Leclerc
Chemical
- Aug 22, 2002
- 73
Our process reaction uses a continuous stream of hydrogen, compressed to 90 barg from an OSBL source. We need to install a 20 m3 compressed hydrogen receiver between the compressor and the reactor.
In the first instance, where should I go to obtain a list of design points/ issues concerned with such a receiver?
regards,
Leclerc
In the first instance, where should I go to obtain a list of design points/ issues concerned with such a receiver?
regards,
Leclerc