Question 107 - In N + 1 Rule in Quantum Chemistry, whenever a spin 1 / 2 nucleus is adjacent to N other nuclei, it is split into N + 1 distinct peaks. In 1 peak or singlet, there is only 1 magnitude. In 2 peaks or doublet, the ratio of magnitude of each peak is 1 : 1. In 3 peaks or triplet, the ratio of magnitude of each peak is 1 : 2 : 1. In 4 peaks or quartet, the ratio of magnitude of each peak is 1 : 3 : 3 : 1. In 5 peaks or quintet, the ratio of magnitude of each peak is 1 : 4 : 6 : 4 : 1. (a) By using binomial coefficients or Triangle of Pascal find the ratio of magnitude of each peak if 6 peaks exists. (b) How many adjacent nuclei are available in a spin 1 / 2 nucleus in such situation of 6 peaks?
Answer Posted / kangchuentat
Answer 107 - (a) 1 : 5 : 10 : 10 : 5 : 1, since (0 + 1) : (1 + 4) : (4 + 6) : (6 + 4) : (4 + 1) : (1 + 0) with reference to the ratio of magnitude of each peak in quintet. (b) Number of adjacent nuclei = Number of peaks - 1 = 6 - 1 = 5. 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
Explain how can you keep our seawater used for heat rejection clean before entering our heat exchangers?
Is it ever advantageous to use shells in series even though it may not be necessary?
What type of flow measurement devices is best for slurries?
What is the import procurement cycle?
What is cathodic protection, how it works in Turbine condensers ?
How can you estimate a gas flow based on two pressure measurements?
What is the angle of repose?
What is the practical particle size limit for pneumatic conveying?
What are the assumptions made on conservation equation?
What are some guidelines for designing for liquid and gas velocities in process plant piping?
Define a barometric condenser?
i m a frsh chemical engineer now i m confuse to attend the interview so anybody pls send model question papers to this christ_vivek33@yahoo.com
What is the most common cause of solid size segregation in bulk solid systems?
Define viscosity?
Explain what information is needed to specify a mixer?