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磁混凝-高氨回用联合处理黑臭水体研究
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作者 薛金凤 蒋佳明 +1 位作者 李乐研 马彦涛 《水处理技术》 CAS CSCD 北大核心 2023年第1期82-86,共5页
基于磁混凝技术的高效除磷和快速沉降的优点和氨氮去除率低的不足,建立了一种无倒吸可稳定运行的低温加热负压抽气高氨回用技术,最佳抽气时间为15 min,进水pH为11.5;黑臭水301.9 mg/L氨氮的回收率为99.6%。通过正交实验明确磁混凝工艺出... 基于磁混凝技术的高效除磷和快速沉降的优点和氨氮去除率低的不足,建立了一种无倒吸可稳定运行的低温加热负压抽气高氨回用技术,最佳抽气时间为15 min,进水pH为11.5;黑臭水301.9 mg/L氨氮的回收率为99.6%。通过正交实验明确磁混凝工艺出水TP、COD、浊度和TN的显著性影响因素是聚铁投加量和pH,并结合单因素实验确定磁混凝最佳工艺条件为:聚铁75 mg/L、磁粉300 mg/L、pH 7.5、PAM最佳用量1.0 mg/L;对黑臭水中浓度分别为950 NTU、5911 mg/L和13.4 mg/L的浊度、COD和TP的去除率分别为99.1%、97.0%和98.3%。将磁混凝与低温加热负压抽气联用处理高有机质高氨氮的黑臭水体,与现有技术相比,COD、TP和氨氮去除率提升24%以上,具有显著优越性。 展开更多
关键词 黑臭水体 磁混凝 氨回用 显著性因素
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氨碱法制碱中基于直接接触膜蒸馏原理的膜吸收氨回用技术
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作者 孙伟 高启君 +4 位作者 吕晓龙 陈华艳 武春瑞 王暄 贾悦 《膜科学与技术》 CAS CSCD 北大核心 2016年第3期118-123,共6页
氨碱法制碱中,为回收氨,氨冷却塔产生的冷凝氨液需经二次蒸氨工序,因此过程能耗高;循环回用的高含水率氨,降低了氨化工序中精盐水的浓度,最终限制了钠利用率的提高.本文采用精盐水作为吸收液,研究基于直接接触膜蒸馏原理的膜吸收氨回用... 氨碱法制碱中,为回收氨,氨冷却塔产生的冷凝氨液需经二次蒸氨工序,因此过程能耗高;循环回用的高含水率氨,降低了氨化工序中精盐水的浓度,最终限制了钠利用率的提高.本文采用精盐水作为吸收液,研究基于直接接触膜蒸馏原理的膜吸收氨回用技术.将模拟冷凝氨液中的氨转移到精盐水中而被吸收,同时抑制与氨传质同向的水传质过程,从而降低回用氨的含水率,节省水的汽化相变热.实验研究了膜吸收组件用聚偏氟乙烯(PVDF)中空纤维疏水膜丝内径ri和组件装填密度δ、吸收液与原料液进入膜组件时的温度差ΔT对膜吸收氨回用过程性能的影响.当ri为0.80mm,δ为16.8%,ΔT为9℃时,氨通量为1.17kg/(m^2·h),水通量仅为0.04kg/(m^2·h),表明该技术具有可行性. 展开更多
关键词 膜吸收 直接接触膜蒸馏 氨回用 含水率 碱法制碱
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陕西省石煤提钒行业存在的问题及对策研究 被引量:4
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作者 兰涛 张晓瑜 +1 位作者 武征 孙愿 《环境科学与管理》 CAS 2013年第5期83-87,共5页
陕西的石煤主要分布在陕南秦岭南坡的商洛地区,但大部分石煤钒矿属于难处理矿,钒大部分以V(Ⅲ)和V(Ⅳ)存在,目前企业大多采用"焙烧+稀酸浸出+氨法沉钒"或者"强酸浸出+氨法沉钒"工艺进行生产。存在的问题一是钒的综... 陕西的石煤主要分布在陕南秦岭南坡的商洛地区,但大部分石煤钒矿属于难处理矿,钒大部分以V(Ⅲ)和V(Ⅳ)存在,目前企业大多采用"焙烧+稀酸浸出+氨法沉钒"或者"强酸浸出+氨法沉钒"工艺进行生产。存在的问题一是钒的综合回收率为65%左右,整体偏低;二是生产废水中含有大量氨使得废水闭路循环难度大;三是矿区大部分位于汉丹江水系的中上游地区或临近出省断面,选址较为敏感。针对以上存在的问题提出了解决建议,并对陕西省石煤提钒行业的发展做出了展望。 展开更多
关键词 石煤提钒 生产工艺 钒回收率 废水回用
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Thermodynamic analysis of simplified dual-pressure ammonia-water absorption power cycle 被引量:5
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作者 华君叶 陈亚平 +1 位作者 刘化瑾 吴嘉峰 《Journal of Central South University》 SCIE EI CAS 2012年第3期797-802,共6页
A simplified dual-pressure ammonia-water absorption power cycle(DPAPC-a) using low grade energy resources is presented and analyzed.This cycle uses turbine exhaust heat to distill the basic solution for desorption.The... A simplified dual-pressure ammonia-water absorption power cycle(DPAPC-a) using low grade energy resources is presented and analyzed.This cycle uses turbine exhaust heat to distill the basic solution for desorption.The structure of the cycle is simple which comprises evaporator,turbine,regenerator(desorber),absorber,pump and throttle valves for both diluted solution and vapor.And it is of high efficiency,because the working medium has large temperature difference in evaporation and small temperature difference in absorptive condensation,which can match the sensible exothermal heat resource and the cooling water simultaneously.Orthogonal calculation was made to investigate the influence of the working concentration,the basic concentration and the circulation multiple on the cycle performance,with 85-110 ℃ heat resource and 20-32 ℃ cooling water.An optimum scheme was given in the condition of 110 ℃ sensitive heat resource and 20 ℃ cooling water,with the working concentration of 0.6,basic concentration of 0.385,and circulation multiple of 5.The thermal efficiency and the power recovery efficiency are 8.06 % and 6.66%,respectively.The power recovery efficiency of the DPAPC-a is 28.8% higher than that of the steam Rankine cycle(SRC) and 12.7% higher than that of ORC(R134a) under the optimized situation. 展开更多
关键词 absorption power cycle AMMONIA-WATER circulation multiple ammonia concentration Kalina cycle
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RECOVERY OF p-AMINOPHENOL (PAP) FROM AQUEOUS SOLUTION BY HYPER-CROSS-LINKED RESIN AND ITS USE FOR WASTEWATER TREATMENT 被引量:1
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作者 ZHANG Haiyun LI Aimin 《Chinese Journal of Reactive Polymers》 2008年第1期18-28,共11页
p-Aminophenol (PAP), a typical amphoteric compound, has been widely used as raw chemical material and important interrnediate in various fields. To study on the recovery of PAP, an experimental comparison of the ads... p-Aminophenol (PAP), a typical amphoteric compound, has been widely used as raw chemical material and important interrnediate in various fields. To study on the recovery of PAP, an experimental comparison of the adsorption and desorption properties of PAP onto three types of hyper-cross-linked resins in aqueous solutions was performed. This paper focuses on the static equilibrium adsorption and desorption behaviors, the adsorption thermodynamics, the column dynamic adsorption and desorption, and other influencing factors of adsorption, such as temperature and pH values. All the isothermal data fit well to the Freundlich model. The capacity of equilibrium adsorption for PAP on NG-10 is the highest within the temperature range 288K-318K, which may greatly contribute to the advantage in specific surface area, especially the micropore area, of the adsorbent. While in the desorption experiments, NG-9 achieved relative well regeneration efficiency whether by ethanol or by 4% hydrochloric acid. Furthermore, the results of column tests and field applications were also proved that NG-9 was an effective sorbent for the reclamation PAP from wastewater. 展开更多
关键词 Adsorption P-AMINOPHENOL Hyper-cross-linked resin Recovery.
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