Category: 101-84-8

The reaction rate of a catalyzed reaction is faster than the reaction rate of the uncatalyzed reaction at the same temperature. 101-84-8, Name is Diphenyl oxide, SMILES is C1(OC2=CC=CC=C2)=CC=CC=C1, in an article , author is Sun, Zhaomin, once mentioned of 101-84-8, Name: Diphenyl oxide.

Enrichment of Alkylglycerols and Docosahexaenoic Acid via Enzymatic Ethanolysis of Shark Liver Oil and Short-path Distillation

Enzymatic alcoholysis of squalene-free shark liver oil (SLO) for the enrichment of alkylglycerols (AKG) and docosahexaenoic acid (DHA) was investigated. The squalene-free SLO contained 75.11% triacylglycerols (TAG) and 18.69% diacylglycerol ethers (DAGE), and its DHA and total AKG contents were 7.52% and 6.17%, respectively. The catalytic discrimination against both DAGE and DHA was observed during the reaction, and the discrimination against DAGE was affected by lipase and reaction conditions. The ethanolysis reaction was carried out at 40 degrees C for 24 h, where the reaction medium contained 20% ethanol and 3% Lipozyme (R) 435. The ethanolysis derivatives with 62.96% monoacylglycerol ethers, 30.93% monoacylglycerols, and 5.88% DAGE were obtained followed by short-path distillation, and its DHA and total AKG contents were improved to 23.17% and 33.98%, respectively. The study provides an approach for value-added utilization of SLO with low contents of AKG and n-3 polyunsaturated fatty acids.

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One of the major reasons for studying chemical kinetics is to use measurements of the macroscopic properties of a system, such as the rate of change in the concentration of reactants or products with time. 101-84-8, Name is Diphenyl oxide, formurla is C12H10O. In a document, author is Chen, Qian, introducing its new discovery. SDS of cas: 101-84-8.

Study on influencing factors of Pickering emulsion stabilized by modified montmorillonite and fatty alcohol polyoxyethylene ether

Pickering emulsion is widely used in food, drug administration, and cosmetics. In practical applications, surfactants are often co-present with particles, so it is particularly critical to study particle-surfactant interactions. Pickering emulsions were prepared using stearyltrimethylammoniumchloride organic montmorillonite (STAC/MMT) and fatty alcohol polyoxyethylene ether (AEO-3) as stabilizers. Effects of AEO-3 content, STAC/MMT content, oil-water ratio, emulsification temperature, emulsification time on emulsion stability were systematically revealed by studying the particle size distribution and phase volume of the emulsion. The formulation of emulsion was optimized by orthogonal experiment and the mechanism of this emulsion system was proposed. The results indicated that the oil-water volume ratio was closely related to the type of emulsification, and when STAC/MMT and AEO-3 were used together, stable W/O emulsions were obtained owing to the synergistic interaction. The orthogonal experiments showed that the emulsion had good static and thermal stability when the STAC/MMT content was 2.0%, the oil-water volume ratio was 1:1, AEO-3 content was 0.25% and emulsification time was 5 minutes. The stability mechanism of this Pickering emulsion was that AEO-3 was used to improve the surface properties of STAC/MMT particles and enhance their emulsifying capacity.

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Reference of 101-84-8, Chemo-enzymatic cascade processes are invaluable due to their ability to rapidly construct high-value products from available feedstock chemicals in a one-pot relay manner. 101-84-8, Name is Diphenyl oxide, SMILES is C1(OC2=CC=CC=C2)=CC=CC=C1, belongs to ethers-buliding-blocks compound. In a article, author is Kerric, Anais, introduce new discover of the category.

Spatial and temporal variations of halogenated flame retardants and organophosphate esters in landfill air: Potential linkages with gull exposure

Landfills represent important sources of local emissions of organic contaminants, including halogenated (HFR) and organophosphate ester (OPE) flame retardants used in a large variety of consumer products. Gulls foraging in landfills may be exposed to elevated atmospheric concentrations of HFRs and OPEs that may vary spatially and temporally within a landfill site, thus modulating their exposure. The objective of the present study was to investigate the spatial and temporal variability of HFR and OPE concentrations in air samples collected from a major landfill in the Montreal area (QC, Canada) that is frequently visited by gulls for foraging. Miniature stationary passive air samplers (PASs) and high-volume active air samplers (AASs) were deployed in six different areas within this landfill site for 34 days to collect HFRs and OPEs in air. During the same period, wild-caught ring-billed gulls (Larus delawarensis) were equipped on their back with a similar miniature PAS that was deployed in the landfill along with a GPS datalogger to monitor their movements for ten days. Elevated concentrations of certain OPEs (e.g., tris(2-chloroethyl) phosphate and tris(2-chloroisopropyl) phosphate) and brominated diphenyl ether (BDE)-209 were measured in stationary PASs and AASs, although they were homogenously distributed within this landfill site. Temporal variability was observed for concentrations of BDE-209, -99 and -47 measured in AASs as well as tributyl phosphate during the 34-day deployment period. Moreover, air concentrations of BDE-209, -207 and -206 and selected OPEs (tris(1,3-dichloro-2-propyl) phosphate and tris(methylphenyl) phosphate) determined using AASs were positively correlated with ambient air temperatures. Gulls that visited a landfill at least once exhibited significantly greater concentrations of BDE-47 measured in PASs they carried on their back, suggesting that landfill air may represent a source of exposure to PBDEs for these birds, and potentially other urban-adapted wildlife using these sites for foraging. (C) 2020 Elsevier Ltd. All rights reserved.

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Researchers who often do experiments know that organic synthesis is a process of preparing more complex target molecules from simple raw materials through one or more chemical reactions. Generally, it requires fewer steps, and cheap raw materials. 101-84-8, name is Diphenyl oxide, A new synthetic method of this compound is introduced below., Recommanded Product: 101-84-8

(1) diphenyl ether (44.2 g, 0.26 mol) was added into a 250 ml four-necked flask and 123.5 g (1.25 mol) of dichloroethane was added and stirred for 1 hour.Cool to -5 ~ 0 ,Bromine (21 g, 0.13 mol) was rapidly added dropwise and stirred for 1 hour. The mixture was cooled to -5~0 C and 30% hydrogen peroxide (15 g, 0.13 mol)With 0.5 to 1 hour dropwise addition and termination,The temperature is controlled between 0 and 5 DEG C, naturally heated to 25 DEG C after dropping, incubated for 32 hours between 27 DEG C and quenched with 49g of 15% sodium bisulfite, after the phase separation,Then washed with water to neutral, to distill dichloroethane distillation, distillation under reduced pressure before recovery of diphenyl ether, and finally collected 4-bromo-diphenyl ether 51.7g, yield 80.0%, content of 98.2%.

The basis of chemical reaction formula synthesis, the synthesis route is composed of some specific reactions and combined according to certain logical thinking. We look forward to the emergence of more reaction modes in the future.

Reference:
Patent; Binhai Extensive Chemical Co., Ltd.; Wu Fucai; (8 pag.)CN106957220; (2017); A;,
Ether – Wikipedia,
Ether | (C2H5)2O – PubChem

101-84-8, The chemical industry reduces the impact on the environment during synthesis 101-84-8, name is Diphenyl oxide, I believe this compound will play a more active role in future production and life.

Example 1; Decabromodiphenyl ether – Simultaneous bromination and milling in a mixed solvent; To a 1 liter round bottomed flask equipped with a mechanical stirrer, a dropping funnel, a thermocouple and a reflux condenser was added 440 g of solvent mixture (DCM 20 %, CBM 40 %, and DBM 40 % w/w) ; bromine, 475 g; AlCl3,4.3 g; and ceramic beads (1.5-3.5 mm diameter), 814 g-A solution of diphenyl oxide (42.5 g, ) in 20 ml of solvent mixture was dropped into the flask during 70 minutes with stirring while keeping the temperature at 7- 13 C . The reaction mixture was refluxed for 4.5 hours, the flask was cooled and 55 ml of water was carefully added to destroy the catalyst. Excess bromine was bleached with sodium bisulfite solution, the aqueous phase was separated and the organic phase was washed with water. The product mixture was passed through a sieve to remove the ceramic beads and the mixture was filtered, washed with water and dried. The product comprised 99.4 % decabromodiphenyl ether and 0.1 % nonabromodiphenyl ether (in the Examples sometimes abbreviated “Deca” and “Nona”, respectively). Particle size 7.1 microns (dg0) .; Example 2 (comparative); Decabromodiphenyl ether – Bromination without milling in a mixed solvent.; The procedure of Experiment 1 was repeated without the ceramic beads present. The product consisted of 94.1 % Deca and 5.8 % Nona. Particle size 98 microns (d90).; Example 3; Decabromodiphenyl ether- increasing the crystal size of milled Deca in a simulated reaction mixture after bromination and destruction of the catalyst.; The product of Example 1, having a particle size of 7.1 microns (dgo) and an assay of 99.4 %, was charged to a 1 liter flask followed by 440 g of solvent mixture (DCM 20 %, CBM 40 %, and DBM 40 %); 4.3 g AlCl3, 50 g of bromine and 50 ml of water to destroy the catalyst. The mixture was refluxed for 5.3 hours, cooled and bleached with bisulfite. The product was filtered, washed with water and dried. The particle size v/as 28.8 microns (dgo), had an assay of 99.7 % and was easily filtered.; Example 7; Decabromodiphenyl ether – Bromination of pre-milled Deca precursor; To a 2 liter jacketed reaction vessel equipped with a mechanical stirrer, a dropping funnel, a thermocouple and a reflux condenser was added 500 g of milled Deca (content 97.3 %, particle size 3.8 microns (d90) ) , 1945 g of solvent mixture, 444 g bromine and 22 g AICI3. The mixture was heated at reflux for 3.5 hours. Water, 260 ml, was added and the excess bromine was bleached with sodium bisulfite solution. To the thick slurry was added 150 ml of water. The mixture was filtered and the dried solid comprised 99.6 % Deca with particle size 38.5 microns (dgo).; Example 8; Decabromodiphenyl ether- Bromination of pre-milled Deca precursor on an industrial scale; A reactor vessel of 16 cubic meters capacity was charged with 7500 liters of solvent consisting of 12.6 % dichloromethane, 32.5 % bromochloromethane and 54.9 % dibromomethane . Aluminum chloride, 150 kg, 8 tons of pre- milled Deca (Deca content 97.9 % with particle size 14 microns (dg0) ) and 1000 kg of bromine were added. The mixture was heated at reflux for 8 hours and was then bleached with 1340 liters of 38 % sodium bisulfite solution. The upper aqueous solution was decanted and the mixture was washed with two 1200 liters portions of water. Sodium hydroxide, 20 %, was added to neutralize the mixture which was then centrifuged. The product was dried and was found to contain 99.3 % Deca with particle size 42 microns (d90).; Example 9; Decabromodiphenyl ethane – Simultaneous bromination and milling in a mixed solvent; To a 1 liter round bottomed flask equipped with a mechanical stirrer, a dropping funnel, a thermocouple and a reflux condenser was added 520 g of solvent mixture (DCM 6 %, CBM 20 %, and DBM 74 % ) ; bromine, 539 g; AlCl3, 9 g; and ceramic beads (1.5-3.5 mm diameter), 840 g.A 55 % solution of diphenyl ethane in DCM (91.1 g, ) was dropped into the flask during 30 minutes with stirring while keeping the temperature at 21-26 0C. The reaction mixture was refluxed for 6.7 hours, and 120 ml of water was carefully added to destroy the catalyst. Bromine was bleached with sodium bisulfite solution, the aqueous phase was separated and the organic phase was washed with water and was neutralized with 20 % NaOH. The product mixture was passed through a sieve to remove the ceramic beads and the mixture was filtered, washed with water and dried. The product comprised 91.4 % decabromodiphenyl ethane and 7.8 % nonabromodiphenyl ethane. Particle size was 6.1 microns (d90).; Example 10 (comparative); Decabromodiphenyl ethane – Bromination without milling in a mixed solvent.; The procedure of Example 9 was repeated without the ceramic beads present. The product comprised 80.6 % decabromodiphenyl ethane and 18.6 % nonabromodiphenyl ethane. Particle size 22 .microns (dgo).

The chemical industry reduces the impact on the environment during synthesis Diphenyl oxide. I believe this compound will play a more active role in future production and life.

Reference:
Patent; BROMINE COMPOUNDS LTD.; WO2008/26215; (2008); A2;,
Ether – Wikipedia,
Ether | (C2H5)2O – PubChem