Table S1.
List of model parameters
Parameter | Unit | Description | Value | Source | |
Li–Rinzel model | |||||
rrel | s−1 | Maximal rate of Ca2+ release | 1.11 | (67) | |
rleak | s−1 | Maximal rate of Ca2+ leak | 0.02035 | (67) | |
vserca | µM·s−1 | Maximal rate of SERCA pumps | 0.9 | (67) | |
kserca | µM | Ca2+ affinity of SERCA pumps | 0.11 | Fitted, Fig. 2B | |
d1 | µM | Li–Rinzel model parameter | 0.13 | (67) | |
d2 | µM | Li–Rinzel model parameter | 1.049 | (67) | |
d3 | µM | Li–Rinzel model parameter | 0.9434 | (67) | |
d5 | µM | Li–Rinzel model parameter | 0.08234 | (67) | |
a2 | µM−1·s−1 | Li–Rinzel model parameter | 0.2 | (67) | |
α | — | Ratio between cytosol and ER volume | 0.185 | (67) | |
[Ca2+]TOT | µM | Total free Ca2+ concentration | 2 | (67) | |
IP3 subsystem | |||||
vPLC | µM·s−1 | Initial value of the maximal rate of IP3 production by PLC | 0.101 | Fitted, Fig. 2B | |
kPLC | µM | ATP dissociation constant | 0.038 | Fitted, Fig. 2B | |
nPLC | — | Hill exponent for ATP-dependent IP3 production | 0.28 | Fitted, Fig. 2B | |
s−1 | Rate of IP3 degradation | 0.13 | Fitted, Fig. 2B | ||
pu | µm3·s−1 | Unitary IP3 permeability of gap junction channels | 72 × 10−3 | (44) | |
V | µm3 | Cell volume | 3,900 | Fitted, Fig. 2B | |
Nch | — | No. channels between two adjacent supporting cells | 935 | Fitted, Fig. S2 and ref. 47 | |
A1 | s | time constant parameter | 1,313 | Fitted | |
A2 | µM−1 | time constant parameter | 0.97 | Fitted | |
A3 | s | time constant parameter | 46.66 | Fitted | |
ATP subsystem | |||||
s−1 | ATP degradation rate | 0.001–100 | Main text | ||
vHC | µM·s−1 | ATP maximal release rate | 0–2000 | Main text | |
D | µm2·s−1 | ATP diffusion coefficient | 363 | (74) | |
k1 | µM−1·s−1 | Hemichannel model constant | 10.619 | Fitted, Fig. 1C | |
k2 | µM−1·s−1 | Hemichannel model constant | 2.47 | Fitted, Fig. 1C | |
k−1 | s−1 | Hemichannel model constant | 3.4 | Fitted, Fig. 1C | |
k−2 | s−1 | Hemichannel model constant | 2.38 | Fitted, Fig. 1C | |
γ | — | Hemichannel model constant | 9 | Fitted, Fig. 1C |