Low-water-gas-ratio CO conversion device and low-water-gas-ratio CO conversion method
A technology for conversion device and water-gas ratio, applied in the direction of climate sustainability, catalytic treatment of combustible gas, sustainable manufacturing/processing, etc., can solve the problems of affecting the service life of the catalyst, difficult to control the depth of the reaction, large steam consumption, etc. , to achieve the effect of reducing subsequent system equipment and pipeline loads, flexible and convenient air volume adjustment, and avoiding over-temperature phenomenon
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Embodiment 1
[0039] The 484880kg / h crude synthesis gas (206℃, 3.84MPa, water-gas ratio: 0.91) from the upstream coal gasification unit enters the 1# gas-liquid separator for gas-liquid separation, and is divided into two streams. The first stream is on the pipeline A flow regulating valve is set to control the flow distribution ratio of the first stream and the second stream to be 6:4. After the first stream (flow rate is 290928kg / h) passes through the steam generator, the by-product is 92503kg / h hLow-pressure saturated steam (165°C, 0.5MPa), after the water-gas ratio of the crude synthesis gas is reduced to 0.24, it enters the 2# gas-liquid separator for gas-liquid separation, and the top gas phase is heated to 200°C by the feed gas heater, After passing through the 1# detoxification tank, it enters the 1# shift furnace for carbon monoxide shift reaction. The inlet temperature of the 1# shift furnace is 200°C, and the outlet temperature of the shift gas at the outlet of the 1# shift furnac...
Embodiment 2
[0041] The 484880kg / h crude synthesis gas (206℃, 3.84MPa, water-gas ratio: 0.91) from the upstream coal gasification unit enters the 1# gas-liquid separator for gas-liquid separation, and is divided into two streams. The first stream is on the pipeline A flow regulating valve is provided to control the flow distribution ratio of the first stream and the second stream to be 5:5. After the first stream (flow rate is 242440kg / h) passes through the steam generator, the by-product is 82146kg / h hLow-pressure saturated steam (165°C, 0.5MPa), after the water-gas ratio of the crude synthesis gas is reduced to 0.2, it enters the 2# gas-liquid separator for gas-liquid separation, and the top gas phase is heated to 225°C by the feed gas heater, After passing through the 1# detoxification tank, it enters the 1# shift furnace for carbon monoxide shift reaction. The inlet temperature of the 1# shift furnace is 225°C, and the outlet temperature of the shift gas at the outlet of the 1# shift fu...
Embodiment 3
[0043] The 484880kg / h crude synthesis gas (206℃, 3.84MPa, water-gas ratio: 0.91) from the upstream coal gasification unit enters the 1# gas-liquid separator for gas-liquid separation, and is divided into two streams. The first stream is on the pipeline A flow regulating valve is provided to control the flow distribution ratio of the first stream and the second stream to be 4:6. After the first stream (flow rate is 193952kg / h) passes through the steam generator, the by-product is 55218kg / h hLow-pressure saturated steam (165°C, 0.5MPa), after the water-gas ratio of the crude synthesis gas is reduced to 0.3, it enters the 2# gas-liquid separator for gas-liquid separation, and the top gas phase is heated to 260°C by the feed gas heater, After passing through the 1# detoxification tank, it enters the 1# shift furnace for carbon monoxide shift reaction. The inlet temperature of the 1# shift furnace is 260°C, and the outlet temperature of the shift gas at the outlet of the 1# shift fu...
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