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Pumps/pumping valve control

There are three basic requirements that Hquid level control devices are designed to satisfy alarm functions, pump/valve control, and transmitted output signal to track level continuously. Alarm devices provide warning or shutdown functions when process levels pass a predeterrnined point in the vessel pump /valve control devices turn on/off pumps or open/close valves at predeterrnined levels in the vessel and transmitters provide a proportional output signal over a predetermined span to send to a local meter or signal back to a control room. [Pg.207]

The plant comprised the wind turbine, the electrolyser unit complete with its built-in controllable power supply, battery storage, a DC-DC controllable converter, and two dump loads (0.5 and 2 kW) controlled by two voltage-actuated relays. The auxiliary equipment (electrolyser pumps, valves, control equipment, and water demineralisation unit) for the demonstration plant were supplied by the grid for convenience. [Pg.90]

A water/charcoal adsorber with a capacity of 50 gallons of water per minute holds 1,800 pounds of activated carbon and costs 9,800, which includes the cost of pipes, pumps, valves, controls, etc. [Pg.199]

In a battery system a portion of the energy will be diverted to auxiliary systems such as thermal management, pumps, valves, controls, and shunt current protection as required. The energy needed for auxiliaries depends on a number of factors, including the efficiency of pumps and motors, pump run time, and system design. Little publicly available data exist... [Pg.1268]

Multiplex wellhead high-pressure control pump valve... [Pg.233]

Following the invention of the hydrauHc press in 1795 (3), the use of hydrauHcs expanded rapidly during the nineteenth century. The weight-loaded accumulator, invented ca 1850, was used to store energy in hydrauHc systems. The elementary press circuit has several parts that are common to all hydrauHc systems a reservoir, a pump, piping, control valves, a motor, which in this case is a hydrauHc cylinder or ram, and the hydrauHc fluid. By ca 1860 hydrauHc presses were used for forging, and an adjustable-speed hydrauHc transmission was perfected in 1906 (2). The manufacture of hydrauHcahy actuated machines attained industrial importance after 1920. [Pg.261]

Each of the membrane devices may be assembled by connecting the modules into combinations of series, pataUel-flow paths, or both. These assembUes ate connected to pumps, valves, tanks, heat exchangers, instmmentation, and controls to provide complete systems. [Pg.303]

The price for an increase in heat-transfer characteristics is a more complex system with more anxihary eqnipmeut low-pressure receivers, refrigerant pumps, valves, and controls. Liquid refrigerant is predominantly pumped by mechanical pumps, however, sometimes gas at condensing pressure is used for pumping, in the variety of concepts. [Pg.1115]

Design equipment to prevent excessively fast feed. Do not oversize pumps or control valves... [Pg.17]

Total flow vacuum pump Exhaust control with bypass controller valve... [Pg.1291]

In most fluid power systems, the motor is required to provide actuating power in either direction. In these applications, the ports are referred to as working ports, alternating as inlet and outlet ports. Either a four-way directional control valve or a variable-displacement pump usually controls the flow to the motor. [Pg.609]

The second valve controls a sample loop, 5 cm long and 1 mm in diameter, packed with dimethyloctadecyl reverse phase comprising of fairly coarse particles 100-120 im in diameter to reduce flow impedance. The sample pump is supplied via a two-way tap from either of two reservoirs, one containing pure water and the other, normal saline. The output of the pump can be used to either force the contents of the open loop sample tube through the packed loop, or to permit washing with an appropriate solvent. The separate pump is necessary to overcome the impedance of the packed loop. [Pg.207]

Fig. 2.9 Schematic diagram of experimental set-up 1 inlet tank, 2 pump, 3 control valve, 4 temperature and pressure measurement ports, 5 sample of porous medium, 6 top of test section, 7 housing, 8 copper rod, 9 heater, 10 insulation, 11 exit tank, 12 electronic scales. Reprinted from Hetsroni et al. (2006a) with permission... Fig. 2.9 Schematic diagram of experimental set-up 1 inlet tank, 2 pump, 3 control valve, 4 temperature and pressure measurement ports, 5 sample of porous medium, 6 top of test section, 7 housing, 8 copper rod, 9 heater, 10 insulation, 11 exit tank, 12 electronic scales. Reprinted from Hetsroni et al. (2006a) with permission...
Most centrifugal pumps are controlled by throttling the flow with a valve on the pump discharge, see Section 5.8.3. This varies the dynamic pressure loss, and so the position of the operating point on the pump characteristic curve. [Pg.210]

Figure 1-7 presents the causes of losses for the largest chemical accidents. By far the largest cause of loss in a chemical plant is due to mechanical failure. Failures of this type are usually due to a problem with maintenance. Pumps, valves, and control equipment will fail if not properly maintained. The second largest cause is operator error. For example, valves are not opened or closed in the proper sequence or reactants are not charged to a reactor in the correct order. Process upsets caused by, for example, power or cooling water failures account for 11 % of the losses. [Pg.16]

In parallel with improvements in chemical sensor performance, analytical science has also seen tremendous advances in the development of compact, portable analytical instruments. For example, lab-on-a-chip (LOAC) devices enable complex bench processes (sampling, reagent addition, temperature control, analysis of reaction products) to be incorporated into a compact, device format that can provide reliable analytical information within a controlled internal environment. LOAC devices typically incorporate pumps, valves, micromachined flow manifolds, reagents, sampling system, electronics and data processing, and communications. Clearly, they are much more complex than the simple chemo-sensor described above. In fact, chemosensors can be incorporated into LOAC devices as a selective sensor, which enables the sensor to be contained within the protective internal environment. Figure 5... [Pg.127]

Simply, SCADA is a computer-based control system that remotely controls processes previously controlled manually. The philosophy behind SCADA control systems can be summed up by the phrase, If you can measure it, you can control it. SCADA allows an operator using a central computer to supervise (control and monitor) multiple networked computers at remote locations. Each remote computer can control mechanical processes (mixers, pumps, valves, etc.) and collect data from sensors at... [Pg.118]

TTie Aroma software controls the sample change, pumps, valves and connected measuring instruments. The software also receives all measured results from the instruments, filters, stores and prints them. [Pg.205]

With an available diesel emergency generator supplying power to critical pumps, the control room operators initiated shutdown procedures for the two reactor areas. An uninterruptible power supply (UPS) kept power to the DCS screens and instruments however, the DCS system was designed close all catalyst preparation and reactor feed valves on loss of power. Outside operators were sent to manually block in reactor feeds. [Pg.370]

Ruy et al. have performed a similar reaction under microreactor conditions in a multiphase solvent system containing an ionic liquid as the catalyst carrier and reaction promoter [35]. Their system consisted of two T-shaped micromixers (i.d. 1,000 and 400 pm) and a capillary stainless steel tube as an RTU (1,000 pm i.d. and 18 m length, giving a 14.1 ml volume), equipped with pumps and control valves. Under the optimized conditions, Pd-catalysed carbonylation of aromatic iodides in the presence of a secondary amine provided only the double carbonylated product, ot-ketoamide, while the amide obtained by the single carbonylation was observed in high quantities only when the reaction was performed in batch (Scheme 13). [Pg.172]

DC Diaphragm controller P Vacuum pump M Measuring and switching device PS Pressure sensor V1 Pump valve V2 Gas inlet valve TH Throttle... [Pg.92]

The diaphragm controller is therefore closed. When the system is started up, the connecting line between the vacuum pump and pump valve V2 is first evacuated. As soon as the pressure drops below the maximum switching point, valve V1 closes. When the pressure falls below the minimum switching point, valve V2 opens. [Pg.93]

DC Diaphragm controller PS Process pressure sensor RS Reference pressure sensor V1 Gas inlet valve V2 Pump valve... [Pg.93]


See other pages where Pumps/pumping valve control is mentioned: [Pg.78]    [Pg.21]    [Pg.534]    [Pg.4485]    [Pg.187]    [Pg.583]    [Pg.1548]    [Pg.109]    [Pg.109]    [Pg.238]    [Pg.55]    [Pg.345]    [Pg.503]    [Pg.25]    [Pg.206]    [Pg.43]    [Pg.282]    [Pg.146]    [Pg.38]    [Pg.61]    [Pg.521]    [Pg.141]    [Pg.392]    [Pg.225]    [Pg.94]   


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