ENGINEERING PHYSICS - EXAMPLE 30.3 : (a) The quantum number m is given by m = -s, -s + 1. If s = 0.5, find the values of m. (b) | T > = (cos T) | V > + (sin T) | H >. The V and H states form a basis for all polarizations. Let cos T = 0.8. (i) If (sin T)(sin T) + (cos T)(cos T) = 1, find the value of sin T. (ii) For | T > = a | V > + b | H >, where a x a represents the probability of | V > and b x b represents the probability of | H >. Which one is more abundant, | V > or | H >? (iii) Find the value of T without using any mathematical tools.
- 1 Answers
- 1370 Views
- I also Faced
- E-Mail Answers
Answer Posted / kangchuentat
ENGINEERING PHYSICS - ANSWER 30.3 : (a) When s = 0.5, m = -s = -0.5 and m = -s + 1 = -0.5 + 1 = 0.5. (b)(i)(sin T)(sin T) = 1 - (cos T)(cos T) = 1 - 0.8 x 0.8 = 0.36. Then sin T = 0.6. (ii) Let a = cos T = 0.8, probability of | V > = a x a = 0.8 x 0.8 = 0.64 (more abundant) and b = sin T = 0.6, probability of | H > = b x b = 0.6 x 0.6 = 0.36 (less abundant). (iii) cos T = 0.8, then T = arc cos 0.8. The answer is given by Kang Chuen Tat; PO Box 6263, Dandenong, Victoria VIC 3175, Australia; SMS +61405421706; chuentat@hotmail.com; http://kangchuentat.wordpress.com.
| Is This Answer Correct ? | 0 Yes | 0 No |
Post New Answer View All Answers
Are there any methods of preventing cracking of carbon steel welds in refining environments?
What are some good uses of low-grade steam at 12 atm and 1920c?
What are the advantages and disadvantages of using gear pumps?
What are the merits of using a falling film evaporator?
Why do we apply on iron articles?
What are the different types of equipments for the conveyance of solids?
What are the steps required to design a vapor-liquid separator or flash drum?
Explain how can you quickly estimate the horsepower of a pump?
How can you determine the largest impeller that a pump can handle?
What is the import procurement cycle? What are the customization steps in sap?
How can we derive power factor equation p=vi cos phi?
How can you estimate a gas flow based on two pressure measurements?
Given, T1=600C, constant temperature of wall 800 , length of wit exchanger L=3m, dia=25 mm, Cp=14.91 KJ/kg.K, density ρ=914 kg/m3,mean velocity vm= 2 m/s, film heat transfer coefficient hf=72 Kcal/h.m2.K, what is the outlet temperature?
How can you prevent bridging in a dilute phase pneumatic conveying system?
We have some pieces of metals that have been 'powder coated', how does that work?
