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poizon [28]
3 years ago
15

Use Lagrange multiplier techniques to find the local extreme values of the given function subject to the stated constraint. If a

ppropriate, determine if the extrema are global. (If a local or global extreme value does not exist enter DNE.) f(x, y)

Engineering
1 answer:
Leno4ka [110]3 years ago
5 0

Answer:

Explanation:

Given f(x, y) = 5x + y + 2 and g(x, y) = xy = 1

The step by step calculation and appropriate substitution is clearly shown in the attached file.

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Agata [3.3K]

Since you have notified the company that they were out of compliance with MS licensing requirement, the next thing to do is to look or ask for the product key that is with the company

The other information would you need is for the company to obtain the product license by buying the product key.

<h3>Do you need a license for Microsoft?</h3>

If you get to buy any of the  standard Microsoft Office or other packages that is said to be the Home and Student edition, a person or firm will need a  license.

Note that the license is one that guarantee one the use of the product and its installation.

Therefore You need to purchase a lot of  copies of it and as such, Since you have notified the company that they were out of compliance with MS licensing requirement, the next thing to do is to look or ask for the product key that is with the company

The other information would you need is for the company to obtain the product license by buying the product key.

Learn more about MS licensing requirement from

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4 0
2 years ago
The water level in a tank is 20 m above the ground. A hose is connected to the bottom of the tank, and the nozzle at the end of
weeeeeb [17]

Answer:

P_{pump}= 68600Pa

Explanation:

We understand that the sum of the pressures in the tank and the pump is equal to that of the Nozzle,

In this way,

P_{tank} + P_{pump} = P_{nozzle}

For the pressure we also know that it is given by

P=\rho gh

\rho gh_1 + P_{pump} = \rho gh_2

So,

P_{pump} = \rho g(h2 - h1)

P_{pump}= 1000*9.8(27-20)

P_{pump}= 68600Pa

7 0
3 years ago
How can I start a new project on solar panels building?​
Alborosie

Answer:so you can start by thinking about it and creating ideas that work well with it

Explanation:

Try u can do it

3 0
4 years ago
An overhead 25m long, uninsulated industrial steam pipe of 100mm diameter is routed through a building whose walls and air are a
DedPeter [7]

Answer:

a) he rate of heat loss from the steam line is 18.413588 kW

b) the annual cost of heat loss from line is $12904.25

Explanation:

a)

first we find the area

A = πdL

d is the diameter (0.1m) and L is the length (25m)

so

A = π ×  0.1 × 25

A = 7.85 m²

Now rate of heat loss through convection

qconv = hA(Ts -Ta)

h is the convective heat transfer coefficient (10 W/m²K), Ts is surface temperature (150°), Ta is temperature of air (25°)

so we substitute

qconv = 10 W/m²K × 7.85 m² × ( 150° - 25°)

qconv = 9817.477 J/s

Now heat lost through radiation

qrad = ∈Aα ( Ts⁴ - Ta⁴)

∈ is the emissivity (0.8), α is the boltzmann constant ( 5.67×10⁻⁸m⁻²K⁻⁴ ),

first we shall covert our temperatures from Celsius to kelvin scale

Ts is surface temperature (150 + 273K ), Ta is temperature of air (25 + 273K)

so we substitute

qrad = 0.8 × 7.854 × 5.67×10⁻⁸ × ( (423)⁴ - (298)⁴ )

qrad = 3.5625×10⁻⁷ × 2.413×10¹⁰

qrad = 8596.112 J/s

Now to get the total rate of heat loss through convection and radiation, we say

q = qconv + qrad

q = 9817.477 + 8596.112

q = 18413.588 J/s ≈ 18.413588 kW

Therefore the rate of heat loss from the steam line is 18.413588 kW

b)

annual cost of heat lost rate

A = C × q/n × ( 3600 × 24 × 365 )

C is the cost of heat per MJ( $0.02/10⁶) n is broiler efficiency ( 0.9)

so we substitute

A = 0.02/10⁶  × 18413.588/0.9 × ( 3600 × 24 × 365 )

A = $12904.25

Therefore the annual cost of heat loss from line is $12904.25

4 0
3 years ago
Refrigerant-134a is to be cooled by water in a condenser. The refrigerant enters
KonstantinChe [14]

Answer:

Refrigerant R-134a is to be cooled by waterin a condenser.The refrigerant enters thecondenser with a mass flow rate of 6 kg/minat 1 MPa and 70 C and exits at 35 C. The cool-ing water enters at 300 kPa and 15 C andleaves at 25 C. Neglecting pressure drops,determine a) the required mass flow rate ofthe cooling water, and b) the heat transferrate from the refrigerant to the water.SolutionFirst consider the condenser as the control volume. The process is steady,adiabatic and no work is done. Thus over any time intervalΔt,ΔEΔt=0and thusXin˙E=Xout˙Ewhere˙E=˙m h+12V2+gz650:351 Thermodynamics·Prof. Doyle Knight37

Background image

I only know this

sorry for errors

4 0
3 years ago
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