Transport Cost

Recirculating systems can make aquaculture feasible in locations where conditions would otherwise not be conducive to successful operations. Such systems can also be used to reduce transportation costs by making it possible to grow animals near markets. In areas where there are concerns about pollution or the use of exotic species, closed systems provide an alternative approach to more extensive types of operations. 

About half of the wodd production comes from methanol carbonylation and about one-third from acetaldehyde oxidation. Another tenth of the wodd capacity can be attributed to butane—naphtha Hquid-phase oxidation. Appreciable quantities of acetic acid are recovered from reactions involving peracetic acid. Precise statistics on acetic acid production are compHcated by recycling of acid from cellulose acetate and poly(vinyl alcohol) production. Acetic acid that is by-product from peracetic acid [79-21-0] is normally designated as virgin acid, yet acid from hydrolysis of cellulose acetate or poly(vinyl acetate) is designated recycle acid. Indeterrninate quantities of acetic acid are coproduced with acetic anhydride from coal-based carbon monoxide and unknown amounts are bartered or exchanged between corporations as a device to lessen transport costs. 

Office of Pohcy, Planning, and Analysis, Assessment of Costs and Benefits ofElexible and Alternative Euel Use in the U.S. Transportation Sector, Technical Report 3 (Methanol Production and Transportation Costs) Pub. DOE/P/E—0093, U.S. Department of Energy, Washington, D.C., Nov. 

The choice of technology, the associated capital, and operating costs for a chlor—alkaU plant are strongly dependent on local factors. Especially important are local energy and transportation costs, as are environmental constraints. The primary difference ia operating costs between diaphragm, mercury, and membrane cell plants results from variations ia electricity requirements for the three processes (Table 25) so that local energy and steam costs are most important. 

The sustained world popularity of NSP results from simplicity of production and high agronomic quaHty as a carrier of available P2O5, calcium, sulfur, and usually some incidental micronutrients. In terms of agronomic value for large numbers of crops, no phosphate fertilizer has been shown to be superior to NSP. It is likely to remain in strong demand in parts of the world where simplicity of production or sulfur fertilization has high priority and where transportation costs are not prohibitive. 

The tabulation of plant nutrient costs, by product, ia Table 16 shows the principal reasoa for the popularity of anhydrous ammonia as a fertilizer ia the United States. The fob price per ton of nitrogen in the form of ammonia is less than half that for any other nitrogen product. Also, ammonia s relatively high nitrogen content of 82.2% favors low transportation costs, in spite of the need for specialized handling equipment and procedures. 

The TOSCOAL Process. The Oil Shale Corp. (TOSCO) piloted the low temperature carbonization of Wyoming subbituminous coals over a two-year period in its 23 t/d pilot plant at Rocky Falls, Colorado (149). The principal objective was the upgrading of the heating value in order to reduce transportation costs on a heating value basis. Hence, the soHd char product from the process represented 50 wt % of the starting coal but had 80% of its heating value. 

Plants for briquette production exist in the eastern part of Germany, AustraHa, and India. German transport costs pet unit of heating value ate about 40% less for briquettes than for lignite. 

The progress of LPG utilization has been closely related to progress in transportation (qv) and storage of this fuel. Large volumes of LPG must be transported from the producing plants to centers of consumption, and transportation costs are a principal factor in the cost of LPG to the consumer. 

Ammonia is usually transported for long distances by barge, pipeline, and rail, and for short distances by tmck Eactors that govern the type of carrier used in anhydrous ammonia transportation systems are distance, location of plant site in relation to consuming area, availabihty of transportation equipment, and relative cost of available carriers. Typical costs (83) of pipeline, barge, and rail modes for long distance transport are 0.0153, 0.0161, and 0.0215 per ton per kilometer, respectively, for distances of about 1600 km. Short distance tmck transportation costs (83) are much higher. Costs are typically 0.0365/(t km) for distances on the order of 160 km. 

Liquids. Some Hquid dyes are made directly from the thionation melt by additions of caustic soda and sodium hydrosulfide. Hydrotropic substances are sometimes added, either at the initial thionation stage or after the polysulfide melt is finished in order to keep the reduced dye in solution. Pardy reduced Hquids are also available. They are usually more concentrated than fully reduced Hquids, thus saving packaging and transportation costs. However, they require a further addition of reducing agent to the dyebath in order to obtain full color value. On the other hand, fully reduced Hquids are... 

Ocean Disposal. Disposal of raw or treated sludge by barging to sea was practiced for many years by some coastal cities, but today is highly controversial, and it appears that this method will be no longer economically feasible. Federal regulations require that sludge be taken to disposal sites about 160 km from the coast, whereas formerly, disposal sites were permitted within 20 km offshore. Transportation costs are expected to be so high that ocean disposal will be discontinued. 

A large portion of the carbon dioxide recovered is used at or near the location where it is generated as an ingredient in a further processing step. In this case, the gaseous form is most often used. Low temperature Hquid and soHd carbon dioxide are used for refrigeration. Where the producer and the consumer are distant, carbon dioxide maybe Hquifted to reduce transportation cost and revaporized at the point of consumption. 

Clays or shales that may be utilized ia the manufacture of bricks, tiles, and other heavy clay products exist ia every state ia the United States. (See Building materials, survey). Some blending of materials is often necessary to control shrinkage of the product, and the economics of manufacture are governed by the demands of fuel, labor, transportation costs, and the market. 

For by-product coke ovens, it is general practice to blend two or more types of coals that have complimentary technical as well as economic characteristics. Because most by-product coke plants are located near the large industrial users of the coke and by-products, coals usually have to be transported from the coal mines to the coke plants. Thus coal blends are designed on integration of coke quaUty needs, by-product quaUty needs, coal costs, transportation costs, impacts of productivity, and impacts on the coke ovens themselves. The physical behavior of coal blends during coking can damage coke ovens. 

Plant locations and capacities. While producing a product at the nearest plant usually lowers transportation costs, plant capacity limitations sometimes dictate otherwise. 

The mixed refrigerant cwcle was developed to meet the need for hq-uefying large quantities of natural gas to minimize transportation costs of this fuel. This cycle resembles the classic cascade cycle in principle and may best be understood by referring to that cycle. In the latter, the natural gas stream after purification is cooled successively by vaporization of propane, ethylene, and methane. Each refrigerant may be vaporized at two or three pressure levels to increase the natural gas coohng efficiency, but at a cost of considerable increased process complexity. 

Advantages of the drum are protection of contents, ease of reclosure, and appreciable reuse-resale value. A serious limitation is the inefficient use of space because of the cylindrical shape, which results in high storage and transportation costs. To overcome this, a fiber drrtm with a square cross section (Ro-Con drum) and the brtlk corrugated bag in box have been developed. 

When customers maintain small inventories, truck dehveiy is often used, provided the location of the supply point is nearby, usually 550 km (300 mi) or less, and dehveries are frequent. If, however, a user maintains large inventories, dehveries are ordinarily made by rail. Other parameters influencing choice are transportation cost operating costs of suppher loading facihties customer receiving and unloading facilities turnaround time for the container and the num-... 

Transportation Costs Most waste trucddug is done by commercial and hazardous waste firms. Costs are quoted per load, based on cost for transport (charged per load mile) from point of generation to its destination at a landfill or TSD facility. A strategy wriich permits shipment of full truckloads minimizes the transportation cost per ton. 

Frequently wall thicknesses are increased to meet the planned service life, resulting in a considerable increase in the materials used. This not only raises installation and transport costs but also the weight, which makes construction more difficult. 

Economic evaluations of waste-reduction options should involve a comparison of operating costs to illustrate where cost savings would accrue. For example, a waste-reduction measure that reduces the amount of raw material lost down the drain during the process will reduce raw-material costs. Raw-material substitution or process changes may reduce the amount of solid waste that must be transported offsite, reducing the transport costs for waste disposal. 

Component and material costs Overheads Packaging costs Transportation costs Development recovery costs Profit margins... 

Cost of business interruption. The cost of business interruption is significantly influenced by various commercial factors. For example, if you are not producing at fiill capacity it may be possible to make up lost production at other facilities or when the plant comes back into operation. The business interruption costs will only be the additional costs of production, transportation and any lost sales. As these conditions can vary from month to month it may be more appropriate to adopt a standard method of calculating business interruption costs for PSM and ESH purposes. One commonly adopted approach is to estimate the tonnage of production lost and calculate the cost as being the difference between the sale price and all manufacturing, storage and transportation costs. 

For many processes, one or more predominant factors effectively minimize the number of possibilities for plant location. Raw material and transportation costs may be such that a plant must be located near a source. Thus, only the sites near to sources of raw material need be studied and these may be few in number. Similarly, labor requirements may be hear y enough to eliminate cities below a certain size. These and other factors serve as effective screening agents that save both time and money. 

The cost of N2, like that of O2, is particularly dependent on electricity costs, though plant maintenance and transport costs also obtrude. Typical prices in 1992 for No in the USA were about 32 per tonne for bulk liquid (exclusive of transportation and handling charges). Costs for small-scale users of N2 from gas cylinders are proportionately much higher. 

The sulfur content of coals available to utilities ranges from about 4 percent in high-sulfur coals to less than 1 percent in some Western coals. Although transportation costs maybe higher for Western coals, many Eastern utilities elect to burn Western coals to comply with increasingly stringent SO, regulations. 

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