Research progress and hot spots of hydrothermal liquefaction for bio-oil production based on bibliometric analysis

Environmental Science and Pollution Research - Hydrothermal liquefaction (HTL) of biomass used HTL reaction under high temperature and pressure to produce bio-oil. This technology is considered as...     

房屋建筑工程施工现场环境保护以及节能降耗控制措施研究

房屋建筑施工阶段是建筑工程中最为重要的阶段,也是资源消耗和环境污染的集中阶段。房屋建筑施工造成的环境污染主要来源于:施工中的固体垃圾、液体垃圾和气体垃圾,且在施工现场,相关人员节能降耗意识薄弱,对于施工中存在的资源浪费现象经常会忽视。基于此,给出了如下措施:加强施工过程的监控,合理排放施工现场的污水和固体废弃物;提高水的利用率,并在施工过程中,通过节水工艺对路面进行喷洒;合理排放施工过程产生的污水,对含有化学品、油漆的建筑材料要实施防渗漏措施;设置封闭式垃圾容器,利用袋装化形式将施工垃圾带出施工现场;倡导绿色施工。     

Effects of irrigation,fertilization and crop straw management on nitrous oxide and nitric oxide emissions from a wheat–maize rotation field in northern China

One-year winter wheat–summer maize rotation is the most popular double cropping system in north-central China, and this highly productive system is an important source of nitrous oxide (N₂O) and nitric oxide (NO) emissions due to the high fertilizer N and irrigation water inputs. To sustain the high crop production and mitigate the detrimental impacts of N₂O and NO emissions, improved management practices are extensively applied. The aim of this study is therefore to evaluate the effects of an improved management practice of irrigation, fertilization and crop straw on grain yield and N₂O and NO emissions for a wheat–maize rotation field in northern China. Using automated and manual chamber measuring systems, we monitored N₂O and NO fluxes for the conventional (CT, 2007–2008), improved (IT, 2007–2008), straw-amended (WS, 2008–2009), straw-not-amended (NS, 2008–2009), and no N-fertilizer treatments (WS–NN, 2008–2009), respectively, for one rotation-year. The grain yields were determined for CT and IT for three rotation-years (2005–2008) and for WS, NS and WS–NN for one rotation-year (2008–2009). The improved management of irrigation and fertilization reduced the annual N fertilization rate and irrigation amount by 17% and 30%, respectively; increased the maize yield by 7–14%; and significantly decreased the N₂O and NO emissions by 7% (p < 0.05) and 29% (p < 0.01), respectively. The incorporation of wheat straw increased the cumulative N₂O and NO emissions in the following maize season by 58% (p < 0.01) and 13%, respectively, whereas the effects of maize straw application were not remarkable. The N₂O and NO emission factors of applied N were 2.32 ± 2.32% and 0.42 ± 1.69% for wheat straw and 0.67 ± 0.23% and 0.54 ± 0.15% for chemical N-fertilizers, respectively. Compared to conventional management practices using high application rates of irrigation water and chemical N-fertilizer as well as the field burning of crop straw, the improved management strategy presented here has obvious environmentally positive effects on grain yield and mitigation of N₂O and NO emissions.     

蒽醌修饰石墨毡电极预处理头孢合成废水

以钛涂钌电极为阳极、自制蒽醌修饰石墨毡电极为阴极,对头孢合成废水(COD=25 000~30 000 mg/L、ρ(NH3-N)=850~1 300 mg/L、色度为2 300~2 680度)进行了电化学氧化预处理,优化了电解条件,并对电化学体系的动力学和稳定性进行了分析。实验结果表明:蒽醌的存在可改善电化学氧化降解效果;在电解时间50 min、电流密度0.14 A/cm2、Na2SO4浓度0.1 mol/L、极板间距2 cm、初始废水p H 7.0的条件下,废水的COD、色度、NH3-N的去除率分别可达45.3%,66.9%,33.6%;BOD5/COD由处理前的0.27增至0.40,可生化性得到改善;COD、色度、NH3-N的电化学氧化降解过程均近似符合一级动力学方程;且该电化学体系的应用稳定性良好。     

Mn/γ-Al2O3催化剂的制备及头孢合成废水的催化臭氧氧化法深度处理

对Mn/γ-Al₂O₃催化剂的制备条件及头孢合成废水的催化臭氧氧化法深度处理工艺条件进行了优化。实验结果表明：以Mn（NO₃）₂溶液为浸渍液,Mn/γ-Al₂O₃催化剂的最优制备条件为浸渍液浓度0.10 mol/L、浸渍时间9 h、焙烧温度400 ℃、焙烧时间2 h;在反应时间为30 min、废水pH为9.0、臭氧通量为4.6 mg/min、催化剂加入量为5 g/L的条件下,当进水COD、BOD₅、ρ（氨氮）和色度分别为220~250 mg/L,8~10 mg/L,10~12 mg/L和60~70倍时,出水COD、BOD₅、ρ（氨氮）和色度的平均去除率分别为53%,30%,33%和93%,出水水质满足GB 21904—2008《化学合成类制药工业水污染物排放标准》的要求。     

Fenton氧化法深度处理抗生素废水二级出水

采用Fenton氧化法对青霉素和土霉素混合废水二级处理出水进行深度处理,通过正交和单因素实验研究了废水初始反应pH值、H2O2投加量、Fe2+/H2O2摩尔比及反应时间等因素对废水处理效果的影响。实验结果表明,Fenton氧化法处理的最佳反应条件为:初始pH值4、H2O2(30%)投加量50 mL/L、Fe2+/H2O2摩尔比1/20和反应时间60 min,处理后出水COD小于120 mg/L,COD去除率在75%以上,急性毒性(HgCl2毒性当量)小于0.07 mg/L,满足《发酵类制药工业水污染物排放标准》(GB21903-2008)表2标准要求。     

Penicillin fermentation residue biochar as a high-performance electrode for membrane capacitive deionization

● We have provided an activated method to remove the toxicity of antibiotic residue. ● PFRB can greatly improve the salt adsorption capacity of MCDI. ● The hierarchical porous and abundant O/N-doped played the key role for the high-capacity desalination. ● A new field of reuse of penicillin fermentation residue has been developed. Membrane capacitive deionization (MCDI) is an efficient desalination technology for brine. Penicillin fermentation residue biochar (PFRB) possesses a hierarchical porous and O/N-doped structure which could serve as a high-capacity desalination electrode in the MCDI system. Under optimal conditions (electrode weight, voltage, and concentration) and a carbonization temperature of 700 °C, the maximum salt adsorption capacity of the electrode can reach 26.4 mg/g, which is higher than that of most carbon electrodes. Furthermore, the electrochemical properties of the PFRB electrode were characterized through cyclic voltammetry (CV) and electrochemical impedance spectroscopy (EIS) with a maximum specific capacitance of 212.18 F/g. Finally, biotoxicity tests have showed that PFRB was non-biotoxin against luminescent bacteria and the MCDI system with the PFRB electrode remained stable even after 27 adsorption–desorption cycles. This study provides a novel way to recycle penicillin residue and an electrode that can achieve excellent desalination.     

铁炭内电解-厌氧-好氧工艺处理阿维菌素废水的试验研究

血清瓶毒性试验表明 ,AVM对厌氧消化产生强烈的抑制作用。AVM废水经铁炭内电解预处理后 ,COD和AVM的去除率分别达到 19.5 %和 6 8.5 % ,可大大降低废水的毒性。预处理出水再经UASB +生物接触氧化反应器进一步处理 ,当生化系统进水COD为 6 0 0 0— 6 5 0 0mg/L时 ,出水COD为 2 5 0— 2 80mg/L ,总COD去除率达到 95 .6 % ,出水达到生物制药行业排放标准     

中国加入WTO对环保机械企业产生的影响

中国加入WTO将使国内环保企业竞争更为激烈 ,使国内环保机械企业生存变得更为艰难。同时 ,由于经验丰富的国外企业已将凭借实力占据国际市场 ,使得我国环保机械企业在国际市场竞争中处于不利地位。从另一方面讲 ,中国加入WTO可以促进我国政府采取有力措施 ,加强对环保市场的监管 ,克服无序竞争 ,为国内企业营造良好的竞争环境 ;加入WTO可以加快国内环保机械企业技术创新 ,开发具有国际水准的拳头产品 ,增强市场竞争力 ,同时 ,可以推动国内产业结构调整及资本运营 ,使环保机械企业快速发展壮大 ;另外 ,WTO的加入可以迫使国内环保机械企业学习国外先进经验 ,掌握全球经济知识 ,夯实参与国际市场竞争的基础。     

剩余污泥臭氧化过程中磷的释放及形态转化

以剩余污泥臭氧化过程中含磷物质的形态分布及变化规律为研究核心,分析了不同臭氧投加量下污泥样品中液相和固相中磷的形态,并探讨了不同磷形态与臭氧相关的释放性能.结果表明,臭氧投加量为0.15 g·g~(-1)时,液相总磷(TP_L)含量为38.26 mg·L~(-1),比氧化前污泥混合液中TP_L含量增加了29倍,因此,可将0.15 g·g~(-1)作为实际释磷工艺最佳臭氧投加量.臭氧氧化过程中污泥固相中各形态磷含量及其所占固相总磷(TP_S)比例的变化趋势基本相同.臭氧可提高污泥中磷潜在的生物可利用性,臭氧投加量为0.15 g·g~(-1)时,生物有效磷含量达20.74 mg·g~(-1),在TP_S中所占比例由原始污泥中的73.60%提高至86.27%.TP_L含量的增加主要来自污泥臭氧氧化过程中污泥解絮和溶胞,每溶解1 g MLSS向液相中释放TP_L的量为0.0324 g.