Big Chemical Encyclopedia

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

Articles Figures Tables About

Wetted parts

Non-Metallic Construction Lined/Coated Metallic wet parts... [Pg.61]

If corrosion exists, the pump-wet parts can be changed for other materials such as stainle.ss steel or composite material. Impellers can be replaced by bronze cast impellers or other materials. [Pg.233]

The hydrostatic testing is the first test used on the lube system. The system is tested while assembled or partially assembled, based on the particular system. A test pressure of VA times the maximum allowable working pressure, a minimum of 20 psi for the oil side, is used for the test. For the oil-wetted parts, the test fluid should be light oil, which is normally the recommended lubricant for the compressor train. The test period is the length of time needed to inspect for leaks, or a minimum ol thirty minutes. Acceptance is based on the lack of leaks as visually observed or the lack of a drop in the test pressure. [Pg.415]

Lubricating oil analysis, as the name implies, is an analysis technique that determines the condition of lubricating oils used in mechanical and electrical equipment. It is not a tool for determining the operating condition of machinery. Some forms of lubricating oil analysis will provide an accurate quantitative breakdown of individual chemical elements, both oil additive and contaminates, contained in the oil. A comparison of the amount of trace metals in successive oil samples can indicate wear patterns of oil wetted parts in plant equipment and will provide an indication of impending machine failure. [Pg.800]

Solutions loading and unloading system, heat exchanger and all other wet parts are manufactured from materials that are suitable for use with aggressive fluoride liquids. [Pg.311]

In addition to the careful selection of structural metals, the cathodic protection of water-wetted parts may also be specified. For most boiler plant systems, however, because of the tortuous and extended waterside surfaces involved, the use of cathodic protection is only a partial solution to controlling corrosion and should never be the sole secondary protocol. Rather, cathodic protection functions well when employed as part of a more comprehensive program that includes appropriate internal chemical treatments. [Pg.167]

The presence of water-in-oil emulsions often leads to corrosion and to the growth of microorganisms in the water-wetted parts of the pipelines and storage tanks. [Pg.325]

Handling the nozzles or wet part of the spray boom with bare hands. [Pg.94]

Any part of the system that is in contact with the mobile phase must be made of materials that are not attacked by any of the solvents that are to be used. The wetted parts are usually made of stainless steel or ptfe although other materials, such as sapphire, ruby, or ceramics are sometimes used. Everything on the high pressure side, ie from the pump outlet to the end of the column, must be strong enough to withstand the pressures involved. [Pg.251]

Wetted parts subject to welding, including fabrication and tack welding (for example, removable wear rings), shall be stress relieved, if required, so that both the welds and the heat-affected zones meet the yield strength and hardness requirements of this paragraph. [Pg.40]

Welding of piping, pressure containing parts, and wetted parts, as well as any weld repairs to such parts, shall be performed and inspected by operators and procedures qualified in accordance with Section VIII, Division 1, and Section IX of the ASME Code. [Pg.40]

A corrosion allowance is acceptable for the shell and support grids. Other wetted parts should have the ability to withstand corrosion,... [Pg.811]

Range of instrument and manufacturer s accuracy Materials of construction, especially of process contact (wetted) parts Process connection details (e.g., chemical seals, capillary lengths, flange rating)... [Pg.602]

The reaction is initiated by the addition of a reactant, which must be exactly at the same temperature as the Dewar contents, in order to avoid the sensitive heat effects. Then the temperature is recorded as a function of time. The obtained curve must be corrected for the heat capacity of the Dewar flask and its inserts, respective of their wetted parts, which are also heated by the heat of reaction to be measured. The temperature increase results from the heat of reaction (to be measured), the heat input by the stirrer and the heat losses. These terms are determined by calibration, which may be a chemical calibration using a known reaction or an electrical calibration using a resistor heated by a known current under a known voltage (Figure 4.2). The Dewar flask is often placed into thermostated surroundings as a liquid bath or an oven. In certain laboratories, the temperature of the surroundings is varied in order to track the contents temperature and to avoid heat loss. This requires an effective temperature control system. [Pg.88]

For the wet part of the shrinkage curve the curvature is negative. In order to show this part of the curvature line in the diagram, we reverse the sign, i.e. in effect we plot the absolute value of n. By differentiating eqn. (4) and setting the result equal to zero, one finds the locations where the absolute values of the curvature are maximal ... [Pg.268]

Figure 5. Shrinkage curve for Nunn clay loam mixed with 10 percent sand (data points from [9] with bimodal curve fitting For the wet part of the curve the following values were used for the parameters k. = 0.859, k. = 1.061, n = 1.695 and e = 0.676. For the dry part of the curve the following values were used for the parameters k. = 0.111, k. = 0.082, n = 1.513 and e = 0.495. Figure 5. Shrinkage curve for Nunn clay loam mixed with 10 percent sand (data points from [9] with bimodal curve fitting For the wet part of the curve the following values were used for the parameters k. = 0.859, k. = 1.061, n = 1.695 and e = 0.676. For the dry part of the curve the following values were used for the parameters k. = 0.111, k. = 0.082, n = 1.513 and e = 0.495.
The probability of impact of particles with the wetted part of their surfaces is the product of both probabilities... [Pg.492]

Hydrodynamic parameters that are required for trickle bed design and analysis include bed void fraction, phase holdups (gas, liquid, and solid), wetting efficiency (fraction of catalyst wetted by liquid), volumetric gas-liquid mass-transfer coefficient, liquid-solid mass-transfer coefficient (for the wetted part of the catalyst particle surface), gas-solid... [Pg.58]

The facilities engineer must consider the materials used to construct the wetted parts of the unit operations used to treat the waste. The goal is to select a cost-effective material that will not degrade in the presence of the waste stream to be treated. In general, the most commonly used materials of construction for the unit operations are 316or316L stainless steel. However, if chlorides, fluorides, and other halogens are present in the CMP chemistry, it may be necessary to consider nickel, titanium, Hastelloy, or other high-performance metals. [Pg.631]

Range of instrument (calibrahon range) or switch set point values Materials of construction of wetted parts Control characterishcs... [Pg.579]

The evaporation of the mobile phase components is most prominent near to their fronts where most of the heat of solvation is affected. Generally, the least polar mobile phase components have the highest volatility e.g., in a ternary mobile phase consisting of diethyl ether-methanol-water, the diethyl ether has the least polarity and is the most volatile component. Parallel to the evaporation of the mobile phase components, their vapour is also condensing on the stationary phase (both on the dry part of the plate before the mobile phase front, but also on the already wetted part behind the front). [Pg.457]

Figure 6, Profiles of the density as a fimction of z, the distance from the center of a parallel-walled slh. The vertical lines show the planes of solid that make up the pore. The density is shown for a conqjletely wet (part a) and a con letely dry (part b) surface. Both the fluid adsorbate and the solid adsorbent are made up of Lennard-Jones atoms with well-depth ratios % /% = 0.85 (part a) and 0.30 (part b). The simulations were performed under conditions such that each system was at bulk liquid-vapor coexistence for 0.7. From Ref [31], J. Stat. Phys. Figure 6, Profiles of the density as a fimction of z, the distance from the center of a parallel-walled slh. The vertical lines show the planes of solid that make up the pore. The density is shown for a conqjletely wet (part a) and a con letely dry (part b) surface. Both the fluid adsorbate and the solid adsorbent are made up of Lennard-Jones atoms with well-depth ratios % /% = 0.85 (part a) and 0.30 (part b). The simulations were performed under conditions such that each system was at bulk liquid-vapor coexistence for 0.7. From Ref [31], J. Stat. Phys.

See other pages where Wetted parts is mentioned: [Pg.25]    [Pg.297]    [Pg.126]    [Pg.907]    [Pg.207]    [Pg.895]    [Pg.59]    [Pg.59]    [Pg.485]    [Pg.623]    [Pg.258]    [Pg.40]    [Pg.52]    [Pg.82]    [Pg.268]    [Pg.65]    [Pg.226]    [Pg.557]    [Pg.172]    [Pg.761]    [Pg.126]    [Pg.105]    [Pg.107]    [Pg.730]    [Pg.606]    [Pg.822]   
See also in sourсe #XX -- [ Pg.95 ]




SEARCH



Pellet partly wetted catalyst

© 2024 chempedia.info