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Feedstock ammonia

The strength and quantity of wastewaters generated by hydrotreating depends upon the subprocess used and feedstock. Ammonia and sulfides are the primary contaminants, but phenols may also be present if the feedstock boiling range is sufficiently high. [Pg.251]

In the past, coal or heavy hydrocarbon feedstock ammonia plants were not economically competitive with plants where the feedstocks were light hydrocarbons (natural gas to naphtha). Because of changing economics, however, plants that can handle heavy hydrocarbon feedstock are now attracting increasing attention- In addition, the continuous development and improvement of partial oxidation processes at higher pressure have allowed reductions in equipment size and cost. Therefore, the alternate feedback ammonia plants based on a partial oxidation process may become economically competitive in the near future. [Pg.85]

In 1991, the relatively old and small synthetic fuel production faciHties at Sasol One began a transformation to a higher value chemical production facihty (38). This move came as a result of declining economics for synthetic fuel production from synthesis gas at this location. The new faciHties installed in this conversion will expand production of high value Arge waxes and paraffins to 123,000 t/yr in 1993. Also, a new faciHty for production of 240,00 t/yr of ammonia will be added. The complex will continue to produce ethylene and process feedstock from other Sasol plants to produce alcohols and higher phenols. [Pg.167]

The only other petrochemical feedstock of significant commercial use is methane (natural gas) which is used primarily to produce ammonia and methanol. Consumption factors are about 28 GJ and 31 GJ per metric ton, respectively (58,300 and 64,700 BTU/lb) (8). Approximately... [Pg.175]

Coal is expected to be the best domestic feedstock alternative to natural gas. Although coal-based ammonia plants have been built elsewhere, there is no such plant in the United States. Pilot-scale projects have demonstrated effective ammonia-from-coal technology (102). The cost of ammonia production can be anticipated to increase, lea ding to increases in the cost of producing nitrogen fertilizers. [Pg.243]

Feedstock Purification Manufacture of Synthesis Gases Hydrogen, Ammonia, Methanol, product bulletin. United Catalysts, Inc., Louisville, Ky. [Pg.462]

This excess hydrogen is normally carried forward to be compressed into the synthesis loop, from which it is ultimately purged as fuel. Addition of by-product CO2 where available may be advantageous in that it serves to adjust the reformed gas to a more stoichiometric composition gas for methanol production, which results in a decrease in natural gas consumption (8). Carbon-rich off-gases from other sources, such as acetylene units, can also be used to provide supplemental synthesis gas. Alternatively, the hydrogen-rich purge gas can be an attractive feedstock for ammonia production (9). [Pg.276]

Operational Constraints and Problems. Synthetic ammonia manufacture is a mature technology and all fundamental technical problems have been solved. However, extensive know-how in the constmction and operation of the faciUties is required. Although apparendy simple in concept, these facihties are complex in practice. Some of the myriad operational parameters, such as feedstock source or quaUty, change frequendy and the plant operator has to adjust accordingly. Most modem facihties rely on computers to monitor and optimize performance on a continual basis. This situation can produce problems where industrial expertise is lacking. [Pg.84]

Amides can be produced from fatty acid methyl esters by reaction with ammonia at 220 °C at 12.4 MPa (1800 psi) pressure. Reaction times are reduced to 1 h by this route however, the fatty acid feedstocks must fkst be converted to methyl esters (21). [Pg.183]

Between 1930 and 1950, the primary emphasis of ammonia process development was ia the area of synthesis gas generation (3) (see Fuels, SYNTHETIC, GASEOUS FUELs). Extensive coal deposits ia Europe provided the feedstock for the ammonia iadustry. The North American ammonia iadustry was based primarily on abundant suppHes of low cost natural gas (see Gas, natural). [Pg.339]

Synthesis Gas Preparation Processes. Synthesis gas for ammonia production consists of hydrogen and nitrogen in about a three to one mole ratio, residual methane, argon introduced with the process air, and traces of carbon oxides. There are several processes available for synthesis gas generation and each is characterized by the specific feedstock used. A typical synthesis gas composition by volume is hydrogen, 73.65% nitrogen, 24.55% methane, <1 ppm-0.8% argon, 100 ppm—0.34% carbon oxides, 2—10 ppm and water vapor, 0.1 ppm. [Pg.340]

AMMONIA Raw material Process description Feedstock conversion reaction V012... [Pg.341]

Of the raw material hydrogen sources—natural gas, coal, and petroleum fractions—natural gas is the most often employed in ammonia plants in the 1990s and steam reforming is by far the most often used process. Partial oxidation processes are utilized where steam-reformable feeds are not available or in special situations where local conditions exist to provide favorable economics. Table 5 fists the contribution of the various feedstocks to world ammonia... [Pg.341]

Table 5. Feedstocks for World Ammonia Capacity, Annual %... Table 5. Feedstocks for World Ammonia Capacity, Annual %...
Table 6. Energy Required for Ammonia Production based on Feedstock Process, GJ/t... Table 6. Energy Required for Ammonia Production based on Feedstock Process, GJ/t...
In the 1980s, however, the prices of oil and natural gas reversed their upward trends. Natural gas discoveries, both on-shore and off-shore, have considerably iacreased the world s energy supply and oil discoveries, many with associated gas, contributed more feedstock potential for ammonia production. [Pg.345]

Steam-Reforming Natural Gas. Natural gas is the single most common raw material for the manufacture of ammonia. A typical flow sheet for a high capacity single-train ammonia plant is iadicated ia Figure 12. The important process steps are feedstock purification, primary and secondary reforming, shift conversion, carbon dioxide removal, synthesis gas purification, ammonia synthesis, and recovery. [Pg.345]

Ammonia production per se is relatively clean compared to other chemical process industries, and presents no unique environmental problems. Synthesis gas generation is the principal area requiring environmental controls and the nature of the controls depends on the feedstock and method of processing. [Pg.353]

As can be seen from this analysis, the natural gas feedstock and capital charges amount to over 93% of the total production cost before return on investment. Therefore, energy consumption and capital investment are the key factors in determining ammonia production profitabiUty. [Pg.356]

Transportation and Distribution Cost. Although much ammonia serves as feedstock for other processes, the largest single use in the United States is as a direct appHcation fertiliser without further processing. This direct appHcation consumption is mosdy in the farm belt and ammonia produced in the Gulf Coast states is shipped to terminal faciUties and then distributed by retail outlets to the farmer. [Pg.356]


See other pages where Feedstock ammonia is mentioned: [Pg.387]    [Pg.128]    [Pg.387]    [Pg.128]    [Pg.128]    [Pg.165]    [Pg.169]    [Pg.216]    [Pg.76]    [Pg.421]    [Pg.428]    [Pg.149]    [Pg.160]    [Pg.457]    [Pg.42]    [Pg.83]    [Pg.83]    [Pg.353]    [Pg.481]    [Pg.206]    [Pg.206]    [Pg.339]    [Pg.341]    [Pg.342]    [Pg.343]    [Pg.344]    [Pg.344]    [Pg.345]    [Pg.352]    [Pg.353]    [Pg.354]    [Pg.355]   


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Ammonia Plants Using Coal as Feedstock

Feedstock for ammonia synthesis

Producing the Feedstocks and Oxidizing Ammonia

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