Source code for biosteam.facilities._process_water_center

# -*- 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.
"""
"""
import biosteam as bst
cost = bst.decorators.cost

__all__ = ('ProcessWaterCenter',)

[docs] @cost('Makeup water flow rate', 'Makeup water pump', CE=551, kW=20*0.7457, cost=6864, S=155564, n=0.8, BM=3.1) @cost('Process water flow rate', 'Process water pump', CE=551, kW=75*0.7457, cost=15292, S=518924, n=0.8, BM=3.1) @cost('Process water flow rate', 'Tank', CE=522, cost=250e3, S=451555, n=0.7, BM=1.7) class ProcessWaterCenter(bst.Facility): """ Create a ProcessWaterCenter object that takes care of balancing the amount of make-up process and reverse osmosis (RO) -grade water required for the process. The capital cost and power are based on the flow rate of process and make-up water as given in[1]_. Parameters ---------- ins : [0] Recycled RO-grade water. [1] Make-up RO-grade water. [2] Recycled process water. [3] Make-up process water. outs : [0] RO-grade water. [1] Process water. [2] Excess water. makeup_water_streams : List[Stream], optional All inlet RO-grade water streams. Defaults to boiler and cooling tower make-up water streams at run time. process_water_streams : List[Stream], optional All inlet process water streams (excluding makeup water streams). Defaults to all fresh process water streams within the system at run time. reverse_osmosis_water_price : float, optional Defaults to 5.6e-4 USD/kg. process_water_price : float, optional Defaults to 2.7e-4 USD/kg. Notes ----- Default prices for the RO-grade and process water are 0.56 and 0.27 USD/m3 as given in Table 17.1 of [2]_. References ---------- .. [1] Humbird, D., Davis, R., Tao, L., Kinchin, C., Hsu, D., Aden, A., Dudgeon, D. (2011). Process Design and Economics for Biochemical Conversion of Lignocellulosic Biomass to Ethanol: Dilute-Acid Pretreatment and Enzymatic Hydrolysis of Corn Stover (No. NREL/TP-5100-47764, 1013269). https://doi.org/10.2172/1013269 .. [2] Seider, W. D., Lewin, D. R., Seader, J. D., Widagdo, S., Gani, R., & Ng, M. K. (2017). Product and Process Design Principles. Wiley. Cost Accounting and Capital Cost Estimation (Chapter 16) """ ticket_name = 'PWC' network_priority = 2 _N_ins = 4 _N_outs = 3 _units = {'Makeup water flow rate': 'kg/hr', 'Process water flow rate': 'kg/hr'} def _init(self, makeup_water_streams=None, process_water_streams=None, reverse_osmosis_water_price=None, process_water_price=None ): if process_water_streams and makeup_water_streams: process_water_streams = list(process_water_streams) for i in makeup_water_streams: if i in process_water_streams: process_water_streams.remove(i) self.makeup_water_streams = makeup_water_streams self.process_water_streams = process_water_streams self.define_utility('Reverse osmosis water', self.makeup_reverse_osmosis_grade_water) self.define_utility('Process water', self.makeup_process_water) if reverse_osmosis_water_price: self.reverse_osmosis_water_price = reverse_osmosis_water_price if process_water_price: self.process_water_price = process_water_price @property def reverse_osmosis_water_price(self): """[Float] Price of reverse osmosis-grade water, same as `bst.stream_utility_prices['Reverse osmosis water']`.""" return bst.stream_utility_prices['Reverse osmosis water'] @reverse_osmosis_water_price.setter def reverse_osmosis_water_price(self, new_price): bst.stream_utility_prices['Reverse osmosis water'] = new_price @property def process_water_price(self): """[Float] Price of process water, same as `bst.stream_utility_prices['Process water']`.""" return bst.stream_utility_prices['Process water'] @process_water_price.setter def process_water_price(self, new_price): bst.stream_utility_prices['Process water'] = new_price @property def recycled_reverse_osmosis_grade_water(self): return self.ins[0] @property def makeup_reverse_osmosis_grade_water(self): return self.ins[1] @property def recycled_process_water(self): return self.ins[2] @property def makeup_process_water(self): return self.ins[3] @property def reverse_osmosis_grade_water(self): return self.outs[0] @property def process_water(self): return self.outs[1] @property def excess_water(self): return self.outs[2] def _assert_compatible_property_package(self): pass def update_process_water(self): process_water_streams = self.process_water_streams if process_water_streams is None: self.process_water_streams = process_water_streams = bst.get_fresh_process_water_streams() process_water = sum([stream.imol['7732-18-5'] for stream in process_water_streams]) self.process_water.imol['7732-18-5'] = process_water def update_reverse_osmosis_grade_water(self): makeup_water_streams = self.makeup_water_streams if makeup_water_streams is None: self.makeup_water_streams = makeup_water_streams = [ i.makeup_water for i in self.system.facilities if hasattr(i, 'makeup_water') ] self.reverse_osmosis_grade_water.imol['7732-18-5'] = sum([stream.imol['7732-18-5'] for stream in makeup_water_streams]) def _run(self): self.update_reverse_osmosis_grade_water() self.update_process_water() s_recycle_rev_os, s_rev_os_makeup, s_recycle_process, s_process_makeup = self._ins rrogw = s_recycle_rev_os.imol['7732-18-5'] rpw = s_recycle_process.imol['7732-18-5'] pw = self.process_water.imol['7732-18-5'] rogw = self.reverse_osmosis_grade_water.imol['7732-18-5'] mrogw = rogw - rrogw if mrogw >= 0.: s_rev_os_makeup.imol['7732-18-5'] = mrogw else: s_rev_os_makeup.imol['7732-18-5'] = 0. rpw -= mrogw # Unused RO-grade water is added to recycled process water mpw = pw - rpw if mpw >= 0.: s_process_makeup.imol['7732-18-5'] = mpw self.excess_water.imol['7732-18-5'] = 0. else: s_process_makeup.imol['7732-18-5'] = 0. self.excess_water.imol['7732-18-5'] = -mpw # Excess recycled water Design = self.design_results Design['Process water flow rate'] = ( self.excess_water.imol['7732-18-5'] + self.process_water.imol['7732-18-5'] ) * 18.015 Design['Makeup water flow rate'] = ( s_process_makeup.imol['7732-18-5'] ) * 18.015