Installations design

Damewood, Glen and Nimitz, Walter, Compressor Installation Design Utilizing an Electro-Acoustical System Analog, ASME 61-WA-290, New York, NY American Society of Mechanical Engineers, 1961. 

A septic tank is a purification installation designed to accept the whole sewage/trade discharge from premises. Its construction is such that it allows the settling out... 

Designs can be prepared once soil resistivities and groundbed locations have been determined. Figure 10.23 illustrates typical installations. Design steps are as follows ... 

Institute and Institute of Electrical and Electronic Engineers, Inc. (IEEE), IEEE Std. 484, Recommended Practice for Installation Design and Installation of large Lead Storage Batteries for Generating Stations and Substations. IEEE, New York, NY, 1987. 

In evaluating a piping installation design to determine what safeguarding may exist or is necessary, the following should be reviewed ... 

For this purpose an elaborate testing Installation, designed to measure deposition parameters, was established on the Eglln Reservation with the place of direct aerial application restricted to an area of approximately 3 km within Test Area C-52A In the southeastern part of the reservation. Massive quantities of herbicides, used In the testing of aerial defoliation spray equipment from 1962 through 1970, were released and fell within the Instrumented test area. The uniqueness of the area prompted the United States Air Force to set aside the area In 1970 for research Investigations. Numerous ecological surveys have been conducted since 1970. As a result, the ecosystem of this unique site has been well studied and documented (2,3). 

Ease of Installation Time-consuming to design and install Design time-consuming Programming can be very time-consuming Simple to program and install... 

The following statement will convey some indication of the energy utilised annually in a typical installation designed to give about 15,000 cubic feet of hydrogen per day If the working day be 24 hours for 300 days per annum, the yearly output will be 15,000 x 300 = 4,500,000 cubic feet. Each cell takes about 400 amps, at 2 volts, that is, 0 8 K.W.H. per hour, and if there be 100 units in the plant, the energy utilised each year will be 100 x 8 x 24 x 300, or 576,000 K.W.H. To this must be added approximately 25 per cent, to allow for loss... 

Flame ionization detectors (FIDs) and photoionization detectors (PIDs) can be used for the detection of hydrocarbons. Both detectors have been utilized for combustibles monitoring in portable and fixed installation designs. The FID actually burns the sample in an H2 flame. A charged electrical field is positioned across the flame, and utilizing the ions in the flame can conduct a current. When most combustible materials are introduced into the flame, they produce ions in their combustion products, and these are detected by the increased flow of current across the electric field (flame). 

Synthesis of carbon nanostructures by pyrolysis and arc discharge in the gas phase has been performed by the known methods. Synthesis in the liquid phase has been carried out on the installation designed specially for these studies (Fig. 2). This installation allows metal and graphite electrodes to be evaporated in the liquid medium at the temperature from 4 to 340 K using an electric arc. The arc temperature near a cathode may be as much as 1,2-104 K at currents of 200-300A (Fig. 3). 

Recently, a completely new approach to the design of HTSR furnaces was placed in pilot plant operation based on process and mechanical design developments by United Technologies Corporation (UTC). This new reformer will be part of the fuels processing system in an electric power installation designed to produce 4.8 MW for the Consolidated Edison Company in... 

Later test work has shown that the severity of cracking from these causes can be reduced significantly by changes in installation design and application technique. 

All installations designed for nuclear industry have to fulfill very strict requirements of safety and rehability in the long mn. Control and monitoring systems, automation, and washing installations are considered as essential part of the design. 

In respect of the activity, selectivity, and economic issues (price, reuse of catalyst, installation design, and cost) the above-mentioned homogeneous catalytic systems may compete with the platinum system commonly used in this type of reaction. 

In Switzerland. The very fine ozone sterilization plant built at Berne includes a novel air-drying installation designed by the Carba Co., Berne. 

To integrate synchronous and asynchronous communication tools into distributed work sessions, a framework was created which rnodularly incorporates different tools into one interface. In this context, synchronous communication comprises all those services which support multimedia conferencing. This includes not only the real-time transmission of audio/video data, but also the usage of locally installed design tools by the whole team. 

In general the installation designer and the nser reqnire confidence that mannfactnred eqnipment for use in a hazardous area carries an internationally recognised certificate. In addition the certificate should be the result of laboratory testing of a sample of the same eqnipment. The laboratory shonld be specialised in the type of testing reqnired. 

The causes have been listed according to their origin as follows installation design, installation construction, execution of start-up tests, modifications executed since start-up, methods associated with normal operation of the installation, equipment failure,... 

This situation should force the pursuit of only those installation designs that do not require excessive expenditures for decommissioning. This important provision will be strictly enforced by the Russian Federation Gosatomnadzor when permits are issued for the design and construction of new installations. This provision is especially important for installations that will process plutonium-containing nuclear materials. 

The tankhouse has been designed to reach a production of 137,000 tonnes of zinc cathode per year. The components have been designed for a potential maximum zinc cathode production of 190,000 t/y. The new D tankhouse is located next to the C cellhouse which was commissioned in May 1991. The space available is limited. The tankhouse footprint has been optimised at 0.02 m per tonne of cathode installed (design production). The supervision and housekeeping of the D and C tankhouses will be shared. This arrangement will reduce the manpower to 0.29, and preventive and predictive maintenance man-hours per tonne of zinc cathode produced to 0.09. 

Most other techniques concentrate on the as-designed system functionality. The CMA ensures that the installed design is free from common causes which can undermine design, quahtative and quantitative predictions. 

AR400 1.128 Installation design and installation of large lead storage batteries for nuclear power plants... 

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