Oil-electricity co-production process using coal and natural gas as raw materials
A natural gas and raw material technology, applied in the field of oil-electricity cogeneration process, can solve the problems of increased investment cost, large energy consumption, and technical difficulty, so as to improve conversion rate and energy utilization rate, improve energy utilization rate, and realize The effect of thermal coupling
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Embodiment example 1
[0028] A kind of oil-electricity cogeneration process using coal and natural gas as raw material, its specific steps are as follows:
[0029] (1) Partial coal gasification unit
[0030] For the pulverized coal processed by a certain enterprise, its element analysis composition is as follows: C content 72.04%, H content 4.08%, O content 7.36%, N content 1.67%, S content 0.65%, other elements content 0.01%, ash content The content is 14.19%, and the low calorific value is 27.80MJ / kg. The feed rate is 3kg / s and sent to the gasifier. The temperature of the gasifier is 976.9°C and the pressure is 29bar. At the same time, medium-pressure steam with a temperature of 520°C and a pressure of 30 bar and oxygen with a pressure of 30 bar are passed into the gasification furnace as gasification agents for coal gasification reaction, wherein the molar ratio of water vapor to carbon content in coal powder is: 0.1, the molar ratio of oxygen and carbon content in coal powder is: 0.18; the tem...
Embodiment example 2
[0046] A kind of specific steps of oil-electricity cogeneration process using coal and natural gas as raw materials, same as implementation case 1, wherein:
[0047] In step (1), the pulverized coal is fed into the gasifier at a flow rate of 5kg / s, the temperature of the gasifier is 975.0°C, and the pressure is 29bar. At the same time, medium-pressure steam with a temperature of 520°C and a pressure of 30 bar and oxygen with a pressure of 30 bar are passed into the gasification furnace as gasification agents for coal gasification reaction, wherein the molar ratio of water vapor to carbon content in coal powder is: 0.12, the molar ratio of oxygen and carbon content in pulverized coal is: 0.2; the temperature of the generated crude syngas is 975°C, the pressure is 29bar, and the molar ratio of hydrogen to carbon monoxide is less than 2; ungasified residual coal Proceed to the next step.
[0048] In step (2), the ungasified residual coal in the gasifier of step (1) is sent into ...
Embodiment example 3
[0056] A kind of specific steps of oil-electricity cogeneration process using coal and natural gas as raw materials, same as implementation case 1, wherein:
[0057] In step (1), the pulverized coal is fed into the gasifier at a flow rate of 8kg / s, the temperature of the gasifier is 920.6°C, and the pressure is 29bar. At the same time, medium-pressure steam with a temperature of 520°C and a pressure of 30 bar and oxygen with a pressure of 30 bar are passed into the gasification furnace as gasification agents for coal gasification reaction, wherein the molar ratio of water vapor to carbon content in coal powder is: 0.4, the molar ratio of oxygen and carbon content in pulverized coal is: 0.25; the temperature of the generated crude syngas is 920.6°C, the pressure is 29bar, and the molar ratio of hydrogen to carbon monoxide is less than 2; ungasified residual coal Proceed to the next step.
[0058] In step (2), the ungasified residual coal in the gasifier of step (1) is sent int...
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