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Separation temperature

If high wellhead pressures are available over long periods, cooling can be achieved by expanding gas through a valve, a process known as Joule Thomson (JT) throttling. The valve is normally used in combination with a liquid gas separator and a heat exchanger, and inhibition measures must be taken to avoid hydrate formation. The whole process is often termed low temperature separation (LTS). [Pg.251]

Chlorodiphenyl. Diazotise 32 g. of o-chloroaniline (Section IV,34) in the presence of 40 ml. of concentrated hydrochloric acid and 22 -5 ml. of water in the usual manner (compare Section IV,61) with concentrated sodium nitrite solution. Transfer the cold, filtered diazonium solution to a 1 5 htre bolt-head flask surrounded by ice water, introduce 500 ml. of cold benzene, stir vigorously, and add a solution of 80 g. of sodium acetate trihydrate in 200 ml. of water dropwise, maintaining the temperature at 5-10°. Continue the stirring for 48 hours after the first 3 hours, allow the reaction to proceed at room temperature. Separate the benzene layer, wash it with water, and remove the benzene by distillation at atmospheric pressure distil the residue under reduced pressure and collect the 2-chlorodiphenyl at 150-155°/10 mm. The yield is 18 g. Recrystalliae from aqueous ethanol m.p. 34°. [Pg.928]

Teirrperamre is often a forgotten variable in HPLC but ean influenee the robustness and seleetivity of many separations or if exploited eair provide novel high temperature separation eonditions with either high effieieney, a unique seleetivity or enable new deteetion methods to be applied. [Pg.16]

These units are designed to allow hydrates to form and to melt them with the heat of the incoming gas stream before they can plug down stream equipment. In addition, the low-temperature separation that occurs in an LTX unit results in stabilizing the liquids as discussed in Chapter 6. This results in an increase in liquids recovered and a corresponding decrease in the heating value of the gas over what would be the case with separation at normal temperatures. [Pg.110]

Figure 5-1 shows a typical LTX process. The inlet gas stream is choked at the well to 2,000 to 3,000 psi or until the temperature declines to approximately 120°F, which is well above the hydrate formation temperature. The inlet stream next enters a coil in the bottom of the low temperature separator. The stream is then cooled to just above the hydrate formation temperature with the outlet gas coming off the low temperature separator. This assures the lowest possible temperature for the inlet stream when it enters the vessel after the choke. This choke is mounted in the vessel itself. When the pressure drop is taken, the temperature will... [Pg.110]

The gas, condensate, and free water are then discharged from the ncs scl through backpressure and liquid dump valves. The gas leaving the separator is saturated with water vapor at the temperature and pressure of the top of the low temperature separator. If this temperature is low enough, the gas may be sufficiently dehydrated to meet sales specifications. Dehydration is discussed in greater detail in Chapter 8. [Pg.111]

From a hydrate melting standpoint it is possible in the winter time to have too cold a liquid temperature and thus plug the liquid outlet of the low temperature separator. It is easier for field personnel to understand and operate a line heater for hydrate control and a multistage flash or condensate stabilizer system to maximize liquids recovery. [Pg.112]

The Gas Processors Suppliers Association [79] provides a more detailed background development of the K-factors and the use of convergence pressure. Convergence pressure alone does not represent a system s composition effects in hydrocarbon mixtures, but the concept does provide a rather rapid approach for systems calculations and is used for many industrial calculations. These are not well adapted for very low temperature separation systems. [Pg.4]

There is an important law referring to such equilibria, which states that if the two phases A and B of a substance, and the two phases A and C are at a given temperature in equilibrium separately, then all three phases will be in equilibrium together at that temperature. Thus if two phases are, at a given temperature, separately in equilibrium with a third phase, they will be in equilibrium with each other. [Pg.213]

For polycarbonates this was checked to be a good approximation [43,195], Since each distribution function P is determined at each temperature separately, the individual p values for different temperatures give the thermodynamic probabilities of a given state, which simply means that ... [Pg.138]

For the sensible heat storage using water, water should not be mixed during operations, because temperature difference must be maintained for sensible storage. To keep water temperature separate, multi-connected tanks and a stratified water tank are used. [Pg.335]

If the feed is partially vaporized, the vapor flow below the feed will be lower than the top of the column. For above ambient temperature separations, the cost of operating the distillation will be dominated by the heat load in the reboiler and the vapor flow in the bottom of the column. For below ambient temperature separations, the cost of operating the column will be dominated by the cost of operating the refrigerated condenser and hence the vapor flow in the top of the column. If constant molar overflow is assumed, the vapor flow in the bottom of the column V is related to the vapor flow in the top of the column by... [Pg.214]

The iron sulphide in South African coals is a mixture of pyrite and marcasite (18). Although marcasite is known to transform into pyrite at elevated temperatures, separate spiking experiments were performed to see if pyrite or marcasite would show a preferential catalytic effect. The addition of pyrite and marcasite minerals (-200 mesh), to the coal showed equivalent total conversions, and yields of oil and asphaltene. [Pg.55]

Recent developments in polymer chemistry have allowed for the synthesis of a remarkable range of well-defined block copolymers with a high degree of molecular, compositional, and structural homogeneity. These developments are mainly due to the improvement of known polymerization techniques and their combination. Parallel advancements in characterization methods have been critical for the identification of optimum conditions for the synthesis of such materials. The availability of these well-defined block copolymers will facilitate studies in many fields of polymer physics and will provide the opportunity to better explore structure-property relationships which are of fundamental importance for hi-tech applications, such as high temperature separation membranes, drug delivery systems, photonics, multifunctional sensors, nanoreactors, nanopatterning, memory devices etc. [Pg.131]

The temperature of the column affects both the vapor pressures of the mixture components and the solubilities of the mixture components in the stationary phase. Sometimes a low temperature separates some mixture components that are not separated at higher temperatures. However, the lower temperature may result in inordinately long retention times for other mixture components. Temperature programming allows the best of both worlds—complete separation of short-retention-time components at the low temperature, while shortening retention times of the others when the column temperature is raised later. [Pg.534]

It has been observed that in homogeneous thermal reactions, for every ten degree rise in temperature, the rate constant is doubled or tripled. The ratio of rate constants at two temperatures separated by 10°C is called the temperature coefficient. Mathematically... [Pg.46]

Kwok and Robbins (4) Precipitation of metals by heating solutions to high temperatures separations involving Cu, Fe, Ni, Zn, Cd and Cr. [Pg.636]

Effect of Temperature on Separation and Pure Water Production Rate(P.W.P.). Fig. 7 shows some results obtained at various temperature with the concentration of NaOCl as 50 mg/l. At lower temperature, sepairation and pure water production rate kept almost constamt value. But with increasing temperature, separation decreases and pure water production rate increases steeply. [Pg.118]

In high temperature separation, hydrogen is separated from the hot product gas at the reaction temperature using porous membranes made of materials such as zirconia. The porous membranes separate the gases through, in general, either mass diffusion or molecular effusion [3,74,79]. In mass diffusion, the... [Pg.57]

In spite of the obvious advantages of elevated temperature, there are examples of cases where better separation is achieved at a reduced temperature, even for simple solutes. Craft et al. [20] recently demonstrated an improved separation of P and y tocopherol at -20°C in THF/acetonitrile when compared to the ambient temperature separation of the compounds in Acetonitrile water. Bohm [21] reported the temperature dependence of the separation of a mixture of five xanthophylls and six carotenes on a C-30 column. The optimum temperature in this case was 23°C with a coelution of some peaks at temperatures below 20°C and others above 35°C. In a study using a 300 A pore C-18 column, Bohm [22] reported dramatic changes in the elution order over the temperature range -7°C to 35°C. On this column, the optimal separation was achieved at low temperatures... [Pg.261]

The injection temperature can be a signiflcant issne for thermally unstable samples or where samples are stored for hours in an antosampler prior to injection. For this reason, most manufacturers sell autosamplers with optional thermostated sample compartments. This can be done either by placing the sample tray in an air bath oven or by a condnctive temperature control of the sample rack. The need to keep samples cool prior to injection when conpled with elevated temperature separation increases the complexity of the flow system reqnired. For such application, a separate mobile phase pre-heater with a low volnme placed between the injector and the column is a good choice. Alternatively, the injector valve wonld need to be monnted ontside the antosampler or in the column oven to insure preheating of the mobile phase before the colnmn. [Pg.272]


See other pages where Separation temperature is mentioned: [Pg.251]    [Pg.348]    [Pg.85]    [Pg.439]    [Pg.110]    [Pg.337]    [Pg.363]    [Pg.543]    [Pg.30]    [Pg.81]    [Pg.299]    [Pg.393]    [Pg.236]    [Pg.117]    [Pg.190]    [Pg.198]    [Pg.47]    [Pg.57]    [Pg.108]    [Pg.257]    [Pg.265]    [Pg.272]    [Pg.151]    [Pg.173]    [Pg.187]    [Pg.201]    [Pg.209]    [Pg.150]   
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See also in sourсe #XX -- [ Pg.193 ]

See also in sourсe #XX -- [ Pg.9 , Pg.12 ]




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Effect of Flow Rate and Temperature on Enantiomeric Separations

Effect of Temperature on Separation Efficiency

Elevated Temperature and Pharmaceutical Separations

Elevated temperature separation chemistry

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Gradient separations temperature dependence

High temperature superconductors phase separation

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Inverse temperature transitions phase separation

Isotope separation by low-temperature countercurrent distillation

Least separation temperature

Lower critical solution temperature , polymer blend phase separation

Microphase separation temperature

Microphase separation temperature transition

Needs for More Binary or Multiple Gas Mixture Separation Data at High Temperatures

Oven temperature control separations

Perovskite Membranes for High Temperature Oxygen Separation

Pharmaceutical separations, elevated temperature

Phase separation critical temperature

Phase separation temperature

Phase separation temperature strength

Phase separation, high temperature

Phase separation, high temperature system

Phase separation, high temperature theoretical model

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Protein separation, temperature effect

Separation Acceleration through Temperature Increase

Separation above glass transition temperature

Separation low temperature

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Separation temperature and

Separation temperature change

Separator temperature

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Separator temperature reactor

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Separators temperature and

Temperature Effect on Separation

Temperature liquid-separation system

Temperature of separation

Temperature polymer blend phase separation

Temperature-induced phase separation

Temperature-induced phase separation TIPS)

Temperature-induced separation

Temperature-programmed separation high-speed

Temperature-programmed separations

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