In nearly all cases, the strength of low-dosage hydrate inhibitors (LDHIs) is evaluated by a comparison of the induction time. Since hydrate nucleation has a stochastic nature, measurement and correlation of the induction time are troublous and nonrepeatable. Thus, the development of new techniques to make the performance of LDHIs predictable and repeatable is necessary. This work aimed at employing the crystal growth inhibition (CGI) approach as a well-known repeatable technique to determine the complete inhibition region (CIR) of methane hydrate in the simultaneous attendance of triethylene glycol (TEG) as thermodynamic hydrate inhibitor (THI) and polyvinyl caprolactam (PVCap-7k) as LDHI. To determine the CIR, the hydrate dissociation measurements were carried out. For this purpose, two aqueous solutions of (0.46 wt % PVCap-7k + 15.00 wt % TEG), and (1.00 wt % PVCap-7k + 15.00 wt % TEG) were prepared. In the previous studies, the dissociation conditions of methane hydrate in the attendance of 0.10, 0.25, and 0.49 wt % of PVCap-7k were experimentally measured. To compare the inhibition impacts of TEG + PVCap-7k with PVCap-7k, the dissociation conditions of methane hydrate in the attendance of (1.00 wt % PVCap-7k) were also experimentally measured. Moreover, for thermodynamic modeling, a package including the van der Waals−Platteeuw (vdW-P) model for the hydrate phase, the Peng−Robinson (PR) equation of state (EoS) for the vapor-gas phase, and the Flory−Huggins (FH) model for the calculation of the water activity in an aqueous liquid phase was applied. It is concluded that the combined utilization of TEG and PVCap-7k results in a thermodynamic promotion impact on the methane hydrate. This is due to the strong thermodynamic promotion effect of PVCap that overcomes the thermodynamic inhibition impact of TEG. From the kinetic viewpoint, the combined utilization of TEG and PVCap-7k leads to a wide CIR (between 9 and 11.5 °C) which means a strong kinetic inhibition performance.