Sulfur Recovery Daily Question 2018.12.28
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Why is 0.3 MPa steam used for heating liquid sulfur pipelines? Answer: Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its flowability is best at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at a pressure of 0.3 MPa to heat the liquid sulfur pipelines can increase the flow rate of liquid sulfur in these pipelines, while also reducing energy losses caused by excessively high heating temperatures.
Liquid sulfur has low viscosity and the best flowability at temperatures between 130 and 160°C. The saturated vapor pressure of water at 143°C is 0.3 MPa; therefore, using steam at 0.3 MPa to heat the liquid sulfur pipelines ensures optimal flowability while also making efficient use of energy.
Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its fluidity is best at temperatures between 130 and 160°C; at 143°C, the saturated vapor pressure of water is 0.3 MPa
Liquid sulfur has low viscosity and the best flowability at temperatures between 130 and 160°C. The saturated vapor pressure of water at 143°C is 0.3 MPa; therefore, using steam at 0.3 MPa to heat the liquid sulfur pipelines ensures optimal flowability while also making efficient use of energy.
Liquid sulfur has low viscosity and the best flowability at temperatures between 130 and 160°C. The saturated vapor pressure of water at 143°C is 0.3 MPa; therefore, using steam at 0.3 MPa to heat the liquid sulfur pipelines ensures optimal flowability while also making efficient use of energy.
Answer: Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its flowability is best at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at a pressure of 0.3 MPa to heat the liquid sulfur pipelines can increase the flow rate of liquid sulfur in these pipelines, while also reducing energy losses caused by excessively high heating temperatures.
Liquid sulfur has low viscosity and the best flowability at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at 0.3 MPa to heat the liquid sulfur pipelines ensures optimal flowability, while also making efficient use of energy
Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its fluidity is best at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at a pressure of 0.3 MPa to heat the liquid sulfur pipelines can increase the flow rate of liquid sulfur within these pipelines, while also reducing energy losses caused by excessively high heating temperatures.
Low-temperature crystallization of liquid sulfur can easily cause pipeline blockages.
Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its flowability is best at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at a pressure of 0.3 MPa to heat the liquid sulfur pipelines can increase the flow rate within these pipelines
Based on the viscosity-temperature properties of liquid sulfur, its viscosity is low and its fluidity is best at temperatures between 130 and 160°C. At 143°C, the saturated vapor pressure of water is 0.3 MPa; therefore, using steam at a pressure of 0.3 MPa to heat the liquid sulfur pipelines can increase the flow rate of liquid sulfur within these pipelines, while also reducing energy losses caused by excessively high heating temperatures.