# -*- coding: utf-8 -*-
# BioSTEAM: The Biorefinery Simulation and Techno-Economic Analysis Modules
# Copyright (C) 2020-2023, Yoel Cortes-Pena <yoelcortes@gmail.com>
#
# This module is under the UIUC open-source license. See
# github.com/BioSTEAMDevelopmentGroup/biosteam/blob/master/LICENSE.txt
# for license details.
"""
"""
from .splitting import Splitter
from .decorators import cost
__all__ = ('MolecularSieve',)
[docs]
@cost('Flow rate', 'Column', kW=151, BM=1.8,
cost=2601000, CE=521.9, S=22687, n=0.6)
class MolecularSieve(Splitter):
"""
Create an ethanol/water molecular sieve for bioethanol plants.
The molecular sieve is modeled as a component wise separator. Costing
is based on scaling by the 6/10ths rule from an NREL TEA report [1]_.
Parameters
----------
ins :
* [0] Feed (gas)
outs :
* [0] Split stream (gas)
* [1] Remainder stream (gas)
split : array_like
Componentwise split to the 0th output stream
Examples
--------
>>> from biosteam import Stream, settings
>>> from biosteam.units import MolecularSieve
>>> settings.set_thermo(['Water', 'Ethanol'], cache=True)
>>> feed = Stream('feed', flow=(75.7, 286), T=351.39, phase='g')
>>> bp = feed.bubble_point_at_T()
>>> feed.T = bp.T
>>> MS1 = MolecularSieve('MS1', ins=feed,
... outs=('ethanol_rich', 'water_rich'),
... split=dict(Water=0.160,
... Ethanol=0.925))
>>> MS1.simulate()
>>> MS1.show(T='degC', P='atm', composition= True)
MolecularSieve: MS1
ins...
[0] feed
phase: 'g', T: 78.24 degC, P: 1 atm
composition (%): Water 20.9
Ethanol 79.1
------- 362 kmol/hr
outs...
[0] ethanol_rich
phase: 'g', T: 78.24 degC, P: 1 atm
composition (%): Water 4.38
Ethanol 95.6
------- 277 kmol/hr
[1] water_rich
phase: 'g', T: 78.24 degC, P: 1 atm
composition (%): Water 74.8
Ethanol 25.2
------- 85 kmol/hr
>>> MS1.results()
Molecular sieve Units MS1
Electricity Power kW 14.2
Cost USD/hr 1.11
Low pressure steam Duty kJ/hr 3.21e+06
Flow kmol/hr 83
Cost USD/hr 19.7
Cooling water Duty kJ/hr -1.18e+05
Flow kmol/hr 80.9
Cost USD/hr 0.0395
Design Flow rate kg/hr 2.13e+03
Purchase cost Column USD 6.85e+05
Total purchase cost USD 6.85e+05
Utility cost USD/hr 20.9
References
----------
.. [1] Process Design and Economics for Biochemical Conversion of
Lignocellulosic Biomass to Ethanol Dilute-Acid Pretreatment and
Enzymatic Hydrolysis of Corn Stover. D. Humbird, R. Davis, L.
Tao, C. Kinchin, D. Hsu, and A. Aden (National Renewable Energy
Laboratory Golden, Colorado). P. Schoen, J. Lukas, B. Olthof,
M. Worley, D. Sexton, and D. Dudgeon (Harris Group Inc. Seattle,
Washington and Atlanta, Georgia)
"""
_units = {'Flow rate': 'kg/hr'}
def _init(self, split, order=None, P=None, approx_duty=True):
Splitter._init(self, order=order, split=split)
self.P = None
self.approx_duty = approx_duty
def _run(self):
Splitter._run(self)
P = self.P
if P is None: P = self.ins[0].P
for i in self.outs: i.P = P
def _design(self):
self.design_results['Flow rate'] = flow = self._outs[1].F_mass
if self.approx_duty:
T = self.outs[0].T
self.add_heat_utility(1429.65 * flow, T)
self.add_heat_utility(-55.51 * flow, T)
