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Process instrumentation

Process Instrumentation and Control Systems. Investment for instmmentation and control systems and their installation typically range between 3 to 10% of the total installed cost for a grassroots continuous process faciUty. Instmmentation and control systems also represent a substantial percentage of the overall faciUty maintenance (qv) costs. Investment costs may be placed in one of two categories, ie, nondiscretionary and discretionary. [Pg.78]

CHOPEY Instrumentation and Process Control CONNELL Process Instrumentation Applications Manual CONSIDINE Process/Industrial Instruments and Controls Handbook, Fourth Edition... [Pg.3]

The flow capacity of the transducer can be increased bv adding a booster relav like the one shown in Fig, 8-7.3/ , The flow capacity of the booster relav is nominally fiftv to one hundred times that of the nozzle amplifier shown in Fig, 8-7.3 3 and makes the combined trans-diicer/booster suitably responsive to operate pneumatic actuators. This type of transducer is stable into all sizes of load volumes and produces measured accuracy (see Instrument Society of America [ISA]-S5l, 1-1979, Process Instrumentation Terminology for the definition of measured accuracy) of 0,5 percent to 1,0 percent of span. [Pg.782]

Instrumentation normally is denoted by a circle in which the variable being measured or controlled is denoted by an appropriate letter symbol inside the circle. When the control device is to be located remotely, the circle is divided in half with a horizontal line. Table 1.3 gives various instrumentation symbols and corresponding letter codes. The specific operating details and selection criteria for various process instrumentation are not discussed in this book. The reader is referred to earlier works by Cheremisinoff [1,2] for discussions on essential control and measurement instrumentation. [Pg.8]

In filled thermometers the thermal expansion of a gas or a liquid is transmitted through a thin capillary tube to a bellows or helix, where the deformation indicates the temperature. The temperature range of filled thermometers is very wide, approximately -200 to +700 °C. They are extremely robust but are not very high in accuracy. The application is mainly for process instrumentation and as stand-alone control devices. [Pg.1137]

Powder and Bulk Solids Handling Processes Instrumentation and Control, Koichi linoya, Hiroaki Masuda, and Kinnosuke Watanabe... [Pg.674]

Figure 1-20B. Commonly used instruments for process instrumentation flowsheets. Adapted by permission, ISA Std. ANSI Y32.20—1975, ISA S5.1—1973, Instrumentation Symbols and Identification," Latest edition, 1984. Figure 1-20B. Commonly used instruments for process instrumentation flowsheets. Adapted by permission, ISA Std. ANSI Y32.20—1975, ISA S5.1—1973, Instrumentation Symbols and Identification," Latest edition, 1984.
Part I Process Instrumentation Control Part II Process Stream Analyzers... [Pg.32]

Micro-organisms with resistance to environmental stresses such as solvents, extremes of pH, high salt concentration, and having broad temperature and dissolved oxygen optima are more suited to process applications. Improved process instrumentation and... [Pg.28]

Establishment of needs-based criteria for evaluating candidate hardware, software, and process instruments. [Pg.470]

The batch process control system we ve purchased provides only a starting point for our process research lab we must also identify and test a comprehensive set of controlled devices and real-time process instruments for chemists and engineers to use as building blocks for real feedback control systems. The technologies we are evaluating for characterization of polymer batches at all process stages include ... [Pg.475]

Powder and Bulk Solids Handling Processes Instrumentation... [Pg.540]

Beckman Instruments, Process Instruments Division, Fullerton, CA, Bulletin 4101-B. [Pg.378]

Comprehensive reviews of process instruments and control equipment are published periodically in the journal Chemical Engineering. These reviews give details of all the instruments and control hardware available commercially, including those for the on-line analysis of stream compositions (Anon., 1969). Details of process instruments and control equipment can also be found in various handbooks, Perry et al. (1997) and Lipak (2003). [Pg.227]

Anon. (1969) Chem. Eng., NY 16 (June 2nd) 136. Process instrument elements. [Pg.238]

A list of onstream process analyzers, operating principles, manufacturers, costs, advantages, and disadvantages is given in reference 2. A list of process instrument elements with their accuracy and principles of operation is given in reference 3. [Pg.163]

Process Instrument Elements, Chemical Engineering, June 2, 1969, pp. 137-164. [Pg.180]

Considine, D.M., Process Instruments and Controls Handbook, Second Edition, McGraw-Hill Book Company, Inc., New York, NY, 1974. [Pg.105]

Fail-safe is a concept used to specify the position of process instrumentation in the event of power, air pressure, or other utility failures. For instance, the valve supplying cooling water to a chemical reactor would fail in the open position ( fail open ) in the... [Pg.465]

Emission spectrum generated by bombardment of sample by argon ions in a sputtering process. Instrumentation... [Pg.294]

Air intakes to heating and ventilation systems, air compressors for process, instrument and breathing air, and to prime movers for gas compressors, power generation and pumps should be located as far as practical from contamination by dust, toxic and flammable materials release sources. They should not be located in electrically classified areas. If close to possible vapor releases (as confirmed by dispersion analyses( they should be fitted with toxic or combustible gas detection devices to warn of possible air intakes hazards and snutdown and isolate the incoming air ductwork and fans. [Pg.100]

Automatic activation from process instrumentation set points. [Pg.117]

Various simple and sophisticated fire and gas detection systems are available to provide early detection and warnings of a hydrocarbon release which supplement process instrumentation and alarms. The overall objective of fire and gas detection systems are to warn of possible impending events that may be threatening to life, property of continued business operations, that are external to the process operation. [Pg.177]

Process controls and instrumentation only provide feedback for conditions within the process system. They do not report or control conditions outside the assumed process integrity limits. Fire and gas detection systems supplement process information systems with instrumentation that is located external to the process to warn of conditions that could be considered harmful if found outside the normal process environment. Fire and gas detection systems may be used to confirm the readings of major process releases or to report conditions that process instrumentation may not adequately report or be unable to report (i.e., minor process releases). [Pg.177]


See other pages where Process instrumentation is mentioned: [Pg.80]    [Pg.757]    [Pg.2058]    [Pg.253]    [Pg.287]    [Pg.550]    [Pg.242]    [Pg.71]    [Pg.72]    [Pg.253]    [Pg.75]    [Pg.118]    [Pg.379]    [Pg.379]    [Pg.194]    [Pg.19]    [Pg.277]    [Pg.3]    [Pg.818]    [Pg.9]   


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