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Plant combustion

Incineration in an approved combustion plant is the preferred method of disposal. Wastewater from succinic acid processes is suitable for biological degradation by activated sludge (188). Polymeric sorbents (189) and ferric chloride treatment processes (190) can also be used for wastes containing... [Pg.538]

Sets out ancillary controls related to air pollution control including regulation of smoke, grit, dust and fume emissions from non-prescnbed mdustnal processes provision of a lower level of control over some smaller combustion plants not covered by IPC or LAAPC prohibition of the emission of dark smoke from any chimney or industrial premises. [Pg.596]

In particular, the cycles involving fuel or oxidant modification do not look sufficiently attractive for their development to be undertaken, with the possible exception of the multiple PO combustion plant proposed by Harvey et al. [14]. The Matiant plant has the advantage of relatively simple CO2 removal and high efficiency and may prove to be attractive, but it again looks complex and expensive. [Pg.163]

EC Directives on emissions from large combustion plant 19/292... [Pg.260]

Details are given of the development of energy and material recycling processes for thermosetting polymer composites. Applications in the cement industry and in coal fired fluidised bed combustion plants are discussed. 3 refs. [Pg.103]

The C02 gas quality has significant impact on the capture cost by this technology, and uncertainties on the future regulatory requirements of C02 quality for its transport and storage has influence on the process configuration of the oxy-combustion plant, gas cleaning unit performance, overall C02 recovery capacity and on the energy requirements for C02 compression and purification. [Pg.88]

An explosion in the vent of an ammonia combustion plant was attributed to deposition of ammonium nitrite/nitrate crystals. It is considered that the very unstable nitrite acts as a sensitiser to the nitrate, and that explosion is triggered by contact with acid. [Pg.1589]

Conventional combustion plants are about 35% efficient (fuel-to-electricity). Coal gasification could boost efficiencies to 50% in the near term and to 60% with technology improvements. Higher efficiencies mean better economics and reduced greenhouse gases. [Pg.198]

Watt, J. D., The Physical, and Chemical Behaviour of the Mineral Matter in Coal Under Conditions Met in Combustion Plant. Part I, The Occurrence, Origin, Identity, Distribution, and Estimation of the Mineral Species in British Coals, British Coal Utilization Research Association, Literature Survey, 121 p., Leatherhead, Surrey, England, 1968. [Pg.26]

LCP Directive Directive 2001/80/EC of the European Parliament and of the Council of 23 October 2001 on the limitation of emissions of certain pollutants into the air from large combustion plants... [Pg.28]

Combustion plants Combustion gases Sulfur dioxide Water, alkaline solutions Pollutant removal Stripping normally not practiced... [Pg.6]

Wood powder is a kind of upgraded fuel that is burned in large-scale combustion plants for heat production. However, it is possible to use wood powder for power generation as well. It is a biofuel made of sawdust, shavings and bark. The raw material is crushed, dried and milled to tine particles in order to obtain the best fuel properties. There are many different wood powder qualities dependant on different physical properties such as particle size distribution, particle shape and also moisture content. The powder is usually handled in a closed system from milling to storing in silos to avoid the risk of dust explosions. The raw materials and type of mill used determine the properties of the wood powder (Paulrud et al, 2002). [Pg.145]

Combustion can be carried out on a small scale (for household heat production), on a medium scale (in hospitals, government offices, etc.) and on a large scale (in combustions plants for industrial purposes) (McKendry, 2002). [Pg.165]

Several proposals have been made to install a catalyst in the space beneath the ammonia oxidation gauzes in the converter. In 1999 BASF was testing a Cu-Zn-Al spinel catalyst in a production plant. They reported an 80% reduction in N20 (from 1000 ppm down to 200 ppm) in an atmospheric combustion plant... [Pg.240]

In order to avoid the unfavorable process conditions, different flue-gas treatment processes for combustion plants based on catalytic filters were developed, which combine fly-ash removal with SCR of ISKh with NH3 [4—8], The advantages of these processes are space and treatment-cost savings, reduced internal and external mass transfer resistances compared to honeycomb SCR catalysts, heat recovery from offgases with good efficiency, and low corrosion problems due to the removal of both dust and NOx at high temperatures. [Pg.438]

Combustion plants are classical chemical fluidization plants. The stationary and circulating fluidized bed combustions must be differentiated one from another. The... [Pg.455]

Korischem and Werner [49, 50] simulated the procedures of flue-gas scrubbing of an industrial waste combustion plant. Their model considered the mass and heat transfer process between gas and liquid phase by neglecting the solids present in the suspension. [Pg.457]

Another approach to the suppression of catalytic activity has been taken by workers at the University of Waterloo.26,42-44 After conducting extensive laboratory trials on flyash obtained from a variety of combustion plants, an amine-based destroyer/inhibitor mixture was formulated. This reactant was injected into the boiler of a MSW incinerator in an amount that represented 7-10% of the flyash loading in the flue gas the destroyer in the temperature window 590 + 50°C, and the inhibitor in the temperature window 375 + 50°C. Overall reductions in PCDD/F formation of 80-94% were claimed. This approach has yet to be made commercially available. [Pg.175]

Okes, E. J Javen, J., and Engstrom, F. Startup and Operating Experience at the Kattua 22-MWe Cogeneration Circulating Fluidized Bed Combustion Plant, Proc. Am. Power Conf., Vol. 44, p. 64 (1982). [Pg.75]

Plass, L., Daradimos, G., and Lienhard, H. Power Plants with Circulating Fluidized-Bed Combustion Plant Design and Operating Experience, VDI-Ber., 574, 125 (1985). [Pg.76]

Table V. Capital Cost of Hydrocarbonization-Pressurized, Fluid-Bed Combustion Plant (1977 Dollars)... Table V. Capital Cost of Hydrocarbonization-Pressurized, Fluid-Bed Combustion Plant (1977 Dollars)...

See other pages where Plant combustion is mentioned: [Pg.522]    [Pg.566]    [Pg.566]    [Pg.567]    [Pg.98]    [Pg.522]    [Pg.566]    [Pg.566]    [Pg.567]    [Pg.87]    [Pg.464]    [Pg.574]    [Pg.273]    [Pg.131]    [Pg.108]    [Pg.30]    [Pg.295]    [Pg.346]    [Pg.456]    [Pg.346]    [Pg.203]   
See also in sourсe #XX -- [ Pg.192 , Pg.193 , Pg.194 ]




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