drying#
This module contains unit operations for drying solids.
- class DrumDryer(ID='', ins=None, outs=(), thermo=None, **kwargs)[source]#
Create a drum dryer that dries solids by passing hot air (heated by burning natural gas).
- Parameters:
ins (
Stream
], optional) –[0] Wet solids.
[1] Dry gas.
[2] Natural gas.
outs (
Stream
], optional) –[0] Dried solids
[1] Hot gas
[2] Emissions
split (dict[str, float]) – Component splits to hot gas (stream [1]).
R (float, optional) – Flow of hot gas over evaporation. Defaults to 1.4 wt gas / wt evap.
H (float, optional) – Specific evaporation rate [kg/hr/m3]. Defaults to 20.
length_to_diameter (float, optional) – Note that the drum is horizontal. Defaults to 25.
T (float, optional) – Operating temperature [K]. Defaults to 343.15.
moisture_content (float) – Moisture content of solids [wt / wt]. Defaults to 0.10.
Notes
The flow rate for gas in the inlet is varied to meet the R specification (i.e. flow of hot gas over flow rate evaporated). The flow rate of inlet natural gas is also altered to meet the heat demand.
The default parameter values are based on heuristics for drying dried distillers grains with solubles (DDGS).
Examples
>>> import biosteam as bst >>> from biorefineries import corn as c >>> bst.settings.set_thermo(c.create_chemicals()) >>> feed = bst.Stream('feed', phase='l', T=352.33, P=101325, ... Water=0.6749, Ethanol=5.041e-06, Ash=0.01978, Yeast=0.008452, ... CaO=0.0001446, TriOlein=0.02702, H2SO4=0.001205, Fiber=0.1508, ... SolubleProtein=0.04805, InsolubleProtein=0.06967, ... total_flow=32720, units='kg/hr', ... ) >>> dryer = bst.DrumDryer('D610', ... (feed, 'dryer_air', 'natural_gas'), ... ('dryed_solids', 'hot_air', 'emissions'), ... moisture_content=0.10, split=dict(Ethanol=1.0) ... ) >>> dryer.simulate() >>> dryer.show('cwt100') DrumDryer: D610 ins... [0] feed phase: 'l', T: 352.33 K, P: 101325 Pa composition (%): Water 67.5 Ethanol 0.000504 Ash 1.98 Yeast 0.845 CaO 0.0145 TriOlein 2.7 H2SO4 0.12 Fiber 15.1 SolubleProtein 4.8 InsolubleProtein 6.97 ---------------- 3.27e+04 kg/hr [1] dryer_air phase: 'g', T: 298.15 K, P: 1.01325e+06 Pa composition (%): O2 29.1 N2 70.9 -- 3.22e+04 kg/hr [2] natural_gas phase: 'g', T: 298.15 K, P: 101325 Pa composition (%): CH4 100 --- 1.11e+03 kg/hr outs... [0] dryed_solids phase: 'l', T: 343.15 K, P: 101325 Pa composition (%): Water 10 Ash 5.48 Yeast 2.34 CaO 0.04 TriOlein 7.48 H2SO4 0.334 Fiber 41.7 SolubleProtein 13.3 InsolubleProtein 19.3 ---------------- 1.18e+04 kg/hr [1] hot_air phase: 'g', T: 343.15 K, P: 1.01325e+06 Pa composition (%): Water 39.4 Ethanol 0.000311 O2 17.6 N2 43 ------- 5.31e+04 kg/hr [2] emissions phase: 'g', T: 373.15 K, P: 101325 Pa composition (%): Water 45 CO2 55 ----- 5.56e+03 kg/hr
>>> dryer.results() Drum dryer Units D610 Electricity Power kW 845 Cost USD/hr 66 Natural gas (inlet) Flow kg/hr 1.11e+03 Cost USD/hr 243 Design Evaporation kg/hr 2.09e+04 Volume 1.05e+03 Diameter m 3.76 Length 94 Peripheral drum area m2 1.11e+03 Purchase cost Drum dryer USD 1.2e+06 Total purchase cost USD 1.2e+06 Utility cost USD/hr 309
References