Pwr Coolant Chemistry
Nuclear / pwr-coolant-chemistry.yamlatomic masses
- units
- g/mol
- e
- 0
- H
- 1.00794
- O
- 15.999
- B
- 10.81
- B10
- 10.0129
- Li
- 6.94
species
H2O
- index
- 1
- symbol
- H2O
- common name
- Water
- state
- liquid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 18.01588
lennard jones
- sigma m
- 2.6050e-10
- epsilon kB K
- 572.4
H2O_v
- index
- 2
- symbol
- H2O_v
- common name
- Water (vapour)
- state
- vapour
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 18.01588
B
- index
- 3
- symbol
- B
- common name
- Boron (natural)
- state
- liquid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 10.81
- nu B
- 1
B10
- index
- 4
- symbol
- B10
- common name
- Boron-10
- state
- liquid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 10.0129
- nu B
- 1
Li
- index
- 5
- symbol
- Li
- common name
- Lithium
- state
- liquid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 6.94
- nu Li
- 1
H3BO3
- index
- 6
- symbol
- H3BO3
- common name
- Boric acid
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 61.83282
- molar volume
- 0.03
- density
- 1.52
- melting temp K
- 458.15
- nu B
- 1
lennard jones
- sigma m
- 2.6050e-10
- epsilon kB K
- 572.4
H3BO3_v
- index
- 7
- symbol
- H3BO3_v
- common name
- Boric acid (vapour)
- state
- vapour
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 61.83282
- nu B
- 1
H4BO4-
- index
- 8
- symbol
- H4BO4-
- common name
- Tetrahydroxoborate
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 78.84076
- molar volume
- 0.03
- nu B
- 1
H5B2O6-
- index
- 9
- symbol
- H5B2O6-
- common name
- Pentahydroxodiborate
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 122.6497
- molar volume
- 0.06
- nu B
- 2
H4B3O7-
- index
- 10
- symbol
- H4B3O7-
- common name
- Tetrahydroxotriborate
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 148.46276
- molar volume
- 0.09
- nu B
- 3
H3B3O6
- index
- 11
- symbol
- H3B3O6
- common name
- Metaboric acid trimer
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 131.45882
- molar volume
- 0.09
- nu B
- 3
Li+
- index
- 12
- symbol
- Li+
- common name
- Lithium ion
- state
- liquid
- charge
- 1
- transport
- true
- reaction
- true
- molar mass
- 6.94
- molar volume
- 0.0025
- nu Li
- 1
LiOH
- index
- 13
- symbol
- LiOH
- common name
- Lithium hydroxide
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 23.93994
- density
- 1.51
- nu Li
- 1
LiBO2
- index
- 14
- symbol
- LiBO2
- common name
- Lithium metaborate
- state
- solid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 49.748
- density
- 1.4
- melting temp K
- 1,118.15
- nu B
- 1
- nu Li
- 1
B2O3
- index
- 15
- symbol
- B2O3
- common name
- Boron trioxide
- state
- solid
- charge
- 0
- transport
- false
- reaction
- false
- molar mass
- 69.617
- density
- 2.46
- melting temp K
- 723.15
- nu B
- 2
OH-
- index
- 16
- symbol
- OH-
- common name
- Hydroxide
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 17.00694
H+
- index
- 17
- symbol
- H+
- common name
- Proton
- state
- liquid
- charge
- 1
- transport
- true
- reaction
- true
- molar mass
- 1.00794
e-(aq)
- index
- 18
- symbol
- e-(aq)
- common name
- Solvated electron
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 0
H
- index
- 19
- symbol
- H
- common name
- Hydrogen radical
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 1.00794
OH
- index
- 20
- symbol
- OH
- common name
- Hydroxyl radical
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 17.00694
HO2
- index
- 21
- symbol
- HO2
- common name
- Hydroperoxyl radical
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 33.00594
HO2-
- index
- 22
- symbol
- HO2-
- common name
- Hydroperoxide
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 33.00594
O-
- index
- 23
- symbol
- O-
- common name
- Oxide radical anion
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 15.999
O2-
- index
- 24
- symbol
- O2-
- common name
- Superoxide
- state
- liquid
- charge
- -1
- transport
- true
- reaction
- true
- molar mass
- 31.998
O
- index
- 25
- symbol
- O
- common name
- Oxygen radical
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 15.999
H2O2
- index
- 26
- symbol
- H2O2
- common name
- Hydrogen peroxide
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 34.01388
O2
- index
- 27
- symbol
- O2
- common name
- Dissolved oxygen
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 31.998
lennard jones
- sigma m
- 3.4580e-10
- epsilon kB K
- 107.4
O2_v
- index
- 28
- symbol
- O2_v
- common name
- Oxygen (vapour)
- state
- vapour
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 31.998
H2
- index
- 29
- symbol
- H2
- common name
- Dissolved hydrogen
- state
- liquid
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 2.01588
- molar volume
- 0.09
- density
- 0.0899
lennard jones
- sigma m
- 2.9200e-10
- epsilon kB K
- 38
H2_v
- index
- 30
- symbol
- H2_v
- common name
- Hydrogen (vapour)
- state
- vapour
- charge
- 0
- transport
- true
- reaction
- true
- molar mass
- 2.01588
species units
- molar mass
- g/mol
- molar volume
- dm^3/mol
- density
- g/cm^3
- melting temp
- K
- lennard jones sigma
- m
- lennard jones epsilon kB
- K
pK correlations
- input variable
- TC [degC]
- model
- 4th-order polynomial in TC
H2O
coefficients (5)
14.93, -0.04131, 1.9030e-4, -4.7050e-7, 5.7240e-10
H
coefficients (5)
10.49, -0.04103, 1.4430e-4, -2.3250e-7, 2.0650e-10
OH
coefficients (5)
12.5, -0.03317, 1.9640e-4, -6.1980e-7, 8.2440e-10
H2O2
- note
- Identical coefficients to pK_OH — acceptable for now, may warrant independent fit in future
coefficients (5)
12.5, -0.03317, 1.9640e-4, -6.1980e-7, 8.2440e-10
HO2
coefficients (5)
4.917, -0.003813, 8.7710e-7, 2.1770e-7, -4.0000e-10
activity coefficients
gamma v
- description
- Activity coefficient for neutral species
- formula
- exp(1.6118 * (1 - exp(-I * 10^(-1.9826 + 0.00495*(T - 298.15)))))
coefficients
- outer prefactor
- 1.6118
- log10 exponent intercept
- -1.9826
- log10 exponent slope
- 0.00495
- T 0
- 298.15
gamma B
- description
- Boron activity coefficient as function of mole fraction xB
- formula
- 1.0 - 5.129*xB + 15.44*xB^2 - 23.77*xB^3
coefficients (4)
1, -5.129, 15.44, -23.77
gamma z
- description
- Charge-scaled activity coefficient
- formula
- gamma1^(z^2)
species assignment
- description
- Maps each species to gamma1 (ionic), gamma2 (neutral), or 1.0
gamma1 (6)
H4BO4-, H5B2O6-, H4B3O7-, Li+, OH-, H+
gamma2 (2)
H3BO3, H3B3O6
unity (3)
LiOH, LiBO2, H2
water activity
aw from xB
- formula
- 1.0 - 1.11277 * xB
- coefficient
- 1.11277
aw from molality
- formula
- mw / (mw + Sigma_m)
- mw
- 0.01801528
aw from concentrations
- formula
- mw / (mw + Sigma_c / (rho_l * zeta))
species summed (7)
H3BO3, H4BO4-, H5B2O6-, H4B3O7-, H3B3O6, Li+, H2
aw pressure correction
- formula
- aw0 * exp(V_molar * (P - P0) / (R * T))
integral Vl atm
- formula
- (P_atm - P0_atm) * 1.8254 / rho_l
- coefficient
- 1.8254
- units
- J/mol
ionic strength
- formula
- 0.5 * sum(m_i * z_i^2)
charged species (6)
#1
- species
- H4BO4-
- z
- -1
#2
- species
- H5B2O6-
- z
- -1
#3
- species
- H4B3O7-
- z
- -1
#4
- species
- Li+
- z
- 1
#5
- species
- OH-
- z
- -1
#6
- species
- H+
- z
- 1
volume fraction
zeta from SigmacVm
- formula
- 1 - (SigmacVm / (rho_l * (1 - SigmacVm)))
zeta from SigmamVm
- formula
- 1 - SigmamVm
precipitation
fp 1
- description
- LiBO2 precipitation factor
- formula
- exp(-1.0e-10 / (c + 1.0e-13))
coefficients
- numerator
- -1.0000e-10
- offset
- 1.0000e-13
fp 2
- description
- Inverse of fp_1
- formula
- -(1.0e-13) - (1.0e-10) / ln(f)
saturation index
SI 1
- formula
- log10((gamma2 * ct * x1 * x3) / (Kp * rho * aw * c7))
SI 2
- formula
- log10((gamma2 * x1 * x3) / (Kp * rho * aw * x7))
rate constants
Dalpha 1
- description
- Alpha dose rate from B-10
- formula
- 5.647e-12 * phi * B / rho
- coefficient
- 5.6470e-12
kG 1
- description
- G-value source term
- formula
- 1000 * ((Gamma_gamma*G_gamma) + (Gamma_n*G_n) + (Gamma_alpha*G_alpha)) * 6.25e13 * rho / (100 * Na)
coefficients
- factor eV conversion
- 6.2500e+13
- Na
- 6.0221e+23
kR rd48 30
- description
- Arrhenius rate constant
- formula
- 1.4096e5 * exp(-Ea / (R * T))
- A
- 140,960
- Ea J mol
- 14,800
- R
- use canonical R = 8.314462618 J/(mol*K)
- note
- CORRECTED: Simu.jl source hardcoded R = 8.1345 in the formula, which is incorrect. The gas constant R = 8.314462618 J/(mol*K) (defined in constants.jl) should be used. Ea = 14800 J/mol is unchanged.
kR 23b
- model
- poly_T3
- formula
- A0 + A1/T + A2/T^2 + A3/T^3 + A4/T^4
coefficients (5)
20.934, -12,360, 6.3640e+6, -1.4750e+9, 1.2370e+11
kR 23
- model
- poly_TC4
- formula
- A0 + A1*TC + A2*TC^2 + A3*TC^3 + A4*TC^4
coefficients (5)
6.6200e+10, 1.4800e+9, 1.2800e+7, -60,300, 128
kR 29
- model
- poly_TC4
coefficients (5)
7.2200e+9, 1.6200e+8, 2.4000e+6, -7,810, 10.6
kR 30
- model
- poly_TC4
coefficients (5)
3.4100e+10, 2.7500e+8, 1.2400e+7, -62,300, 131
conversions
ppm to molarity
- formula
- ppm * 1.0e-6 * density / molar_mass
gas volume to molarity
- formula
- (cc_per_kg / 22414.0) * density
- STP molar volume cc
- 22,414
l1
- description
- Primary liquid-phase diffusion models
boron species
- model
- D_Stokes_Einstein_scaling
- group
- effective
- note
- No stored D0 — requires runtime T, mu, T_ref, mu_ref, D_ref
species (5)
H3BO3, H4BO4-, H5B2O6-, H4B3O7-, H3B3O6
Li plus
- model
- poly_e_A5
- group
- effective
- formula
- A[0] * exp(A[1] + A[2]/T + A[3]/T^2 + A[4]/T^3)
coefficients (5)
1.0000e-4, -6.881, -716.5, 152,100, -3.8100e+7
species (2)
Li+, LiOH
OH minus
- model
- poly_10_A5
- group
- effective
- formula
- A[0] * 10^(A[1] + A[2]/T + A[3]/T^2 + A[4]/T^3)
coefficients (5)
1.0000e-9, 3.324, -1,729, 589,000, -9.1880e+7
species (1)
OH-
H plus
- model
- poly_10_A5
- group
- effective
coefficients (5)
1.0000e-9, 2.672, -984.7, 330,600, -5.6210e+7
species (1)
H+
e aq
- model
- poly_e_A3
- group
- liquid
- formula
- A[0] * exp(A[1]/T + A[2])
coefficients (3)
2.4750e-8, -925, -95
species (1)
e-(aq)
H radical
- model
- poly_e_A3
- group
- liquid
coefficients (3)
3.8500e-8, -925, -95
species (1)
H
OH radical
- model
- poly_e_A3
- group
- liquid
coefficients (3)
1.5375e-8, -925, -95
species (1)
OH
HO2
- model
- poly_e_A3
- group
- liquid
coefficients (3)
1.1000e-8, -925, -95
species (1)
HO2
HO2 minus
- model
- poly_10_A5
- group
- liquid
coefficients (5)
1.0000e-8, 4.311, -2,722, 856,500, -1.1810e+8
species (1)
HO2-
O2 minus
- model
- poly_e_A3
- group
- liquid
coefficients (3)
9.6250e-9, -925, -95
species (1)
O2-
H2O2
- model
- poly_e_A3
- group
- liquid
coefficients (3)
1.2125e-8, -925, -95
species (1)
H2O2
O2
- model
- k_Arrhenius
- group
- liquid
- formula
- A * exp(-Ea/(R*T))
- Ea J mol
- 14,603
- A m2 s
- 8.0300e-7
species (1)
O2
H2
- model
- poly_e_A4
- group
- liquid
- formula
- A[0] * exp(A[1] + A[2]/T + A[3]/T^2)
coefficients (4)
1.0000e-4, -5.700267, -296.7439, -288,379.2
species (1)
H2
l2
- description
- Stokes-Einstein scaling from reference D0 at 298.15 K
- model
- D_Stokes_Einstein_scaling
- T ref K
- 298.15
entries (10)
#1
- species
- OH-
- group
- effective
- D0 m2 s
- 5.3000e-9
#2
- species
- H+
- group
- effective
- D0 m2 s
- 9.3000e-9
#3
- species
- e-(aq)
- group
- liquid
- D0 m2 s
- 4.8200e-9
#4
- species
- H
- group
- liquid
- D0 m2 s
- 7.0000e-9
#5
- species
- OH
- group
- liquid
- D0 m2 s
- 2.2000e-9
#6
- species
- HO2
- group
- liquid
- D0 m2 s
- 2.3000e-9
#7
- species
- O2-
- group
- liquid
- D0 m2 s
- 1.7500e-9
#8
- species
- H2O2
- group
- liquid
- D0 m2 s
- 2.3000e-9
#9
- species
- O2
- group
- liquid
- D0 m2 s
- 2.4000e-9
#10
- species
- H2
- group
- liquid
- D0 m2 s
- 4.8000e-9
l3
- description
- Alternative polynomial and Arrhenius fits
OH minus
- model
- poly_A4
- group
- effective
- formula
- A[0] + A[1]*T + A[2]*T^2 + A[3]*T^3
coefficients (4)
2.6660e-9, 9.7690e-11, 3.3030e-13, -7.2950e-16
species (1)
OH-
H plus
- model
- poly_A4
- group
- effective
coefficients (4)
5.3610e-9, 1.6590e-10, -7.4800e-14, -1.0018e-16
species (1)
H+
H2O2
- model
- k_Arrhenius
- group
- liquid
- Ea J mol
- 14,603
- A m2 s
- 8.0300e-7
species (1)
H2O2
H2
- model
- poly_e_A4
- group
- liquid
coefficients (4)
1.0000e-4, -5.700267, -296.7439, -288,379.2
species (1)
H2
H2O
- model
- poly_A7
- group
- liquid
- formula
- A[0] + A[1]*T + A[2]*T^2 + ... + A[6]*T^6
coefficients (7)
1.0704e-9, 4.7082e-11, -1.2633e-14, 5.0605e-15, 2.3048e-17, 2.9217e-20, 1.3128e-23
species (1)
H2O
l4
- description
- Arrhenius scaling from reference temperature
- model
- k_Arrhenius_scaling
- formula
- k0 * exp(-(Ea/R)*(1/T - 1/T_ref))
- T ref K
- 298.15
entries (2)
#1
- species
- H+
- group
- effective
- Ea J mol
- 12,000
- k0 m2 s
- 1.0000e-8
#2
- species
- OH-
- group
- effective
- Ea J mol
- 12,000
- k0 m2 s
- 5.0000e-9
l5
- description
- Linear interpolation between T_min and T_max for PWR conditions
- model
- poly_min_max
- note
- D linearly interpolated between (T_min, D_min) and (T_max, D_max)
entries (5)
#1
- species
- H3BO3
- group
- effective
- T min K
- 590
- T max K
- 670
- D min m2 s
- 1.5600e-8
- D max m2 s
- 2.1000e-8
#2
- species
- H4BO4-
- group
- effective
- T min K
- 590
- T max K
- 670
- D min m2 s
- 1.7100e-8
- D max m2 s
- 2.3100e-8
#3
- species
- Li+
- group
- effective
- T min K
- 590
- T max K
- 670
- D min m2 s
- 3.7200e-8
- D max m2 s
- 4.1500e-8
#4
- species
- H+
- group
- effective
- T min K
- 590
- T max K
- 670
- D min m2 s
- 1.5800e-7
- D max m2 s
- 2.2100e-7
#5
- species
- OH-
- group
- effective
- T min K
- 590
- T max K
- 670
- D min m2 s
- 9.1300e-8
- D max m2 s
- 1.2800e-7
v1
- description
- Chapman-Enskog vapour diffusion with Lennard-Jones parameters
- model
- Dv
- formula
- D = (3/16) * sqrt(2*pi*kB*T/M) / (Na * P * sigma^2 * Omega_D)
- Omega D fit
- 1.06036 / T_star^0.15610
constants
- kB
- 1.3806e-23
- NA
- 6.0221e+23
entries (3)
#1
- species
- H3BO3
- epsilon kB K
- 572.4
- sigma m
- 2.6050e-10
- M g mol
- 61.83282
#2
- species
- O2
- epsilon kB K
- 107.4
- sigma m
- 3.4580e-10
- M g mol
- 31.998
#3
- species
- H2
- epsilon kB K
- 38
- sigma m
- 2.9200e-10
- M g mol
- 2.01588
vapour diffusion units
- D
- m^2/s
- T
- K
- Ea
- J/mol
gamma correlations
- units
- molecules/100eV
- input variable
- TC [degC]
e aq
- intercept
- 2.56
- slope
- 0.0034
OH
- intercept
- 2.64
- slope
- 0.00717
H2
- intercept
- 0.43
- slope
- 6.9000e-4
H2 plus H
- intercept
- 0.97
- slope
- 0.00198
H
- intercept
- 0.54
- slope
- 0.00128
H2O2
- intercept
- 0.72
- slope
- -0.00149
H2O2 alt
- intercept
- 0.66
- slope
- -5.5000e-4
sets
G1
OH- (3)
0.01, 0, 0
H+ (3)
2.76, 0, 0
e aq (3)
2.66, 0.61, 0.06
H (3)
0.55, 0.34, 0.21
OH (3)
2.67, 2.02, 0.24
HO2 (3)
0, 0.05, 0.22
H2O2 (3)
0.72, 0.65, 0.985
H2 (3)
0.45, 1.26, 1.3
G2
e aq (3)
3.54, 0.65, 0.15
H (3)
0.87, 0.46, 0.2
OH (3)
4.51, 2, 1.13
HO2 (3)
0, 0.05, 0
H2O2 (3)
0.55, 0.65, 1.12
H2 (3)
0.6, 1.17, 1.96
G3
H+ (3)
3.6, 0.65, 0.05
e aq (3)
3.6, 0.65, 0.05
H (3)
0.8, 0.3, 0.16
OH (3)
5, 2, 0.56
H2O2 (3)
0.35, 0.7, 1.43
H2 (3)
0.65, 1.225, 1.605
G4
H+ (3)
3.207, 0.13, 0.05
e aq (3)
3.207, 0.13, 0.05
H (3)
0.9814, 0.53, 0.16
OH (3)
5.111, 1.6, 0.56
H2O2 (3)
0.2065, 1.2, 1.43
H2 (3)
0.6678, 1.67, 1.605
G5
- note
- Alpha-only yields
OH (3)
0, 0, 0.8
H2O2 (3)
0, 0, 1.2
H2 (3)
0, 0, 1.605
g value set units
- g values
- molecules/100eV
- columns
- [gamma, neutron, alpha]
distribution coefficients
- units
- bar*dm^3/mol
- input variable
- TC [degC]
- model
- poly_10_A6
- formula
- 10^(a0 + a1*TC + a2*TC^2 + a3*TC^3 + a4*TC^4 + a5*TC^5)
H3BO3
coefficients (6)
-3.72722, 0.0251402, -1.1191e-4, 3.6020e-7, -7.3823e-10, 6.3139e-13
O2
coefficients (6)
6.37388, -0.0148058, 0, 0, 0, 0
H2
coefficients (6)
6.94554, -0.0262353, 6.8026e-5, -1.9720e-7, 3.8252e-10, -3.7118e-13
solubility
- units
- mol/(kg*bar)
- input variable
- T [K]
- reference
- Henshaw et al. (2002)
O2
- formula
- exp(-146.819 + 7453.009/T + 20.2112*ln(T))
coefficients
- A
- -146.819
- B
- 7,453.009
- C
- 20.2112
H2
- formula
- exp(-104.288 + 4804.235/T + 14.2283*ln(T))
coefficients
- A
- -104.288
- B
- 4,804.235
- C
- 14.2283
henry
simple
- formula
- -9.01e4 + 5.83e7/T
- input variable
- T [K]
- units
- atm/mole_fraction
- reference
- EPRI (2006)
coefficients
- A
- -90,100
- B
- 5.8300e+7
partitioning conversions
Klv from Dlv
- formula
- 100.0 * Dlv / (R * T)
- description
- Convert Dlv [bar*dm^3/mol] to dimensionless Klv
D Boron 25C
- value
- 1.5600e-9
- units
- m^2/s
- description
- Boric acid diffusion coefficient at 25 degC in water
reference concentration units
mol/dm^3
studies
Park
- H3BO3
- 0.09897
- H4BO4-
- 0.01186
- H5B2O6-
- 8.3000e-5
- H4B3O7-
- 1.3170e-8
- H3B3O6
- 1.3470e-10
- Li+
- 2.0000e-4
- OH-
- 2.9400e-5
- H+
- 4.1700e-8
- e aq
- 7.4000e-8
- H
- 3.8700e-7
- OH
- 3.5700e-8
- HO2
- 2.9600e-11
- HO2-
- 9.6400e-8
- O-
- 2.5200e-9
- O2-
- 4.3500e-9
- O
- 7.1700e-9
- H2O2
- 5.0900e-8
- O2
- 5.9800e-11
- H2
- 7.5900e-4
Botani
- H3BO3
- 0.004138
- H4BO4-
- 2.5700e-5
- Li+
- 8.1100e-5
- OH-
- 2.9400e-5
- H+
- 4.1700e-8
Henshaw
- H3BO3
- 0.0762
- Li+
- 1.8200e-4
- H+
- 2.1880e-8
- OH
- 9.5520e-9
- H2O2
- 2.0980e-8
- H2
- 3.3370e-4
Mac06
- OH-
- 0.00294
- H+
- 4.1700e-6
- e aq
- 7.4000e-6
- H
- 3.8700e-5
- OH
- 3.5700e-6
- HO2
- 2.9600e-9
- HO2-
- 9.6400e-6
- O-
- 2.5200e-7
- O2-
- 4.3500e-7
- O
- 7.1700e-7
- H2O2
- 5.0900e-6
- O2
- 6.8200e-8
- H2
- 0.0759
Mac22
- H3BO3
- 0.09
- H4BO4-
- 1.0000e-4
- H5B2O6-
- 3.0000e-5
- H4B3O7-
- 1.5000e-6
- Li+
- 1.5000e-4
- OH-
- 2.0000e-5
- H+
- 1.0000e-7
- e aq
- 8.0000e-6
- H
- 2.0000e-8
- OH
- 9.0000e-8
- HO2
- 6.0000e-11
- HO2-
- 1.0000e-10
- O2-
- 8.0000e-9
- H2O2
- 5.0000e-8
- O2
- 5.0000e-13
- H2
- 9.0000e-4
Joe
- H3BO3
- 8.3300e-8
- H2O2
- 7.4500e-4
- O2
- 1.7600e-4
- H2
- 7.0500e-4