The irreversible gas-phase reaction A +B → C + D is carried out in an isothermal packed bed reactor. The feed is equimolar, with CA0 = CB0 = 2 mol/L. The initial volumetric flow rate is 4 L/s. The reaction is first order with respect to A and first order with respect to B, and the rate constant is 0.01 L mol-1 s-1. The pressure drop parameter, α, is 0.0015 kg-1. Starting from the differential form of the design equation, what is the percent conversion of A, expressed to one decimal place. if 400 kg of catalyst are used in the reactor? Note that this problem may be solved either using a math solver (Matlab, Polymath, etc) or by hand. You are encouraged to try both methods.

the focus of lesson 1 is newton's first law of motion - sometimes referred to as the law of inertia. newton's first law of motion is often stated as. an object at rest stays at rest and an object in motion stays in motion with the same speed and in the same direction unless acted upon by an unbalanced force.

explanation:

we have been given a quadratic function and we need to restrict the domain such that it becomes a one to one function.

we know that vertex of this quadratic function occurs at (5,2).

further, we know that range of this function is .

if we restrict the domain of this function to either or , it will become one to one function.

let us know find its inverse.

upon interchanging x and y, we get:

let us now solve this function for y.

hence, the inverse function would be if we restrict the domain of original function to and the inverse function would be if we restrict the domain to .

you can cut your hand off if your not