In [1]:
import ThermoPyle as TP
from ThermoPyle import *
import matplotlib
import pandas as pd
import numpy as np
import matplotlib.pyplot as plt, mpld3
%matplotlib notebook
mpld3.enable_notebook()
In [60]:
%run ../scripts/der_CSV_gen.py --no-write
Iteration 0
Generating Initial Fluid Object.
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Iteration 1 of 124:
Calculating Column d(P)/d(G)|S
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Calculating Column d(U)/d(T)|G
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Calculating Column d(T)/d(D)|G
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Calculating Column d(U)/d(D)|S
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Calculating Column d(P)/d(D)|G
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Calculating Column d(G)/d(T)|S
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Calculating Column d(G)/d(U)|P
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Calculating Column d(U)/d(P)|G
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Calculating Column d(G)/d(T)|D
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Iteration 10 of 124:
Calculating Column d(G)/d(D)|U
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Calculating Column d(T)/d(S)|P
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Calculating Column d(D)/d(T)|G
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Calculating Column d(T)/d(D)|P
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Iteration 14 of 124:
Calculating Column d(S)/d(D)|P
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Calculating Column d(G)/d(S)|P
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Iteration 16 of 124:
Calculating Column d(P)/d(T)|D
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Calculating Column d(T)/d(G)|P
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Iteration 18 of 124:
Calculating Column d(T)/d(D)|S
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Iteration 19 of 124:
Calculating Column d(P)/d(G)|U
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Iteration 20 of 124:
Calculating Column d(U)/d(D)|T
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Calculating Column d(G)/d(T)|U
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Calculating Column d(G)/d(U)|T
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Calculating Column d(D)/d(P)|T
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Calculating Column d(T)/d(S)|D
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Calculating Column d(S)/d(U)|T
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Iteration 31 of 124:
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Iteration 42 of 124:
Calculating Column S
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Calculating Column d(G)/d(D)|T
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Iteration 48 of 124:
Calculating Column D
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Iteration 49 of 124:
Calculating Column d(T)/d(P)|S
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Calculating Column d(G)/d(S)|D
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Iteration 56 of 124:
Calculating Column PHASE
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Iteration 57 of 124:
Calculating Column d(D)/d(P)|S
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Iteration 59 of 124:
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Iteration 60 of 124:
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Iteration 61 of 124:
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Calculating Column d(T)/d(P)|G
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Iteration 65 of 124:
Calculating Column d(U)/d(G)|S
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Iteration 66 of 124:
Calculating Column d(T)/d(S)|U
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Iteration 67 of 124:
Calculating Column d(G)/d(D)|P
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Calculating Column d(T)/d(U)|S
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Iteration 69 of 124:
Calculating Column d(G)/d(D)|S
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Calculating Column d(S)/d(P)|T
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Calculating Column d(T)/d(G)|S
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Calculating Column d(G)/d(S)|U
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Calculating Column G
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Iteration 75 of 124:
Calculating Column d(T)/d(P)|D
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Calculating Column d(U)/d(D)|G
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Calculating Column d(D)/d(P)|G
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Calculating Column d(S)/d(U)|D
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Calculating Column d(P)/d(G)|T
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Calculating Column d(U)/d(T)|P
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Calculating Column d(D)/d(G)|P
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Calculating Column d(D)/d(U)|S
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Calculating Column d(U)/d(D)|P
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Calculating Column d(G)/d(T)|P
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Calculating Column d(S)/d(D)|T
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Calculating Column d(U)/d(S)|G
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Calculating Column d(G)/d(P)|U
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Calculating Column d(D)/d(G)|T
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Calculating Column d(D)/d(G)|U
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Calculating Column d(G)/d(U)|S
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Calculating Column d(P)/d(D)|S
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Calculating Column d(P)/d(U)|D
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Calculating Column d(P)/d(T)|G
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Calculating Column d(S)/d(D)|G
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Calculating Column d(P)/d(G)|D
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Calculating Column d(G)/d(U)|D
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Calculating Column d(U)/d(S)|P
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Calculating Column d(D)/d(T)|S
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Iteration 120 of 124:
Calculating Column d(U)/d(G)|D
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Iteration 121 of 124:
Calculating Column d(S)/d(U)|G
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Iteration 122 of 124:
Calculating Column d(D)/d(S)|T
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Iteration 123 of 124:
Calculating Column d(U)/d(P)|S
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Iteration 124 of 124:
Calculating Column d(G)/d(P)|S
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This Iteration: 0 hours, 0 minutes, 12.283 seconds
Time Elapsed: 0 hours, 23 minutes, 37.566 seconds
Total running time: 0 hours, 23 minutes, 37.876 seconds.
In [62]:
times = np.array(itertimes)
times[:,2].mean()
Out[62]:
11.293975878982417
In [82]:
Water = myfluid.copy()
In [83]:
Water.clean()
Water.refresh()
print("\n".join(Water.vars))
T
P
U
d(P)/d(G)|S
d(U)/d(T)|G
d(T)/d(D)|G
d(U)/d(D)|S
d(P)/d(D)|G
d(G)/d(T)|S
d(G)/d(U)|P
d(U)/d(P)|G
d(G)/d(T)|D
d(G)/d(D)|U
d(T)/d(S)|P
d(D)/d(T)|G
d(T)/d(D)|P
d(S)/d(D)|P
d(G)/d(S)|P
d(P)/d(T)|D
d(T)/d(G)|P
d(T)/d(D)|S
d(P)/d(G)|U
d(U)/d(D)|T
d(G)/d(T)|U
d(G)/d(U)|T
d(D)/d(P)|T
d(G)/d(P)|T
d(D)/d(U)|P
d(T)/d(S)|D
d(T)/d(S)|G
d(S)/d(U)|T
d(U)/d(S)|T
d(U)/d(G)|P
d(D)/d(P)|U
d(D)/d(U)|G
d(P)/d(D)|T
d(P)/d(U)|S
d(D)/d(T)|U
d(T)/d(U)|D
d(G)/d(S)|T
d(T)/d(U)|G
d(S)/d(G)|U
d(U)/d(P)|T
d(S)/d(T)|P
S
d(G)/d(D)|T
d(U)/d(T)|D
d(S)/d(T)|D
d(T)/d(D)|U
d(S)/d(P)|U
D
d(T)/d(P)|S
d(D)/d(U)|T
d(P)/d(S)|U
d(D)/d(T)|P
d(D)/d(S)|U
d(D)/d(S)|P
d(G)/d(S)|D
PHASE
d(D)/d(P)|S
d(S)/d(G)|D
d(T)/d(G)|U
d(U)/d(S)|D
d(S)/d(P)|G
d(P)/d(T)|U
d(T)/d(P)|G
d(T)/d(P)|U
d(U)/d(G)|S
d(T)/d(S)|U
d(G)/d(D)|P
d(T)/d(U)|S
d(G)/d(D)|S
d(D)/d(S)|G
d(S)/d(P)|T
d(T)/d(G)|S
d(G)/d(S)|U
G
d(T)/d(P)|D
d(U)/d(D)|G
d(D)/d(P)|G
d(S)/d(U)|D
d(P)/d(G)|T
d(U)/d(T)|P
d(P)/d(D)|U
d(P)/d(U)|G
d(T)/d(U)|P
d(S)/d(G)|P
d(D)/d(G)|P
d(D)/d(U)|S
d(U)/d(D)|P
d(P)/d(U)|T
d(S)/d(P)|D
d(U)/d(P)|D
d(G)/d(T)|P
d(S)/d(D)|T
d(U)/d(S)|G
d(G)/d(P)|U
d(D)/d(G)|T
d(D)/d(G)|U
d(G)/d(U)|S
d(S)/d(D)|U
d(P)/d(T)|S
d(S)/d(G)|T
d(P)/d(D)|S
d(P)/d(U)|D
d(P)/d(T)|G
d(S)/d(D)|G
d(S)/d(T)|U
d(G)/d(P)|D
d(U)/d(G)|T
d(D)/d(G)|S
d(S)/d(U)|P
d(U)/d(T)|S
d(T)/d(G)|D
d(P)/d(S)|T
d(P)/d(S)|D
d(P)/d(S)|G
d(S)/d(T)|G
d(P)/d(G)|D
d(G)/d(U)|D
d(U)/d(S)|P
d(D)/d(T)|S
d(U)/d(G)|D
d(S)/d(U)|G
d(D)/d(S)|T
d(U)/d(P)|S
d(G)/d(P)|S
In [81]:
Water.data["V"] = Water.M / Water.data["D"]
Water.vars.append("V")
Water.refresh()
Water.data
Out[81]:
T
P
U
d(P)/d(G)|S
d(U)/d(T)|G
d(T)/d(D)|G
d(U)/d(D)|S
d(P)/d(D)|G
d(G)/d(T)|S
d(G)/d(U)|P
...
d(P)/d(G)|D
d(G)/d(U)|D
d(U)/d(S)|P
d(D)/d(T)|S
d(U)/d(G)|D
d(S)/d(U)|G
d(D)/d(S)|T
d(U)/d(P)|S
d(G)/d(P)|S
V
0 rows × 128 columns
In [25]:
"{:.4E}".format((lambda x,y: x*y)(*Water.data.shape))
Out[25]:
'1.0221E+07'
In [37]:
Water.xvar = "P"
Water.yvar = "T"
Water.zvar = "D"
Water.refresh()
Water.clean()
TP.fluid_contour_plot(Water, "d(U)/d(S)|T")
In [85]:
Water.xvar = "P"
Water.yvar = "T"
Water.zvar = "d(U)/d(T)|P"
Water.refresh()
Water.clean()
TP.fluid_plot(Water, xvar="D", yvar="S", zvar="U", coloring="G")
In [14]:
Water.write_data(path="../finalData/", filename="with_ders_and_enthalpy", mode="dual")
In [58]:
print("\n".join([key for key in vars().keys()]))
__name__
__doc__
__package__
__loader__
__spec__
__builtin__
__builtins__
_ih
_oh
_dh
_sh
In
Out
get_ipython
exit
quit
_
__
___
_i
_ii
_iii
_i1
permutations
Any
Callable
ClassVar
Generic
Optional
Tuple
Type
TypeVar
Union
AbstractSet
GenericMeta
ByteString
Container
Hashable
ItemsView
Iterable
Iterator
KeysView
Mapping
MappingView
MutableMapping
MutableSequence
MutableSet
Sequence
Sized
ValuesView
Reversible
SupportsAbs
SupportsFloat
SupportsInt
SupportsRound
Counter
Deque
Dict
DefaultDict
List
Set
FrozenSet
NamedTuple
Generator
AnyStr
cast
get_type_hints
NewType
no_type_check
no_type_check_decorator
overload
Text
TYPE_CHECKING
Awaitable
Coroutine
AsyncIterable
AsyncIterator
Collection
ContextManager
ChainMap
AsyncGenerator
TP
json
deepcopy
randint
arrow
CP
plt
np
pd
matplotlib
cm
mlab
pyr
get
Axes3D
T
C
UNITS
ThermoFluid
CSVFluid
fluid_plot
rescale
fluid_contour_plot
mpld3
_i2
__nonzero__
timeit
argparse
make_Time
d_vars
newCols
parser
args
start
gstart
myfluid
gstop
numCols
i
col
istart
istop
stop
total_time
_i3
_3
_i4
_i5
_5
_i6
_i7
Water
_i8
_8
_i9
_9
_i10
_i11
_11
_i12
_i13
_i14
_i15
_15
_i16
_16
_i17
_17
_i18
_i19
_19
_i20
_i21
_i22
_22
_i23
_23
_i24
_24
_i25
_25
_i26
_i27
_i28
_i29
_i30
_i31
_i32
_i33
_i34
_i35
_i36
_i37
_i38
_i39
_i40
_i41
_i42
_i43
_i44
_i45
_i46
_i47
_i48
_i49
_49
_i50
_i51
_51
_i52
_52
_i53
_i54
_54
_i55
_55
_i56
_56
_i57
_i58
In [ ]:
Content source: nick5435/thermo-bridge
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