1)  anaerobic sequencing batch reactor(ASBR)
厌氧序批式间歇活性污泥法反应器
2)  anaerobic
厌氧
1.
Research of side cantilever agitator of anaerobic moving bed bio-film reactor;
厌氧移动床生物膜反应器侧伸式搅拌装置的试验研究
2.
Characteristic research of anaerobic granules;
厌氧颗粒污泥的性能研究
3.
Treatment of ammonium and sulfate wastewater by using an anaerobic attached-growth bioreactor;
厌氧附着生长反应器处理氨氮和硫酸盐废水的研究
3)  anaerobe
厌氧
1.
The anaerobe and aerobe training, filtrating and re-mating were investigated; the results showed that blowing-anaerobic-aerobic biologic combined Process can decrease the organic pollution concentration.
研究表明,通过对厌氧菌和好氧菌的驯化、筛选和复配采用吹脱-厌氧-好氧串联工艺可有效降低废水的有机污染指标。
4)  anaerobic process
厌氧
5)  anaerobic digestion
厌氧
1.
Two-phase anaerobic digestion with three stages treatment of sapogenin wastewater;
皂素生产废水综合治理技术研究(Ⅱ)——三阶段两相厌氧工艺技术
2.
The effects of Fe3+,Cu2+ and Zn2+ on the two-phase anaerobic digestion of kitchen wastes at different pH values were studied by intermittent experiments.
通过间歇实验研究了在pH=7和不调节pH两种情况下添加不同浓度的Fe3+、Cu2+和Zn2+对厌氧消化水解酸化阶段有机酸组分和含量的影响。
3.
Bench-scale composting experiment was made to study the features of methane produced in anaerobic digestion.
通过厌氧堆肥试验,对厌氧堆肥产甲烷的基本特征进行了研究,结果表明:在厌氧堆肥开始阶段,气体中只有8%的甲烷,二氧化碳产率是甲烷产率的4倍左右;而随着反应的进行,二氧化碳产率呈下降趋势,甲烷产率逐渐升高,并于3个月时达到最高值45%;此后二氧化碳及甲烷产率都逐渐降低。
6)  anaerobic treatment
厌氧
1.
Anaerobic sequencing batch biofilm reactor(ASBBR),an innovative anaerobic treatment technique,was used to treat composite mustard tuber wastewater with high concentration organic substances(COD 4 000 mg/L),high salt(10 gCl~-/L) and high nitrogen.
采用ASBBR反应器作为高盐(10 gC l-/L)、高有机物浓度(COD为4 000 mg/L)榨菜废水的厌氧处理单元,考察了挂膜密度、负荷、水温等对去除COD的影响。
2.
When the loop-flow aeration technology is used to treat oil-containing chemical wastewater with COD concentration of 4 000 mg/L after anaerobic treatment,the effluent COD,BOD5 and NH3-N are 110 to 150 mg/L,8 to 13 mg/L and 5 to 9 mg/L respectively.
对经厌氧处理后COD约为4 000 mg/L的油脂化工废水采用环流曝气工艺进行处理,出水COD为110~150 mg/L、BOD5为8~13 mg/L、NH3-N为5~9 mg/L。
3.
The combined process of anaerobic treatment,drop-aeration bio-contact oxidation and aquatic vegetable wetland was used to treat rural domestic sewage.
采用厌氧/跌水充氧接触氧化/水生蔬菜型人工湿地组合工艺处理农村生活污水,考察了工艺的运行效果及各处理单元对去除污染物的贡献率。
参考词条
补充资料：罐式间歇溶解器
分子式：
CAS号：

性质：是最常用的间歇溶解器。它的优点是：乏燃料加料简单，一次投料一大批；操作简单；易于自动控制；不存在启动和停车造成产品不合格问题。间歇溶解的缺点是溶解速率不稳定。间歇溶解的工艺控制是控制溶解液的加料浓率，催化剂量和留底量。溶解器尺寸由生产速率和总溶解速率来定。溶解器备有加料斜槽和料筐，燃料块从设备室顶加入，往缓冲板和斜槽进入料筐。溶解器装有蒸气夹套和加热、冷却蛇管，用以控制温度和溶解速率。溶解是在沸点以下负压下进行。溶解器顶部装有冷凝蛇管用来回流冷凝硝酸和水蒸气。尾气经排气管排到废气处理系统。

说明：补充资料仅用于学习参考，请勿用于其它任何用途。