INFRARED THERMOCHEMICAL GAS AND VAPOR DETECTOR STUDY

Author(s):  
L.V. ILIYASOV ◽  

The results of experimental study of the thermochemical gas and vapor detector (ITCGVD) are given. Functional principle of this detector is based on the measurement of infrared radiation intensity formed during catalytic combustion of flammable gases and vapors on the pellistor surface. The ITCGVD scheme is described. It contains the measuring and the comparing cells equipped with pellistors and infrared diodes working in photogalvanic mode and a counter connected ensuring their signal difference formation, which is registered after amplification by a potentiometer. The dependences of ITCGVD signal on most important parameters were determined as a result of experimental study with use of impulse method of analyzing gases input. These parameters are as follows: analyzing gas concentration in carrier gas (air) flow, a pellistor supply voltage, a distance of a pellistor from infrared photodiode window, carrier gas flow rate. The possibility of ITCGVD use in alerters and analyzers of flammable gasses and vapors micro concentration in air was determined. Experimental correlation of detector signal to hydrogen, methane and propane volume concentration in air was developed. Possibility of ITCGVD application in gas chromatography by using the analysis of calibration gas-air mixture is shown. Basic metrological characteristics of ITCGVD were determined. They are as follows: sensitivity threshold 4 . 10–5 volume percent, maximum concentration within a linear statistical characteristic – 0.4 volume percent; linear dynamic range 1 . 104; the drift of apparent zero signal – 0.6 mV/h; time constant 0.3…1 s (depends on carrier gas flow). Measuring and comparing cell volume was 0.3 ml.

2020 ◽  
pp. 002029402096423
Author(s):  
Shi Rui Guo ◽  
Qian Qian Yin ◽  
Lu Jun Cui ◽  
Xiao Lei Li ◽  
Ying Hao Cui ◽  
...  

This paper investigates the influence of carrier gas flow on the external flow field of coaxial powder feeding nozzle. FLUENT software was adopted to establish gas-solid two-phase flow. The simulation of powder stream field under different carrier gas flow was also carried out. Results show that the larger the flow of carrier gas is, the higher the gas flow field velocity at the nozzle outlet is. At the same time, the concentration at the convergence point is lower, and the convergent point is maintained at 0.015 m. Under the condition of 4 L/min, the powder flow convergence is good. When it exceeds 4 L/min, powder spot diameter increases. The experiment of powder aggregation and laser cladding forming were completed, which shows that the forming effect is the best one under the condition of 4 L/min. It is consistent with the simulation analysis results and has a high reference to the optimization of the process parameters of coaxial nozzle.


1966 ◽  
Vol 38 (1) ◽  
pp. 7-9 ◽  
Author(s):  
Gary. Horlick ◽  
W. E. Harris ◽  
H. W. Habgood

1985 ◽  
Vol 8 (9) ◽  
pp. 580-584 ◽  
Author(s):  
R. E. Kaiser ◽  
R. I. Rieder ◽  
Lin Leming ◽  
L. Blomberg ◽  
P. Kusz

2013 ◽  
Vol 39 (3) ◽  
pp. 258-261 ◽  
Author(s):  
A. G. Kurenya ◽  
D. V. Gorodetskiy ◽  
V. E. Arkhipov ◽  
A. V. Okotrub

2015 ◽  
Vol 430 ◽  
pp. 87-92 ◽  
Author(s):  
Ming Li ◽  
Jingyun Wang ◽  
Kan Li ◽  
Yingjie Xing ◽  
H.Q. Xu

2016 ◽  
Vol 18 (3) ◽  
pp. 88-96 ◽  
Author(s):  
Najaf Ali ◽  
Mahmood Saleem ◽  
Khurram Shahzad ◽  
Sadiq Hussain ◽  
Arshad Chughtai

Abstract The yield and composition of pyrolysis products depend on the characteristics of feed stock and process operating parameters. Effect of particle size, reaction temperature and carrier gas flow rate on the yield of bio-oil from fast pyrolysis of Pakistani maize stalk was investigated. Pyrolysis experiments were performed at temperature range of 360-540°C, feed particle size of 1-2 mm and carrier gas fl ow rate of 7.0-13.0 m3/h (0.61.1 m/s superficial velocity). Bio-oil yield increased with the increase of temperature followed by a decreasing trend. The maximum yield of bio-oil obtained was 42 wt% at a temperature of 490°C with the particle size of around 1.0 mm and carrier gas flow rate of 11.0 m3/h (0.9 m/s superficial velocity). High temperatures resulted in the higher ratios of char and non-condensable gas.


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