Recent content by bigufo

yes it's about a binary gas mixture, but it doesn't depend on the temperature since there are only gases and i just the weight composition. if you don't know any method to calculate this composition, can you give me any useful website or tables about this?? thank you very much for replying Gokul

no one has any idea?:frown:

hello, (it was just a mistake when i double-posted dear moderator/administrator, so please let this thread on:rolleyes: ) how I can calculate the composition of a gas binary mixture of vinyl chloride and water knowing that I have only the following informations: the water is saturated by the...

hello, how I can calculate the composition of a gas binary mixture of vinyl chloride and water knowing that I have only the following informations: the water is saturated by the vinyl chloride the pressure of the mixture is 4bars or can you tell me what I have to look as information to...

thank you very much mbeychok, you were really very helpful.

mbeychok: if the pressure would not increase in the storage tank it's because of its vent. so if i connect a hose from the truck vent back to the storage tank the HCl vapor will escape through the storage tank's vent. "As you pump into the truck, the level rises and "pushes" vapor out of the...

mbeychok: if the pressure would not increase in the storage tank it's because of its vent. so if i connect a hose from the truck vent back to the storage tank the HCl vapor will escape through the storage tank's vent. "As you pump into the truck, the level rises and "pushes" vapor out of the...

hi mbeychok, do you know how can i quantify or measure these losses?

mbeychok yes, that's right it's about losses from the tank truck vents while loading the solution into it from the storage tanks, but i can't simply vent the trucks back into the storage tanks because the losses are gases and it will increase the pressure into the storage tank.

ok, i admit that it was a difficult question, so i have to deal with the problem using the actual few informations thank you again

there are many ideas depending on the process you're using, but the main key , i think, is to try to emerge the gases in water and wait until its concentration reach the amount you want before recycling it

i'm talking about storage in static tanks and transportation by trucks. it's economical? well, it depends on how much costs HCl in your region, and the cost of the recovering plant conceived? do you have any idea how can i measure or calculate these losses?

Q Goest: 33% HCl 67% water (mole percent) Bystander: you're right that is what i need. the loading operation is a dump from the top and splash, and the tank is a horizontal cylinder with a circular opening in the summit for the load. so my question is : is there any correlation between (tank...

the concentration of HCl is 33%

HCl evaporation rate Thank you very much FredGarvin and Q_Goest for your answers, but the pumping is made under atmospheric conditions (pressure & temperature) and nevertheless there are gases that escape, it is a small quantity but I have to recover it. It can be due to the barbotage caused...