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Everyone, please tell us what devices you are working with now

2008-01-18View Original

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Let’s all talk about the equipment we work with and the volume of processing involved, to see if the people here at Haichuan can build China’s most comprehensive petrochemical plant
Reply #22008-01-18
Let me explain: I work in hydrogenation; I am involved in medium-pressure hydrogenation, as well as in the hydrogenation of lubricating oils, and I have also worked on gasoline hydrogenation
Reply #32008-01-18
I work in the catalytic cracking workshop.
Reply #42008-01-18
I have been working in the factory for two and a half years. The units I have worked on include: a vacuum distillation unit with a capacity of 1 million tons per year, a gas fractionation unit with a capacity of 80,000 tons per year, and a non-hydrogenated gasoline upgrading unit with a capacity of 70,000 tons per year. Now I am working at the new facility to set up new units, and the units under my responsibility there are the delayed coking unit and the vacuum distillation unit. I have quite a bit of experience, right? :lol :lol :victory: :victory:
Reply #52008-01-18
I worked at a Sinopec refinery for six years, handling lubricant hydrogenation as well as medium-pressure diesel hydrogenation
Reply #62008-01-19
5 years for gasoline and diesel hydrogenation, 1 year for catalysis
Reply #72008-01-19
CHEMCHINA. 8 years in oil storage and transportation. The atmospheric and vacuum distillation unit: 6 years, from 100,000 tons to 300,000 tons to 1.2 million tons. This post was last edited by yinyueming on 2008-1-19 11:02.]
Reply #82008-01-19
1.2 million tons of atmospheric and vacuum distillation – it’s been almost a year already!
Reply #92008-01-19
Currently, we are carrying out C9 hydrogenation at 10W; we will soon start tar hydrogenation, also at 10W.
Reply #102008-01-20
I work in chemical process design; it’s a technical field! ! It’s only been six months
Reply #112008-01-20
I have been handling 3 million tons of vacuum distillation per year, and 1.4 million tons of heavy oil catalysis for 7 years until now
Reply #122008-01-20
The project for producing *** toluene from nitrotoluene spans 2 years; everyone here is in the oil and petrochemical industry, right?
Reply #132008-01-21
I admire all of you, experts in this field~~~~ You’re amazing. I’ve been working with chemical processing equipment for 3 years. The last edit to this post was made by Qi Tianyu on 2008-1-21 at 14:56.]
Reply #142008-01-24
My unit is for dry gas, LPG desulfurization, and gasoline desulfurization. A production facility with an annual capacity of 600,000 tons for gas separation and 200,000 tons for MTBE was put into operation; I started contributing to its development from the stage of thorough inspections and adjustments, and now, two years later, the facility is operating normally
Reply #152008-01-24
I’m currently working at a private research institute on the design of catalytic cracking and hydrogen production via hydrogenation processes; please give me your support in the future
Reply #162008-01-25
I work in air separation; I’ve been in this field for four years now: lol
Reply #172008-01-25
A small hydrogen production facility (1500) is under construction; 12 years of experience in chemical engineering projects
Reply #182008-01-27
I’m a newcomer to the field of dry gas processing; I’ve worked on the hydrogenation of gasoline and diesel, and I’ve also studied the production of hydrogen from dry gas. This post was last edited by Liu Jingguo on 2008-1-27 at 09:43.]
Reply #192008-01-27
Catalytic cracking newcomer – I can do the outdoor tasks for you
Reply #202008-01-30
Urgent again: 140W for 3 years; catalytic reforming for 30W for 2 years, hehe

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