Regen notebooks

CalebBell · CalebBell · commit 486536ac62bb · 2025-10-25T11:34:55.000-06:00
diff --git a/docs/Data/Friction.ipynb b/docs/Data/Friction.ipynb
diff --git a/docs/Data/Pipe Schedules.ipynb b/docs/Data/Pipe Schedules.ipynb
diff --git a/docs/Data/Sieve Sizes for Particle Size Distributions.ipynb b/docs/Data/Sieve Sizes for Particle Size Distributions.ipynb
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.1 Smooth Pipe (Plastic).ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.1 Smooth Pipe (Plastic).ipynb
@@ -27,8 +27,8 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      "Reynolds number = 101023.65443218236 dimensionless\n",
-      "Darcy friction factor = 0.01810798369184942 dimensionless\n"
+      "Reynolds number = 101022.58866016791 dimensionless\n",
+      "Darcy friction factor = 0.01810802221356977 dimensionless\n"
      ]
     }
    ],
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.11 Flat heating Coils - Water.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.11 Flat heating Coils - Water.ipynb
@@ -25,7 +25,7 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      "Pressure drop = 18501.7753353607 pascal\n"
+      "Pressure drop = 18501.926546734972 pascal\n"
      ]
     }
    ],
@@ -72,7 +72,7 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      "Pressure drop = 18539.73002741304 pascal\n"
+      "Pressure drop = 18539.503000119756 pascal\n"
      ]
     }
    ],
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.14 Bernoulli's Theorem-Water.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.14 Bernoulli's Theorem-Water.ipynb
@@ -26,13 +26,13 @@
     {
      "data": {
       "text/html": [
-       "262809.7611610049 pascal"
+       "262808.2444679967 pascal"
       ],
       "text/latex": [
-       "$262809.7611610049\\ \\mathrm{pascal}$"
+       "$262808.2444679967\\ \\mathrm{pascal}$"
       ],
       "text/plain": [
-       "262809.7611610049 <Unit('pascal')>"
+       "<Quantity(262808.2444679967, 'pascal')>"
       ]
      },
      "execution_count": 1,
@@ -99,13 +99,13 @@
     {
      "data": {
       "text/html": [
-       "262439.4308380222 pascal"
+       "262435.73531100823 pascal"
       ],
       "text/latex": [
-       "$262439.4308380222\\ \\mathrm{pascal}$"
+       "$262435.73531100823\\ \\mathrm{pascal}$"
       ],
       "text/plain": [
-       "262439.4308380222 <Unit('pascal')>"
+       "<Quantity(262435.73531100823, 'pascal')>"
       ]
      },
      "execution_count": 2,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.18 Gas.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.18 Gas.ipynb
@@ -65,7 +65,7 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      "According to the full isothermal equation, the flowrate is 103.434 MMscfd\n"
+      "According to the full isothermal equation, the flowrate is 103.434 dimensionless MMscfd\n"
      ]
     }
    ],
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.19 Water.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.19 Water.ipynb
@@ -46,7 +46,7 @@
        "$136.70828839615876\\ \\frac{\\mathrm{gallon}}{\\mathrm{minute}}$"
       ],
       "text/plain": [
-       "136.70828839615876 <Unit('gallon / minute')>"
+       "<Quantity(136.70828839615876, 'gallon / minute')>"
       ]
      },
      "execution_count": 1,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.23 Flow Through Orifice Meters.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.23 Flow Through Orifice Meters.ipynb
@@ -48,7 +48,7 @@
        "$105.73900650508152\\ \\frac{\\mathrm{gallon}}{\\mathrm{minute}}$"
       ],
       "text/plain": [
-       "105.73900650508152 <Unit('gallon / minute')>"
+       "<Quantity(105.73900650508152, 'gallon / minute')>"
       ]
      },
      "execution_count": 2,
@@ -74,8 +74,8 @@
     {
      "data": {
       "text/plain": [
-       "(0.6067029339232126 <Unit('dimensionless')>,\n",
-       " 0.6260667537160854 <Unit('dimensionless')>)"
+       "(<Quantity(0.6067029339232126, 'dimensionless')>,\n",
+       " <Quantity(0.6260667537160854, 'dimensionless')>)"
       ]
      },
      "execution_count": 3,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.24 Laminar Flow.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.24 Laminar Flow.ipynb
@@ -64,10 +64,10 @@
        "1947.5090707193106 dimensionless"
       ],
       "text/latex": [
-       "$1947.5090707193106\\ dimensionless$"
+       "$1947.5090707193106\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "1947.5090707193106 <Unit('dimensionless')>"
+       "<Quantity(1947.5090707193106, 'dimensionless')>"
       ]
      },
      "execution_count": 2,
@@ -112,10 +112,10 @@
        "1707.4277843809423 dimensionless"
       ],
       "text/latex": [
-       "$1707.4277843809423\\ dimensionless$"
+       "$1707.4277843809423\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "1707.4277843809423 <Unit('dimensionless')>"
+       "<Quantity(1707.4277843809423, 'dimensionless')>"
       ]
      },
      "execution_count": 3,
@@ -152,10 +152,10 @@
        "0.7156763185721802 dimensionless"
       ],
       "text/latex": [
-       "$0.7156763185721802\\ dimensionless$"
+       "$0.7156763185721802\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "0.7156763185721802 <Unit('dimensionless')>"
+       "<Quantity(0.7156763185721802, 'dimensionless')>"
       ]
      },
      "execution_count": 4,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.25 Rectangular Duct - Application of Hydraulic Radius to Flow Problems.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.25 Rectangular Duct - Application of Hydraulic Radius to Flow Problems.ipynb
@@ -102,7 +102,7 @@
        "$61407.46714336768\\ \\frac{\\mathrm{foot}^{3}}{\\mathrm{second}}$"
       ],
       "text/plain": [
-       "61407.46714336768 <Unit('foot ** 3 / second')>"
+       "<Quantity(61407.46714336768, 'foot ** 3 / second')>"
       ]
      },
      "execution_count": 3,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.26 Pipe Partially Filled with Flowing Water.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.26 Pipe Partially Filled with Flowing Water.ipynb
@@ -42,10 +42,10 @@
     {
      "data": {
       "text/plain": [
-       "(0.20670024467339204 <Unit('meter ** 2')>,\n",
-       " 1.1647220208174018 <Unit('meter')>,\n",
-       " 0.1774674480081778 <Unit('meter')>,\n",
-       " 0.7098697920327112 <Unit('meter')>)"
+       "(<Quantity(0.20670024467339204, 'meter ** 2')>,\n",
+       " <Quantity(1.1647220208174018, 'meter')>,\n",
+       " <Quantity(0.1774674480081778, 'meter')>,\n",
+       " <Quantity(0.7098697920327112, 'meter')>)"
       ]
      },
      "execution_count": 2,
@@ -80,7 +80,7 @@
        "$24410.948055443227\\ \\frac{\\mathrm{gallon}}{\\mathrm{minute}}$"
       ],
       "text/plain": [
-       "24410.948055443227 <Unit('gallon / minute')>"
+       "<Quantity(24410.948055443227, 'gallon / minute')>"
       ]
      },
      "execution_count": 3,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.28 Checking for Choked Flow Conditions in a Control Valve.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.28 Checking for Choked Flow Conditions in a Control Valve.ipynb
@@ -23,8 +23,8 @@
     {
      "data": {
       "text/plain": [
-       "(18.966081253330014 <Unit('pound_force_per_square_inch')>,\n",
-       " 70.8 <Unit('pound_force_per_square_inch')>)"
+       "(<Quantity(18.966081253330014, 'pound_force_per_square_inch')>,\n",
+       " <Quantity(70.8, 'pound_force_per_square_inch')>)"
       ]
      },
      "execution_count": 1,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.29 Orifice Flow Rate Calculation.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.29 Orifice Flow Rate Calculation.ipynb
@@ -29,7 +29,7 @@
        "$0.07366\\ \\mathrm{meter}$"
       ],
       "text/plain": [
-       "0.07366 <Unit('meter')>"
+       "<Quantity(0.07366, 'meter')>"
       ]
      },
      "execution_count": 1,
@@ -61,9 +61,9 @@
     {
      "data": {
       "text/plain": [
-       "(999.149354395164 <Unit('kilogram / meter ** 3')>,\n",
-       " 0.0011375132802133906 <Unit('pascal * second')>,\n",
-       " 1.329536639348325 <Unit('dimensionless')>)"
+       "(<Quantity(999.1352849261882, 'kilogram / meter ** 3')>,\n",
+       " <Quantity(0.001138094575222139, 'pascal * second')>,\n",
+       " <Quantity(1.329536639348325, 'dimensionless')>)"
       ]
      },
      "execution_count": 2,
@@ -88,8 +88,8 @@
      "name": "stdout",
      "output_type": "stream",
      "text": [
-      "7.704278611291563 kilogram / second\n",
-      "462.6502680946246 liter / minute\n"
+      "7.704252842651099 kilogram / second\n",
+      "462.65523551519385 liter / minute\n"
      ]
     }
    ],
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.30 Nozzle Sizing Calculations.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.30 Nozzle Sizing Calculations.ipynb
@@ -102,10 +102,10 @@
        "0.9839001432452787 dimensionless"
       ],
       "text/latex": [
-       "$0.9839001432452787\\ dimensionless$"
+       "$0.9839001432452787\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "0.9839001432452787 <Unit('dimensionless')>"
+       "<Quantity(0.9839001432452787, 'dimensionless')>"
       ]
      },
      "execution_count": 3,
@@ -133,7 +133,7 @@
        "$1.2691031722533113\\ \\mathrm{pound\\_force\\_per\\_square\\_inch}$"
       ],
       "text/plain": [
-       "1.2691031722533113 <Unit('pound_force_per_square_inch')>"
+       "<Quantity(1.2691031722533113, 'pound_force_per_square_inch')>"
       ]
      },
      "execution_count": 4,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.32 NPSH Available Calculation.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.32 NPSH Available Calculation.ipynb
@@ -32,7 +32,7 @@
        "$13.887316780096477\\ \\mathrm{foot}$"
       ],
       "text/plain": [
-       "13.887316780096477 <Unit('foot')>"
+       "<Quantity(13.887316780096477, 'foot')>"
       ]
      },
      "execution_count": 1,
@@ -77,7 +77,7 @@
        "$26.0\\ \\mathrm{foot}$"
       ],
       "text/plain": [
-       "26.0 <Unit('foot')>"
+       "<Quantity(26.0, 'foot')>"
       ]
      },
      "execution_count": 2,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.33 Pump Affinity Rules.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.33 Pump Affinity Rules.ipynb
@@ -24,9 +24,9 @@
     {
      "data": {
       "text/plain": [
-       "(194.28571428571428 <Unit('gallon / minute')>,\n",
-       " 29.725714285714286 <Unit('foot')>,\n",
-       " 2.0053061224489794 <Unit('horsepower')>)"
+       "(<Quantity(194.28571428571428, 'gallon / minute')>,\n",
+       " <Quantity(29.725714285714286, 'foot')>,\n",
+       " <Quantity(2.0053061224489794, 'horsepower')>)"
       ]
      },
      "execution_count": 1,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.6 Reduced Port Ball Valve.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.6 Reduced Port Ball Valve.ipynb
@@ -85,12 +85,12 @@
      "output_type": "stream",
      "text": [
       "Flow rate = 792.5474399133158 liter / minute\n",
-      "Flow rate = 748.2664116002655 liter / minute\n",
-      "Flow rate = 746.5628913428789 liter / minute\n",
-      "Flow rate = 746.4941928055326 liter / minute\n",
-      "Flow rate = 746.4914172120895 liter / minute\n",
-      "Flow rate = 746.491305062719 liter / minute\n",
-      "Flow rate = 746.4913005312487 liter / minute\n"
+      "Flow rate = 748.2591680181063 liter / minute\n",
+      "Flow rate = 746.5551120286623 liter / minute\n",
+      "Flow rate = 746.4863810741674 liter / minute\n",
+      "Flow rate = 746.4836037325604 liter / minute\n",
+      "Flow rate = 746.483491494833 liter / minute\n",
+      "Flow rate = 746.4834869590761 liter / minute\n"
      ]
     }
    ],
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.8 Laminar flow in Valves, Fittings, and Pipe - SAE oil through a pipe and globe valve.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.8 Laminar flow in Valves, Fittings, and Pipe - SAE oil through a pipe and globe valve.ipynb
@@ -32,7 +32,7 @@
        "$4575.571013232576\\ \\mathrm{pascal}$"
       ],
       "text/plain": [
-       "4575.571013232576 <Unit('pascal')>"
+       "<Quantity(4575.571013232576, 'pascal')>"
       ]
      },
      "execution_count": 1,
diff --git a/docs/Examples/Crane TP 410 Solved Problems/7.9 Laminar Flow in Valves, Fittings, and Pipe.ipynb b/docs/Examples/Crane TP 410 Solved Problems/7.9 Laminar Flow in Valves, Fittings, and Pipe.ipynb
@@ -26,8 +26,8 @@
     {
      "data": {
       "text/plain": [
-       "(26.063989664869815 <Unit('pound_force_per_square_inch')>,\n",
-       " 6.414177533606955 <Unit('foot / second')>)"
+       "(<Quantity(26.063989664869815, 'pound_force_per_square_inch')>,\n",
+       " <Quantity(6.414177533606955, 'foot / second')>)"
       ]
      },
      "execution_count": 1,
@@ -85,9 +85,9 @@
     {
      "data": {
       "text/plain": [
-       "(8.0 <Unit('dimensionless')>,\n",
-       " 150.0 <Unit('dimensionless')>,\n",
-       " 20.00000000000006 <Unit('dimensionless')>)"
+       "(<Quantity(8.0, 'dimensionless')>,\n",
+       " <Quantity(150.0, 'dimensionless')>,\n",
+       " <Quantity(20.00000000000006, 'dimensionless')>)"
       ]
      },
      "execution_count": 2,
@@ -110,10 +110,10 @@
        "29.991124449003742 dimensionless"
       ],
       "text/latex": [
-       "$29.991124449003742\\ dimensionless$"
+       "$29.991124449003742\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "29.991124449003742 <Unit('dimensionless')>"
+       "<Quantity(29.991124449003742, 'dimensionless')>"
       ]
      },
      "execution_count": 3,
@@ -139,7 +139,7 @@
        "$6.414177533606955\\ \\frac{\\mathrm{foot}}{\\mathrm{second}}$"
       ],
       "text/plain": [
-       "6.414177533606955 <Unit('foot / second')>"
+       "<Quantity(6.414177533606955, 'foot / second')>"
       ]
      },
      "execution_count": 4,
@@ -159,8 +159,8 @@
     {
      "data": {
       "text/plain": [
-       "(0.0381948926809522 <Unit('dimensionless')>,\n",
-       " 0.01543941031464228 <Unit('dimensionless')>)"
+       "(<Quantity(0.0381948926809522, 'dimensionless')>,\n",
+       " <Quantity(0.01543941031464228, 'dimensionless')>)"
       ]
      },
      "execution_count": 5,
@@ -190,10 +190,10 @@
        "1675.616699190696 dimensionless"
       ],
       "text/latex": [
-       "$1675.616699190696\\ dimensionless$"
+       "$1675.616699190696\\ \\mathrm{dimensionless}$"
       ],
       "text/plain": [
-       "1675.616699190696 <Unit('dimensionless')>"
+       "<Quantity(1675.616699190696, 'dimensionless')>"
       ]
      },
      "execution_count": 6,

Original file line number	Diff line number	Diff line change
`@@ -27,8 +27,8 @@`
`27`	`27`	`"name": "stdout",`
`28`	`28`	`"output_type": "stream",`
`29`	`29`	`"text": [`
`30`		`- "Reynolds number = 101023.65443218236 dimensionless\n",`
`31`		`- "Darcy friction factor = 0.01810798369184942 dimensionless\n"`
	`30`	`+ "Reynolds number = 101022.58866016791 dimensionless\n",`
	`31`	`+ "Darcy friction factor = 0.01810802221356977 dimensionless\n"`
`32`	`32`	`]`
`33`	`33`	`}`
`34`	`34`	`],`
Original file line number	Diff line number	Diff line change
`@@ -25,7 +25,7 @@`
`25`	`25`	`"name": "stdout",`
`26`	`26`	`"output_type": "stream",`
`27`	`27`	`"text": [`
`28`		`- "Pressure drop = 18501.7753353607 pascal\n"`
	`28`	`+ "Pressure drop = 18501.926546734972 pascal\n"`
`29`	`29`	`]`
`30`	`30`	`}`
`31`	`31`	`],`
`@@ -72,7 +72,7 @@`
`72`	`72`	`"name": "stdout",`
`73`	`73`	`"output_type": "stream",`
`74`	`74`	`"text": [`
`75`		`- "Pressure drop = 18539.73002741304 pascal\n"`
	`75`	`+ "Pressure drop = 18539.503000119756 pascal\n"`
`76`	`76`	`]`
`77`	`77`	`}`
`78`	`78`	`],`
Original file line number	Diff line number	Diff line change
`@@ -65,7 +65,7 @@`
`65`	`65`	`"name": "stdout",`
`66`	`66`	`"output_type": "stream",`
`67`	`67`	`"text": [`
`68`		`- "According to the full isothermal equation, the flowrate is 103.434 MMscfd\n"`
	`68`	`+ "According to the full isothermal equation, the flowrate is 103.434 dimensionless MMscfd\n"`
`69`	`69`	`]`
`70`	`70`	`}`
`71`	`71`	`],`
Original file line number	Diff line number	Diff line change
`@@ -46,7 +46,7 @@`
`46`	`46`	`"$136.70828839615876\\ \\frac{\\mathrm{gallon}}{\\mathrm{minute}}$"`
`47`	`47`	`],`
`48`	`48`	`"text/plain": [`
`49`		`- "136.70828839615876 <Unit('gallon / minute')>"`
	`49`	`+ "<Quantity(136.70828839615876, 'gallon / minute')>"`
`50`	`50`	`]`
`51`	`51`	`},`
`52`	`52`	`"execution_count": 1,`
Original file line number	Diff line number	Diff line change
`@@ -48,7 +48,7 @@`
`48`	`48`	`"$105.73900650508152\\ \\frac{\\mathrm{gallon}}{\\mathrm{minute}}$"`
`49`	`49`	`],`
`50`	`50`	`"text/plain": [`
`51`		`- "105.73900650508152 <Unit('gallon / minute')>"`
	`51`	`+ "<Quantity(105.73900650508152, 'gallon / minute')>"`
`52`	`52`	`]`
`53`	`53`	`},`
`54`	`54`	`"execution_count": 2,`
`@@ -74,8 +74,8 @@`
`74`	`74`	`{`
`75`	`75`	`"data": {`
`76`	`76`	`"text/plain": [`
`77`		`- "(0.6067029339232126 <Unit('dimensionless')>,\n",`
`78`		`- " 0.6260667537160854 <Unit('dimensionless')>)"`
	`77`	`+ "(<Quantity(0.6067029339232126, 'dimensionless')>,\n",`
	`78`	`+ " <Quantity(0.6260667537160854, 'dimensionless')>)"`
`79`	`79`	`]`
`80`	`80`	`},`
`81`	`81`	`"execution_count": 3,`