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Horizontal development

The anticircular development chamber contains many of the features. found in the D-chamber. The plate is developed horizontally, the chamber volume is small, and the vapor phase can be controlled by external means [111]. An outer circle is cut fron... [Pg.364]

It is recognized that within the range where drag reduction occurs, the solids concentration is so dilute that the averaged distance between particles is usually 10 or more particle diameters. Therefore, under this flow condition, interparticle effects can be neglected. Consider the case of a fully developed horizontal pipe flow with negligible electrostatic effects. From Eq. (11.6), the pressure drop depends only on the wall friction, as given by... [Pg.470]

A 17-year-old man developed horizontal diplopia in all directions of gaze while using ecstasy tablets every 5-7 days for 2 months. A diagnosis of bilateral sixth nerve palsy was confirmed. Ocular motility returned to... [Pg.594]

The important development methods in pharmaceutical and drug analysis include classical linear ascending development, horizontal development, gradient TLC with AMD, OPLC, and two-dimensional (2D) development. These development methods will be described briefly. Other development methods, such as circular, anticircular, continuous, and rotational, will not be covered. [Pg.540]

This system is represented by a closed basin, made of impermeable rocks and filled in the past by a saline alkaline lake. Water in this case could not permeate downwards but only evaporate, so the deposit develops horizontally, instead of vertically as in the previous occurrence. Here pH and salinity in the fluids tend to increase, giving rise to brines, c.g., basic, alkali-rich solutions. Concentric zones of authigenic minerals are so formed, from an outer and upper ring of little altered glass and clay minerals, to zeolites, analcime and a finally alkali-feldspars. A good example for this type of occurrence is Lake Tecopa, California, where the zeolitic ring is constituted by phillipsitc, clinoptilolite and erionite, followed by the central feldspar zone [36]. [Pg.21]

Events that enter an and gate are developed horizontally as shown for the expansion of G-002 (Figure 15.18). All the events on a line must occur for the cut set to deliver a positive output. The cut sets are now ... [Pg.621]

Developing horizontal and variable screw feed systems. [Pg.168]

As shown in Fig. 2, increment, rises as the drop of the temperature and shrinkage of volume from crystallization. Meanwhile, solidifyed layer of the part develops horizontal strain under the action of packing pressm-e. Under the actions of, and 4, the spring is forced to move and lead to elastic strain 2, which brings an elastic stress field. Furthermore,... [Pg.255]

Carbonate rocks are more frequently fractured than sandstones. In many cases open fractures in carbonate reservoirs provide high porosity / high permeability path ways for hydrocarbon production. The fractures will be continuously re-charged from the tight (low permeable) rock matrix. During field development, wells need to be planned to intersect as many natural fractures as possible, e.g. by drilling horizontal wells. [Pg.85]

It is worth noting that if field development using horizontal wells is under consideration, then horizontal appraisal wells will help to gather representative data and determine the benefits of this technique, which is further discussed in Section 9.3. [Pg.177]

The wells provide the conduit for production from the reservoir to the surface, and are therefore the key link between the reservoir and surface facilities. The type and number of wells required for development will dictate the drilling facilities needed, and the operating pressures of the wells will influence the design of the production facilities. The application of horizontal or multi-lateral wells may where appropriate greatly reduce the number of wells required, which in time will have an impact on the cost of development. [Pg.213]

Figure 9.8 Gas cresting in oil rim development with horizontal wells... Figure 9.8 Gas cresting in oil rim development with horizontal wells...
New technology is applied to existing fields to enhance production. For example, horizontal development wells have been drilled in many mature fields to recover remaining oil, especially where the remaining oil is present in thin oil columns after the gas cap and/or aquifer have swept most of the oil. Lately, the advent of multi-lateral wells drilled with coiled tubing have provided a low cost option to produce remaining oil as well as low productivity reservoirs. [Pg.340]

In traditional Fan-Beam CT the radiation emitted from the X-ray tube is collimated to a planar fan, and so most of the intensity is wasted in the collimator blades (Fig. 2a). Cone-Beam CT, where the X-rays not only diverge in the horizontal, but also in the vertical direction, allows to use nearly the whole emitted beam-profile and so makes best use of the available LINAC photon flux (Fig. 2b). So fast scanning of the samples three-dimensional structure is possible. For Cone-Beam 3D-reconstruction special algorithms, taking in consideration the vertical beam divergence of the rays, were developed. [Pg.493]

Figure A3.14.12. The first experimental observation of a Turing pattern in a gel strip reactor. Solutions containing separate components of the CIMA/CDIMA reaction are flowed along each edge of the strip and a spatial pattern along the horizontal axis develops for a range of experimental conditions. (Reprinted with pennission from [38], The American Physical Society.)... Figure A3.14.12. The first experimental observation of a Turing pattern in a gel strip reactor. Solutions containing separate components of the CIMA/CDIMA reaction are flowed along each edge of the strip and a spatial pattern along the horizontal axis develops for a range of experimental conditions. (Reprinted with pennission from [38], The American Physical Society.)...
To be eonformable to multiplieation, the horizontal dimension of A must be the same as the vertieal dimension of B, that is, n = mg. Square matr ices of the same size are always eonformable to multiplieation. This unusual definition of multiplieation, with its rorles for dimensions, will beeome elear with repeated use. The matriees we shall be interested in will usually be square you should assume that the matriees diseussed below are square unless otherwise stipulated. The rules for reetangular matriees and eolumn and row matriees will be developed as needed. [Pg.33]

The Aromax process was developed in the early 1970s by Toray Industries, Inc. in Japan (95—98). The adsorption column consists of a horizontal series of independent chambers containing fixed beds of adsorbent. Instead of a rotary valve, a sequence of specially designed on—off valves under computer control is used to move inlet and withdrawal ports around the bed. Adsorption is carried out in the Hquid phase at 140°C, 785—980 kPA, and 5—13 L/h. PX yields per pass is reported to exceed 90% with a typical purity of 99.5%. The first Aromax unit was installed at Toray s Kawasaki plant in March 1973. In 1994, IFP introduced the Eluxyl adsorption process (59,99). The proprietary adsorbent used is designated SPX 3000. Individual on-off valves controlled by a microprocessor are used. Raman spectroscopy to used to measure concentration profiles in the column. A 10,000 t/yr demonstration plant was started and successfully operated at Chevron s Pascagoula plant from 1995—96. IFP has Hcensed two hybrid units. [Pg.420]

Horizontally Mixing Aspirator Aerators. An aerator using a horizontally mixing aspirator has a marine propeller, submerged under water, attached to a soHd or a hoUow shaft. The other end of the shaft is out of the water and attached to an electric motor. When the propeller is rotated at high velocity, at either 1800 or 3600 rpm, a pressure drop develops around the propeller. Air is then aspirated under the water and mixed with the water, and moved out. This type of aerator, shown ia Figure 3g, is very efficient ia mixing wastewater. [Pg.342]

The Oldshue-Rushton column (Eig. 15d) was developed (162) in the early 1950s and has been widely used in the chemical industry. It consists essentially of a number of compartments separated by horizontal stator-ring baffles, each fitted with vertical baffles and a turbine-type impeller mounted on a central shaft. Columns up to 2.74 m in diameter have been reported in service (162—167). Scale-up is reported to be reliably predictable (168) although only limited performance data are available (169). A detailed description and review of design criteria are available (170). [Pg.76]

Horizontal Rotating Pan Filters. These filters (Fig. 10) represent a further development of the tipping pan filter for continuous operation. They consist of a circular pan rotating around the central filter valve. The pan is divided into wedge-shaped sections covered with the filter medium. Vacuum is appHed from below. Each section is provided with a drainage pipe which connects to a rotary filter valve of the same type as in dmm filters. [Pg.395]

Horizontal vessel filters with vertical rotating elements have been under rapid development with the aim of making truly continuous pressure filters, particularly for the filtration of fine coal. [Pg.402]

Horizontal or vertical vessel filters, especially those with vertical rotating elements, have undergone rapid development with the aim of making truly continuous pressure filters, particularly but not exclusively for the filtration of fine coal. There are basically three categories of continuous pressure filters available, ie, disk filters, dmm filters, and belt filters including both hydrauHc and compression varieties. [Pg.405]

A test unit has been developed of a small dmm filter, total filter area of 0.7 m with 30% submergence, housed in a large horizontal pressure vessel. [Pg.406]

Wet Oxidation Reactor Design. Several types of reactor designs have been employed for wet oxidation processes. Zimpro, the largest manufacturer of wet oxidation systems, typically uses a tower reactor system. The reactor is a bubble tower where air is introduced at the bottom to achieve plug flow with controlled back-mixing. Residence time is typically under one hour. A horizontal, stirred tank reactor system, known as the Wetox process, was initially developed by Barber-Cohnan, and is also offered by Zimpro. [Pg.502]


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See also in sourсe #XX -- [ Pg.106 ]




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