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1)  organic waste liquid and waste residue
有机废液和废渣
2)  organic wastewater
有机废液
1.
The capacity of CaO for binding HCl from incineratio n of organic wastewater which contains C 2H 3Cl 3O 2 was investigated at 500— 800 ℃ in a bubbling fluidized bed.
在500~800 ℃的温度范围内, 在流化床反应器床料中添加 CaO吸收剂, 进行含氯有机废液 (含三氯乙醛) 的焚烧脱氯实验。
2.
The incineration temperature selected in incinerating organic wastewater and discharge of specific pollutant are illuminated, and several key issues encountered during handling organic wastewater by incineration in the world are described.
论述了有机废液焚烧处理时焚烧温度的选择、特殊污染物的排放、有机废液焚烧所面临的问题等几个关键问题。
3)  organic liquid wastes
有机废液
1.
Incineration of high concentration organic liquid wastes containing inorganic salts;
高浓度含盐有机废液焚烧技术
2.
High concentration organic liquid wastes cannot be disposed effectively by routine treatment methods.
化工、制药、造纸等行业的发展排放了大量的含低熔点碱金属盐和碱土金属盐的高浓度有机废液,这些废液往往毒性较高,如果直接排放将造成严重的环境污染,而常规的生化处理方法等又无法解决此类污染问题。
4)  organic waste liquid
有机废液
1.
The high concentration organic waste liquid discharged from printed circuit factory should be collected by classification.
印刷电路板生产线所产生的高浓度有机废液,宜分类收集,并应针对废液的特性,采取诸如混凝、酸化破乳、混凝破乳等预处理措施。
2.
With coal serving as an auxiliary fuel heat balance equations were established for the burning of organic waste liquid in the dense phase zone and rare phase zone of a fluidized bed incinerator.
建立了以煤为辅助燃料 ,有机废液在流化床中焚烧密相区及稀相区的热平衡方程 ,在此基础上计算获得废液在密相区的焚烧量占总处理量的份额 ,密相区焚烧温度 ,炉膛出口空气过剩系数以及预热空气温度对辅助燃料耗量及炉膛出口温度的影响关系曲线。
3.
Temperature distribution of the bed, safety and stability of incineration, pollutant emissions were examined and the feasibility of incineration of the organic waste liquid in a 20t/hCFB was analyzed.
在燃煤循环流化床燃烧试验装置上对含盐化工有机废液(红水)进行焚烧试验,重点考察焚烧炉内温度场分布、燃烧的安全性及稳定性、污染物排放特性。
5)  the organic wastewater
有机废碱液
6)  organic acid waste liquid
有机酸废液
补充资料:亚硫酸酯废液与蒸煮废液和甲醛的聚合物
CAS:70528-79-9
分子式:(CH2O·W99)x
中文名称:亚硫酸酯废液与蒸煮废液和甲醛的聚合物
英文名称:Sulfite liquors and cooking liquors, spent, polymer with formaldehyd
Spent pulping liquor, formaldehyde polymer
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
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