Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Hazards of Water in Refinery Process

Some years ago, Standard Oil Company (Indiana) published a 70-page booklet entitled Hazards of Water in Refinery Process Equipment. [1] This booklet appears to be a bible for hands-on refinery employees, and it provides easy-to-understand fundamentals on the hazards. The booklet concludes with these thoughts ... [Pg.57]

A similar incident involving steam condensation was reported in the Hazard of Water in Refinery Process Systems [6], where the caption on a photo of a badly damaged tank states, A vacuum vent and one open hatchway was not enough to prevent damage when steam condensed and pulled in the top two courses of this 35 ft. diameter by 21 ft. high wash tank. ... [Pg.87]

Standard Oil Company (Indiana), Hazards of Water in Refinery Process Systems, Chicago, 111.,... [Pg.90]

The Hazards of Water in Refinery Process Systems booklet [IJ states that confined water will increase 50 psi (345 kPa) for every degree Fahrenheit in a typical case of moderate temperatures. In short, a piece of piping or a vessel that is completely liquid-full at 70° F and 0 psig will rise to 2,500 psig if it is warmed to 120° F. This concept is displayed better in Figure 3-8. [Pg.60]

The Hazard of Water in Refinery Process Systems [6] illustrates the benefits of a vapor space with increasing temperature of water. If water is confined in a piping system with a vapor space, and then heated, the pressure rises more slowly until it becomes too small due to compression or disappears due to the solubility of air in water. If a simple water system piping has a vapor space of 11.5% air at 70°F (21°C) and atmospheric pressure (0 psi or 0 kPa), if it is heated to 350°F (177°C) the pressure will rise to 285 psi (1954 kPa) with only a 1.2% vapor space remaining. Pressures shoot up in the next 20°F as the vapor space compresses to near 0%. [Pg.158]

Sharing the Experience booklets 2003-2004 are now available to refinery and chemical process employees for a wide range of topics of interest. BP is currently reinvigorating the series, but as of this time it is not distributed via the normal book sales route (I do not think it ever was). These superb booklets cover fundamentals and are backed up by numerous case histories of hard-learned lessons. They are chock-full of easily understood illustrations and up-to-date color photos. The Sharing the Experience booklet series is a practical, timeless process safety masterpiece that should be available in every control room. The booklet on the hazards of water was first published about 50 years ago and improved to perfection. [Pg.308]

According to a USEPA survey, many of the more than 150 separate processes used in petroleum refineries generate large quantities of hazardous wastes. Typical wastes generated from refinery processes include bottom sediments and water from crude storage tanks, spent amines, spent acids and caustics, spent clays, spent glycol, catalyst fines, spent Streford solution and sulfur. [Pg.261]

Cyanide compounds are useful to society in terms of their key role in synthetic and industrial processes, for certain fumigation and agricultural uses, and for some therapeutic applications (Ballantyne and Marrs 1987). Cyanides are present in effluents from iron and steel processing plants, petroleum refineries, and metal-plating plants, and constitute a hazard to aquatic ecosystems in certain waste-receiving waters (Smith et al. 1979) and to livestock (USEPA 1980 Towill et al. 1978). Cyanide serves no useful purpose in the human body, yet it is present in our food, air, and water (Becker 1985). [Pg.907]

Another means of protecting against the explosion hazard in flammable atmospheres is to employ gas detectors. The principle is that the gas detectors detect flammable gas/air mixtures at a low percentage, typically 10%, of the LEL and cause an alarm to sound. If the concentration reaches 25% or so of the LEL, the system automatically initiates a shutdown of the process. This type of technique is commonly used in process plants such as oil and gas refineries, LEG storage tank farms, chlorine doping rooms in water treatment plants, and on vehicles such as electric fork lift trucks operating in Zone 1 and 2 areas. [Pg.271]


See other pages where Hazards of Water in Refinery Process is mentioned: [Pg.67]    [Pg.67]    [Pg.129]    [Pg.661]    [Pg.96]    [Pg.744]    [Pg.203]    [Pg.99]    [Pg.132]    [Pg.509]    [Pg.97]    [Pg.87]    [Pg.1392]    [Pg.361]    [Pg.411]    [Pg.243]    [Pg.372]    [Pg.93]    [Pg.317]    [Pg.501]    [Pg.907]    [Pg.271]   


SEARCH



Hazard of Water in Refinery Process Systems

Process hazards

Process water

Refineries

Refinery processes

Water hazards

Water processing

© 2024 chempedia.info