SlideShare a Scribd company logo
Values of R (Gas Constant)
Value Units (V.P.T −1
.n−1
)
8.314 4621(75) J K−1
mol−1
5.189 × 1019 eV K−1
mol−1
0.082 057 46(14) L atm K−1
mol−1
1.985 8775(34) cal K−1 mol−1
1.985 8775(34) × 10−3 kcal K−1 mol−1
8.314 4621(75) × 107 erg K−1 mol−1
8.314 4621(75) L kPa K−1 mol−1
8.314 4621(75) m3 Pa K−1 mol−1
8.314 4621(75) cm3 MPa K−1 mol−1
8.314 4621(75) × 10−5 m3 bar K−1 mol−1
8.205 746 × 10−5 m3 atm K−1 mol−1
82.057 46 cm3 atm K−1 mol−1
84.784 02 × 10−6 m3 kgf/cm2 K−1 mol−1
8.314 4621(75) × 10−2 L bar K−1 mol−1
62.363 67(11) L mmHg K−1 mol−1
62.363 67(11) L Torr K−1 mol−1
6.132 440(10) ft lbf K−1 g-mol−1
1,545.348 96(3) ft lbf °R−1 lb-mol−1
10.731 59(2) ft3 psi °R−1 lb-mol−1
0.730 2413(12) ft3 atm °R−1 lb-mol−1
1.314 43 ft3 atm K−1 lb-mol−1
998.9701(17) ft3 mmHg K−1 lb-mol−1
1.986 Btu lb-mol−1
°R−1

More Related Content

What's hot

Distillation column design
Distillation column designDistillation column design
Distillation column designFaruk Eyigün
 
Ch 6- fugacidad mezcla
Ch 6- fugacidad mezclaCh 6- fugacidad mezcla
Ch 6- fugacidad mezclaGiovanni Hoyos
 
Fluidization and fluidized bed
Fluidization and fluidized bedFluidization and fluidized bed
Fluidization and fluidized bedRahat Inayat Ali
 
Chilton Colburn Analogy - Overall Concept
Chilton Colburn Analogy - Overall ConceptChilton Colburn Analogy - Overall Concept
Chilton Colburn Analogy - Overall ConceptSyedHameedAnwarSahib
 
Reactive distillation
Reactive distillationReactive distillation
Reactive distillationKarnav Rana
 
Chap 1(a) molecular-diffusion_in_gas(2)
Chap 1(a) molecular-diffusion_in_gas(2)Chap 1(a) molecular-diffusion_in_gas(2)
Chap 1(a) molecular-diffusion_in_gas(2)Charice Wan
 
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)Gas Absorption & Stripping in Chemical Engineering (Part 2/4)
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)Chemical Engineering Guy
 
Shell and tube heat exchanger
Shell and tube heat exchangerShell and tube heat exchanger
Shell and tube heat exchangerPaul singh
 
Fluidization and Fluidized Beds
Fluidization and Fluidized BedsFluidization and Fluidized Beds
Fluidization and Fluidized BedsAijaz Ali Mooro
 
Use and Applications of Membranes
Use and Applications of MembranesUse and Applications of Membranes
Use and Applications of MembranesGerard B. Hawkins
 
Processing of petroleum types of reflux
Processing of petroleum types of refluxProcessing of petroleum types of reflux
Processing of petroleum types of refluxKarnav Rana
 
Absorption and Stripping - mass transfer
Absorption and Stripping - mass transferAbsorption and Stripping - mass transfer
Absorption and Stripping - mass transfermegr1412
 
Excess gibbs free energy models
Excess gibbs free energy modelsExcess gibbs free energy models
Excess gibbs free energy modelsSunny Chauhan
 
Shell and tube heat exchanger
Shell and tube heat exchangerShell and tube heat exchanger
Shell and tube heat exchangerPraveen Sharma
 
Koushik sn assignment - leaching equipment (1)
Koushik sn   assignment - leaching equipment (1)Koushik sn   assignment - leaching equipment (1)
Koushik sn assignment - leaching equipment (1)KoushikS13
 

What's hot (20)

Distillation column design
Distillation column designDistillation column design
Distillation column design
 
Ch 6- fugacidad mezcla
Ch 6- fugacidad mezclaCh 6- fugacidad mezcla
Ch 6- fugacidad mezcla
 
Fluidization and fluidized bed
Fluidization and fluidized bedFluidization and fluidized bed
Fluidization and fluidized bed
 
Chilton Colburn Analogy - Overall Concept
Chilton Colburn Analogy - Overall ConceptChilton Colburn Analogy - Overall Concept
Chilton Colburn Analogy - Overall Concept
 
Survey of unit operations
Survey of unit operationsSurvey of unit operations
Survey of unit operations
 
Reactive distillation
Reactive distillationReactive distillation
Reactive distillation
 
Chap 1(a) molecular-diffusion_in_gas(2)
Chap 1(a) molecular-diffusion_in_gas(2)Chap 1(a) molecular-diffusion_in_gas(2)
Chap 1(a) molecular-diffusion_in_gas(2)
 
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)Gas Absorption & Stripping in Chemical Engineering (Part 2/4)
Gas Absorption & Stripping in Chemical Engineering (Part 2/4)
 
Shell and tube heat exchanger
Shell and tube heat exchangerShell and tube heat exchanger
Shell and tube heat exchanger
 
Fluidization and Fluidized Beds
Fluidization and Fluidized BedsFluidization and Fluidized Beds
Fluidization and Fluidized Beds
 
Single effect evaporation
Single effect evaporationSingle effect evaporation
Single effect evaporation
 
Che 412 cre 1 notes
Che 412 cre 1 notesChe 412 cre 1 notes
Che 412 cre 1 notes
 
Use and Applications of Membranes
Use and Applications of MembranesUse and Applications of Membranes
Use and Applications of Membranes
 
Classification of mass transfer processes
Classification of mass transfer processesClassification of mass transfer processes
Classification of mass transfer processes
 
Processing of petroleum types of reflux
Processing of petroleum types of refluxProcessing of petroleum types of reflux
Processing of petroleum types of reflux
 
Absorption and Stripping - mass transfer
Absorption and Stripping - mass transferAbsorption and Stripping - mass transfer
Absorption and Stripping - mass transfer
 
Excess gibbs free energy models
Excess gibbs free energy modelsExcess gibbs free energy models
Excess gibbs free energy models
 
Convective mass transfer
Convective mass transferConvective mass transfer
Convective mass transfer
 
Shell and tube heat exchanger
Shell and tube heat exchangerShell and tube heat exchanger
Shell and tube heat exchanger
 
Koushik sn assignment - leaching equipment (1)
Koushik sn   assignment - leaching equipment (1)Koushik sn   assignment - leaching equipment (1)
Koushik sn assignment - leaching equipment (1)
 

Gas constant

  • 1. Values of R (Gas Constant) Value Units (V.P.T −1 .n−1 ) 8.314 4621(75) J K−1 mol−1 5.189 × 1019 eV K−1 mol−1 0.082 057 46(14) L atm K−1 mol−1 1.985 8775(34) cal K−1 mol−1 1.985 8775(34) × 10−3 kcal K−1 mol−1 8.314 4621(75) × 107 erg K−1 mol−1 8.314 4621(75) L kPa K−1 mol−1 8.314 4621(75) m3 Pa K−1 mol−1 8.314 4621(75) cm3 MPa K−1 mol−1 8.314 4621(75) × 10−5 m3 bar K−1 mol−1 8.205 746 × 10−5 m3 atm K−1 mol−1 82.057 46 cm3 atm K−1 mol−1 84.784 02 × 10−6 m3 kgf/cm2 K−1 mol−1 8.314 4621(75) × 10−2 L bar K−1 mol−1 62.363 67(11) L mmHg K−1 mol−1 62.363 67(11) L Torr K−1 mol−1 6.132 440(10) ft lbf K−1 g-mol−1 1,545.348 96(3) ft lbf °R−1 lb-mol−1 10.731 59(2) ft3 psi °R−1 lb-mol−1 0.730 2413(12) ft3 atm °R−1 lb-mol−1 1.314 43 ft3 atm K−1 lb-mol−1 998.9701(17) ft3 mmHg K−1 lb-mol−1 1.986 Btu lb-mol−1 °R−1