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ProMax® - Separator Sizing

The package included in ProMax is capable of helping you both horizontal and vertical separation vessels in a multitude of process conditions, including separators, scrubbers, knockouts, flash , and slug catchers. The methodology focuses on a minimization of mass while achieving the required separation.

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  • Vapor–liquid separator -

    Vapor–liquid separator -

    Method of operation. For the common variety, gravity is utilized in a vertical vessel to cause the liquid to settle to the bottom of the vessel, where it is withdrawn. In low gravity environments such as a space station, a common liquid separator will not function because gravity is not usable as a mechanism.In this case, centrifugal force needs to be utilised in a spinning ...

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  • Page 8_2 Frame - nawabi.de

    Page 8_2 Frame - nawabi.de

    Designing the steam . Minimum Diameter of steam disengaging relys on experience as much as specifics, but the following guidelines should be considered. Except for very special designs, the minimum inside diameter of steam for HRSG service should be a minimum of 48 inches.

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  • Flare System: Types, Segregation, Tips, Purge System and More

    Flare System: Types, Segregation, Tips, Purge System and More

    of liquid droplet of 300-600 microns considering the design case for the flare 20-30 minutes of liquid hold-up time based on a relief case that results in maximum liquid No internals to facilitate separation

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  • Steam quality and drum sizing - Boiler and Pressure Vessel ...

    Steam quality and drum sizing - Boiler and Pressure Vessel ...

     · The disengagement height is only relevant for low pressure with no seperators . If seperators are installed, the max water level is based on avoiding have the water height exceed teh steam outlet of teh seperator, since that would cause reentrainment of water.

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  • [EXCEL] How to Design Entrainment Separation Vessels ...

    [EXCEL] How to Design Entrainment Separation Vessels ...

    A Knockout with a mist eliminator is common whenever a process requires entrained droplets to be separated from a vapor stream. A simple knockout no mist eliminator will remove droplets larger than about 380 microns by gravity settling M. generally gravity settling removes more than 90% of the liquid entering the vessel .However the remaining droplets smaller than 380 microns can ...

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  • Drum Separator is Another Pre-cleaning Machine in Flour ...

    Drum Separator is Another Pre-cleaning Machine in Flour ...

    separator is widely applied in many different ways for pre-cleaning materials. It is successfully used in the reception of granular, mealy, and floury bulk materials in grain mills, bulk storage systems, and other plants in the food processing and feed manufacturing industries.

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  • Demisting / Droplet Separation | Begg Cousland - Applications

    Demisting / Droplet Separation | Begg Cousland - Applications

    PROCESS INFORMATION. The primary function of the boiler steam is separate water from steam which prevents carryover of the condensate into to the steam header the separated steam is sent to super heaters and the water is recirculated for conversion to steam with …

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  • Flash Drum - Student - Cheresources.com Community

    Flash Drum - Student - Cheresources.com Community

    Considering the following, for the same service and conditions: Diameter, existing: X1 Diameter, new: X2 Flow, existing: Y1 Flow, new: Y2 If I want to quickly a for an increased flowrate, could I just take the ratio of the flow rates and multiply that number by the existing diameter to get a new diameter?

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  • Flash Separators, Condensate Handling, Flash Steam ...

    Flash Separators, Condensate Handling, Flash Steam ...

    Selecting a Flash Separator: Flash Separators are sized for the condensate flow entering the tank and the amount of flash steam that is produced when venting to a lower pressure. To select a flash separator use Chart "A" to determine the flash steam amount and Chart "8" that gives the size of tank and nozzle connection sizes required.

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  • Introduction to Chemical Engineering for Lecture 7: Flash ...

    Introduction to Chemical Engineering for Lecture 7: Flash ...

    ash , the of the and the liquid and vapor compositions and ow rates. Which of these variables are speci ed and which need to be chosen depend on the application2. Normally, the feed is speci ed, ie. the ow rate F, composition z, pressure P F and enthalpy h F are known3. The other variables are the vapor ow rate V, vapor ...

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  • Equipment Fundamentals: Separation & Fractionation

    Equipment Fundamentals: Separation & Fractionation

     · efficiency & decreases overall of vessel No internals –bulk with no obstructions e.g., flare knock out Mesh pad Vane packs Cyclones Combination internals 19 Ref: GPSA Data Book, 13th ed.

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  • 2 phase separator design calculator – Vertical Knock Out Drum

    2 phase separator design calculator – Vertical Knock Out Drum

    This calculator can be used to a vertical two phase separator for removal of liquid droplets or a vertical Knock Out or Reflux vessel. This calculator determines the minimum required of such a separator to handle the given flowrates based on terminal settling velocity of liquid droplets also reported in results.

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  • Souders–Brown equation -

    Souders–Brown equation -

    The diameter of a vapor–liquid separator drum is dictated by the expected volumetric flow rate of vapor and liquid from the drum. The following sizing methodology is …

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  • EQUIPMENT DESIGN - جامعة تكريت - كلية ...

    EQUIPMENT DESIGN - جامعة تكريت - كلية ...

    TANKS, VESSELS & Rules of Thumb 1. Holding time for most intermediate storage vessels, half full, is 10 minutes. 2. Holding time for feed tank to a furnace , half full, is 30 minutes. 3. Optimum L/D ratio is 3, however a range of 2 to 5 is common. 4. Vessels of …

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  • Design of vapor-liquid separator knockout drum, flash drum

    Design of vapor-liquid separator knockout drum, flash drum

    The a vapor-liquid separator or knock-out pot, or flash , or compressor suction should be dictated by the anticipated flow rate of vapor and liquid from the . The following methodology is based on the assumption that those flow rates are known.

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  • CORRECT STEAM SEPARATION - Inveno Engineering

    CORRECT STEAM SEPARATION - Inveno Engineering

    stage process. The first stage is a coalescing effect, where the steam is introduced to a stainless steel mesh that makes the steam flow change directions. This first stage agglomerates the fine water particles, causing them to coalesce by bringing the water droplets together, increasing their and mass. The higher condensate

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