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MDEA - Magnum Solvent

    https://www.magnumsolvent.com/productdata/Product%20Literature/Dehydration%20and%20Acid%20Gas%20Removal/Product%20Data%20Sheet%20-%20MDEA.pdf
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N-Methyldiethanolamine (MDEA) - Dow

    https://www.dow.com/en-us/pdp.n-methyldiethanolamine-mdea.85619z.html
    Monoethanolamine (MEA), LFG 90 A Low Freeze Grade blend of Monoethanolamine and 10% water to lower the freezing point for easier handling. Triethanolamine (TEA) A colorless to yellow liquid. It is completely soluble in water and has an ammonia-like smell. Building block in the manufacture of triazine based corrosion inhibitors.

Methyldiethanolamine - an overview | ScienceDirect Topics

    https://www.sciencedirect.com/topics/engineering/methyldiethanolamine
    MDEA has the lowest heat requirements for regeneration as it has the lowest heats of reaction with H 2 S and CO 2. Beside this it has the lowest specific heat solvent losses and a low the freezing point (about − 32°C). MDEA is used in many special solvent formulations especially in combination with Piperazine to enhance its reaction rate.

(522a) Thermal Degradation of Aqueous …

    https://www.aiche.org/conferences/aiche-annual-meeting/2015/proceeding/paper/522a-thermal-degradation-aqueous-methyldiethanolamine-mdea-continuous-injection-h2sco2-high-pressure
    traces are present in fresh MDEA. Figure1 shows the formation of formic and acetic acid over degradation period of 865 hours. The rate of formation of formic acid on fresh MDEA is higher than acetic acid while for lean MDEA the formation rate was almost equal (Figure1). \s Figure1. Organic acids as HSS on thermal degradation of fresh and lean MDEA

Treating high CO2 gases with MDEA - DigitalRefining

    https://www.digitalrefining.com/article/1000573/treating-high-co2-gases-with-mdea
    MDEA is a tertiary amine whose amine group lacks even the single proton that is so essential to react directly with CO2. In terms of its chemistry, the most that MDEA can do is provide a sink for the hydrogen ions produced when CO2 hydrolyses in water: CO2 + H2O ⇔ H+ + HCO3- HCO3- ⇔ H+ + CO3= H+ + R3N ⇔ R3NH+

Methyldiethanolamine - Welcome to the NIST WebBook

    https://webbook.nist.gov/cgi/cbook.cgi?ID=C105599&Mask=4
    Δ vap H (kJ/mol) Temperature (K) Method Reference Comment; 71.5: 422. EB: Kim, Svendsen, et al., 2008: Based on data from 409. - 435. K.; AC: 73.0: 405. A ...

Thermal Degradiation Temperature Of Mdea - Cheresources.com

    https://www.cheresources.com/invision/topic/17514-thermal-degradiation-temperature-of-mdea/
    At present our MDEA regenarator bottom temperature is 130 ~ 131 DegC and Top pressure is 1.2 Barg. However when Regen pressure fluctuate due to any upset, pressure increase and consequently Regn bottom temperature also increase ( exceed 132 C), and still more than 12 years of plant running we are not facing any corrosion or any integrity issue.

METHYL DIETHANOLAMINE MDE - NOAA

    https://cameochemicals.noaa.gov/chris/MDE.pdf
    Use water spray to cool exposed containers. ExposureCALL FOR MEDICAL AID. VAPOR Move victim to fresh air. If breathing has stopped, give artificial respiration. If breathing is difficult, give oxygen. LIQUID Irritating to skin and eyes. Remove contaminated clothing and shoes. Flush affected areas with water.

Amine Types: MEA, DGA, DEA, DIPA, MDEA - SourGas

    https://sourgas.wordpress.com/2016/02/21/amine-types-mea-dga-dea-dipa-mdea/
    MEA is a primary amine. It is the oldest solvent used in modern Gas Sweetening plants. Gas sweetening process using MEA is in the public domain. Concentration MEA is used in aqueous solutions with concentrations between 10 and 20 Wt. % MEA. By far the most common concentration is 15 Wt. % MEA. A 15 Wt. % MEA solution freezes at -4 deg.C.

Comparative study of DEA and MDEA treatments of acid …

    http://gasprocessingnews.com/features/202006/comparative-study-of-dea-and-mdea-treatments-of-acid-gas.aspx
    MDEA results: Removal of H 2 S from sweet gas = 99.95%, and removal of H 2 S and CO 2 = 68.95% Average price of MDEA chemical = 1,207,296 LE (Egyptian pounds)/d Total mass flow required for DEA = 786 kg/hr. The simulation results show that both DEA and MDEA are effective sweetening agents for acid gas.

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