Structure Responses of n-Heptane/Air Counterflow Flames to Air-Side Partial Premixing of Dimethyl Ether

2019 ◽  
Vol 33 (7) ◽  
pp. 6754-6766
Author(s):  
Xiaoqin Lu ◽  
Ge Hu ◽  
Yituan He ◽  
Shiyong Liao ◽  
Xiaochun Jian ◽  
...  
Fuel ◽  
2018 ◽  
Vol 234 ◽  
pp. 974-984 ◽  
Author(s):  
Yanzhen Li ◽  
Ge Hu ◽  
Shiyong Liao ◽  
Chun Yuan ◽  
Yong zhang

2009 ◽  
Vol 23 (7) ◽  
pp. 1885-1892 ◽  
Author(s):  
Tae-Hyun Kim ◽  
Jong-Min Kim ◽  
Cheol-Hong Hwang ◽  
Sung-Min Kum ◽  
Chang-Eon Lee

2005 ◽  
Vol 128 (4) ◽  
pp. 361-367 ◽  
Author(s):  
Hemant P. Mungekar ◽  
Arvind Atreya

Motivated by heat transfer and environmental concerns, a study of flame radiation and soot particulate emission is reported for partial premixing in low strain-rate (<20s−1) methane counterflow flames. Temperature, OH concentration, and soot volume fraction distributions were measured along the stagnation streamline for progressive addition of oxygen to methane. These measurements along with an optically thin model for soot and gas radiation were used to study the effect of partial premixing on flame radiation and soot emission. It was found that with progressive partial premixing, the peak soot loading and the thickness of the soot zone first decreased and then increased, and while the gas radiation was enhanced, the gas radiative fraction (gas radiation per unit chemical energy release) showed a systematic decrease. The net radiative fraction (soot+gas), however, first decreased and then increased. A configuration with the soot zone spatially entrapped between the premixed and non-premixed reaction zones was experimentally found. This flame configuration has the potential to enhance radiative heat transfer while simultaneously reducing soot and NOx emissions.


Author(s):  
S. Majid Abdoli ◽  
Mahsa Kianinia

Background: Ethylene, propylene, and butylene as light olefins are the most important intermediates in the petrochemical industry worldwide. Methanol to olefins (MTO) process is a new technology based on catalytic cracking to produce ethylene and propylene from methanol. Aims and Objective: This study aims to simulate the process of producing ethylene from methanol by using Aspen HYSYS software from the initial design to the improved design. Methods: Ethylene is produced in a two-step reaction. In an equilibrium reactor, the methanol is converted to dimethyl ether by an equilibrium reaction. The conversion of the produced dimethyl ether to ethylene is done in a conversion reactor. Changes have been made to improve the conditions and get closer to the actual process design done in the industry. The plug flow reactor has been replaced by the equilibrium reactor, and the distillation column was employed to separate the dimethyl ether produced from the reactor. Result and Conclusion: The effect of the various parameters on the ethylene production was investigated. Eventually, ethylene is


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