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Liquid sulfur product temperature

The production of biodiesel from low quality oils such as animal fats, greases, and tropical oils is challenging due to the presence of undesirable components especially FFA and water. A pre-treatment step is required when using such high fatty-acid feedstock. Generally, this esterification pre-treatment employs liquid sulfuric acid catalyst which must subsequently be neutralized and either disposed of or recycled. However, requirement of high temperature, high molar ratio of alcohol to FFA, separation of the catalyst, enviromnental and corrosion related problems make its use costly for biodiesel production. [Pg.280]

Syngas cleanup system - low or high temperature and processes used to remove sulfur, nitrogen, particulates, and other compounds that may impact the suitability of the syngas for specific applications (i.e., turbine and fuel cell for electric power generation, hydrogen production, liquid fuel production, or chemical production). [Pg.9]

About 40ml of liquid sulfur dioxide is condensed in a 25(Kml pressure bottle containing a solution of 50g of acetoxime in 50ml of water. The procedure of method (II) is used and the sealed bottle is allowed to stand for at least 5 hours at room temperature. After re-cooling, the excess of sulfur dioxide is allowed to escape, the product is collected by filtration, washed with 75ml of alcohol, and with the same volume of ether. [Pg.155]

We may seem to have contradicted ourselves because Equation 10-1 shows a carbocation to be formed in bromine addition, but Equation 10-5 suggests a bromonium ion. Actually, the formulation of intermediates in alkene addition reactions as open ions or as cyclic ions is a controversial matter, even after many years of study. Unfortunately, it is not possible to determine the structure of the intermediate ions by any direct physical method because, under the conditions of the reaction, the ions are so reactive that they form products more rapidly than they can be observed. However, it is possible to generate stable bromonium ions, as well as the corresponding chloronium and iodonium ions. The technique is to use low temperatures in the absence of any strong nucleophiles and to start with a 1,2-dihaloalkane and antimony penta-fluoride in liquid sulfur dioxide ... [Pg.366]

Japanese investigators reported that liquid sulfur dioxide polymerizes styrene derivatives (e.g., p-methyl styrene, a-methyl styrene) (19). Unfortunately, the experiments were not executed under rigorously anhydrous conditions (high vacuum) so that the possibility for proton (e.g., sulfurous or sulfuric acid) initiation exists although the authors seem to believe that S02 is the catalyst, probably by the following process 2S0a SO2 +SO e. The cationic nature of the mechanisms was proven by the facts that no polysulfones formed, that the polymerization was inhibited by bases, and that free radical inhibitors did not affect the reaction. These authors also claim that formaldehyde is polymerized by sulfur dioxide to a product which does not contain sulfur and whose infrared spectrum closely resembles that of a low temperature sample. [Pg.511]

Liquid sulfur-dicyclopentadiene (DCP) solutions at 140°C undergo bulk copolymerization where the melt viscosity and surface tension of the solutions increase with time. A general melt viscosity equation rj == tj0 exp(aXH), at constant temperature, has been developed, where tj is the viscosity at time t for an S -DCP feed composition of DCP mole fraction X and rj0 (in viscosity units), a (in time 1), and b (a dimensionless number, -f- ve for X < 0.5 and —ve for X > 0.5) are empirical constants. The structure of the sul-furated products has been analyzed by NMR. Sulfur non-crystallizable copolymeric compositions have been obtained as shown by thermal analysis (DSC). Dodecyl polysulfide is a viscosity suppressor and a plasticizer for the S8-DCP system. [Pg.38]

Photolytically, reduction of SF5CI with H2 gives the largest known binary sulfur fluoride, disulfur decafluoride. It is also a trace by-product of the industrial preparation of SFe, but it is not isolated and is destroyed by heating to 400 °C. Disulfur decafluoride is a liquid at room temperature that will completely decompose at 200 °C to SF4 and SFe. It is intermediate in properties when compared to SF4 and SFe. It is not hydrolyzed by water alone, but it is slowly attacked by aqueous NaOH. Disulfur decafluoride can be stored at room temperature as a liquid for years. Like SF4, it is extremely... [Pg.1354]

In a leaching reaction where elemental sulfur is one of the by-products, it becomes important to carry out the reaction at temperatures below the melting point of monoclinic sulfur (119°C). Liquid sulfur will prevent the reactions of the other constituents in the aqueous phase. [Pg.51]

The reactions of oxygen atoms with solid and liquid sulfur have also been studied, Cramarossa et reported results of the heterogeneous system in the temperature region of 50-160 °C. They found the rate of reaction at temperatures below the melting point of S to vary as [O] . They concluded that the immediate product of the heterogeneous reaction was SO, as did Liuti et al.. When evaporation of molecular sulfur becomes important then additional SO can be formed in the vapor phase by such stepr as... [Pg.44]

One g-mole of pure liquid sulfuric acid at temperature To (°C) is mixed with r g-moles of liquid water, also at temperature 7 o(°C). in an adiabatic container. The final solution temperature is 7,( 0). The mass heat capacities of the pure acid, pure water, and the product solution [J/(g C)j are Cpa, and Cps, respectively, all of which may be taken to be constant (independent of temperature). [Pg.436]

A 600-ml. steel reaction vessel (Note 1) is precooled before loading by filling it between one fourth and one half full of methanol and Dry Ice. After removal of the methanol and Dry Ice, the autoclave is charged with 120 g. (176 ml., 1.76 moles) of isoprene (Note 2), 113 g. (80 ml, 1.76 moles) of liquid sulfur dioxide, 88 ml. of methanol, and 4 g. of hydroquinone. The vessel is sealed, heated slowly to 85°, and maintained at that temperature for 4 hours. It is then cooled, the sulfone removed, the bomb rinsed with methanol, and the combined product and washings are treated hot with 5 g. of Norite. The filtered solution is concentrated to a volume of 250-300 ml., and the sulfone is allowed to crystallize. The material is filtered and washed with 50 ml. of cold methanol. Recrystallization from methanol (20 ml. per 25 g. of sulfone) yields 140-150 g. of thick, colorless plates. Concentration of the mother liquors raises the total yield to 182-191 g. (78-82%) (Note 3), melting at 63.5-64° (Note 4). [Pg.59]

With the corresponding zirconium(IV) derivatives, Zr( j -C5H5)2(Me)2 treatment with liquid sulfur dioxide at dry-ice temperature yields the product resulting from insertion into the zirconium-methyl and the zirconium-cyclopentadienyl bonds ... [Pg.649]

Rotatins-Shelf Type The patented Roto-shelftype (Fig. ll-55c) features (1) a large heat-transfer surface provided over a small floor space and in a small building volume, (2) easy floor cleaning, (3) non-hazardous machinery, (4) stainless-steel surfaces, (5) good control range, and (6) substantial capacity by providing as needed 1 to 10 shelves operated in parallel. It is best suited for thick-cake production and burden materials having an indefinite solidification temperature. Sohdification of liquid sulfur into 13- to 19-mm- (Vt- to thick... [Pg.1258]

On the other hand, when the content of sulfur in the gas was sufficiently high (1000-2(X)0 ppmv) for bulk nickel sulfide (NijSj) formation (ascertained by X-ray diffraction analysis), the distribution of sulfur in the catalyst bed was fairly even in different parts of the bed (Table 1) and also within catalyst particles. According to SEM/EDS analysis the content of sulfur on the surface ranged from 4.0 to 7.5 wt% and in the middle of particles from 5.3 to 9.3 wt%. However, nickel forms a liquid sulfide product at temperatures above 635 C [18, 19]. According to the SEM analysis of the firesh and spent catalyst particles, no liquid formation on the catalysts was detected. [Pg.474]

Thermodynamically, S12 is the second most stable sulfur ring after Sg. Therefore, S12 is formed in many chemical reactions in which elemental sulfur is a product. In addition, S12 is a component of liquid sulfur at all temperatures. The same holds for Sis and S20 which are often formed together with S12 ... [Pg.10]


See other pages where Liquid sulfur product temperature is mentioned: [Pg.46]    [Pg.46]    [Pg.266]    [Pg.284]    [Pg.1091]    [Pg.37]    [Pg.24]    [Pg.213]    [Pg.48]    [Pg.307]    [Pg.607]    [Pg.35]    [Pg.52]    [Pg.1295]    [Pg.607]    [Pg.28]    [Pg.96]    [Pg.267]    [Pg.338]    [Pg.339]    [Pg.1295]    [Pg.705]    [Pg.914]    [Pg.298]    [Pg.362]    [Pg.35]    [Pg.242]    [Pg.21]    [Pg.32]    [Pg.36]    [Pg.35]    [Pg.106]    [Pg.2489]    [Pg.51]    [Pg.495]    [Pg.59]   


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