Device and method for preparing methanol from synthesis gas by coupling with Kalina cycle
A Karina cycle and synthesis gas technology, applied in chemical instruments and methods, preparation of organic compounds, refrigeration and liquefaction, etc., can solve the problems of not considering the generation and utilization of heat, low energy utilization rate, and less waste heat, etc. , to achieve the effect of improving waste heat recovery and energy utilization efficiency
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment
[0026] The flow rate of the synthesis gas inlet stream is 11450 kmol / h, the temperature is 50°C, and the pressure is 51.2 bar. The feed contains 67.45% hydrogen, 22.97% carbon monoxide, 6.86% carbon dioxide, 0.23% water, and 2.48% nitrogen. The temperature of the second separator SE2 was 38°C. The reaction pressure, medium temperature and reactor inlet temperature of syngas to methanol are 74.6bar, 173.2°C and 123.7°C, respectively. The evaporation temperature, evaporation pressure, ammonia mass fraction and working fluid flow rate of the Karina cycle are 144.3℃, 68.5bar, 0.894 and 110.0kg / s, respectively.
[0027] By adopting the device and method of the present invention, the energy of producing methanol from synthesis gas can be utilized and recovered to the greatest extent. The net power production of the entire coupling design unit is 15206.3kW, which includes the power consumption of syngas to methanol and the power production of the Karina cycle.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 
