thermocompressor design calculation

Design Inputs On Sizing Rotary Drier

Thermocompressor Design And Operation For High Efficiency The dryers on this machine consumed 125 000 kg/hr of steam with 44 000 kg/hr being motive steam to the thermocompres-sors The mill had previously changed from rotary to stationary syphons but did not evaluate the sizing and performance of the thermocompressors

Desuperheaters

Use of desuperheaters in the sugar industry Desuperheating of Steam Rapid Design Do desuperheater calculations online A desuperheater is a device that cools superheated steam to a temperature close to its saturation temperature ususally by spraying atomised droplets of water into the flow of

Thermocompressor Calculation

2020-5-22Thermocompressor Calculation - posted in Student: Dear all I would like to do thermocompressor calculation but I do not have any idea how to do it and would like to ask advise from everybody here For example I have high pressure steam (around 50barG) as motive steam and would like to increase low pressure steam (near atmospheric) to probably about 15 barG by using thermocompressor

Liquid Jet Ejectors

Liquid Jet Ejectors are specially designed to operate using water solvent or any other clear liquid and generate vacuum corresponding to the vapor pressure of the liquid They are very useful for applications when expensive process fluid is to be recovered They are most suitable for low non-condensable and high condensable loads in applications like distillationRead more

Dedert Corporation :: Thermal Vapor Recompression

Steam is once again the source of energy Economics and product characteristics determine the suitability of thermal vapor recompression operation This design provides improved steam economy with less costly equipment than straight steam heated designs but requires higher pressure steam

Evaporators

A two-effect falling-film evaporator with thermocompressor requires about 0 32 kg of steam to evaporate 1 kg of water and a five-effect evaporator requires 0 09 kg of steam Without the thermocompressor the specific steam consumption would be approx 0 55 and 0 2 kg per kg of water evaporation respectively

LEHENG

2020-7-20Through accurate calculation accurate balance of investment and output ratio our company design can obtain the reasonable processing capacity in evaporation system fully utilize the function of the equipment and achieve the best cost performance With leading technology stable performance and longer service life LH Centrifugal steam

Liquid Jet Ejectors

Liquid Jet Ejectors are specially designed to operate using water solvent or any other clear liquid and generate vacuum corresponding to the vapor pressure of the liquid They are very useful for applications when expensive process fluid is to be recovered They are most suitable for low non-condensable and high condensable loads in applications like distillationRead more

Pulp and Paper

2015-8-20on technology design For example in the tissue industry many newer machines are Through Air Drying (TAD) design These are more energy intensive but have other product benefits • Bar 4 – Energy Gap: Subtract the benchmark (Bar 3) from the energy use for your mill (Bar 2) This is the energy gap between your mill and the benchmark Although

construction of falling film evaporator design calculation

Formulas and design consideration parameters in Robert Evaporator Design and also provided online calculation sheet with formulas A general guide to design of falling film evaporators Request PDF on ResearchGate | On Mar 23 2015 S Bigham and others published A general guide to design of falling film evaporators utilized in multi effect

Thermocompressor

A Steam Jet Thermocompressor is an energy saving device that compresses low pressure steam often waste steam to a higher usable pressure It offers an advantage over mechanical compressors/blowers due to its smaller size while handling a very large vapour volume under vacuum conditions Due to its size and absence of mechanical parts it requiresRead more

SJT Steam Jet Thermocompressor

The Steam Jet Thermocompressor is a prime example of this commitment the SJT is an energy saving device that compresses low pressure steam often waste steam to a higher useable pressure All of Spirax Sarco's SJT Steam Jet Thermocompressors are designed and built to the customers specific criteria for their intended application to provide

Desuperheaters

Use of desuperheaters in the sugar industry Desuperheating of Steam Rapid Design Do desuperheater calculations online A desuperheater is a device that cools superheated steam to a temperature close to its saturation temperature ususally by spraying atomised droplets of water into the flow of

Product Catalog

2020-7-20• For the design in individual cases our order confirmation is binding and not the catalog sheet • Where necessary installation and operat-ing instructions are made available • Normally cast apparatuses are supplied with flanges bored to DIN PN 10 unless otherwise agreed If specified flanges according to ASME BS or other special

Steam Jet Thermocompressor

Reusing waste steam with a Steam Jet Thermocompressor will improve steam generation efficiency and reduce your energy costs It's simple compact and lightweight construction means it's easy to install into a pipeline and enables overhead installations It has low

DE

5 2 4 Triple-effect evaporators' calculation method 1 Determine the boiling point in the last effect from the known outlet concentration and pressure in the last effect 2 Determine the total amount of vapor evaporated by performing an overall material balance 3 Estimate the temperature drops ∆T 1 ∆T 2 and ∆T 3 in the three

Fundamentals of Paper Drying Theory and Application

2018-9-2555% depending on the paper grade and press se ction design The third part of the paper machine is called the drying or dryer section The paper web passes over rotating heated cast iron cylinders and the most of the remaining water is removed by evaporation When the paper leaves the dryer section its solid content has increased to about 90-95%

EXHAUST SYSTEMS

2019-9-4design requirements Refer to Figure 1 for manifold configurations Figure 1 Dry Manifolds Dry manifolds are the preferred manifold design They are cost effective and by providing the maximum possible exhaust energy to the turbocharger they offer the highest overall efficiency Dry manifolds however also radiate the

University of New Orleans ScholarWorksUNO

2020-1-6alternative design with a minimized footprint The analysis showed theoretical flaws and design weaknesses in the evaporator including violation of the first law of thermodynamics An alternative thermal compressor design was created through computational fluid dynamics using spreadsheet methods developed in house aided by the software product

new computation method

This paper presented a kind of new computation method for the sprocket design of double pitched roller chain Comparison and analysis have been carried out on the calculated results obtained from this method and those obtained from the design in GB5269-85 A satisfactory result was obtained and thus indicates that this method is effective

Triple

Triple-Effect Falling Film Evaporator - Calculation - posted in Industrial Professionals: Dear i need help to make calculation on these evaporator evaporator have thermo compresor PID is in attachment my asking inputs are 10 000 kg / hr temp of input material is 60 C input is 8 Bx asking output is 55 Bx Question is could this machine do this? what vacuum pump is needed ( there is no known

Ejector Design Software

This website offers the following: Ejector Design Software to do conceptual design and generate ejector sizes The ejector design principles used in the ejector calculations for the program are explained including the ejector energy balance and effects of the ejector flow cones Free demo programs for a short time are offered to let you see how the ejector program works - they are not

Liquid Jet Ejectors

Liquid Jet Ejectors are specially designed to operate using water solvent or any other clear liquid and generate vacuum corresponding to the vapor pressure of the liquid They are very useful for applications when expensive process fluid is to be recovered They are most suitable for low non-condensable and high condensable loads in applications like distillationRead more

An investigation of thermo

2013-5-1The lack of useful curves and detailed design procedures that could be used to clarify an optimum geometry for the "converging zone" of ejectors and thermo-compressors in recent studies was the main inducement of this article Therefore the aim of this study is to describe an efficient method for the TVC geometry design on the basis of a

An investigation of thermo

2013-5-1The lack of useful curves and detailed design procedures that could be used to clarify an optimum geometry for the "converging zone" of ejectors and thermo-compressors in recent studies was the main inducement of this article Therefore the aim of this study is to describe an efficient method for the TVC geometry design on the basis of a