Showing posts with label u tube. Show all posts
Showing posts with label u tube. Show all posts

Monday, 2 February 2015

MECHANICAL AND THERMAL DESIGN OF THE CEBAF HALL A BEAM CALORIMETER

Abstract

   A calorimeter is being fabricated to provide 0.5% - 1.0% absolute measurement of the beam current in the Hall A end station of the Continuous Electron Beam Accelerator Facility (CEBAF) at Jefferson Lab (JLAB).  Modern powder metallurgy processes have produced high density, high thermal conductivity tungsten-copper composite materials that minimize electromagnetic and hadronic energy loss while maintaining a rapid thermal response time.  Heat leaks are minimized by mounting the mass in vacuum on glass ceramic mounts.  A conduction cooling scheme utilizes an advanced carbon fiber compliant thermal interface material.  Transient finite difference and finite element models were developed to estimate heat leaks and thermal response times.

INTRODUCTION

An experiment scheduled for the Hall A end station of the JLAB CEBAF machine requires that absolute beam current be measured to the 0.5% - 1.0% level for currents around 1A (Ref. [1]).  The existing beam current diagnostic devices would have uncertainties of about 30% for currents at the 1A level.  A calorimeter has been designed to improve beam current measurements (see figure 1).  The calorimeter will measure the temperature rise in a metal slug after it intercepts the electron beam with well-defined energy for a well-defined time.  The measured temperature rise is then used to calculate the average beam current during the exposure to the beam.  Large copper and silver calorimeters built at the Stanford Linear Accelerator Center (SLAC) in the 1960’s achieved precisions of about 1% (Ref. [2]).

The calorimeter is designed to contain the energy of the incident beam.  Any significant energy loss compromises the ultimate accuracy.  Simulations of electromagnetic and hadronic showers produced in the calorimeter show that a 16cm diameter by 16cm long tungsten mass with a 1cm diameter by 2.5cm long entrance hole would limit escaping charged and neutral energy to 0.4+/-0.2% while maintaining rapid thermal response times (Ref. [3]).  To calibrate the device a cartridge heater controlled by a precision power supply is embedded into the mass.

A current measurement must be performed using only a few minutes of beam time and be able to be repeated within about 30 minutes.    The calorimeter will provide precision measurements for beam powers between 0.5kW – 5kW at beam energies ranging from 800 MeV - 12GeV.

MECHANICAL DESIGN

Pure tungsten shapes are typically produced by pressing and sintering tungsten powder followed by an extrusion or swaging operation to reduce porosity.  Operations to reduce the as-sintered porosity are not practical for a part this large.  An extensive search for a fully dense, high thermal conductivity, high density, tungsten composite material identified Tungstar (Ref. [4]), a tungsten-copper (95:5) powder produced by OSRAM Sylvania.  This powder allows a tungsten-copper part to be made without an infiltration of copper into a sintered tungsten framework (infiltration would not be an option for a part this large).  The powder is pressed then sintered producing a very dense (~99%), homogeneous, machinable part.

Since the calorimeter must be installed upstream of the physics target, the tungsten-copper mass must be inserted into the beamline to intercept the electron beam then removed to allow normal beam operations to resume.



Figure 1: Hall A Calorimeter

A three position actuation scheme (using a three position air cylinder) minimizes actual beam time required to take a current measurement: 1) in-beam-charging, 2) out of beam-equilibrating, and 3) out of beam-cooling.  The mass support frame incorporates an oversized beamline tube that allows beam to pass through the device in both the equilibrating and cooling positions (see figure 2).
Electrical wires for thermometry, charge bleed off, and the calibration heater are routed to the mass through electrical vacuum feed-throughs, then down the vertical support tube, eliminating the need for a service loop inside the vacuum chamber (see figure 2).  The electrical feed through/support tube is guided using linear ball bushings and precision shafting.



Figure 2: Mechanism
Socket set screws with glass ceramic inserts are used to position and support the mass inside the frame while providing thermal and electrical isolation.  Three adjustable rods support the cooling plate foundation and allow alignment to the flat lower surface on the tungsten-copper mass (see figure 3).



Figure 3: Mass Mount & Cooling Plate
THERMAL DESIGN

Heat leaks to and from the mass during exposure to the beam and during equilibration must be minimized, or at least known with sufficient certainty (<<1% of total absorbed energy).
Advanced compliant thermal interface materials with good conductance in vacuum at low interface pressures allow the mass to be cooled for subsequent measurements by bringing it in contact with a cold plate rather than embedding or otherwise attaching cooling tubes.  The mass is gold coated and the vacuum vessel electro-polished to reduce radiation exchange.  The ceramic inserts used in the mounts minimize conductive heat transfer.  The thermometry devices (RTD’s) are mounted 120° apart on the outer surface of the slug at each end.

ANALYSIS

Initial modeling of the thermal response time, radiative and conductive heat exchange was done using a transient two-dimensional axisymmetric implicit finite difference (FD) model written using Visual Basic for Applications in Excel.  A lumped mass model that assumes minimal spatial variation in temperature was used to estimate the time required to cool the mass to repeat a measurement.
The FD model was checked using the IDEAS finite element (FE) TMG transient solver.  The FE model allowed a more detailed analysis of the transient heat flow out of (and into) the tungsten-copper mass during each of the three stages of operation (i.e., charging, equilibrating, and cooling).


Figure 4: Finite Element Model
RESULTS

Simulations for a 48sec exposure to I*E = 5kW beam power are presented here.  The thermal response at the RTD positions is shown in figure 5.

Figure 5: Thermal Response

The conductive heat leaks from the wires and mounts are shown in figure 6.

Figure 6: Conductive Heat Loss

Radiation heat losses during the charging and equilibrating phases estimated using the FD model are shown in figure 7.

Figure 7: Radiation Heat Loss

The integrated radiation and conductive losses during the charging and equilibrating phases are combined in figure 8.


Figure 8: Integrated Total Heat Loss

The total energy deposited is 48sec*5kW=240kJ.  This produces a ΔT of ~30K.  Experiments performed on the thermometry instrumentation and controls show that this rise is more than sufficient to achieve the required precision (Ref. [5]).  From figure 8, the total energy lost during the measurement is 531J.  At the simulated beam power of 5kW, the thermal losses amount to only 0.2% of the deposited energy.  The plan is to calibrate the thermal loss model with the measured test data, and then correct the beam current calibration for the calculated thermal losses.
 Refinements to the FE model could include radiation exchange and a model of the heater cartridge for comparisons between simulated calibration and electron beam heating.
Thermal stress calculations are ongoing at this time.  Preliminary conservative estimates show stresses high enough to warrant more refined analyses.

SUMMARY

The Hall A calorimeter thermal and mechanical design limits heat losses to the ~0.2% level.  The design minimizes actual beam time required to take a measurement and allows a measurement to be repeated within ~20min.
The device is currently in fabrication with initial bench testing (using the heater) expected to begin this summer.  Installation into the Hall is planned for early 2006.

REFERENCES

[1] R. Gilman, “Hall A Beam Calorimeter: Overview, Specifications, Operations”, JLAB internal document, May 6, 2004
[2] G.E. Fischer and Y. Murata, “A Beam Monitor System for High-Intensity Photon Beams in the Multi-GeV Range”, NIM volume 78, pages 25-39, 1970, SLAC-PUB-0605
[3] P. Degtiarenko, “Tungsten Calorimeter Model Calculations and Radiation Issues”, JLAB internal document, May 14, 2004
[4] Tungstar is a registered trademark of OSRAM Sylvania, http://www.sylvania.com
[5] A. Freyberger, JLAB internal communication

Tuesday, 6 January 2015

Heat Exchanger FAQs and Answers

Many people who purchase heat exchangers and other such appliances often complaint that they have not gotten the thing they were looking for or that the seller has not given them the item he had initially described. While it is true that the seller may trick customers, it is also widely known that many customers only have themselves to blame for the deceit. This is because they do not conduct enough research before they go out to purchase the product and hope to believe everything that the seller tells them about it. Since it is very important to conduct proper research, a list of the most Frequently Asked Questions about the heat exchanger have been listed and answered.

What is it?
In the easiest possible words, heat exchangers are things that transfer heat from one appliance to another, or from one medium to another. For example, heat exchangers installed in a swimming pool will use hot water stored up in a boiler to heat up the water in the pool or a Jacuzzi. Also, hydraulic coolers will use cold water or air to make sure that the heat of oil used to run the machine is cooled down as well. The actual exchange of energy happens through the conductors that are separating the two opposing forces. Conductors may take the form of tubes or pipes through which fluids run.

What are the types?
Many people also want to know the man types of heat exchangers available in the markets today. To begin with, there is the shell and tube heat exchanger. Many small sized tubes are contained inside a shell in the shape of a cylinder. A tube stack is used to make sure that the tubes are properly positioned inside the shell.In many cases, the tube stack lets the tube bundle grown larger or smaller in accordance with the amount and temperature of the fluids within.

Moving on, plate heat exchangers are probably the most common form of heat exchangers used today. They are quite similar to the typical shell and tube exchanger but instead of tubes, it uses a stack or collection of plates. They may be gasketed if the fluids and the setup inside the exchanger allows the change. They are mostly built with stainless steel and are perfect for refrigerators.

Lastly, there are the air cooled heat exchangers that are widely used in cars and other such vehicles to keep the engines cool and functional. They are mostly placed in areas where there is no source of cool water available at all times. They may sometimes bring together water, air and charge air coolers into a single entity to make sure that lesser space is consumed for the same effectiveness. Cool air comes from a fan or the sir coming into the cooler when the vehicle moves.

Which fluids are needed?
Not all liquids are able to work within a heat exchanger and one will have to select the fluids appropriately. To begin with, one will have to consider where the specific exchanger is being used and the different appliances used in the exchanger itself. Material used to construct the exchanger will also matter a lot. The most common types of fluids include simple water, sea water and even oil (especially in air cooled exchangers) but other fluids which are more corrosive may also be used. These include chorine induced water and other acids. They may work better temporarily but will, undoubtedly, damage the exchanger.

How to increase the life?

Since many heat exchangers, specifically those bought for bigger equipment and appliances, are so expensive; many people wish to know how they can care for the exchanger to extend its life. The only way to do this is through regular checks, maintenance and repairs so that no damage comes to the exchanger and danger is discovered before it occurs.  

Wednesday, 17 December 2014

Important Parts of a Tube Bundle & their Uses

A tube bundle is used for many reasons, and one of the most important ones includes heat exchange in various commodities. These bundles are available in a wide range of different sizes, diameters, shapes, materials as well as designs. Choosing the most appropriate one depends on whichever industrial application it has to be used for in the first place, which has to be decided by the user. There are many parts of these bundles, all of which are unique in their own way and without them; these bundles tend to not work as efficiently as they do otherwise.

Tubesheet Material
Being a part of the tube bundle, the tubesheet thickness is something that can be easily measured. While the thickness may vary always, individuals who wish to use these bundles can always select the type of tubesheet thickness which suits them best and that usually tends to depend on the type of application it is being used for. The diameter can also be checked without having to face any issue and for those who are interested in knowing the actually thickness of the tubesheet which is majorly found in these bundles, it varies from 5” to 3” thick at best.

Presence of Bolt Holes
On the other hand, these bundles also are inclusive of bolt holes which can be found in abundance. People should be aware of the fact that the bolt holes always tend to go around the tubesheet and on through it, which is a common misconception amongst a lot of individuals who decide to use the tube bundle for a variety of different reasons. However, some of these bundles many have bolt holes and on the other hand, some may as well not have them too. Although knowing the size of the bolt holes present in these bundles along with their sizes and length is exceptionally important.

Materials of the Tube
Individuals going ahead in order to use a tube bundle should always check out the tube materials beforehand. This basically ensures the material that has been used in the manufacturing of the bundles in the first place. Mostly, they are made of cooper and that is easy enough to find. However, in case these ones are not available for some reason, there is a wide range of other tube materials which are available for the convenience of users. These materials generally are inclusive of carbon steel, titanium, cupro-nickel and many more which are equally as effective.

Type of Tubes

While some bundles are straight tube whereas the other ones are “U”. U tubes as well as straight tubes are significant in their own way and are used for various reasons and industrial applications. Choosing whichever is needed usually depends but they both are most likely to come in handy. Recognizing these different kinds of a tube bundle is exceptionally easy as the straight ones are rather plain and quite in symmetry whereas the U tubes are literally in the shape of a U – which is very easy to spot. The more commonly used type of tubes is the U ones, since they are more easily available and beneficial in comparison with the straight ones.

Thickness of Tubes
The thickness of the tube is another factor that should be checked out before buying these bundles for any sort of uses, particularly for heat exchange. Certain standards of tube thickness have been set for people to see and decide which one they prefer more. The thickness of tubes actually makes the outer walls heavy, making the bundles much more solid and efficient in the long run. For all that these bundles have to offer, these should definitely be used for heat exchange and all the industrial uses related to it in general.



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