1) Clinsulf-SDP sulfur recovery unit
Clinsulf-SDP硫磺回收装置
2) sulfur recovery unit
硫磺回收装置
1.
Sulfur condenser leakage in sulfur recovery unit was widespread,seriously impeded the long-term running of the sulfur recovery unit,leakage’s reasons were variety.
硫冷凝器是硫磺回收装置的核心设备之一,硫冷凝器泄漏是硫磺回收装置中普遍存在的问题,严重制约了硫磺回收装置的长周期运行,泄漏的原因多种多样,管板产生裂纹是导致泄漏的主要原因之一,解决该问题能有效提高硫磺回收装置的运行周期,本文将实践中总结的效果较好的硫冷凝器管板裂纹处理方法从原理分析、处理方案到处理效果作了详细介绍,并提出了改进建议。
2.
Electric heat tracing and steam jacket heat tracing in sulfur recovery unit have been compared in the light of economy and unit features.
从经济及装置特点两方面对硫磺回收装置电伴热和蒸汽夹套伴热进行了比较。
3.
In allusion to the problems existing in the sulfur recovery unit the main factors effecting the total recovery rate are analyzed and summarized from the aspects of process, catalyst and equipment etc.
针对硫磺回收装置存在的问题 ,从工艺、催化剂及设备等方面对影响总硫回收率的主要因素进行分析总
4) Sulphur Recovery Plant
硫磺回收装置
1.
Applications of Dow's Fire and Explosion Index in Sulphur Recovery Plants
道氏指数法在硫磺回收装置中的应用
2.
This article expatiates on the existent problems of sulphur recovery plant in imported branch plant,including sulphur recovery in main combustion chamber is low and the color of liquid sulphur is poor.
阐述了卧龙河引进分厂硫磺回收装置存在的问题,以及主燃烧炉硫收率低、液硫颜色差的情况,总结了主燃烧炉燃烧器整改后的运行情况,从工艺操作、硫收率及硫磺质量等方面说明了新燃烧器运行的成功性。
6) Clinsulf SDP process
Clinsulf-SDP工艺
补充资料:SDP
分子式:C12H10O4S
分子量:250.27
CAS号:80-09-1
性质:熔点245-250°C。水溶性1.1 g/L (20°C)。
分子量:250.27
CAS号:80-09-1
性质:熔点245-250°C。水溶性1.1 g/L (20°C)。
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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