sulfur recovery信息详情
硫磺回收
sulfur───n.硫，硫磺；硫磺色；美洲粉蝶；v.用硫磺处理；用硫消毒（或熏制）
recovery───n.恢复，复原；痊愈；重获
sulfur content───含硫量，硫分；硫含量
shoveling sulfur───铲硫磺（shoveling是shovel的现在分词）
cobaltous sulfur───钴硫
sulfur dioxide───[无化]二氧化硫；n.二氧化硫
sulfur trioxide───[无化]三氧化硫（等于sulphurtrioxide）
lime sulfur───石灰硫磺合剂；[农药]石硫合剂
orthorhombic sulfur───正交硫
The equipment for sulfur recovery requires a wide operating range.───硫磺回收装置的设备需要有较大的操作弹性。
Presents the basic principle, technical features and catalyst of no on line furnace sulfur recovery process.───介绍了无在线炉硫回收工艺的基本原理、技术特点和催化剂使用情况。
This work has offered a useful exploration in stabilizing the sulfur recovery rate of imported unit.───本研究工作为稳定引进装置硫磺回收率作了有益的探索。
The main reason of difficult operation is the low concentration and large amount of sour gas in the sulfur recovery unit.───酸性气浓度低、量大，是硫回收装置操作困难的主要原因。
Through structural and operating parameters in both the optimization of the new sulfur recovery by burning stove.───通过结构参数及操作参数两方面的优化，得到了新型硫磺回收尾气处理灼烧炉。
Gas streams with a molar concentration of sulfur dioxide from 1 to 100% may be processed to achieve nearly 100% sulfur recovery efficiency.───以二氧化硫摩尔浓度从1至100%天然气流，可处理，以达到接近100%的硫磺回收效率。
Introduces the design method and fabricating, erection requirement of steam jacket in sulfur recovery units.───介绍了硫磺回收装置蒸汽夹套管道设计方法及制作安装要求。
Rational selection of R value calculation method is critical to obtain accurate sulfur recovery rate data.───如何获得准确的硫收率数据，关键在于选择合理的R值的计算方法。
Sulfur recovery technology of improving the total sulfur recovery rate───提高总硫回收率的硫磺回收工艺
The author develops a mathematical model which is necessary for technological calculation and draws up a simulated program of Claus sulfur recovery technology.
DCS has been used in 40 kt a sulfur recovery plant.
The preparation, characterization and activity evaluation of LS-971 deoxygenation protection catalyst for sulfur recovery were introduced.
Gas streams with a molar concentration of sulfur dioxide from 1 to 100% may be processed to achieve nearly 100% sulfur recovery efficiency.
Based on the JX-300DCS, we used the complicated control schemes such as proportional control, cascade control and override control to realize the automatic control in sulfur recovery unit.
Under normal conditions, the major odor pollutants come from alkali waste treatment unit, sour water stripping unit, ammonia refining unit, sulfur recovery unit as well as waste water treatment site.