solids_separation#
This module contains unit operations for the separation of solids (e.g. centrifugation, expression, filtration).
- class SolidsSeparator(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create SolidsSeparator object.
- Parameters:
ins (
Stream
], optional) – Inlet fluids with solids.outs (
Stream
], optional) –[0] Retentate.
[1] Permeate.
split (array_like) – Component splits to 0th output stream
moisture_content (float) – Fraction of water in solids
- class SolidsCentrifuge(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create a solids centrifuge that separates out solids according to user defined split. Capital cost is based on [1].
- Parameters:
ins (
Stream
], optional) – Inlet fluid with solids.outs (
Stream
], optional) –[0] Solids-rich stream.
[1] Liquid-rich stream.
order=None (Iterable[str]) – Species order of split. Defaults to Stream.chemicals.IDs.
moisture_content (float) – Fraction of water in stream.
centrifuge_type (str) – Type of the centrifuge, either ‘reciprocating_pusher’ (1-20 ton/hr solids) or ‘scroll_solid_bowl’ (2-40 ton/hr solids).
- class RotaryVacuumFilter(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create a RotaryVacuumFilter object.
- class PressureFilter(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create a pressure filter for the separation of structural carbohydrates, lignin, cell mass, and other solids. Capital costs are based on [2].
- Parameters:
ins (
Stream
], optional) – Contains structural carbohydrates, lignin, cell mass, and other solids.outs (
Stream
], optional) –[0] Retentate (i.e. solids)
[1] Filtrate
split (array_like or dict[str, float]) – Splits of chemicals to the retentate. Defaults to values used in the 2011 NREL report on cellulosic ethanol as given in [2].
moisture_content (float, optional) – Moisture content of retentate. Defaults to 0.35
- class ScrewPress(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create screw press unit operation for the expression of liquids from solids. Capital cost is based on [1].
References