국내에서는 생활수준 향상으로 가축 사육두수가 증가하여 고농도의 질소와 인을 함유한 가축분뇨의 발생량도 증가하고 있으나, 대부분 전통적인 생물학적 방법으로 처리하고 있어 부영양화의 원인으로 지목되고 있다. 현재에는 가축분뇨의 재활용을 통해 이러한 문제를 해결하고자 혐기 소화 후 퇴?액비로 보급하고 있으나, 오히려 환경오염이 가중되고 있는 실정이다. 최근 인광석의 고갈에 대한 우려와 자원의 순환적 이용이 부각되면서 가축분뇨내 질소와 인은 처리의 대상에서 회수되어야 하는 자원으로 인식이 전환되어 스트루바이트 결정화 기술이 주목받고 있다. 스트루바이트 결정화 기술은 고농도의 질소와 인을 회수할 수 있는 최적의 기술임에도 불구하고 아직까지 경제성이 낮다는 이유로 폭넓게 적용되지 못하고 있는 실정이다. 이에 본 연구에서는 경제성을 확보하기 위하여 스트루바이트 결정화 기술의 최적 운전조건을 도출한 후 전처리를 통한 인의 가용화 가능성, 저렴한 마그네슘 공급원으로서 해수담수화 공정에서 발생하는 농축수의 사용 가능성, 결정핵(seed material) 투입에 따른 회수효율 향상 및 입자 크기 증대 가능성, 작물실험을 통한 비료로써의 상용화 가능성을 평가하고 운전조건별 경제성 분석을 통해 상용화를 위한 최적 운영방안을 수립하였다. 실험결과, 스트루바이트 결정화를 위한 마그네슘 : 암모니아 : 인산염 인의 최적 몰 농도 비율은 pH 9.0에서 1.2 : 1.0 : 1.1로 평가되었고 pH 8.0이상에서의 스트루바이트 입자 크기는 큰 차이를 나타내지는 않았다. Visual MINTEQ 3.0을 이용하여 pH에 따른 침전물의 성분을 예측한 결과, 순수한 스트루바이트를 생산하기 위한 최적 pH 범위는 7.5에서 10.5로 예측되었다. 따라서 경제성을 고려할 때, 최적 pH 범위는 8.0에서 9.0로 판단되었다. 가축분뇨내 인산염 인의 농도를 증가시키기 위하여 초음파 전처리를 실시한 결과, 1,000kJ/L에서 인산염 인의 농도가 77.4% 증가하였고 pH 8.0과 9.0에서 인산염 인의 비율이 총인의 약 84%를 나타내어 초음파 전처리를 통해 인의 가용화율을 향상시킬 수 있는 것으로 판단되었다. 질소와 인의 제거효율 향상 및 스트루바이트 입자의 크기를 증대시키기 위한 결정핵(seed material) 투입 실험결과, 제올라이트(zeolite) 결정핵의 투입은 질소 제거효율을 크게 향상시켰으며, 입자 크기를 효과적으로 증가시켰다. 그러나, 구리와 아연같은 중금속이 소량 발견되었으나, 법적 기준을 만족하여 사용이 가능할 것으로 판단되었다 경제적인 관점에서 마그네슘 원으로 해수 담수화 역삼투 공정에서 발생하는 농축수의 이용 가능성을 평가한 결과, XRD 분석을 통해 합성 스트루바이트의 피크와 동일한 것을 확인하였고 염화마그네슘(MgCl2) 비해 질소 제거효율은 다소 낮았으나, 인의 회수효율은 향상되어 경제적 측면에서 활용이 가능할 것으로 판단되었다. 실제 폐수에서 생산된 스트루바이트의 영양염류 용출특성을 분석한 결과, 인의 경우, 최대 63일동안 용출되어 완효성 비료로 판단되었다. 실제 폐수에서 회수된 스트루바이트를 이용해 고추, 배추, 오이를 재배한 결과, 시비 기준량을 준수한 경우에는 모든 작물들의 성장에 매우 효과적이었으나, 고추를 제외한 배추와 오이에서는 과잉으로 시비할 경우, 비효가 발생하는 것으로 평가되었다. 운전조건에 따른 경제성을 분석한 결과, 결정핵으로 제올라이트를 유입폐수량의 2.5%를 투입하고 MgO를 마그네슘원으로 이용하며, 유입수내 인의 몰 농도를 기준으로 스트루바이트를 생산해 토양개량제로 판매한다면 경제성이 확보될 수 있는 것으로 평가되었다.
Struvite precipitation has been proven to be an effective method in removing and recovering ammonia nitrogen (N) and phosphate phosphorus (P) from wastewater. This study investigated the effect of magnesium, ammonium and phosphate molar rations to improve struvite crystallization using the effluent of anaerobically digested livestock wastewater and the effect of pH on ammonia N and phosphate P removal and recovery. The magnesium : ammonium : phosphate ratio of 1.2 : 1.0 : 1.0 was found to be optimal. From the analysis, the optimum pH was between 8.0 and 9.0 for maximum phosphate P release and from 8.0 to 10.0 for maximal ammonia N and phosphate P removal from real wastewater. As a result of analyzing the effect of pH on the size distribution of struvite crystal, the particle size distribution value (D90) at 90% the cumulative distribution was increased up to a maximum 177% at pH 9.0 condition. Precipitates analysis showed that phosphorus and magnesium in the collected precipitate had almost same values as theoretical values, but the ammonia content was less than the theoretical value. The result of modelling by Visual MINTEQ 3.0 was predicted to struvite formation as the dominant solid phase in the pH from 7 to 11 and the pure struvite crystals would be formed between pH 7.5 and 10.5. Generally, the livestock wastewater contains less phosphate compared to nitrogen. So it is necessary to add a source of phosphate to optimize the struvite crystallization process. In order to prevent the additional chemical supply has to solubilize of the particulate phosphate. The effect of pre-treatments was also studied for changes in phosphate P release from the effluent of livestock wastewater anaerobic digestion. Also, in view of the high cost of supplementing magnesium, the concentrated water from a seawater desalination plant was investigated as a potential source of magnesium. Finally, the effect of seed material addition on struvite crystallization was investigated. Microwave and ultrasonic pre-treatments were also investigated for phosphate P release from solid phases for increased recovery of phosphorus from wastewater. Ultrasound pre-treatment had the highest phosphate P release of 77.4% at 1,000kJ/L of energy dose but the microwave pre-treatment had no effect under the tested conditions. The results of all the experiments showed that struvite formation was successfully performed in the effluent. Removal efficiencies of up to 94.5% for phosphate and 12.7% for ammonium were achieved under normal operating conditions. Seed materials were successfully used as nucleation sites to enhance the purity of the struvite and the crystal size. The removal efficiencies of phosphate and ammonia could be improved up to 97% and 84%, respectively, by adding phosphate and seed materials. Also, Adding seed materials could increase the particle size of struvite crystals and improve the recovery efficiency of phosphorus. Struvite has similar properties to the traditional ammonium-phosphate fertilizer, in which without burning the roots due to its slow releasing characteristics. Struvite is an effective fertilizer as its nutrient releasing rate is very slow. Rate of ammonia and phosphate release in soil also depends on the size of the crystals. In this study the nutrients leaching pattern compared by three different types of struvite crystals and liquid fertilizer by using soil column. Struvite crystals and liquid fertilizer were also tested by growing potted vegetables. X-Ray Fluorescence Spectrometer analysis was conducted to investigate the potential use of struvite as a fertilizer. Contents of heavy metals such as copper and zinc were very low level. As a result of the soil column test, the nutrient leaching of liquid fertilizer and recovered zeolite seed struvite from livestock wastewater were 11 and 63 days, respectively. Recovered struvite as fertilizers was very effective to cultivation of all applied vegetables. Recovered struvite did not show inhibition to chili pepper cultivation but inhibition was observed to chinese cabbage and cucumber at over dose of struvite fertilizer. For the successful operation of the struvite crystallization process, an economically sustainable operation plan must be developed. In this study, we tried to evaluate the economic aspects of various scenarios to ensure process stability. The total capital investment cost was estimated by designing full scale through mass balance analysis. Operating costs were analyzed according to five scenarios. Scenarios 1, 2 and 3 compare the economics of MgCl2, concentrated seawater and MgO as Mg sources for phosphorus removal. In scenario 4, the economics of zeolite input were evaluated based on the results of scenarios 1, 2 and 3. In scenario 5, when the nitrogen removal is aimed, the economics of the optimal Mg source and zeolite input are evaluated. The configuration of major facilities at full scale is as follows: a reactor to induce struvite crystallization reaction, a filter press to separate struvite and water, a drying bed for natural drying, and a granulator to increase the particle size of the struvite and a packing system for selling the product. In the case of the Mg source for phosphorus removal, the economic efficiency was improved when using MgO in scenario 3, but the economic efficiency was inefficient because the struvite production was 262kg/d. The addition of zeolite not only greatly increased struvite production, but also enabled it to be sold as a soil conditioner, leading to a significant improvement in profitability. As a result, in scenario 4, the struvite selling cost to the operating cost was 102%, which was evaluated as having a sufficient economic efficiency. When all the nitrogen is removed, the NaOH input is greatly increased by the addition of H3PO4. As a result, operating costs are greatly increased and economic efficiency is greatly reduced. In the case of removing all the nitrogen, it is considered that a phosphorus source which is cheap enough to minimize the pH increase should be found.
Chapter 1. Introduction 11.1 Overview 11.2 Objectives 41.3 Structure of the dissertation 5Chapter 2. Background and literature review 82.1 Physical and chemical properties of struvite 82.2 The mechanisms of struvite crystallization 112.2.1 Nucleation and nucleation rate 132.2.2 Induction time 142.2.3 Crystal growth 172.3 Factors affecting struvite crystallization 182.3.1 Molar ratio 182.3.2 pH 212.3.3 Aeration rate 232.3.4 Supersaturation ratio 242.3.5 Temperature 252.3.6 Mixing energy or turbulence 262.3.7 Presence of foreign ions 262.4 Fertilizer quality of struvite 272.4.1 Nutrient leaching rate 272.4.2 Soil type and struvite 29Chapter 3. Effects of pH and molar ratios on phosphorus recovery through struvite crystallization 46Abstract 463.1 Introduction 473.2 Materials and methods 493.2.1 Materials 493.2.2 Crystallizations experiments 503.2.3 Struvite crystal size distribution experiments 503.2.4 Crystal growth analysis and MINTEQ model 533.3 Results and discussion 533.3.1 Effect of magnesium, ammonium, and phosphate molar ratios onstruvite formation 533.3.2 Effect of pH on ammonia N and phosphate P removal 623.3.3 Effect of pH on struvite crystal size distribution 663.3.4 Composition of recovered struvite 713.4 Conclusion 73Chapter 4. Application of the pre-treatment, seed materials and the concentrate water from seawater desalination to improve the struvite crystallization 79Abstract 794.1 Introduction 804.2 Materials and methods 834.2.1 Pre-treatment for phosphate P release 834.2.2 Concentration water 844.2.3 Anaerobically digested effluent of livestock wastewater 854.2.4 Reactor operation 854.2.5 Analysis 874.3 Results and discussion 884.3.1 Pre-treatments affecting phosphate P release 884.3.2 Formation of struvite by using concentrated seawater 924.3.3 Effect of phosphate injection 924.3.4 Effect of seed materials 924.4 Conclusion 96Chapter 5. Characteristics of vegetables crop cultivation and nutrient leaching as a slow-release fertilizer 101Abstract 1015.1 Introduction 1025.2 Materials and methods 1045.2.1 Anaerobically digested effluent of livestock wastewater 1045.2.2 Struvite crystallization 1045.2.3 Soil column test for nutrients leaching 1065.2.4 Vegetables growth experiment 1075.2.5 Analytical methods 1085.3 Results and discussion 1115.3.1 Crystallization of struvite 1115.3.2 Nutrients leaching from soil column 1145.3.3 Cultivation of vegetables using wastewater struvite 1165.4 Conclusion 124Chapter 6. An economic evaluation of phosphorus recovery as struvite from anaerobically digested effluent 127Abstract 1276.1 Introduction 1286.2 Economic assessment 1306.2.1 Economic evaluation conditions and selection of scenarios 1306.2.2 Total capital investment cost 1326.2.3 Operating cost 1356.3 Results and discussion 1376.4 Conclusion 139Chapter 7. Conclusions and future works 1427.1 Summary and conclusions 1427.2 Future works 144Abstract (in Korean) 145