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Cathode carbon

The cell for this process is unlike the cell for the electrolysis of aluminum which is made of carbon and also acts as the cathode. The cell for the fused-salt electrolysis is made of high temperature refractory oxide material because molten manganese readily dissolves carbon. The anode, like that for aluminum, is made of carbon. Cathode contact is made by water-cooled iron bars that are buried in the wall near the hearth of the refractory oxide cell. [Pg.496]

If too large a current is drawn from a Ledanche cell, the ammonia forms a gaseous insulating layer around the carbon cathode. When this happens, the voltage drops sharply and then returns slowly to its normal value of 1.5 V. This problem can be avoided by using an alkaline dry cell, in which the paste between the electrodes contains KOH rather than NH4CL In this case the overall cell reaction is simply... [Pg.500]

The Li-SOCl2 battery consists of a lithium-metal foil anode, a porous carbon cathode, a porous non-woven glass or polymeric separator between them, and an electrolyte containing thionyl chloride and a soluble salt, usually lithium tetrachloro-aluminate. Thionyl chloride serves as both the cathode active material and the elec-... [Pg.40]

Sulfur dioxide is soluble in the electrolyte. Sulfur is soluble up to about 1 mol dm 3, but it precipitates in the cathode pores near the end of discharge. Lithium chloride is essentially insoluble and precipitates on the surfaces of the pores of the carbon cathode, forming an insulating layer which terminates the operation of cathode-limited cells [37],... [Pg.41]

Most sulphones are known to react with chemical reducing reagents like dissolved metals or amalgams. However, electron transfers may be produced also directly from metallic or conducting carbon cathodes maintained at a certain potential depending on the desired reducing power. We will discuss the reactivity of sulphones towards electrons issued from cathodes, especially in the light of recent results. [Pg.1002]

The ammonium polysulfide, (NH4)2SX (with x=2 to 6) is produced in an electrochemical cell where aqueous ammonium sulfide, (NH4)2S, solution is supplied as electrolyte. The cell comprises an anode and a gas diffusion carbon cathode over which gaseous 02 is supplied in contact with the electrolyte.11 The cell operated continuously at pressures up to 60 bar. The applied potential, UWc> was 0.01 to 5 V. Pronounced electrochemical promotion behaviour was observed at Uwc values as low as 0.02 V with a current 1=0.5 A. [Pg.482]

Oxidation of thiophene with Fenton-like reagents produces 2-hydroxythiophene of which the 2(570 One isomer is the most stable (Eq. 1) <96JCR(S)242>. In contrast, methyltrioxorhenium (Vn) catalyzed hydrogen peroxide oxidation of thiophene and its derivatives forms first the sulfoxide and ultimately the sulfone derivatives <96107211>. Anodic oxidation of aminated dibenzothiophene produces stable radical cation salts <96BSF597>. Reduction of dihalothiophene at carbon cathodes produces the first example of an electrochemical halogen dance reaction (Eq. 2) <96JOC8074>. [Pg.78]

Button cells consist of cathode and anode cans (used as the terminals), powdered zinc anode, containing gelled electrolyte and the corrosion inhibitor, separator with electrolyte, thin (0.5 mm) carbon cathode with catalyst and PTFE, waterproof gas-permeable (teflon) layer and air distribution layer for the even air assess over the cathode surface. Parameters of battery depend on the air transfer rate, which is determined by quantity and diameters of air access holes or porosity of the gas-diffusion membrane. Air-zinc batteries at low rate (J=0,002-0,01C at the idle drain and J= 0,02-0,04C at the peak continuous current) have flat discharge curves (typical curve is shown by Figure 1). [Pg.164]

Coimmobilization of the viologen and the VAPOR enzyme at the surface of a carbon cathode can be used for the electrochemical production of NADH from NAD+ at a rate of 9 nmolh-1 cm-2 [55,61,62]. [Pg.109]

Several publications deal with acetylenic halides that can undergo reductive intramolecular cyclization [37]. For example, electrolysis of 6-iodo-l-phenyl-l-hexyne at a carbon cathode gives benzylidenecy-clopentane in 36% yield. [Pg.223]

C arbon amxie Carbon cathode Dhri d cell... [Pg.59]

Figure 18. Discharge mechanism of a Li—SOCij ceii. The cell can operate until the surface of the carbon cathode is fully covered by electronically insulating LiCI and S discharge products. The Li—SO2 cell is also a soluble cathode system with a cell construction similar to that of the Li—SOCI2 cell. It follows a similar discharge reaction where the reaction product is L1S204. Figure 18. Discharge mechanism of a Li—SOCij ceii. The cell can operate until the surface of the carbon cathode is fully covered by electronically insulating LiCI and S discharge products. The Li—SO2 cell is also a soluble cathode system with a cell construction similar to that of the Li—SOCI2 cell. It follows a similar discharge reaction where the reaction product is L1S204.
Li2S204 being the SEI component at the Li anode and the solid discharge product at the carbon cathode. The Li—SOCI2 and Li—SO2 systems have excellent operational characteristics in a temperature range from —40 to 60 °C (SOCI2) or 80 °C (SO2). Typical applications are military, security, transponder, and car electronics. Primary lithium cells have also various medical uses. The lithium—silver—vanadium oxide system finds application in heart defibrillators. The lithium—iodine system with a lithium iodide solid electrolyte is the preferred pacemaker cell. [Pg.18]

Figure 3. Electrolyses of 50 mM Na2S04 adjusted to pH 2 continuously saturated with O2 at a reticulated vitreous carbon cathode in a flow-cell. Plots of H2O2 formed versus electrolysis time for... Figure 3. Electrolyses of 50 mM Na2S04 adjusted to pH 2 continuously saturated with O2 at a reticulated vitreous carbon cathode in a flow-cell. Plots of H2O2 formed versus electrolysis time for...
Figure 10. COD evolution as a function of electrolysis time for electrolysis of solutions containing 50 mMNa2S04 + 1 mMFe + dye (a) 0.082 mMDR23, (b) 0.25 mM A07, (c) 0.33 mM Am, (d) 0.1 mM AG25, (e) 0.1 mM Am, (f) 0.17 mM BB9. Electrolyses were carried out in a membrane cell with a reticulated vitreous carbon cathode (5 cm x 5 cm x 1 cm). Figure 10. COD evolution as a function of electrolysis time for electrolysis of solutions containing 50 mMNa2S04 + 1 mMFe + dye (a) 0.082 mMDR23, (b) 0.25 mM A07, (c) 0.33 mM Am, (d) 0.1 mM AG25, (e) 0.1 mM Am, (f) 0.17 mM BB9. Electrolyses were carried out in a membrane cell with a reticulated vitreous carbon cathode (5 cm x 5 cm x 1 cm).
The feasibility of benzenic ring amines, benzenic ring structures and aliphatic acids oxidation by means of Fenton chemistiy was tested in synthetic, acidic wastewaters by Fenton s reagent electrogenerated at a reticulated vitreous carbon cathode using the flow-cell. The organic molecules considered were phenol (Ph), cresol (Cr), aniline (An) hydroquinone (HQ), catechol (Cat), parabenzoquinone (pBQ) and oxalic acid (OxAc). Their initial... [Pg.211]

Radical intermediates are also trapped by intramolecular reaction with an alkene or alkyne bond. At a mercury cathode this process competes with formation of the dialkylmercury [51], At a reticulated vitreous carbon cathode, this intramolecular cyclization of radicals generated by reduction of iodo compounds is an important process. Reduction of l-iododec-5-yne 5 at vitreous carbon gives the cyclopentane... [Pg.102]

Dibromobutane affords 29 % cyclobutane along with butane and butene at a vitreous carbon cathode. Addition of l,l,l,3,3,3-hexafiuoropropan-2-ol as a proton... [Pg.113]

Tetraalkylammonium salts are frequently used as the inert electrolyte in electrochemical reactions. These salts are however reductively decomposed in dimethylformamide at potentials around -2.96 V vs. see. At a glassy carbon cathode, tetra-... [Pg.164]


See other pages where Cathode carbon is mentioned: [Pg.142]    [Pg.163]    [Pg.96]    [Pg.97]    [Pg.100]    [Pg.143]    [Pg.144]    [Pg.199]    [Pg.118]    [Pg.654]    [Pg.40]    [Pg.65]    [Pg.15]    [Pg.369]    [Pg.142]    [Pg.175]    [Pg.222]    [Pg.228]    [Pg.288]    [Pg.75]    [Pg.75]    [Pg.164]    [Pg.201]    [Pg.201]    [Pg.204]    [Pg.104]    [Pg.114]    [Pg.117]    [Pg.148]   
See also in sourсe #XX -- [ Pg.242 , Pg.344 ]




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Carbon Cathode Bottom Blocks

Carbon as a cathode

Carbon cathode reaction

Carbon-sulfur cathode

Carbonation cathodic protection

Cathode catalyst Carbonate

Cathodes Carbonate

Cathodes Carbonate

Cathodes, aluminum carbon

Defects in Carbon Cathode Blocks

Interaction of Carbon Cathode Blocks with Electrolyte During Startup and in Service Wear. Infiltration

Microbial carbon cathodes

Molten carbonate cathodic oxygen reduction

Molten carbonate fuel cells cathodes

Nano-carbon materials cathode

Oxygen and Carbon on the Cathode Side

Oxygen cathodic reduction, molten carbonate fuel

Porous carbon cathode

Refractories and Carbon Cathode Materials for Aluminium Reduction Cells

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