Txheat,
The hydraulics are very important, but the vendor is getting paid to address this via the design and it is best not to try and do his mechanical design job. Concentrate on the process design, and then check his proposal to see if it is reasonable.
In the case of a vertical thermosyphon reboiler, you will fill out a TEMA sheet with process data, and provide some elevation details (operating liquid levels, return nozzle elevation, etc). You will already know the composition, tower bottoms pressure, and duty required. You can calculate the other necessary process data (usually by simulation) but there are two common decision pitfalls on the process data to be aware of:
1) The vapor generated by the reboiler is typically only 10% to 20% of the total circulation through the reboiler. You need to specify the total circulation requirement at the reboiler inlet (from outlet vapor flow and vapor fraction matching the duty). The vendor will design the needed length of exchanger, tube count and diameter, and piping size needed to achieve this circulation rate from the elevations you provided.
2) If the heating medium is steam, you must decide a condensing (chest) pressure. This is usually less than the supply pressure (pitfall) because the steam rate is controlled by a control valve. You should choose a condensing pressure which corresponds to a reasonable value above the process temperature. This decision affects the exchanger size, control valve size, amount of flashing in the condensate system, actual steam rate, etc.
A thermosyphon reboiler assignment is where new process engineer can really demonstrate his skill. You will understand more than half of all process engineers I have met if you can explain: what process side vapor rate corresponds to a specified duty, how the vapor rate relates to the total circulation rate by hydraulics, how to calculate the steam rate needed for a specified duty and chest pressure, and how the chest pressure affects the exchanger area (via Q=U*A*MTD).
best wishes always,
SShep