Abstract BST Units¶
Note
These units are for process simulation only and do not have design and cost algorithms.
QSDsan: Quantitative Sustainable Design for sanitation and resource recovery systems
This module is developed by:
Yalin Li <mailto.yalin.li@gmail.com>
Joy Zhang <joycheung1994@gmail.com>
Jianan Feng <jiananf2@illinois.edu>
Part of this module is based on the biosteam package: https://github.com/BioSTEAMDevelopmentGroup/biosteam
This module is under the University of Illinois/NCSA Open Source License. Please refer to https://github.com/QSD-Group/QSDsan/blob/main/LICENSE.txt for license details.
- class qsdsan.unit_operations.bst._abstract.FakeSplitter(ID='', ins: Sequence[AbstractStream] | None = None, outs: Sequence[AbstractStream] | None = (), thermo=None, init_with='WasteStream', include_construction=True, construction=[], transportation=[], equipment=[], add_OPEX={}, uptime_ratio=1.0, lifetime=None, F_BM_default=None, isdynamic=False, exogenous_vars=(), **kwargs)¶
Similar to
biosteam.units.FakeSplitter, but can be initialized withqsdsan.SanStreamandqsdsan.WasteStream.See also
- line: str = 'Fake splitter'¶
class-attribute Name denoting the type of Unit class. Defaults to the class name of the first child class
- run()¶
Run mass and energy balance. This method also runs specifications user defined specifications unless it is being run within a specification (to avoid infinite loops).
See also
_run,specifications,add_specification,add_bounded_numerical_specification
- class qsdsan.unit_operations.bst._abstract.Mixer(ID='', ins: Sequence[AbstractStream] | None = None, outs: Sequence[AbstractStream] | None = (), thermo=None, init_with='WasteStream', F_BM_default=None, isdynamic=False, rigorous=False, conserve_phases=False)¶
Similar to
biosteam.units.Mixer, but can be initialized withqsdsan.SanStreamandqsdsan.WasteStream, and allows dynamic simulation.See also
- line: str = 'Mixer'¶
class-attribute Name denoting the type of Unit class. Defaults to the class name of the first child class
- run()¶
Run mass and energy balance. This method also runs specifications user defined specifications unless it is being run within a specification (to avoid infinite loops).
See also
_run,specifications,add_specification,add_bounded_numerical_specification
- property state¶
The state of the Mixer, including component concentrations [mg/L] and flow rate [m^3/d].
- class qsdsan.unit_operations.bst._abstract.ReversedSplitter(ID='', ins: Sequence[AbstractStream] | None = None, outs: Sequence[AbstractStream] | None = (), thermo=None, init_with='WasteStream', include_construction=True, construction=[], transportation=[], equipment=[], add_OPEX={}, uptime_ratio=1.0, lifetime=None, F_BM_default=None, isdynamic=False, exogenous_vars=(), **kwargs)¶
Similar to
biosteam.units.ReversedSplitter, but can be initialized withqsdsan.SanStreamandqsdsan.WasteStream.See also
- line: str = 'Reversed splitter'¶
class-attribute Name denoting the type of Unit class. Defaults to the class name of the first child class
- run()¶
Run mass and energy balance. This method also runs specifications user defined specifications unless it is being run within a specification (to avoid infinite loops).
See also
_run,specifications,add_specification,add_bounded_numerical_specification
- class qsdsan.unit_operations.bst._abstract.Splitter(ID='', ins: Sequence[AbstractStream] | None = None, outs: Sequence[AbstractStream] | None = (), thermo=None, *, split, order=None, init_with='WasteStream', F_BM_default=None, isdynamic=False)¶
Similar to
biosteam.units.Splitter, but can be initialized withqsdsan.SanStreamandqsdsan.WasteStream, and allows dynamic simulation.See also
- line: str = 'Splitter'¶
class-attribute Name denoting the type of Unit class. Defaults to the class name of the first child class
- run()¶
Run mass and energy balance. This method also runs specifications user defined specifications unless it is being run within a specification (to avoid infinite loops).
See also
_run,specifications,add_specification,add_bounded_numerical_specification
- property state¶
Component concentrations and total flow rate.