Manganese continued

Manganese (continued) carbonyl halides, 3 78, 79-80 complexes with phosphine, etc., 6 10 carbonyls... 

Manganese (.continued) salen complexes, 46 394-400 salts, lattice energy and thermochemistry, 22 48-51... 

Manganese. Continuous series of solid solutions. Alloys with more than 40 per cent, cobalt are markedly magnetic, this property increasing with cobalt content. Hiege, Zeitsch. anorg. Chem., 1913, 83, 253. 

Table 7-1. Regulations and Guidelines Applicable to Manganese (continued)...

Most all the serious emptions of manganese furnaces can be traced to a set of conditions that cause bridging or hang-up of the charge materials so that the normal downward movement through the furnace is dismpted or retarded. As electrical energy continues to be suppHed to the furnace with Httie... 

Electrolytic Manganese Dioxide. The anodic oxidation of an Mn(II) salt to manganese dioxide dates back to 1830, but the usefuhiess of electrolyticaHy prepared manganese dioxide for battery purposes was not recognized until 1918 (69). Initial use of electrolytic manganese dioxide (EAfD) for battery use was ia Japan (70) where usage continues. 

Eigure 3 is a flow diagram which gives an example of the commercial practice of the Dynamit Nobel process (73). -Xylene, air, and catalyst are fed continuously to the oxidation reactor where they are joined with recycle methyl -toluate. Typically, the catalyst is a cobalt salt, but cobalt and manganese are also used in combination. Titanium or other expensive metallurgy is not required because bromine and acetic acid are not used. The oxidation reactor is maintained at 140—180°C and 500—800 kPa (5—8 atm). The heat of reaction is removed by vaporization of water and excess -xylene these are condensed, water is separated, and -xylene is returned continuously (72,74). Cooling coils can also be used (70). 

Fig. 7. Performance comparison of "D"-size alkaline—manganese vs carbon-zinc batteries at 21°C on (a) alight drain 150-Q continuous test at 21°C, and...

Oxidation. Carbon monoxide can be oxidized without a catalyst or at a controlled rate with a catalyst (eq. 4) (26). Carbon monoxide oxidation proceeds explosively if the gases are mixed stoichiometticaHy and then ignited. Surface burning will continue at temperatures above 1173 K, but the reaction is slow below 923 K without a catalyst. HopcaUte, a mixture of manganese and copper oxides, catalyzes carbon monoxide oxidation at room temperature it was used in gas masks during World War I to destroy low levels of carbon monoxide. Catalysts prepared from platinum and palladium are particularly effective for carbon monoxide oxidation at 323 K and at space velocities of 50 to 10, 000 h . Such catalysts are used in catalytic converters on automobiles (27) (see Exhaust CONTHOL, automotive). 

Catalytic Oxidation for Straight-Chain Paraffinic Hydrocarbons. Synthetic fatty acids (SFA) are produced by Eastern European countries, Russia, and China using a manganese-catalyzed oxidation of selected paraffinic streams. The technology is based on German developments that were in use during World War II. The production volume in 1984 was estimated to be about 5.5 x ICf t/yr. The oxidation is highly exothermic and is carried out at about 105—125°C, mostly in continuous equipment. 

The EBDCs are prepared by reaction of EDA with carbon disulfide in the presence of sodium or ammonium hydroxide initially, then with 2inc and/or manganese salts, as appropriate (156—160). A continuous process has recendy been reported (161). The common names of these salts are nabam [142-59-6] (Na salt), amobam (ammonium salt), 2ineb [12122-67-7] (Zn salt), maneb [12427-38-2] (Mn salt), andmanco2eb. 

---