This work presents new data to further develop the hydrate-based process for the separation of CH 4 from the low-concentration coal mine methane gas (30 mol % CH 4 /N 2 ) through the formation of tetra- n -butyl ammonium bromide (TBAB) semiclathrate hydrate. The TBAB semiclathrate hydrate formed from the 30 mol % CH 4 /N 2 gas mixture has more favorable equilibrium conditions than the gas hydrate formed from the same gas mixture. The incipient equilibrium conditions at 0.17, 0.29, and 0.62 mol % TBAB were experimentally determined and reported. The experiments of forming TBAB semiclathrate hydrate from the 30 mol % CH 4 /N 2 gas mixture were performed in both semibatch and batch operation under a fixed driving force of 3.5 MPa. The results indicate that CH 4 is preferentially encaged into the TBAB hydrate. The use of a 0.29 mol % TBAB solution is preferred over the 0.17 and 0.62 mol % TBAB solutions. The semibatch operation is more effective than the batch operation for the separation of CH 4 from the 30 mol % CH 4 /N 2 gas mixture. The CH 4 recovery was found to be approximately 25% at 0.29 mol % TBAB concentration in the semibatch operation and the corresponding CH 4 concentration released from the TBAB hydrate was nearly 43 mol %. A CH 4 -rich stream (70 mol % CH 4 /N 2 ) was obtained after two stages of TBAB semiclathrate hydrate formation.
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Zhong et al. (2012) studied this question.
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