Mechatronic,
What type of Chloride are you using. HCl or Cl2 and what is your temperature range ?.
The other thing which is important is what the shutdown / maintenenace stratigy on the linework you are using. If you have a annual shutdown with moderate corrision it may be accepable to use CS pipes and change them out every year - and in some cases thats cheaper than using a corrision resistance alternative. We have high Cl content and certain parts of the plant we do use CS but change them out on a set out frequency.
If you are using HCl I would say, you need to be below 40C and have less than ppm levels of Cl. I think there are tables of corrision data for HCL in carbon steel environments - ie how much thickness you lose per year. They maybe in the US mechanical standards. Those you could use as a guide.
Hope this helps.
James