic Knowledge of Coffee Waste Waters. GTZ-PPP Project "Improvement of coffee quality and sustainability of coffee production in Vietnam".

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