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Shut-downs

Ultimately, the process might be permanently shut down or given a major revamp. This marks the end of the project, H. If the process is shut down, working capital is recovered, and there may be salvage value, which would create a final cash inflow at the end of the project. [Pg.423]

Capital and operating costs will increase as more separator stages are added to the process line, so a balance has to be struck between increased oil yield and cost. It is uncommon to find that economics support more than 3 stages of separation and one or two stage separation is more typical. The increased risk of separation shut down is also a contributing factor in limiting numbers. [Pg.244]

The legs of the platform can be used as settling tanks or temporary storage facilities for crude oil where oil is exported via tankers, or to allow production to continue in the event of a pipeline shut down. The Brent D platform in the North Sea weighs more than 200,000 tonnes and can store over a million barrels of oil. Topside modules are either installed offshore by lift barges, or can be positioned before the platform is floated out. [Pg.266]

In any case it has to be taken into account, that the paper mills have to reduce their shut down periods to an absolute minimum because of the economical pressure coming from the globalisation of the industry. [Pg.33]

Beside all these safety reasons, we are able to test 2 or 3 drums at the same time and by some improvements of the application we are able to reduce the test-period down to 4 hours, which results in an also for the production sufficient number of tested drums during the short shut down periods. These increase the availability and the production output of a plant and result therefore in a gain of safety an economical competitiveness of the European industry. [Pg.34]

Even the replacement of the hydrotest by a NDT method is only sufficient, if you perform much more than it is usual today e.g. a complete ET of the cylindrical part, which requires the possibility to rotate the drum during the shut down and is therefore much more time consuming and expensive. [Pg.34]

The only meaningful solution is a pneumatic test in conjunction with an AE. Beside the high sensitivity of an AE and its reliability in combination with an established and proven data base, the method can be performed by experienced testing agencies easily and within short shut down period. A lot of 4 up to 9 drums can be tested within one day. [Pg.34]

By analysing the scans, different types of tube characteristics, wastage patterns or profiles can be documented and effectively used to make immediate decisions during shut downs and in planning maintenance programs. [Pg.1033]

Wlien a strong electron-donor ligand such as pyridine is added to tlie reaction mixture, it can bond so strongly to tlie Rli tliat it essentially drains off all tlie Rli and shuts down tlie cycle it is called a catalyst poison. A poison for many catalysts is CO it works as a physiological poison in essentially the same way as it works as a catalyst poison it bonds to tlie iron sites of haemoglobin in competition witli O. ... [Pg.2703]

The commercial form of Cartesian manostat, model 7A, is depicted in Fig. II, 23, 7 it is normally charged with mercury except for very low pressures when di-w-butyl phthalate is employed. The manostat is highly sensitive in its action furthermore, once the pressure has been set in the instrument, the system may be shut down without disturbing the setting. [Pg.116]

In many applications of mass spectrometry, it is necessary to obtain a mass spectrum from a sample dissolved in a solvent. The solution cannot be passed directly into the mass spectrometer because, in the high vacuum, the rapidly vaporizing solvent would entail a large pressure increase, causing the instrument to shut down. [Pg.389]

Chain reactions do not go on forever. The fog may clear and the improved visibility ends the succession of accidents. Neutron-scavenging control rods may be inserted to shut down a nuclear reactor. The chemical reactions which terminate polymer chain reactions are also an important part of the polymerization mechanism. Killing off the reactive intermediate that keeps the chain going is the essence of these termination reactions. Some unusual polymers can be formed without this termination these are called living polymers. [Pg.346]

Most aquaculture faciUties release water constandy or periodically into the environment without passing it through a municipal sewage treatment plant. The effects of those efduents on natural systems have become a subject of intense scmtiny in recent years and have, in some instances, resulted in opposition to further development of aquaculture faciUties in some locales. There have even been demands that some existing operations should be shut down. [Pg.20]

Single-point cahbrations and 2ero deterrninations are performed whenever instmments are shut down and/or relocated to a different sampling location. Should the recahbration vary by more than 10% of the value obtained during the initial cahbration, the analy2er is recahbrated until stable cahbration data are obtained. [Pg.90]

U.S. producers and capacities for PX, OX, and EB are summarized ia Table 8. Amoco is the only producer of MX with an annual capacity of 110,000 t. In recent years, many small xylene plants have shut down because the operations were not economic or the technology being used was obsolete. [Pg.423]

In the 1980s cost and availabiUty of acetylene have made it an unattractive raw material for acrylate manufacture as compared to propylene, which has been readily available at attractive cost (see Acetylene-DERIVED chemicals). As a consequence, essentially all commercial units based on acetylene, with the exception of BASF s plant at Ludwigshafen, have been shut down. AH new capacity recendy brought on stream or announced for constmction uses the propylene route. Rohm and Haas Co. has developed an alternative method based on aLkoxycarbonylation of ethylene, but has not commercialized it because of the more favorable economics of the propylene route. [Pg.152]

These processes use expensive C2 hydrocarbons as feedstocks and thus have higher overall acrylonitrile production costs compared to the propylene-based process technology. The last commercial plants using these process technologies were shut down by 1970. [Pg.184]

Sodium Hydroxide. Before World War 1, nearly all sodium hydroxide [1310-93-2], NaOH, was produced by the reaction of soda ash and lime. The subsequent rapid development of electrolytic production processes, resulting from growing demand for chlorine, effectively shut down the old lime—soda plants except in Eastern Europe, the USSR, India, and China. Recent changes in chlorine consumption have reduced demand, putting pressure on the price and availabiHty of caustic soda (NaOH). Because this trend is expected to continue, there is renewed interest in the lime—soda production process. EMC operates a 50,000 t/yr caustic soda plant that uses this technology at Green River it came onstream in mid-1990. Other U.S. soda ash producers have aimounced plans to constmct similar plants (1,5). [Pg.527]

The KDF filter was first tested in prototype on a coal mine in northern Germany. It was installed in parallel with existing vacuum filters and it produced filter cakes consistendy lower in moisture content by 5 to 7% than the vacuum filters. Two production models have been installed and operated on a coal mine in Belgium. The filter is controlled by a specially developed computer system this consists of two computers, one monitoring the function of the filter and all of the detection devices installed, and the other controlling the filtration process. The system allows optimization of the performance, automatic start-up or shut-down, and can be integrated into the control system of the whole coal washing plant. [Pg.406]

Coal Liquefaction at Wilsonville. Starting ia 1974 the Advanced Coal Liquefaction R D Facihty at WilsonviUe, Alabama operated a 6 t/d pilot plant and studied various coal Hquefaction processiag schemes. The facihty, cosponsored by the DOE, the Electric Power Research Institute (EPRI) and Amoco Oil Co, was shut down ia early 1992. [Pg.92]

These units have been shut down. [Pg.360]

The mode of action is by inhibiting 5-enolpymvyl-shikimate-3-phosphate synthase. Roundup shuts down the production of the aromatic amino acids phenylalanine, tyrosine, and tryptophane (30). Whereas all these amino acids are essential to the survival of the plant, tryptophane is especially important because it is the progenitor for indole-3-acetic acid, or auxin, which plays an important role in growth and development, and controls cell extension and organogenesis. [Pg.421]

There have been many variations in the design of electric arc reactors but only three have been commercialized. The most important is the installation at Hbls. The other commercial arc processes were those of Du Pont (3) (a high speed rotating arc) and a Romanian process that produced both ethylene and acetylene. The Hbls process and the Romanian process (at Borzesti, Romania) are still operating, but the Du Pont process has been shut down since 1969. [Pg.384]

A commercial-scale SNG plant, the Great Plains Plant in North Dakota, was actually built and operated for several years using a scheme based on coal. However, upon termination of the government subsidy, the plant s owner, ANR Inc., found it uneconomical to continue plant operation and shut down the plant in the late 1980s. [Pg.399]

Stainless steel alloys show exceUent corrosion resistance to HCl gas up to a temperature of 400°C. However, these are normally not recommended for process equipment owing to stress corrosion cracking during periods of cooling and shut down. The corrosion rate of Monel is similar to that of mild steel. Pure (99.6%) nickel and high nickel alloys such as Inconel 600 can be used for operation at temperatures up to 525°C where the corrosion rate is reported to be about 0.08 cm/yr (see Nickel and nickel alloys). [Pg.446]


See other pages where Shut-downs is mentioned: [Pg.237]    [Pg.259]    [Pg.284]    [Pg.284]    [Pg.331]    [Pg.343]    [Pg.344]    [Pg.347]    [Pg.31]    [Pg.33]    [Pg.950]    [Pg.1032]    [Pg.816]    [Pg.2596]    [Pg.335]    [Pg.322]    [Pg.91]    [Pg.411]    [Pg.155]    [Pg.247]    [Pg.494]    [Pg.42]    [Pg.45]    [Pg.84]    [Pg.394]   
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Active shut-down systems

Emergency shut-down

Emergency shut-down stations

Engines shut-down system

Exchanger shut down procedures

Government shut-down

Mass balances for startup and shut down

Operating Procedures shut down

Output voltage shut-down

Passive shut-down mechanism

Plant shut-down

Plant start up/shut down

Precautions required when systems are shut down

Reactor shut-down

Reactor shut-down system

Self-actuated shut-down system

Shut-down circuits

Shut-down control

Shut-down system

Start-up/shut-down

Start-up/shut-down procedures

Startup-shut down cycles

Temporary shut-down

Ultimate shut-down systems

Vacuum systems shutting down

Water shut-down

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