Sentence examples for bed reactor was designed from inspiring English sources

A mesophilic unsaturated flow (trickle bed) reactor was designed and tested for H2 production via fermentation of glucose.

A three-stage counter-current fluidized bed reactor was designed, fabricated and operated and range of stable operation for lime and sand particles has been determined.

In this study, a fluidized bed reactor was designed to modify FA by the fluidized bed reactor vapor deposition (FBR-VD), using NaOH solution as the activation material.

A conical spouted bed reactor was designed and tested for fast catalytic pyrolysis of miscanthus × giganteus over Zeolite Socony Mobil-5 (ZSM-5) catalyst, in the temperature range of 400 600 °C and catalyst to biomass ratios 1 1 5:1 1 5

To study the mechanism of SO2 and Hg removal from flue gas, an experimental packed bed reactor was designed to simulate the dry FGD, where a mixture of lime and fly ash in ratio 1 3 w/w was used as the SO2 and Hg sorbent, and steam at temperature of 100 °C was applied for activation of the sorbent, while the activation time set to 20 min.

In this research, a novel fixed-bed reactor was designed with a nanofiber membrane composed of a polyvinyl alcohol (PVA)/chitosan nanofiber blend prepared using an electrospinning technique.

A new fixed-bed reactor was designed to perform the reduction tests, along with the development of a mathematical model that considers reduction reactions, mass balance and energy equations for both gas and solid phases.

An up-flow fixed-bed reactor was designed for laboratory experiments in which a nitrosamine solvent stream along with hydrogen was passed into the reactor over a selected catalyst bed.

A novel two-stage fluidised-bed/fixed-bed reactor was designed to investigate the effects of volatile-char interactions on the volatilisation of alkali and alkaline earth metallic (AAEM) species during the pyrolysis of Victorian brown coal at 900 °C.

A novel flat-bed reactor was designed to measure the concentration profiles of the monolithic catalyst beds under different operation conditions: water-to-methanol mole ratio (W/M) between 1 and 1.5; oxygen-to-methanol mole ratio (O/M) in the range of 0.1 0.3; space velocity ranging from 1840 to 2890 h− 1; and reaction temperature in the scale of 400 440 °C.

For this purpose, a 1.47 L expanded granular sludge bed (EGSB) reactor was designed and run for 241 days treating artificial AMX manufacture wastewater.