Shell and Tube type Heat Exchanger

Introduction:

We have played an important part in the design, manufacture and installation for an important client located in Raipur, Madhya Pradesh. The requirement was for a  9.0 MVA Ferro Alloy Furnace for the reduction of the Exhaust Gases.

Our client had been facing the problem in the furnace because the Gas Cleaning Plant (GCP)had temperature reduction done by FD cooler, but the working efficiency was very poor and we at Clair proposed to assess the performance of the GCP.

On visiting the site, the basic type of application and product line was understood that is given in Table 1 while, the technical specifications are mentioned in Table 2.

There were many factors on which we proposed the following:-

  • Forced Draft Coolers are installed to cool the hot process gases to desired temperatures and filter the dusty gases in APC equipment
  • Forced Draft Coolers use Cooling air Fans to cool the hot process gases
  • Forced Draft Coolers, in general are shell & tube type, with hot dusty gases inside tubes & cooling air over the tubes
  • Cooling air fans can be either Axial or Centrifugal type depending on site space availability
  • Number of passes – Based on process parameters and target temperature gradients

Data/ Table:

Table 1: Basic Details collected during Visit

S.No

Particulars

Description

1.

Dust Details

Fine Particles generated during production of Ferro Alloy Mainly Oxides and Chlorides

2.

Product

FeMn /SiMn

3.

Fuel Used in the Furnace

Coal + Coke

Table 2: Technical Specifications Of Heat Exchanger

S.No

Description

Units

Value

1.

Gas volume at normal conditions

N.cu.m/hr

74,000

2.

Gas temperature at Heat Exchanger inlet

o C

250 – 280 (normal opg),

350 (peak for ½ hr)

3.

Gas inlet volume at operating temperature

cu.m/hr

1,40,000

4.

Gas temperature at Heat Exchanger outlet

o C

120 to 130

5.

Gas outlet volume at operating temperature        

cu.m/hr

1,07,800

6.

Dust concentration in gases   

gms/cu.m

5

7.

Number of passes for flue gas

Nos.

1

8.

Tube diameter and length

mm ¯X mm lg.

108 OD X 10460

9.

Total number of tubes            

Nos.

280

10.

Total heat transfer area          

sq.m

956

12.

Tube material

Not Applicable

MS ERW

13.

Pressure drop across the Heat Exchanger

mm WC

40

14.

Cooling air volume                 

cu.m/hr

2,00,000

15.

Cooling air inlet temperature

o C

35

16.

Number of cool air fans

Nos.

4

17.

Capacity of cool air fans                                

cu.m/hr

50,000 @ 75 mm WC

18.

Motor capacities of cool air fans

HP

30

19.

Total weight of Heat Exchanger with tubes

MT

60 approx.

Observations:

Clair took up the challenge and following solution was proposed and implemented:

  • The provided FD Cooler is Air to Air FD Cooler with 3 No. passes installed in series arrangement
  • Since the Air to Air heat transfer is very low compared to any other heat exchange, the care has been taken to select appropriate overall heat transfer coefficient
  • Since the flue gases contain the dust, the probable dust coating on tubes is also considered in deciding the heat transfer area required
  • The tube diameter selected is 135.7 mm ID considering the dust concentration of flue gases and the large diameters avoids the problem of choking of the tubes
  • The gas velocities inside the tubes has been considered taking into account the abrasive nature of the dust
  • Three pass FD Cooler is designed for efficient cooling of the gases
  • Gas flow in tubes in every pass with appropriate velocities to avoid dust deposition in the tubes
  • Top entry for the first pass is designed for uniform gas distribution in the tubes
  • Tubes are arranged in triangular pitch for better contact between cool air and tubes
  • Axial fans are selected as cool air fans for better heat transfer
  • Hoppers are provided for each pass. The dust from the hoppers is continuously transported via dust disposal system with Knife edge gate valve, dome valves & conveying system of Mecgale make

Clair successfully implemented and commissioned the installation of NewShell and Tube type Heat Exchanger in 2018with  emissions of 80,000 Nm3/Hr at 280oC.

Pictures:

Figure 1: Our HE installation for the site location
Figure 2: The tube arrangement for the HE at site.

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