Nutrient Recovery from Human Urine by Struvite Crystallization with Ammonia Adsorption on Zeolite and Wollastonite Bo-Bertil Lind A,*,Zso®A Ban B, Stefan BydEn B

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Nutrient Recovery from Human Urine by Struvite Crystallization with Ammonia Adsorption on Zeolite and Wollastonite Bo-Bertil Lind A,*,Zso®A Ban B, Stefan BydEn B Bioresource Technology 73 (2000) 169±174 Nutrient recovery from human urine by struvite crystallization with ammonia adsorption on zeolite and wollastonite Bo-Bertil Lind a,*,Zso®a Ban b, Stefan Byden b a Earth Sciences Centre, Goteborg University, Box 460, SE-405 30 Goteborg, Sweden b Division of Environmental Sciences, Goteborg University, Box 464, SE-405 30 Goteborg, Sweden Received 26 June 1999; received in revised form 26 September 1999; accepted 9 October 1999 Abstract Urine-separation toilets are a possible route for achieving maximum recovery and recycling of urine nutrients not contaminated by hazardous compounds such as heavy metals. However, the direct use of human urine as agricultural fertiliser is problematic and controversial with regard to hygiene, storage, transport and spreading. In this paper, simple methods for capturing the nutrients in urine by transformation into solid mineral form are presented. On the addition of small amounts of MgO to synthetic or natural human urine most of the phosphorous and signi®cant amounts of the potassium and nitrogen were precipitated, with crystalline struvite [Mg K; NH4 PO4Á6H2O] as a major component together with montgomeryite, newberyite, brucite and epsonite. Ni- trogen recovery could be improved by adsorption. Clinoptilolite, wollastonite and a natural zeolite all showed excellent adsorbent properties in contact with ammoniacal solutions. In combination with struvite crystallisation 65±80% of the nitrogen was recovered as crystalline or adsorbed ammonium. Ó 2000 Elsevier Science Ltd. All rights reserved. Keywords: Struvite; Clinoptilolite; Wollastonite; Ion exchange; Adsorption; Zeolite; Ammonia; Nutrient recovery 1. Introduction Karrman, 1997). However, life cycle assessment-studies of urine-separation systems also show that the storage, About 94% of the nitrogen, phosphorus and potas- transport and spreading of large amounts of urine, sium in toilet wastewater emanates from the urine, to- presents serious obstacles to system eciency (Jenssen gether with abundant micronutrients in balanced and Etner, 1996; Larsen and Gujer, 1996; Hoglund et concentrations (Wolgast, 1993). New ideas for eco-cy- al., 1998). Large volumes of urine are needed to fertilise cling of nutrients from waste water have been proposed typical farmland, leading to high transport costs. An- based on urine separation, in order to maximise the other problem of urine-separation systems is the loss of recovery and recycling of nutrients and to reduce eu- nitrogen by ammonia evaporation during storage and trophication in freshwater and coastal ecosystems. Ur- spreading (Hanaeus et al., 1996). Furthermore in many ine separating toilets have been developed and installed countries the spreading of liquid urine fertiliser is re- in several eco-villages around the world, including dif- stricted to certain periods of the year. ferent parts of Sweden. We believe that many of the problems connected with Life cycle comparisons of conventional and urine- urine separation could be met by transforming the nu- separation wastewater systems show that urine-separa- trients in the urine into solid minerals. Handling and tion systems have many advantages related to emissions storage could be substantially improved, the volume and nutrient recovery (Bengtsson et al., 1997). Exergy would be dramatically reduced compared with liquid (energy eciency) analyses of sewage treatment systems urine, loss of nitrogen into the atmosphere would be show that phosphorous and nitrogen-recycling eciency eliminated, a high level of hygiene could be maintained is highest if urine separation is used (Hellstrom and and spreading on arable land could be much more ¯exible in terms of time and dosage. * This paper presents the results of a pilot study of Corresponding author. Present address: Swedish Geotechnical nutrient recovery from human urine by struvite crys- Institute, Nya Tingstadsgatan 1, SE-422 44 Hisings Backa, Sweden. Tel.: +46-31-65-65-36; fax: +46-31-65-65-77. tallisation with further ammonia recovery using zeolites E-mail address: [email protected] (B.-B. Lind). or wollastonite. 0960-8524/00/$ - see front matter Ó 2000 Elsevier Science Ltd. All rights reserved. PII: S 0 9 6 0 - 8 5 2 4 ( 9 9 ) 0 0 157-1 170 B.-B. Lind et al. / Bioresource Technology 73 (2000) 169±174 2. Crystallisation and adsorption of nutrients from human sorption a NH4Cl solution was prepared with concen- urine trations similar to synthetic human urine without and with urea hydrolysis; 0.02 and 1 M, respectively. All Human urine is a complex aqueous solution con- solutions were stored at room temperature. taining sodium chloride (NaCl) and urea (CO(NH2)2)as The chemical compositions of the adsorbents are dominant compounds but also potassium (K), calcium presented in Table 1. The adsorbent minerals were not (Ca), sulfate (SO4) and phosphate (PO4) in low con- pretreated or activated in any way, just crushed and centrations. One of the most important compounds that sieved to speci®c grain size fractions. Deionised water can precipitate from human urine is the mineral struvite, was used for all dilution, washing and preparation. Mg NH4 PO4Á6H2O, formed by reaction of magne- Ammonium measurements were made using a Metrohm sium with ammonical phosphate solutions and usually calibrated ammonia-selective electrode, complemented found in deposits of guano or animal dung. Human with Kjeldahl nitrogen analysis. urine contains an excess of ammonium relative to phosphate, but is de®cient in magnesium. The normal 3.1. Struvite crystallization pH of human urine is between 5.6 and 6.8 and most of 2 the phosphate is present as H2PO4 or HPO4 . With the Laboratory experiments were based on dephosphati- addition of MgO the pH increases, shifting the phos- sation procedures, using 98% pure MgO. First, dierent 3 phate equilibrium toward PO4 and magnesium is pro- amounts of MgO were added to 20 ml samples of syn- vided for struvite crystallisation. Struvite precipitation thetic urine in 50 ml test tubes. The pH was measured may be a method to remove phosphate but if it happens continuously and MgO additions were adjusted to give spontaneously it can also cause operational problems in pH values ranging from approximately 6.5±10. The tests sewage systems. Struvite formation from mixed waste were made at room temperature (20°C). Additional ex- water has been studied by e.g., Liberti et al. (1986), Sen periments were done using fresh, human urine. The and Randall (1988), Mohajit et al. (1989), Maqeda et al. MgO added was more than sucient to supply the (1994), Momberg and Oellermann (1992), Perez Rodrõguez et al. (1992), Wrigley et al. (1992a,b) and Battistoni et al. (1997). The potential of struvite crys- Table 1 Chemical composition of adsorbent minerals tallisation for direct nutrient recovery from human urine has to our knowledge not been investigated before. Component % Clinoptilolite, Mad, Hungary In fresh urine ammonium NH4 is formed from the decomposition of urea (Hanaeus et al., 1996). This oers SiO2 62.43 Al O 10.95 possibilities for nitrogen recovery by ammonium uptake 2 3 MoO3 0.11 to speci®c adsorbents such as zeolite or wollastonite FeO 0.12 minerals. The ion exchange properties of natural zeolites MgO 0.79 CaO 3.17 especially clinoptilolite R Na; K6 Al6Si30O72Á20H2O are well documented (c.f. Breck, 1974; Jorgensen et al., Na2O 0.13 K2O 2.74 1976; Gottardi and Galli, 1985; Tomazovic et al., 1996). Totala 80.44 The use of wollastonite for removing heavy metals from aqueous solutions was investigated by e.g. Sharma et al. Wollastonite, Hulta East, Sweden SiO 63.16 (1990) and Lifvergren (1997). The use of zeolite or wo- 2 Al2O3 4.20 llastonite as adsorbents for ammonium recovery from Fe2O3 1.12 human urine has not been investigated before. MnO 0.26 CaO 3.12 Na2O 0.12 K O 2.62 3. Methods 2 P2O5 0.01 Totala 74.61 Synthetic human urine containing 11 solutes, in Zeolite-mix, Mad, Hungary concentrations equivalent to the daily average urine of SiO2 68.48 normal healthy men was prepared according to con- Al2O3 12.48 ventional urological methods (Grith et al., 1976a,b) FeO 0.05 for use in the experiments. Synthetic urine is free of CaO 3.46 pyrophosphates, organic macromolecules (matrix) and Na2O 0.02 K2O 3.27 unspeci®ed substances that could enhance or inhibit the MgO 1.12 nutrient recovery. In addition struvite precipitation was TiO2 0.08 also tested using fresh human urine from ®ve healthy, Totala 88.90 a young to middle-aged people. For studies of NH4 ad- Does not include water. B.-B. Lind et al. / Bioresource Technology 73 (2000) 169±174 171 stoichiometric ratio, Mg:P; 1.71:2.21, for urine containing 0.5 g P/l and to raise the pH to about 10. The precipitates were ®ltered, dried at 40°C and weighed. Electron microscope, energy dispersive X-ray analysis (EDS) and X-ray diraction (XRD) analyses were made of the precipitates. The combination of struvite precipitation with fur- ther ammonium uptake by clinoptilolite and wollas- tonite was also investigated. 3.2. Batch adsorption experiments At constant room temperature (20°C) 25 ml solution, synthetic human urine or NH4Cl solution, was used together with 0.5 g of adsorbent mineral for each ex- periment. Stirring at 200±250 rpm established contact between adsorbent and solution. pH and ammonium Fig. 1. SEM photo of struvite crystal (´ 1000). were measured during each experiment, after which the liquid was separated from the adsorbent with a vacuum ®lter. This process was repeated with the following of 1.71:2.21 magnesium to phosphorous. It is also clear variables: that potassium as well as calcium was included in the 1. three dierent mineral adsorbents: clinoptilolite, wo- precipitate. Natural struvite does not have a pure end- llastonite and mixed zeolite, member composition as shown in Table 2.
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