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In a process for the manufacture of chlorine by direct oxidation of HCl with air over a catalyst to form C12 and H2O (only), the exit product is composed of HCI (4.4%), CZ (19.8%), 02 (4,0%), and N2 (52.0%). What was? a) The limiting reactant? b) The percent excess reactant? The degree of completion of the reaction? d) The extent of reaction

3. In incremental launching method of bridge construction, what are the measures adopted to enhance sufficient resistance of the superstructure during the launching process?


2. What is “preset” during installation of bridge bearings?


1. Under what situation shall engineers use jacking at one end only and from both ends in prestressing work?


If 8.5 moles of propylene(gas) reacts completely with hydrogen to form propane(liq). Determine the total heat of reaction(KJ) at 25 oC and 1 atm.


Methane reacts completely with oxygen to produce carbon dioxide(gas) and water(liq). What is the extent of reaction if 105 moles of water(liq) are produced?

Just write the final answer correct to 2 decimal places. Show all workings.

How will you prepare 10 ml of 0.025 M acetate buffer (pH 4.33) from stock solution of 0.05 M acetic acid
and 0.03 M sodium hydroxide ?

a) We are planning to operate a mixed flow reactor to convert A into R. This is a liquid phase reaction, with the stoichiometryA→R. The rate of reaction is given below. What size of mixed flow reactor is needed to achieve 75% conversion of a feed stream of 1000 moles of A per hour?

CA,mol/l. 0.1 0.2 0.3 04 0.5 0.6 0.7 0.8 1 1.3 2. -rA,mol/(l.min). 0.1 0.3 0.5 0.6 0.5 0.25 0.1 0.06 0.05 0.045 0.042

Solve this problem with step by step process?


At present the conversion is 66.7% for the elementary second order reaction 2A→2R when operating in an isothermal plug flow reactor with a recycle ratio of unity. Determine the conversion if recycle is shut off.

Solve this problem with step by step process?


Gaseous reactant A decomposes as per the following reaction stoichiometry and kineticsA→3R.-rA= 0.60CA mol/l min. Determine the conversion of A in a 50 % A +50% inerts fed at 180 l/min.(330mmol/min) to a 1000 liter mixed flow reactor.
Solve this problem with step by step process?
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