vacuum_system#
- class VacuumSystem(unit=None, vacuum_system_preference=None, F_mass=None, F_vol=None, P_suction=None, vessel_volume=None)[source]#
Create an auxiliary vacuum system for a unit operation.
- Parameters:
unit (
Unit
, optional) – Main unit operation containing the auxiliary vacuum system. Missing parameters are estimated through this unit operation, if given.F_mass (
float
, optional) – Vapor mass flow rate entering vacuum system from vessel [kg/hr] (not including inleakage). Defaults to the vapor volumetric flow rate exiting unit.F_vol (
float
, optional) – Vapor volumetric flow rate entering vacuum system from vessel [m3/hr] (not including inleakage). Defaults to the vapor mass flow rate exiting unit.P_suction (
float
, optional) – Suction pressure [Pa]. Defaults to unit.P or the minimum outlet pressure.vessel_volume (
Union`[:py:class:`float
,list`[:py:class:`float
],None
]) – Vacuum volume [m3]. Defaults to unit.design_results[‘Total volume’].vacuum_system_preference (
str
, optional) – Name(s) of preferred vacuum systems. Valid names include ‘Liquid-ring pump’, ‘Steam-jet ejector’, and ‘Dry-vacuum pump’.
Notes
The vacuum system is sized/costed based on the vapor flow rate through the vacuum system, which includes the inleakage into the vessel through fixtures and cracks. The inleakage is a function of the suction pressure and the total vessel volume as in [1].
BioSTEAM’s CSTR, Flash, and Distillation columns automatically include a vacuum system when needed.
Examples
Create vessel with a vacuum system:
>>> import biosteam as bst >>> class VacuumVessel(bst.Unit): ... auxiliary_unit_names = ('vacuum_system',) # Mark attributes as auxiliary ... _units = {'Total volume': 'm3'} # This is needed for the vacuum system ... P = 1000 # Pa ... tau = 4 # hr ... ... def _run(self): ... self.outs[0].P = 1000 # Pa ... ... def _design(self): ... self.design_results['Total volume'] = self.feed.F_vol * self.tau ... self.vacuum_system = bst.VacuumSystem(self) ... >>> bst.settings.set_thermo(['Water']) >>> feed = bst.Stream('feed', Water=1e6) >>> V1 = VacuumVessel('V1', ins=feed) >>> V1.simulate() >>> V1.results() Vacuum vessel Units V1 Medium pressure steam Duty kJ/hr 1.04e+07 Flow kmol/hr 288 Cost USD/hr 79.3 Cooling water Duty kJ/hr -9.37e+06 Flow kmol/hr 6.4e+03 Cost USD/hr 3.12 Design Total volume m3 7.23e+04 Purchase cost Vacuum system - Steam-jet ejecto... USD 8.18e+04 Total purchase cost USD 8.18e+04 Utility cost USD/hr 82.4
For simplicity, this example does not include the cost of the vessel, but vessel costs should be included for techno-economic analysis.
References