Answer / hari

"If A and C are each in thermal equilibrium with B, A is
also in thermal equilibrium with C."

Answer / anish

if two bodies are in thermal equilibrium with the third
body then the the two bodies are themselves said to be in
thermal equilibrium

Answer / dhaval modh

if A is in eqillibrium with B & B is in eqillibrium with C
Then A & C also in themally eqillibrium with each other.

Answer / sanjay kumar

"if two bodies A and B are in thermal equilibrium ,and if B is in eqilibrium with body C ,then A and C will also be in thermal equilibrium".

Answer / anurag kesharwani

I had read all answers ,which are all correct.I only want to add that
Actually, zeroth law is responsible for the concept of term temperature.

Answer / sudansu

i have studied the ans. but one thing if the three boby r
not in contact with each other (means A is in isolated
system then)

what is the hearth and arch pressure in furnace?

0 Answers   Essar, TATA,

What are flameless oxidizers?

0 Answers  

What is the process of including heat exchangers in ammonia refrigeration system?

0 Answers  

In DM plant, If pH in anion outlet is 7.2 and Mixed bed pH is 6.2, wat could be the reason.

8 Answers   Cipla, Jindal,

Explain what particle sizes are electrostatic precipitators used to remove?

0 Answers  

Question 56 - The kinetic behavior of an enzyme could be described using Michalis - Menten equation : Vo = Vmax [S] / (Km + [S]). Derive this equation from [ES] = [E]total [S] / (Km + [S]), Vmax = Kcat [E]total, Vo = Kcat [ES].

1 Answers  

What are the design considerations for a piping system for the transfer of slurries?

0 Answers  

What does the catalystic converter on an automobile really do?

0 Answers  

testing formula for oxygen by ammonium chloride,ammonium hydroxide and copper

0 Answers  

Are there flow velocity restrictions to avoid static charge build up in pipelines?

0 Answers  

Are there any methods of preventing cracking of carbon steel welds in refining environments?

0 Answers  

PROCESS DESIGN - EXAMPLE 21.1 : According to rules of thumb in chemical process design, consider the use of an expander for reducing the pressure of a gas when more than 20 horsepowers can be recovered. The theoretical adiabatic horsepower (THp) for expanding a gas could be estimated from the equation : THp = Q [ Ti / (8130a) ] [ 1 - (Po / Pi) ^ a ] where 3 ^ 3 is 3 power 3 or 27, Q is volumetric flowrate in standard cubic feet per minute, Ti is inlet temperature in degree Rankine, a = (k - 1) / k where k = Cp / Cv, Po and Pi are reference and systemic pressures respectively. (a) Assume Cp / Cv = 1.4, Po = 14.7 psia, (temperature in degree Rankine) = [ (temperature in degree Celsius) + 273.15 ] (9 / 5), nitrogen gas at Pi = 90 psia and 25 degree Celsius flowing at Q = 230 standard cubic feet per minute is to be vented to the atmosphere. According to rules of thumb, should an expander or a valve be used? (b) Find the outlet temperature To by using the equation To = Ti (Po / Pi) ^ a.

1 Answers