兰州新区节水型生态小区规划和中水回用技术研究
[Abstract]:Lanzhou New Area is the fifth national-level new area approved by the State Council. Because Lanzhou New Area is located in the northwest of China and belongs to the water-deficient area, it is a feasible way to build a water-saving new area. As the main part of the city, residential district has certain social and economic benefits for the construction of Lanzhou New Area. The construction of water-saving ecological community in Northwest China has a certain demonstration and leading role, which is of practical significance to alleviate the pressure of urban water use.
Starting from the basic situation and existing problems of Lanzhou New Area, combining with the planning experience of water-saving ecological district at home and abroad, this paper provides a reasonable planning scheme for the construction of water-saving ecological district in Lanzhou New Area, and plans the district in accordance with the principles of ecology, systematization, economy and sustainability. First of all, the residents of the district should be aware of water-saving and take all the water. Secondly, MBR process is used as reclaimed water reuse technology to treat the miscellaneous drainage, which can be reused for toilet flushing, greening and car washing to maximize the utilization of water resources. In order to maintain the balance of water system and the construction of water-saving ecological community, it is necessary to strengthen the management and maintenance, formulate corresponding laws and regulations, and raise residents'awareness of water-saving.
Based on the analysis of domestic and foreign references and practical experience, this study decided to adopt MBR process as the core process of reclaimed water reuse. Through the study of integrated MBR process, A/O-MBR process and BCOR-MBR process, the effect of each process on residential sewage treatment was investigated, and the treatment results were analyzed. The removal rates of D, ammonia nitrogen, total nitrogen and total phosphorus were 92.07%, 99%, 22.69%, 26.20% respectively. The average effluent turbidity was less than 0.26NTU, ammonia nitrogen < 2.56mg/L, COD < 25mg/L, total nitrogen < 49.58mg/L, total phosphorus < 3.32mg/L. The effluent indexes were in accordance with the water quality standard for urban miscellaneous water (GBT18920-2002).
On the basis of integrated MBR, anoxic zone was added, and A/O-MBR process was adopted. Hydraulic residence time was 2.8 hours, dissolved oxygen was less than 0.2 mg/L, hydraulic residence time in aerobic zone was 6 hours, and dissolved oxygen in aerobic zone was generally between 3-5 mg/L. Compared with the integrated MBR, the removal efficiency of COD is similar, the average removal rate is 93.78%, the system has strong impact resistance and stable operation; the removal rate of ammonia nitrogen is also maintained at a high level, the removal rate is as high as 98%, and the effluent ammonia nitrogen is always lower than 2mg/L. For total nitrogen and phosphorus, the removal efficiency has been significantly improved, total nitrogen from the original average 22.69% to 40.44%, total phosphorus from the original average 26.20% to 41.39%.
BCOR-MBR (Contact Oxidation-MBR) process was used to treat the reclaimed water in the residential area. The packing was made of polyurethane foam with larger porosity and specific surface area. Square polyurethane foam filler with 20-25mm side length was used. The packing was placed on the hollow plastic sphere and the density was lighter than that of water. The filling amount was about 50% of the whole reactor. The optimum parameters were obtained by the integrated MBR, and the effluent indexes were as follows: COD removal rate was 94.24%, COD was lower than 15mg/L in the later stage; NH3-N removal rate was 99.25%, NH3-N was lower than 1.9mg/L in the effluent; TN effluent was 44.58mg/L, the average effluent rate was 36.24%; total phosphorus removal rate was 43.58%, and the average effluent was 2.4mg/L.
Membrane fouling is an unavoidable problem in MBR process. Membrane fouling can be mitigated as much as possible through the causes of membrane fouling. Membrane fouling control methods include low pressure operation, aeration, backwashing and membrane cleaning. Membrane cleaning methods include air-washing, air-water backwashing, drug cleaning, ultrasonic cleaning and so on. Cleaning, removal of residual substances attached to the membrane surface, slowing membrane fouling, achieving membrane flux recovery purposes.
【学位授予单位】:兰州交通大学
【学位级别】:硕士
【学位授予年份】:2014
【分类号】:X703;TV213.4
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