Sentence examples for stripper temperature from inspiring English sources

Stripper temperature profile shows that temperature swing is pronounced at the bottom, suggesting that CO2 desorption takes place more at the lower stages.

8 ml of sample with and without CO2 were introduced directly into the cylinder, placed in a Memmert 600 oven and heated at 135 °C, above the stripper temperature (to accelerate the reaction).

The outlet stream from the bottom of Stripper at temperature of 249 °C should be sent to distillation section to fractionalize.

While regeneration energy of aqueous amine increased with an increase in flue gas temperature and stripper pressure, it decreased with an increase in injection height of absorbent.

The riser and regenerator temperature, the stripper and regenerator pressure drop and the composition of the regenerator flue gas are measured on line and are used for verification of the ability of the simulator to predict the dynamic transients between steady states in both open- and closed-loop unit operation.

In the distillation section the temperature of stripper bottom stream had to be raised to 310 °C using distillation furnace.

The regeneration energy using 30 wt% MEA solution was 3.92 GJ/ton CO2 in 90% CO2 removal, flue gas temperature of 40 °C, stripper pressure of 0.5 kgf/cm2 and L/G ratio of 3.7 kg/Sm3.7

The case presented in this chapter consists of controlling the bottom level and the reboiler temperature of a stripper distillation column, which belongs to the naphtha hydrotreater (Hydrobon) plant located at REPSOL-YPF Plaza Huincul refinery.

From another perspective, if stripper pressure is higher, the temperature in the reboiler is also higher, and then higher pressure steam is required for solvent regeneration.

Thermal degradation occurs due to the high temperature in the stripper, and may also occur in the cross heat exchanger and the reclaimer, depending on the configuration [7, 8].

The process uses a high-temperature, high-pressure stripper (HPHTS) to separate the feed into a gas phase, which is hydrotreated with a WNiPd/Al2O, catalyst, and in a liquid phase which is hydrotreated with a WNiPd/TiO2Al2O3 catalyst.