## What is NTU method?

NTU (Number of transfer units) gives the heat transfer capacity of the heat exchanger. In the NTU method, the effectiveness of the heat exchanger is expressed in the form of three non-dimensional terms.

The NTU method is useful when minimum data is provided for calculating heat transfer.

**In this article, we’re going to discuss:**

- NTU method formula:
- NTU special cases:
- Effectiveness:
- Numerical on NTU method:

## NTU method formula:

The method has different effectiveness formulae for parallel flow and counterflow heat exchangers.

**1) For parallel-flow heat exchanger:**

The effectiveness of The parallel-flow heat exchanger is given by,

`\varepsilon _{PARALLEL}`=`\frac{1-exp[-NTU(1+R)]}{1+R}`

Where,

R (specific heat ratio) = `\frac{C_{min}}{C_{max}}`

Where Cmin is the minimum between Cc and Ch while the Cmax is the maximum between the same.

Where,

`C_{c}=\dot{m}C_{pc}`

`C_{h}=\dot{m}C_{ph}`

And, NTU = `\frac{UA}{C_{min}}`

Where U = Overall heat transfer coefficient

A = Area of the heat exchanger.

**2) For counter-flow heat exchanger:**

The effectiveness of the counterflow heat exchanger is given by,

`\varepsilon _{counter}`=`\frac{1-exp[-NTU(1+R)]}{1-R[-NTU(1-R)]}`

Where, R = `\frac{C_{min}}{C_{max}}`

and, NTU = `\frac{C_{UA}}{C_{min}}`

## NTU special cases:

**Case 1] For condenser and evaporators:**

For evaporating and condensing liquid the value of specific heat is considered as infinity.

Therefore, Cmax= ∞

∴ R = `\frac{C_{min}}{C_{max}}=\frac{C_{min}}{\infty}` =0

For R=0, the effectiveness is given by,

`\varepsilon = 1-exp(-NTU)`

**Case 2] For regenators:**

For regenerators the specific heat of both fluid is same

`\therefore R=\frac{C_{min}}{C_{max}}=1`

∴ a] For parallel flow heat exchanger:-

`\varepsilon _{PARALLEL}`=`\frac{1-exp(-2NTU)}{2}`

b] For counter flow heat exchanger:-

`\varepsilon _{counter}=\frac{NTU}{1+NTU}`

## Effectiveness:

The effectiveness of the heat exchanger is in the ratio of actual heat transfer to the maximum heat transfer.

`\therefore \varepsilon =\frac{Q_{actual}}{Q_{max}}`

## Numerical on NTU method:

*Hot process fluid with cp = 2.6 Kj/Kg.°C enters in a parallel-flow heat exchanger at 100 °C at a mass flow rate of 25000 Kg/hr while the cooling water with cp = 4.2 Kj/Kg.°C enters into the heat exchanger at 10°C at a mass flow rate of 45000 Kg/hr. The heat exchanger has a heat transfer area of 11 m² with an overall heat transfer coefficient equal to 1000 W/m².°C.Find,*

*1] Hot fluid outlet temperature*

2]Cold fluid outlet temperature

2]Cold fluid outlet temperature

**Solution:-**

Given:-

Cph = 2.6 KJ/Kg °C

Thi = 100 °C

`\dot{m}_{h}` = 25000 Kg/hr

Cpc = 4.2 KJ/Kg °C

Tci = 10 °C

`\dot{m}_{c}` = 45000 Kg/hr

A = 11 m²

U = 1000 W/m² °C

**Step-1) Find Cmin, Cmax:-**

Ch = `\dot{m}_{h}` Cph = 25000 x 2.5 = 62500 KJ/hr °C

Cc = `\dot{m}_{c}` Cpc = 45000 x 4.2 = 189000 KJ/hr °C

∴ Cmax = Cc = 189000 KJ/hr °C and

Cmin = Ch = 62500 KJ/hr °C

**Step-2) Find R & NTU:-**

R = `\frac{C_{min}}{C_{max}}` =`\frac{62500}{189000}`= 0.3306

NTU = `\frac{UA}{C_{min}}`=`\frac{1000\times 11}{62500}`=0.176

NTU = 0.176

**Step-3) Find effectiveness (ε)**:-

For parallelflow heat exchanger,

`\epsilon_{PARALLEL}`=`\frac{1-exp[-NTU(1+R)]}{1+R}`

`\epsilon_{PARALLEL}`=`\frac{1-exp[-0.176(1+0.3306)]}{1+0.3306}`

`\epsilon_{PARALLEL}`= 0.1569

**Step-** **5) Exit temperature of hot fluid:-**

By formula of effectiveness,

`\epsilon=\frac{C_{h}(T_{hi}-T_{ho})}{C_{min}(T_{hi}-T_{ci})} `

`0.1569=\frac{62500(100-T_{ho})}{62500(100-10)}`

`T_{ho}`= 85.879 °C —**Answer 1]**

This is the exit temperature of the hot fluid.

**Step-6) Exit temperature of cold fluid:-**

By using the formula of effectiveness,

`\epsilon=\frac{C_{c}(T_{co}-T_{ci})}{C_{min}(T_{hi}-T_{ci})}`

`0.1569=\frac{189000(T_{co}-10)}{62500(100-10)}`

`T_{co}`= 14.66 °C —**Answer 2]**

This is the exit temperature of the cold fluid.

Thanks pratik it’s easy to understand 🙌