2) glycerol distilled residue
甘油蒸馏残渣
1.
Recovery of polyglycerol from crude glycerol distilled residue;
从粗甘油蒸馏残渣中回收聚合甘油
3) distilled monoglycerides
蒸馏单甘酯
1.
Study on improvement of the methods for limit test of heavy metals in distilled monoglycerides;
蒸馏单甘酯的重金属限量试验改进研究
4) tar distillation
焦油蒸馏
1.
Discussion on safely valve of tar distillation still top;
关于焦油蒸馏釜顶安全阀的讨论
2.
The process of the first 300 000t/a coal tar distillation plant that has been licensed from abroad is introduced and so is the quality of the main middle fractions, besides, the advantages reflected in the product quality, energy balance and environmental protection are presented.
介绍了国内首套引进的30万t/a煤焦油蒸馏装置的工艺情况及主要中间馏分质量情况,指出了该装置在产品质量、能量平衡和环境保护等方面的优势,提出了我国煤焦油加工应该改进的方面。
5) crude oil distillation
原油蒸馏
1.
Simulation and analysis of crude oil distillation units;
原油蒸馏过程的模拟与分析
2.
Commercial application of energy conservation technologyfor crude oil distillation;
原油蒸馏节能技术的工业应用
3.
A nonlinear soft-sensing strategy with bootstrap aggregated neural network is proposed to solve the poor adaptability of conventional soft-sensor methods when feedstock varies in crude oil distillation.
针对原油蒸馏过程常规软测量模型难以适应原油进料性质变化的问题,提出Bootstrap多神经网络的非线性软测量处理策略。
6) crude distillation
原油蒸馏
1.
Data reconciliation and operating optimization of crude distillation process;
原油蒸馏过程中的数据协调与操作优化
2.
In regard to the speciality, such as processing different types of crude oils with changeable mixing ratio, of a refinery, some improvements were made on the original crude distillation model in order to make the software more suitable to present operation.
针对某炼油厂加工原油品种繁多,且混炼比例变化大的特点,对原油蒸馏塔原模型软件系统进行了改进,使它能更好地适应炼油厂的生产。
3.
In order to investigate the productive conditions of the crude distillation unit and find a way to save the energy,the energy balance and exergic balance of the No.
为了考察原油蒸馏装置的生产情况,找出今后装置节能的途径,本文运用热力学第一、第二定律,对燕化炼油厂三蒸馏车间蒸馏装置的能量平衡进行标定核算。
补充资料:甘油蒸馏
分子式:
CAS号:
性质:粗甘油经过汽化和冷凝制取精甘油的工序。甘油蒸馏设备由蒸馏罐、多组串联冷凝器以及受器组成。一般采用间歇或半连续工艺操作。甘油首先在蒸馏罐中减压下受热汽化(为了帮助汽化往往鼓入直接蒸汽),甘油蒸汽在串联的多组冷凝器中分级冷凝(通过控制冷凝器温度达到)。冷凝器可以是空气冷凝器也可以是受控的水冷凝器。浓度和纯度达到要求的即为精甘油产品。蒸馏罐内保持真空压力低于5kPa,液温在170℃。新型蒸馏系统中,压力降低到400~530Pa,液温155℃,可提高蒸馏得率。
CAS号:
性质:粗甘油经过汽化和冷凝制取精甘油的工序。甘油蒸馏设备由蒸馏罐、多组串联冷凝器以及受器组成。一般采用间歇或半连续工艺操作。甘油首先在蒸馏罐中减压下受热汽化(为了帮助汽化往往鼓入直接蒸汽),甘油蒸汽在串联的多组冷凝器中分级冷凝(通过控制冷凝器温度达到)。冷凝器可以是空气冷凝器也可以是受控的水冷凝器。浓度和纯度达到要求的即为精甘油产品。蒸馏罐内保持真空压力低于5kPa,液温在170℃。新型蒸馏系统中,压力降低到400~530Pa,液温155℃,可提高蒸馏得率。
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