double pipe heat exchanger design equations

Double Pipe Heat Exchanger Design By knowing some specifications of double pipe heat exchangers and your demands design can be done by simple heat transfer equation as below. L 273π x 0025 348 m.


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Example 4 Steam required to heat soup in jacketed pan Estimate the steam requirement as you start to heat 50 kgof soup in a jacketed pan if the initial temperature of the soup is 18Cand the steam used is at 100 kPa gauge.

. 47 Without loss of generality the viscosity correction factor in the Sieder and Tate correlation in eq 46 has also been omitted ie theratiobetweenbulkandwallviscositieswereconsideredequal to 1. Double pipe heat exchanger design equations Written By leebolon50108 Saturday April 30 2022 Add Comment Edit. Calculate the heat transfer area of the double pipe heat exchanger in the lab.

The Simplest Heat Exchanger. The experiment system has two cycles hot water cycle and cold water cycle. Morrison Michigan Tech U.

The schematic of the experiment system is shown in Fig. Flow Heat Capacity C mc eg C mc p H pH13 Minimum Heat Capacity Cmin the smaller of CHand CC Maximum Heat Capacity Cmax the larger of CHand CC Heat Capacity Ratio 0 C 1 C C C R max min R 14 Effectiveness C T - T C T - T. The equation to be used is shown below for both the hot fluid and the cold fluid.

Double Pipe Heat Exchangers are also known as Hairpin Heat Exchangers. Double Pipe Heat Exchanger Design. Exchanger pipe inside another for either counter current flo w or parallel flow.

316L SST Hastelloy Inconel Titanium etc. Φ Φ fo o fin root finR h A A R 11 25 where Φis the fin efficiency and is given by. Heat exchanger calculations and modeling to get the output.

Calculate the rotameter setting for the desired water-side flow rate. Compare this length with the assumed length if considerable difference is there use this length and repeat above steps till there is no change in length calculated. In this paper the optimal design of the exchanger has been formulated as a geometric programming with a single degree of difficulty.

Retain extra sig figs since this is an intermediate calculation. Dodr m 3 1 1 2 Φ26 where R kY h m H fow o 1 2 27 Also d LNs s Y s Aroot drLΠrf Π28 and Afindo drLNf 22 4 2 π 29. 46 Nut Ret Prt Nuttheo ST.

In order to study the heat transfer heat transfer coefficient and pressure drop on large tube side for transient flow in a double pipe heat exchanger a fully instrumented experimental setup is developed. Determination of the heat transfer surface area needed for a double pipe heat exchanger design can be done using the basic heat exchanger equation. It is one heat.

Q m H C pH T Hin T Hout m C C pC T Cout T Cin where m H is the mass flow rate of the hot fluid in slugshr kghr for SI. Balance on the inside system 2. ST 13 ST.

From Equations 74 75 78 79 and 710 the hydraulic diameter for the Reynolds number and the pressure drop is and the equivalent diameter based on heat transfer For a double-pipe heat exchanger of length L the unfinned bare and finned areas are respectively 28. K t. Define process requirements for the new exchanger.

Ad Standard Custom. A double-pipe helical heat exchanger was numerically modeled for laminar fluid flow and heat transfer characteristics under different fluid flow rates. Double Pipe Heat Exchanger Design consists of one pipe placed inside another pipe of a larger diameter with appropriate fittings to guide the flow from section to another.

In heat exchanger design there is a trade off between the cost of the heat exchanger which is a function of the heat transfer area and of. The total heat transfer area to be provided is around 6159 m 2 which suggests that double pipe exchangers would be the best type of heat exchanger equipment for the process. The fact that the optimal weight w 1 is greater than w 2 tells that the heat transfer.

Thermal conductivity of tube material. The pan has a heating surface of 1 m2. Define design parameters such as - number of tube passes tube size shell ID etc.

Q is the rate of heat transfer between the two fluids in the heat exchanger in Btuhr U is the overall heat transfer coefficient in BTUhr-ft2-oF. DoublePipe Heat exchanger counter current Faith A. The heat exchanger design equation Q U A ΔTlm can be used to determine the required heat transfer area A for a heat exchanger.

Select a suitable type of shell and tube exchanger. Double pipe heat exchanger design as contained in this technical paper is very s traight forward. T1 T2 T1 T2 cold less cold less hot hot Inside System Outside System 𝑸 𝑄 Ü á L𝑸 L F𝑄 Ü á 𝑚 𝑚 𝑚 𝑚 𝑇 5 𝑇 6 𝑇 5 ñ 𝑇 6 ñ Another way of looking at it.

Area Q U LMTD L Area π Do. Salient pointsThe outer diameter of the heat exchanger is around 18 times the inner diameter. Although the necessary equations for heat transfer and the pressure drop in a double pipe heat exchanger are available using these equations the optimization of the system cost is laborious.

Shell and tube heat exchanger design is an iterative process which goes through the following steps. Calculate Area and length of double pipe exchanger as following. One fluid flows through the inside tube while the other fluid flows through the annular passage.

C pH is the specific heat of the hot fluid in Btuslug- o F kJkg-K for SI. The fluid flows in the inner pipe is the tube side and in exchange another fluid flows in the outer pipe annulus. Write in your lab notebook.

Q UA ΔTlm where. 7 rows Outer Pipe Pipe Size inch 05 075 1 15 2 3 4 6 8 10 12 14 16 18 20 24 26 28 30 32 34 36 38. Base your calculation on the outside area of the inside pipe.


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