methanol vapor
Recently Published Documents


TOTAL DOCUMENTS

144
(FIVE YEARS 21)

H-INDEX

19
(FIVE YEARS 2)

Author(s):  
Mohammad Ramezani ◽  
Marjan Khorshidizadeh ◽  
Seyed Morteza Zamir ◽  
Milad Ferdowsi

Author(s):  
Faiz Almansour ◽  
Monica Alberto ◽  
Rupesh S. Bhavsar ◽  
Xiaolei Fan ◽  
Peter M. Budd ◽  
...  

AbstractPhysical aging is currently a major obstacle for the commercialization of PIM-1 membranes for gas separation applications. A well-known approach to reversing physical aging effects of PIM-1 membranes at laboratory scale is soaking them in lower alcohols, such as methanol and ethanol. However, this procedure does not seem applicable at industrial level, and other strategies must be investigated. In this work, a regeneration method with alcohol vapors (ethanol or methanol) was developed to recover permeability of aged PIM-1 membranes, in comparison with the conventional soaking-in-liquid approach. The gas permeability and separation performance, before and post the regeneration methods, were assessed using a binary mixture of CO2 and CH4 (1:1, v:v). Our results show that an 8-hour methanol vapor treatment was sufficient to recover the original gas permeability, reaching a CO2 permeability > 7000 barrer.


2021 ◽  
Vol 368 ◽  
pp. 137624
Author(s):  
Ivneet Banga ◽  
Anirban Paul ◽  
Abha Umesh Sardesai ◽  
Sriram Muthukumar ◽  
Shalini Prasad

Processes ◽  
2021 ◽  
Vol 9 (1) ◽  
pp. 181
Author(s):  
Ravisut Vitidsant ◽  
Satoshi Kodama ◽  
Hidetoshi Sekiguchi

Ultrasonic spraying was used in a three-phase reactor to produce small droplets of triolein mixed with CaO as a solid catalyst at temperatures above the boiling point of methanol for enhancement of the transesterification of triolein. Droplets fell in the methanol countercurrent flow and were collected at the bottom of the reactor, followed by circulation to the ultrasonic spray system. The experimental parameters included triolein flow rates of 2.5–9.0 mL/min, reaction temperatures of 70–100 °C, and catalyst contents of 1.0–7.0 wt%. The methanol feed rate was set to be constant. The results suggested that the enhancement was successful after using the three-phase reactor by generating a high contact surface area for the droplets, which was a key factor for determining the performance. Comparing the results with conventional transesterification in the liquid phase using the same CaO at 60 °C, the three-phase reactor produced a methyl ester yield 2–5% higher during the 60 min trial period. However, the yield became lower after 60 min because the mass transfer of methanol to the droplets was limited. The transesterification kinetics were estimated based on the experimental data—assuming a first-order reaction—and the results indicated a range of the rate constant, an apparent activation energy, and a pre-exponential factor of 1.21–3.70 × 10−2 min−1, 36.1 kJ mol−1, and 64.9 min−1, respectively, suggesting that the three-phase reactor was effective for fast transesterification at the initial stage.


AMB Express ◽  
2021 ◽  
Vol 11 (1) ◽  
Author(s):  
Bashir L. Rumah ◽  
Christopher E. Stead ◽  
Benedict H. Claxton Stevens ◽  
Nigel P. Minton ◽  
Alexander Grosse-Honebrink ◽  
...  

AbstractWaste plastic and methane emissions are two anthropogenic by-products exacerbating environmental pollution. Methane-oxidizing bacteria (methanotrophs) hold the key to solving these problems simultaneously by utilising otherwise wasted methane gas as carbon source and accumulating the carbon as poly-3-hydroxybutyrate, a biodegradable plastic polymer. Here we present the isolation and characterisation of two novel Methylocystis strains with the ability to produce up to 55.7 ± 1.9% poly-3-hydroxybutyrate of cell dry weight when grown on methane from different waste sources such as landfill and anaerobic digester gas. Methylocystis rosea BRCS1 isolated from a recreational lake and Methylocystis parvus BRCS2 isolated from a bog were whole genome sequenced using PacBio and Illumina genome sequencing technologies. In addition to potassium nitrate, these strains were also shown to grow on ammonium chloride, glutamine and ornithine as nitrogen source. Growth of Methylocystis parvus BRCS2 on Nitrate Mineral Salt (NMS) media with 0.1% methanol vapor as carbon source was demonstrated. The genetic tractability by conjugation was also determined with conjugation efficiencies up to 2.8 × 10–2 and 1.8 × 10–2 for Methylocystis rosea BRCS1 and Methylocystis parvus BRCS2 respectively using a plasmid with ColE1 origin of replication. Finally, we show that Methylocystis species can produce considerable amounts of poly-3-hydroxybutyrate on waste methane sources without impaired growth, a proof of concept which opens doors to their use in integrated bio-facilities like landfills and anaerobic digesters.


2021 ◽  
Author(s):  
Akifumi Sumida ◽  
Hiroaki Imoto ◽  
Kensuke Naka

The development of turn-on detection sensors for methanol vapor remains challenging in material science. Methanol sensing materials are generally based on vapor-triggered color changes or are turn-off types. Additionally, in...


2020 ◽  
Vol 1003 ◽  
pp. 156-162
Author(s):  
Ke Le Yan ◽  
Yu Lin ◽  
Wang Qian

The adsorption behavior of methanol vapor onto three commercial silica gels named SG-1, SG-2 and SG-3 were investigated in this paper. The experimental results showed that SG-1 has the rich microporous, and the larger surface area and microporous volume than SG-2 and SG-3. The equilibrium adsorption data showed that the adsorption capacities of SG-1 was superior to SG-2 and SG-3 for lower concentration of methanol (<150 g/m3). However, SG-2 had higher adsorption capacities than SG-1 and SG-3 for higher concentration of methanol resulting from the condensation in mesopore channels. Three kinds of adsorption equilibrium equations including Langmuir equation, Freundlich equation and Dubinin-Astakov (D-A) equation were used to fit the methanol vapor adsorption isotherms. The results indicated that the experimental data can be well-fitted by D-A equation.


2020 ◽  
Vol 32 (9) ◽  
pp. 514-517
Author(s):  
M. Konstantaki ◽  
D. Skiani ◽  
D. Vurro ◽  
A. Cucinotta ◽  
S. Selleri ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document