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Temperature moderating steam

In addition to coal moisture, water is often added to the process as temperature-moderating steam or as liquid transport medium. Consequentiy, reactions such as a water-gas shift (4.9) or homogeneous methanation (4.10) may influence the final gas composition. [Pg.109]

At present, the most important industrial method for producing hydrogen is the three-step, steam-hydrocarbon re-forming process. The first step in the process is the conversion of steam and methane to a mixture of carbon monoxide and hydrogen known as synthesis gas (so-called because it can be used as the starting material for the synthesis of liquid fuels). The reaction requires high temperature, moderately high pressure, and a nickel catalyst ... [Pg.579]

Optionally, the gasifier may be fed with a slurry of coal in oil and a controlled amount of reaction temperature moderator, such as steam. Facilities for recycling unconverted coal are also provided. A schematic flow diagram of the process is shown in Figure 2. [Pg.192]

The complete oxidation to carbon dioxide and water and the water gas shift reaction are both highly exothermic and, for heavy hydrocarbon feeds, a temperature moderator such as steam or carbon dioxide must be used to control the temperature and adjust the Hj/CO ratio of the syngas product [17]. A moderator is not needed for natural gas feedstock. [Pg.69]

As with silicone mbber, ethylene propylene mbber can give an aldehyde odour. Ethylene propylene mbber is highly resistant to water, alkali and dilute acids, and moderately to poorly resistant to hydrocarbons, lipids and concentrated acids. It is resistant to the high temperatures of steam sterilisation. [Pg.511]

In terms of dry feeding, every stream preheat requires higher moderator steam consumption in order to maintain a constant temperature, leading to increased H2 production. [Pg.164]

The heat loss through the wall can be used to generate jacket steam on an appropriate pressure level, which can be easily integrated to the process as temperature moderator. [Pg.251]

All non-slurry systems require moderator steam to process Pitt 8 coal this applies to all new concepts. For SAf coal, mineral matter moderates the temperature to some extent. Consequently, only the fluid-bed systems require steam as a gasifying agent. Only for the standard Siemens, new Shell, and new GE-Q configurations is there any question as to whether the moderator steam demand can be covered by the internal steam production during gasification. [Pg.327]

Under current LWR design standards, bottom mounted inlet coolant pipes are not allowed from LOCA considerations. The inlet coolant compressors are necessary. These are larger in capacity and power consumption than feedwater pumps of LWRs, because of the low density of the high temperature supercritical steam. These factors finally led to a loss of interest in developing the water moderated, supercritical steam cooled reactor. [Pg.623]

Recovery of Ammonia. The filter Hquor contains unreacted sodium chloride and substantially all the ammonia with which the brine was originally saturated. The ammonia may be fixed or free. Fixed ammonia (ammonium chloride [12125-02-97]) corresponds stoichiometrically to the precipitated sodium bicarbonate. Free ammonia includes salts such as ammonium hydroxide, bicarbonate, and carbonate, and the several possible carbon—ammonia compounds that decompose at moderate temperatures. A sulfide solution may be added to the filter Hquor for corrosion protection. The sulfide is distilled for eventual absorption by the brine in the absorber. As the filter Hquor enters the distiller, it is preheated by indirect contact with departing gases. The warmed Hquor enters the main coke, tile, or bubble cap-fiUed sections of the distiller where heat decomposes the free ammonium compounds and steam strips the ammonia and carbon dioxide from the solution. [Pg.523]

The monochlorotoluenes are stable to the action of steam, alkahes, amines, and hydrochloric and phosphoric acids at moderate temperatures and pressures. Three classes of reactions, those involving the aromatic ring, the methyl group, and the chlorine substituent, are known for monochlorotoluenes. [Pg.53]


See other pages where Temperature moderating steam is mentioned: [Pg.530]    [Pg.177]    [Pg.205]    [Pg.213]    [Pg.530]    [Pg.1563]    [Pg.7]    [Pg.367]    [Pg.157]    [Pg.160]    [Pg.173]    [Pg.247]    [Pg.258]    [Pg.264]    [Pg.273]    [Pg.294]    [Pg.304]    [Pg.306]    [Pg.344]    [Pg.38]    [Pg.621]    [Pg.250]    [Pg.832]    [Pg.269]    [Pg.503]    [Pg.505]    [Pg.59]    [Pg.421]    [Pg.36]    [Pg.212]    [Pg.220]    [Pg.512]    [Pg.234]    [Pg.255]    [Pg.526]    [Pg.110]    [Pg.110]    [Pg.268]    [Pg.269]   
See also in sourсe #XX -- [ Pg.109 ]




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Moder

Moderant

Moderants

Moderate temperature

Moderates

Moderation

Moderator

Moderator temperature

Steam temperature

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