To be safe, the burst pressure should be 205 psig. However, can your process live with this low burst pressure when the other pipe is not flowing? If not, then another technology will be needed. If a relief device can be used, either a balanced bellows or pilot relief valve can be used. If a positive seal is needed, a rupture pin device may be applicable. Rupture Pin Technologies has a balanced version of their Model C valve.
Just a note. When sizing the rupture disk in this situation the standard vapor or liquid sizing equations are not applicable. A full hydraulic analysis of the relief piping, including to 2000 feet of piping to the other tank while the other pipe is flowing is required.
--Mike--