Device for separating and sequestering carbon dioxide in gas mixtures by hydrate method with coupled cold storage

A device for separating and sequestrating carbon dioxide in mixed gas by hydrate method coupled with cold storage, comprising:

• a gas separation system of the device is provided with a primary separation trunk circuit and two parallel separation branches, the primary separation trunk circuit is a biogas bottle, connected to a primary biogas refrigeration cycle heat exchanger by a primary gas compressor and then connected to a secondary biogas refrigeration cycle heat exchanger by a secondary gas compressor, and then connected in turn to a primary hydrate formation reactor and a primary hydrate decomposition reactor;
• said primary hydrate decomposition reactor is connected to the primary hydrate formation reactor via a primary hydrate pump and a primary hydrate heat exchanger;
• said primary biogas refrigeration cycle heat exchanger is connected to a primary biogas cooling tower for circulating heat exchange, and the secondary biogas refrigeration cycle heat exchanger is connected to a secondary biogas cooling tower for circulating heat exchange;
• the two parallel separation branches include a first branch and a second branch, the first branch is to recover carbon dioxide gas from the higher concentration methane separation gas, and the second branch is to purify the carbon dioxide gas from the primary hydrate decomposition gas;
• wherein the carbon dioxide gas is sequestered into gas hydrate in a porous medium through a sequestered gas compressor;
• the first branch is connected from the primary hydrate formation reactor through a secondary high concentration methane compressor, a secondary high concentration methane heat exchanger, a secondary high concentration methane hydrate formation reactor and a secondary high concentration methane hydrate decomposition reactor;
• the secondary high concentration methane hydrate decomposition reactor is connected to the secondary high concentration methane hydrate formation reactor via a methane hydrate decomposition water pump and a methane hydrate decomposition water heat exchanger;
• said secondary high concentration methane heat exchanger is connected to a secondary high concentration methane cooling tower for circulating heat exchange, and the methane hydrate decomposition water heat exchanger is connected to a methane hydrate decomposition water cooling tower for circulating heat exchange;
• the second branch is connected from the primary hydrate decomposition reactor through a secondary high concentration carbon dioxide compressor, a secondary high concentration carbon dioxide heat exchanger, a secondary high concentration carbon dioxide hydrate formation reactor and a secondary high concentration carbon dioxide hydrate decomposition reactor in that order;
• the secondary high concentration carbon dioxide hydrate decomposition reactor is connected to the secondary high concentration carbon dioxide hydrate formation reactor via a carbon dioxide hydrate decomposition water pump, a carbon dioxide hydrate decomposition water heat exchanger formation;
• said secondary high concentration carbon dioxide heat exchanger is in heat exchange cycle with a secondary high concentration carbon dioxide cooling tower, and the carbon dioxide hydrate decomposition water heat exchanger is in heat exchange cycle with a carbon dioxide hydrate decomposition water cooling tower.