Quick answer. Heat transfer rigs measure something nobody can see, and almost every wrong student result has the same cause: heat left the apparatus by a path the equation did not include. So the question to ask of a rig is not what it demonstrates, which is printed on every brochure, but how it deals with its losses - whether each one is guarded, measured, or merely ignored. After that, three things decide whether the data is usable: the thermocouple arrangement, the heater rating and how it is controlled, and flow measurement on anything with a fluid in it. This page sets out how to specify on those grounds, and ends with an honest note about this listing, which contains roughly 22 distinct experiments spread over 57 records.
A heat transfer experiment is an energy balance. The student measures the electrical power into a heater and some temperatures, and calculates a conductivity, a coefficient or an emissivity on the assumption that the measured power went where the theory says it went. It never all does. Some leaves through the mountings, some down the thermocouple wires, some off the back of the specimen, some by radiation when the calculation assumed only convection.
There are only three honest ways to deal with a loss, and one dishonest one.
The teaching value of this equipment is in making students confront that fourth option. A rig that hides its losses produces tidy numbers and no understanding. A rig that exposes them - by giving the student the extra thermocouples and asking for a loss estimate - produces a worse-looking result and an engineer. Specify for the second.
Read this column by column rather than row by row. The third column is the one a quotation never mentions and the one that decides your data.
| Experiment | Quantity measured | Loss that dominates | How a good rig handles it |
|---|---|---|---|
| Conduction through a composite wall | Thermal resistance in series; interface resistance | Edge losses radially outward from the stack | Guard ring or generous lagging, plus a stated edge-loss bound |
| Conductivity of a metal rod | Axial conductivity from a temperature gradient | Radial loss along the whole rod | Heavy lagging, a thermocouple on the lagging surface, and a water-cooled far end whose duty is measured |
| Conductivity of an insulating powder | Conductivity of a poor conductor | Departure from the assumed spherical or cylindrical symmetry | Concentric geometry held true, and a stated fill procedure - the packing density is part of the measurement |
| Guarded hot plate on a slab | Conductivity of a slab to a recognised method | Lateral flow out of the main heater | A separately controlled guard heater with its own differential thermocouple |
| Lagged pipe | Conductivity and critical thickness of lagging | Axial loss along the pipe and out of the ends | End sections heated separately, or long enough that the central section is one-dimensional |
| Pin fin | Fin efficiency; natural against forced convection | Conduction into the base plate, and radiation at higher temperatures | A base thermocouple so base temperature is measured rather than assumed |
| Natural convection | Convective coefficient on a vertical cylinder or plate | Radiation from the hot surface, and any air movement in the room | A surroundings thermocouple so the radiation term can be subtracted, and an enclosure or shield |
| Forced convection | Coefficient against Reynolds number in a duct | Loss through the duct wall; unknown velocity profile at the test section | A lagged duct, a calibrated orifice or anemometer, and a long enough entry length |
| Emissivity comparison | Emissivity of a test plate relative to a reference | Convection from both plates, and any difference between them other than emissivity | Identical geometry and identical power, inside an enclosure, with the reference coating specified |
| Stefan-Boltzmann | The fourth-power law and the constant | Conduction into the test disc holder; non-black enclosure | A thin, low-mass disc, a hemispherical enclosure at a measured temperature |
| Heat exchanger, any type | Overall coefficient, LMTD, effectiveness | Loss to the room from pipework, and error in the flow measurement | Lagged pipework and a flow measurement whose calibration fluid and temperature are stated |
| Dropwise and filmwise condensation | The step change in coefficient between the two modes | Non-condensable gas in the shell, which destroys the result | A venting arrangement and a procedure for purging before readings |
Almost every experiment in this listing is a steady-state measurement, and the single most common procedural failure is that readings are taken when the timetable runs out rather than when the apparatus has settled. A heavily lagged pipe or a thick insulating slab has a long time constant by design - the better the lagging, the longer the wait - so the apparatus that gives the cleanest result is the one students are most likely to read too early.
The fix is to make steady state a stated criterion rather than a judgement. A department should write a tolerance into the lab sheet: for example, no measured temperature changing by more than 0.2 °C over five minutes, on at least three consecutive readings. The particular numbers belong to your apparatus and your tolerance for lab time, and should be established once by running one experiment to true equilibrium and watching the approach; the point is that a criterion exists and is written down, so that a student who is running late has to record that the criterion was not met rather than quietly taking the reading anyway.
Two practical consequences for specification:
On this equipment the sensors are not an accessory. Every number the student calculates is a difference between two temperatures, so an error in one reading propagates straight into the result, and the usual errors are mechanical rather than electrical.
A natural convection apparatus beside a door, under a ceiling fan, or in front of an air conditioner is a forced convection apparatus. The whole experiment rests on the air moving only because the surface heated it, and a draught of a fraction of a metre per second is enough to change the coefficient materially. This is worth deciding before the bench layout is fixed: the natural convection rig wants a corner away from doors and vents, and ideally a shield or enclosure. It is also the experiment where the radiation term is largest relative to the convection being measured, so the surroundings thermocouple is not optional - without it the student is attributing radiation to convection and getting a coefficient that is too high.
The teaching point is spectacular - the coefficient changes by an order of magnitude between the two modes on the same surface - and it is destroyed by air in the shell. Non-condensable gas blankets the condensing surface and collapses the coefficient, so a rig without a proper vent and a written purge procedure will show a difference far smaller than the real one, or none. Ask specifically how the shell is vented and what the start-up procedure is.
Every exchanger rig in this listing gives the student a free check on their own data, and most lab sheets do not use it. The duty calculated on the hot side and the duty calculated on the cold side are measurements of the same quantity, so they should agree within a stated tolerance.
As with any teaching laboratory, specify by ratio rather than by item. Decide the class size, the batch size at one rig, and the number of weeks in the rotation; those three numbers determine how many of each experiment you need, and the answer is almost never one of everything.
A defensible core for an undergraduate heat transfer course, in buying order:
Shared services matter more than any single rig: a stable supply, a reliable cooling-water supply at a known temperature, and a data logger used across rigs. See shared engineering lab instruments for the pumps, gauges and general instruments these rigs assume you already have.
We would rather say this than let you discover it halfway down page four. This listing holds 57 records, HTL-0001 to HTL-0057, which resolve to roughly 22 distinct experiments. Several experiments appear three times under different codes - the emissivity apparatus, the Stefan-Boltzmann apparatus, the pin fin, the forced convection unit and the dropwise/filmwise condensation unit each have three records. Two codes are used twice over (HTL-0039 and HTL-0045), HTL-0034 is missing, and a few names carry typing errors that have travelled with the data: Insulting Powder for insulating, Citical Radius for critical, Parrallel, and Stefan Boltzman. One record, HTL-0049 Heat Transfer Sheet, is not a product.
So do not order by code from this page. Tell us the experiment and the class size and we will quote the current model, confirm the specification in writing, and tell you which code it ships against. We have recommended internally that this listing be consolidated, and the duplicate records removed rather than renamed.
Within physics lab for engineering students: thermodynamics for compressors, calorimeters, steam and refrigeration-cycle rigs, hydraulics for the bench, Bernoulli and notch experiments, and analytical instruments for pH, conductivity and photometry. Momentum transfer lab equipment covers the fluid-flow side of the same transport-phenomena syllabus. The full engineering lab equipment category lists the rest.
Because heat left by a path the equation ignored, and almost always radially through the lagging rather than axially along the rod. The measured power is divided by a gradient that is steeper than the axial flow alone would produce, so the conductivity comes out low. The apparatus is usually working correctly. The fix is not a better rig but a better calculation: measure the lagging surface temperature and the far-end cooling duty, estimate the loss, and subtract it. That estimate is the most valuable thing in the experiment.
A guard heater surrounds the main heater and is held at the same temperature, so there is no sideways temperature difference and no sideways heat flow - which means all the measured power goes through the specimen. It removes the error instead of correcting for it, and it is the recognised method for insulating slabs. It is worth paying for if you need defensible conductivity values or you teach the standard method. If the aim is to show that insulation resists heat flow, an unguarded apparatus with honest loss accounting teaches that at lower cost.
Longer than the timetable allows, which is why it needs a written criterion rather than a judgement. Establish it once by running an experiment to true equilibrium and watching the approach, then write a tolerance into the lab sheet - no temperature changing by more than a stated amount over a stated interval, on several consecutive readings. Well-lagged apparatus takes longest, so your cleanest experiment is the one most likely to be read too early. Running at lower heater power shortens the wait and shrinks the losses at the same time.
In a corner away from doors, windows, ceiling fans and air-conditioner outlets, ideally with a shield or enclosure. The experiment assumes the air moves only because the surface heated it, and a slight draught turns it into a forced convection experiment with an unknown velocity. Decide this before the bench layout is fixed, and specify the surroundings thermocouple, because radiation is a large fraction of the total here and without that channel the student attributes it to convection.
Close the energy balance. The duty on the hot side and the duty on the cold side measure the same quantity, so compute both every run; a gap beyond your stated tolerance means something is wrong before any coefficient is believable. When they disagree, suspect the flow measurement rather than the exchanger - a rotameter calibrated for cold water reads wrong on hot - and check the pipework lagging. Verify one flow point against a measuring tank and a stopwatch.
Because it does. The listing has grown to 57 records covering about 22 experiments, with duplicate entries for the emissivity, Stefan-Boltzmann, pin fin, forced convection and condensation units, two codes used twice, and one missing code. We have said so on the page rather than leaving you to find it, and we have recommended consolidation. In the meantime, enquire by experiment and class size rather than by code, and we will confirm the model and specification in writing.
Ray Export is a manufacturer and exporter of laboratory, scientific and educational equipment based at Plot No. 449, HSIIDC Industrial Area, Saha, Ambala, Haryana 133104, India. Enquiries: [email protected], +91-9817319615.
Written by Palak Mall, Senior Content Writer. Technically reviewed by Arvind Kumar, Lab Equipment Specialist, 12+ years in laboratory and testing instrumentation. Last updated: 17 October 2026.
The steady-state tolerance given in this page is an illustrative criterion for a department to set and verify against its own apparatus, not a measured property of any product. Thermocouple type characteristics are given at the level of standard reference practice; the applicable temperature range, tolerance class and compensation arrangement for a specific unit will be confirmed in writing on the quotation, as will heater ratings, insulation, flow-measurement calibration conditions, services and footprint. Record counts and product-name defects described above were read from this listing on 15 October 2026 and will change as the listing is corrected. No price is quoted on this page; prices for this equipment depend on specification, instrumentation and destination and are issued as dated written quotations.
The setup comprises of a radiator sandwiched between two arrangements of pieces. Three sorts of sections are given on either sides of radiator, which shapes a composite structure. A little hand squeeze outline is given to guarantee the ideal contact between the pieces. A variac is accommodated shifting the contribution to the warmer and Digital Voltmeter and Digital Ammeter show the warmth input. Warmth delivered by radiator streams pivotally on both the sides. Temperature Sensors are implanted between interfaces of sections to decide the temperature slope. The trial can be led at different estimations of information and computation can be made as needs be
Tests
To decide add up to warm protection and warm conductivity of composite divider
To plot temperature slope along composite divider structure
Utilities Required
Power Supply: 1Phase, 220 V AC, 2 Amp.
Table for set-up help
The setup is outlined and created to contemplate slacking marvel if there should be an occurrence of funnels. It comprises of three concentric channels of little thickness when contrasted with width and are orchestrated concentrically, and shut with the assistance of two circles. Two distinctive protecting materials fill the annuli between the barrels minimally. Temperature Sensors are fitted to gauge the temperature of pipe dividers for spiral outward warmth stream estimation. Inside the inward pipe, a Nichrome wire radiator is put pivotally. Warmth contribution to the warmer is given through a variac and estimated by Digital Voltmeter and Digital Ammeter. By shifting the warmth input rates, extensive variety of tests can be performed
Tests
To evaluate the real rate of warmth exchange through the composite barrels from the deliberate interface temperature of the known estimation of warm conductivity of the two protecting materials.
To decide the viable warm conductivity of the composite chambers
To decide the hypothetical temperature profile inside the composite chambers
Utilities Required
Power Supply: 1Phase, 220 V AC, 2 Amp.
Table for set-up help
It is a super-directing gadget and includes the exchange of warmth by bubbling and buildup of a liquid and thus exchange of warmth happens under almost isothermal condition. In this mechanical assembly the examination of warmth pipe with the copper pipe as great transmitter of warmth and with the stainless steel pipe as same material of development is made. It comprises of three indistinguishable barrel shaped conductors In regard of geometry. One end of these is warmed electrically while there are little limit tanks going about as warmth sinks at the opposite end. The unit comprises of a warmth pipe a copper pipe and a stainless steel pipe. Temperature sensors are implanted along the length to gauge the temperature dispersion and the warmth exchange rate is noted as far as the temperature ascend in the warmth sink tanks.
The execution of the warmth pipe as a super-directing gadget can be examined well as far as the temperature appropriation along the length at a given moment and can be contrasted and other two individuals. About isothermal temperature dispersion and quick ascent of temperature in warm sink tank uncovers the warmth pipe prevalence over the regular conductors
Analyses
To show the super warm conductivity of Heat Pipe and to contrast its working and best conductor i.e. Copper pipe and Stainless steel pipe as same material of development.
To plot the temperature v/s time reaction of three funnels
To plot the temperature dispersion along the length of three channels
Utilities Required
Power Supply: 1Phase, 220 V AC, 2 Amp.
Table for set-up help
Protecting Powder Apparatus is intended to decide the warm conductivity of protecting powder. The Apparatus comprises of two thin-walled concentric copper circles. Internal circle houses Nichrome Wire warming curl. Protecting powder is filled between the circles. Warmth streams radially outwards. Temperature sensors at legitimate positions are fitted to quantify surface temperatures of circles. Warmth contribution to the radiator is given through a variac and estimated by Digital Voltmeter and Digital Ammeter. By fluctuating the warmth input rates, extensive variety of examinations can be performed
Investigations
Assurance of warm conductivity of protecting powder
Examination of warm Conductivity of protecting powder at various temperatures
Utilities Required
Power Supply: 1Phase, 220 V AC, 2 Amp.
Table for set-up help
The exploratory set up comprises of metal bar, one end of which is warmed by an electric radiator while the opposite end of the bar extends inside the cooling water coat. A barrel shaped shell loaded with the asbestos protecting powder encompasses the center part of the bar. The temperature of the bar is estimated at various areas. Warmth Input to the radiator is given through variac and estimated by Digital Voltmeter and Digital Ammeter. By fluctuating the warmth input rates, extensive variety of examinations can be performed. Water under steady head condition is coursed through the coat and its stream rate and temperature rise is noted.
Trials
To plot the temperature appropriation along the length of Bar
To decide the warm conductivity of given bar at different temperatures
Utilities Required
Water supply 3 lit/min (approx.)
Deplete
Power Supply: 1 Phase, 220 V AC 2 Amp.
Table for set-up help
The present mechanical assembly is intended to decide warm conductivities of various fluids. The mechanical assembly comprises of a warmer. The radiator warms a thin layer of fluid. A cooling plate expels warm through fluid layer, guaranteeing unidirectional warmth stream. Temperature is estimated over the fluid layer and finish get together is appropriately protected. A legitimate course of action for changing the fluids is given. The entire get together is kept in chamber.
Investigations
Assurance of Thermal conductivity of various fluids and to make a near report
Investigation of variety of warm conductivity of various fluids with temperature
Utilities Required
Water supply 5 lit/min (approx.)
Deplete.
Power Supply: I Phase, 220 V AC, 2 Amp.
Table for set-up help
The setup is intended to contemplate the warmth move in a stick blade. It comprises of stick write blade fitted in pipe. A fan is given on one side of pipe to lead tests under constrained draft conditions. Wind stream rates can be fluctuated with the assistance of damper gave in the conduit. A warmer warms one end of blade and warmth streams to another end. Warmth contribution to the radiator is given through Variac. Advanced Temperature Indicator measures temperature conveyance along the blade.
Trials
To contemplate temperature appropriation along the length of blade in both Free and constrained convection
Correlation of hypothetical temperature appropriation with tentatively acquired circulation
Utilities Required
Power Supply: 1 Phase, 220 V AC, 5 Amp.
Table for set-up help
The contraption comprises of Blower unit fitted with the test pipe. Nichrome wire warmer encompasses the test segment. Four Temperature Sensors are implanted on the test area, two put noticeable all around stream at the passageway and exit of the test segment to gauge the gulf and outlet air temperature. Test pipe is associated with the conveyance side of the blower alongside the Orifice to gauge stream of air through the pipe. Consistent warmth motion is given to pipe by an electric warmer through a variac and estimated by Digital Voltmeter and Digital Ammeter.
Trials
To decide normal surface warmth exchange coefficient for a pipe losing heat by constrained convection.
Examination of warmth exchange coefficient for various wind stream rates and warmth stream rates.
To plot surface temperature appropriation along the length of pipe
Utilities Required
Power Supply: 1 Phase, 220 V AC, 10Amp.
Floor region of 1.2mx 0.5m
The setup comprises of a metal tube fitted in a rectangular conduit in a vertical design. The channel is open at the best and base, and structures a nook and fills the need of undisturbed encompassing. One side of the conduit is fitted with a straightforward decent quality Acrylic window for representation. An electric warming component is kept in the vertical tube that in turns warms the tube surface. The warmth is lost from the tube to the encompassing air by characteristic convection. The temperature of the vertical tube is measure by Temperature Sensors and showed by a Digital Temperature Indicator with multi-channel switch. The warmth contribution to the radiator is estimated by a Digital Ammeter and a Digital Voltmeter and is differed by a variac. The tube surface is cleaned to limit the radiation misfortunes.
Investigation
To decide normal warmth exchange coefficient
Utilities Required
Power Supply: I Phase, 220 V AC, 2 Amp.
Table for set-up help
The present Set-up is intended to gauge the emissivity of test plate. The test plate involves a mica radiator sandwiched between two round plates. Dark plate is indistinguishable with test plate, yet its surface is darkened. As all the physical properties, measurement and temperature are equivalent; warm misfortunes from the two plates will be same aside from radiation misfortune. Thus the information distinction will be because of contrast in emissivity. The two plates are upheld on singular sections in a wooden walled in area with one side glass to guarantee consistent climatic conditions. Temperature Sensors are given to quantify the temperature of each plate and encompassing. Supply is given to radiators through independent variacs so temperatures of both can be kept equivalent and is estimated with Digital Voltmeter and Digital Ammeter.
Tests
Deciding the Emissivity of a test plate.
Concentrate the variety of emissivity of test plate regarding total temperature.
Utilities Required
Power Supply: 1Phase, 220 VAC, 4 Amp.
Table for set-up help