Open zasddsgg opened 1 month ago
Hello, I have added the following picture to illustrate the problem. Since the MESP
obtained by the above two methods
is quite different, I am not sure which method is correct. Could I trouble you take some time to have a look. Thanks again for your help.
Or does the strb
have to be recycled to reactor R
(as shown in the following picture) for the calculated MESP to be correct? Is it possible for strb
to flow without recirculating back to reactor R
as in the two methods a
and b
above? Is this calculation of the MESP correct?
I tried to recycle stream strb
to the reactor R
(as shown in the figure below), then the makeup
amount of component a
was 300 kg/h
(obtained by adding specifications), the stra
flow rate was still 500 kg/h, and the code of the stream set was as follows. The MESP obtained by this way was completely different from the MESP obtained by the second method above. May I ask you which method of MESP obtained is correct?
Stream makeup= bst.Stream(‘makeup, a=1, price=17) # only contain chemical a
Stream strb = bst.Stream(‘strb’)
Stream stra = bst.Stream(‘stra’)
Hello, in the process, stream
stra
is the chemical stream needed for the reactorR
(streamstra
only contains chemicala
), streamstrb
is the stream only contains componenta
recovered by the recycling section, I did not recycle it back to the reactorR
, but only as an outlet stream. When calculating TEA, the following two setting methods get different MPSP (I use the TEA calculation method of cellulosic model), may I ask which setting method is right? Assume that the price of componenta
is 17, the initial input of streamstra
is 500, and the quality difference of componenta
between streamstra
and streamstrb
is 300, that is, the net consumption of componenta
is 300.The first method: Let BioSTEAM automatically subtract the cost of stream
strb
. The code is as follows:The second method: The price of component
a
in streamstra
is set according to the net consumption ofa
. The code is as follows: