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Multi-stage

Multi-stage separation may also be constrained by low wellhead pressures. The separation process involves a pressure drop, therefore the lower the wellhead pressure the less scope there is for separation. [Pg.244]

Arosolvan process. A/-meth5i-2-pyrr a polar mixing compo-nent, either NMP—glycol, 60 vertical multi-stage the quantity of mix-ing... [Pg.78]

D. Florjancic, Influence of Gas andMirMdmission on the Behavior of Single- and Multi-Stage Pumps, Sul2er Research, No. 1970. [Pg.303]

The possible mechanism of ionization, fragmentation of studied compound as well as their desoi ption by laser radiation is discussed. It is shown that the formation of analyte ions is a result of a multi stage complex process included surface activation by laser irradiation, the adsoi ption of neutral analyte and proton donor molecules, the chemical reaction on the surface with proton or electron transfer, production of charged complexes bonded with the surface and finally laser desoi ption of such preformed molecules. [Pg.103]

The method of the analysis of the CS described in the international standai d ASTM (D 820 - 93) is a long time, multi-stage procedure. Accuracy of AIST determination is low, since surfactants determined by an indirect method of subtraction. Thus, the objective of our research was to develop an exact and express method of AIST determination in CS. [Pg.133]

There are two main approaches to its solution. Traditional approach is based on preliminary separation of UGC samples to gaseous and liquid phases and their subsequent analyses [1]. This approach is well-developed and it allows obtaining quite precise results being used properly. However, this method is relatively complicated. Multi-stage procedure is a source of potential errors, then, it makes the analyses quite time consuming. More progressive approach is based on the direct analysis of the pressurized UGC samples. In both cases the determination of heavy hydrocarbons (up to C ) is made by capillary gas chromatography. [Pg.184]

Single Stage. Multi - Stage. Open Impeller. Closed Impeller. [Pg.52]

In this group the impeller or impellers are mounted onto the shaft with the bearings on both ends. The impellers are mounted between the bearings. These types of pumps are further divided into single stage (one impeller) or multi-stage pumps (multiple impellers). [Pg.57]

The majority of centrifugal pumps have performance curves with the aforementioned profiles. Of course, special design pumps have curves with variations. Eor example, positive displacement pumps, multi-stage pumps, regenerative turbine type pumps, and pumps with a high specific speed (Ns) fall outside the norm. But you ll find that the standard pump curve profiles are applicable to about 95% of all pumps in the majority of industrial plants. The important thing is to become familiar with pump curves and know how to interpret the information. [Pg.85]

The need to keep a concave temperature profile for a tubular reactor can be derived from the former multi-stage adiabatic reactor example. For this, the total catalyst volume is divided into more and more stages, keeping the flow cross-section and mass flow rate unchanged. It is not too difficult to realize that at multiple small stages and with similar small intercoolers this should become something like a cooled tubular reactor. Mathematically the requirement for a multi-stage reactor can be manipulated to a different form ... [Pg.203]

It has been proposed that rapidly eooling the expander with steam eombined with flue gas would leave tlie expander free of deposits. This suggestion is unlikely to work witli multi-stage expanders beeause eatalyst residue is likely to remain in the spaee between the disks. Moreover, there is a eoneern that this type of eooling eould eause loealized eooling in the expander and partial deformation of eomponents. [Pg.470]

This standard covers the minimum requirements for general-purpose, enclosed single- and multi-stage gear units incorporating parallel-shaft... [Pg.154]

Petroleum products may be treated with various solvents for the removal by selective solubility of undesirable constituents or for the recovery of by-products. The solvent and solute must be separated to yield the desired product and to recover the solvent for reuse. The solvents normally boil at a lower temperature than the products from which they are to be removed and so are generally distilled off as overhead products. The pipe stills used for this service may be single-stage or multi-stage units, depending on the service involved. Some solvents can be removed by the use of steam heated stills. In other cases, the high temperature required necessitates the use of fired heaters and vacuum towers. [Pg.212]

Low-pressure stage casings and interstage circuits on both centrifugal and positive displacement multi-stage compressors are not normally designed for full discharge pressure and must also be provided with overpressure protection. [Pg.139]

MULTI-STAGE CONTINUOUS FLOW STIRRED TANK REACTOR ... [Pg.327]

Multi-stage preheating, pre-calciners, kiln combustion system improvements, enhancement of internal heat transfer in kiln, kiln shell loss reduction, optimize heat transfer in clinker cooler, use of waste fuels Blended cements, cogeneration... [Pg.755]

For speeds shown, units in the area to the right of these lines should be Single Stcge as Multi-Stage would be less efficient... [Pg.681]

In the more favored multi-stage axial flow design the bladeing is of the impulse type (known as a Rateau or Curtis type stage) or of the reaction type. It is popular among manufacturers to design multi-stage machines with a combination of these two types, and the most common combinations are ... [Pg.202]


See other pages where Multi-stage is mentioned: [Pg.314]    [Pg.480]    [Pg.122]    [Pg.247]    [Pg.282]    [Pg.58]    [Pg.75]    [Pg.66]    [Pg.261]    [Pg.1164]    [Pg.90]    [Pg.81]    [Pg.84]    [Pg.85]    [Pg.85]    [Pg.114]    [Pg.75]    [Pg.155]    [Pg.330]    [Pg.346]    [Pg.346]    [Pg.332]    [Pg.471]    [Pg.471]    [Pg.471]    [Pg.472]    [Pg.472]    [Pg.662]   


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Adsorption multi-stage operation

Cancer theory, multi-stage

Clustering Multi-Stage

Design Study for the Multi-stage Adiabatic Mode

Drug multi-stage

Ejector multi-stage

Liquid multi-stage extraction

Multi-Stage Steam Jet Vacuum Pumps

Multi-Stage Vacuum

Multi-stage Level Combined Effect of Phase and Chemical Equilibrium

Multi-stage Level Reactive Azeotropy

Multi-stage SJE system

Multi-stage adsorption

Multi-stage continuous flow stirred tank

Multi-stage continuous flow stirred tank reactor

Multi-stage continuous processes

Multi-stage continuous system

Multi-stage evaporation

Multi-stage fluidized beds

Multi-stage fractionation

Multi-stage heat exchange reactors

Multi-stage jets

Multi-stage mass change

Multi-stage mass spectrometry

Multi-stage membrane systems

Multi-stage model

Multi-stage production process

Multi-stage reactor

Multi-stage steam jet vacuum

Multi-stage stochastic programs

Multi-stage systems

Multi-stage tandem mass spectrometry

Multi-stage techniques

Multi-stage treatment

Multi-stage turbine

Objective Optimization of Multi-Stage

Process multi-stage

Production Scale Multi-Stage Process

Rectification multi stage

Screw multi-stage

Separation multi-stage

Single- and Multi-Stage Operations for Adsorption

The Initial Stage of Bubble Growth in a Multi-Component Solution

The Investigation of Multi-Stage Processes

Towards a Multi-Stage Drug Delivery System

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