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can anyone tell me is there any way to calculate ignition temperature of a gas mixture?

Hello, I need to design an amine contactor. The flare gas recovered from the flare gas recovery system is fed to the amine contactor for acid gas removal. Before the gas is fed to the contactor it is saturated with water. My question is why do you want to saturate the gas with water and what...

can anyone tell me the relation between foaming factor, % flooding and system factor.

I just wanted to know the liquid retention time for the liquid in the bottom of the column beneath the packed bed.

Hi, I am designing amine contactor for H2S removal using MDEA. I am using packed tower with IMTP packing of 1.57inch diameter and the bed diameter is of 3ft. I want to calculate the column height, I need information regarding the retention time of the liqulid in the column. Can anyone help me...

If the atmospheric crude tower doesn't converge with the given specifications what are the main things to be focused upon to converge the column??

I have a question, the assay data types we have in hysys are TBP, ASTM D86, ASTM D1160, ASTM D86-D1160, ASTM D2887, CHROMATOGRAPH and EFV. What if in the laboratory the crude is analysed using differt method i.e ASTM D7169. How do you input the results of this method in hysys??

I have the ASTM D86 assay data for that I need to enter data only on volume basis. HYSYS does not accept data on mass basis and I have the data for % mass recovered.

I have started atmospheric crude tower simulation using hysys. I have the laboratory data of boiling points and the mass% recovered determined by ASTM D86 method. My question is regarding inputing these values to the simulator. In the assay type data of the simulator I have entered ASTM D86 and...

If process design for desalting crude oil is to be carried out can the design be done using any simulation software? I am not sure if my question is menaingful. I have lots of questions regarding desalting crude oil. Can anyone help me regarding this? Thank You.