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  1. Normally the extraction plants of LNG are attached to plants of fractionation, where are extracted the c3, c4, c5+, separately, in this way could obtain part of the flow of c3 for refrigeracion,if this is not truth, could add a tower depropanizer to the process, although i do not think that is very feasible, is preferable to have a plant fractionation complete.

    Although i am just a student of engineering of gas, would be good the opinion of a professional with experience.

  2. Quote Originally Posted by gasengineer+ View Post
    Normally the extraction plants of LNG are attached to plants of fractionation, where are extracted the c3, c4, c5+, separately, in this way could obtain part of the flow of c3 for refrigeracion,if this is not truth, could add a tower depropanizer to the process, although i do not think that is very feasible, is preferable to have a plant fractionation complete.

    Although i am just a student of engineering of gas, would be good the opinion of a professional with experience.
    You are right my friend, I also think isn't feaseble but is an idea to change the actual process. Just to fill some requirements of my final project. They said that had to be done something different of the actual project. Thank for the opinion. Another thing, do you have some kind of messenger? I would like to practice my spoken english with some one, if you or anybody else be intersted. AIM: EngThiagoBrazil MSN: eng_thiago_br@hotmail.com yahoo: eng_thiago_br@yahoo.com Skype: engthiagobrazil
    sds
    Thiago

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