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             \author[1]{Bhupinder Singh  Gill}

             \affil[1]{  Manav Rachna International Institute of Research and Studies, Faridabad, India}

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\date{\small \em Received: 16 December 2019 Accepted: 2 January 2020 Published: 15 January 2020}

\maketitle


\begin{abstract}
        


The compressible flow analysis is traditionally done by referring to tables where various ratios are listed for various values of Mach number M. Here a different approach is presented which does not require any reference to any tables and the problems can be solved much more comprehensibly and which gives more accurate values.

\end{abstract}


\keywords{}

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\let\tabcellsep& 	 	 		 
\section[{Introduction}]{Introduction}\par
n aerodynamics the air flows over (aircraft wing) or inside (pipes and nozzles) solid bodies. Low speed flows are usually treated as 'incompressible', that is, changes in density of air as it flows are ignored (density is assumed constant). However, that is only an assumption and not a reality; in fact Anderson 1 calls it a myth. The analysis of flows as incompressible will always be in error, howsoever small, but the results may be in error by a small amount which may be acceptable in practical life. It would be preferable if the analysis can be carried out as compressible flow provided the mathematics is not too involved. That is an aim of this communication. 
\section[{II.}]{II.} 
\section[{Analysis of Normal Shock Wave}]{Analysis of Normal Shock Wave}\par
Fig,  {\ref 1} shows the sketch of a normal shock wave. V 1 , P 1 , T 1 and ? 1 are the velocity, pressure, temperature and density of air just before the shock The parameters are related to each other by the following equations:Continuity: ? 1 .V 1 = ? 2 .V 2\par
(1)Momentum: P 1 + ? 1 .V 1 2 = P 2 + ? 2 .V 2 2\par
(2)\par
Gas law: P 1 = ? 1 .R.T 1 and P 2 = ? 2 .R.T 2 (3)\par
Where R is the gas constant. R = 287 J/kg.K for air. Energy equation:\par
(4)\par
Dividing eqn 2 by eqn 1:\par
(5)\par
Using gas law (eqn.3), eqn 5 can be simplified to: With V 2 known, T 2 can be calculated from eqn 7. Eqn 5 can be simplified with the help of eqn 1:\par
(10) III. 
\section[{Solution of Equations}]{Solution of Equations} 
\section[{I}]{I}\par
.\par
(India). e-mail: bsgill.fet@mriu.edu.in V 2 can be determined from eqn 9. It is, however, not easy to solve the equation. The 'goal seek' facility of spreadsheet (like Excel of Microsoft Office) is used for this purpose. Once V 2 is known, temperature, pressure and density downstream of the shockwave are easily calculated. Downstream pressure P 2 can be calculated from eqn 10. Downstream density ? 2 can be calculated from eqn 3 as all parameters are known. wave. V 2 , P 2 , T 2 and ? 2 are the parameters just after the shock wave.\par
It may be noted that V 2 can be determined from It can thus be seen that it is not necessary to read Mach number from any table for solving the normal shock wave problem. The sonic velocity and Mach number at both upstream and downstream regions of the shock wave can be easily calculated. Procedure for arriving at the solutions is described below.\par
In this example V 1 = 680 m/s which means the flow is supersonic before the shock wave. The flow will then be subsonic after the shock wave. This means there will be two solutions of the equations: one where there is no shock and the second where a shock wave occurs. To arrive at the first solution (case 1), assume an arbitrary value of V 2 greater than 680 m/s, say 800 m/s. In this case LHS is 1. 403 (cell C15). Click on Data and then What-if Analysis in the spreadsheet. Then select Goal Seek. In Set Cell enter C15, the cell that contains value of LHS. In 'To value' enter 2.251, the value of RHS in cell C11. In 'By changing cell' enter C14, the cell that contains the value of V 2 . Click OK. The cell C14 will now show value close to 680 which is the same as value of V 1 . This means that no shock has occurred in this case. This shows that the Excel has been properly filled. Click OK. The values of T 2 , P 2 , ? 2 , c 2 , M 2 and P0 2 in cells C19, C20, C22, C24, C26 and C28 respectively will automatically update.\par
If a shock has occurred then, downstream of the shock wave, the velocity will be subsonic. Refer to values in column D (case 2). Enter a small value, say 50, in cell D1. Values in subsequent cells will change. Use Data-What if analysis-Goal Seek as before and enter D15 in Set Cell, 2.251 in 'To Value' and D14 in 'By changing cell' and click OK. The value of V 2 in cell D14 is now 255.139 m/s. The values of T 2 , P 2 , ? 2 , c 2 , M 2 and P0 2 are automatically updated. It can be noted that P 2 = 4.495 atm and M 2 = 0.578. A complete solution of the problem is thus in the Spreadsheet.\par
It can be observed that there was no need to read Mach number value from charts; the problem could be easily solved in a normal mathematical fashion. However, if desired values of sonic velocity and mach number before and after the shock could be easily calculated as shown in Table \hyperref[tab_0]{1}. Even total pressure values upstream and downstream of the normal shock could be calculated. 
\section[{IV.}]{IV.} 
\section[{Pitot Tube Analysis}]{Pitot Tube Analysis}\par
Pitot static tubes are used to measure flow velocities. There are three cases, viz. incompressible subsonic, compressible subsonic and compressible supersonic. These cases are analyzed below. 
\section[{a) Incompressible subsonic flow}]{a) Incompressible subsonic flow}\par
The instrument used to measure velocity of fluid at any location is called Pitot-static tube. The Pitot has two openings, one which faces opposite to the flow direction and another which is perpendicular to the flow direction. The former measures the total or stagnation pressure at the location of the Pitot tube and the latter measures the static pressure. No flow takes place through any of these two openings. The stagnation pressure represents a sum of the static pressure and the dynamic pressure. The difference between the stagnation pressure and the static pressure is measured by appropriate means. Bernoulli's equation is applied to the two readings. The stagnation pressure P0 is related to the static pressure P1 by the equation:   
\section[{b) Compressible subsonic flow}]{b) Compressible subsonic flow}\par
The Pitot tube can also be used to determine flow velocity in high speed but subsonic flow. The formula for velocity V1 in a compressible subsonic flow is:\par
For the case with P0 = 1104326 Pa, P1 = 101325 Pa, ? = 1.4 and ? = 1.225 kg/m3, V 1 = 69.61 m/s. It may be noted that the difference between incompressible velocity and compressible velocity is hardly 0.39 m/s or 0.56\%.\par
In case P 0 = 140000 Pa, the incompressible velocity will be 251.28 m/s whereas compressible velocity will be 236.63 m/s. The difference is 14.65 m/s or 6.19\% which may be difficult to ignore. 
\section[{c) Supersonic flow}]{c) Supersonic flow}\par
When a Pitot tube is used to measure flow velocity in supersonic flow, it acts as an obstruction to the flow and velocity is brought down to zero in front of it. But transition from supersonic flow to subsonic flow means a shock has occurred somewhere on the way. It is apparent that the Pitot tube will measure total pressure behind the shock; hence it is necessary to determine relationship between dynamic or total pressure behind the shock and flow velocity before the shock. Table  {\ref 2} shows the calculation.\par
Column C gives data for a random case in supersonic flow. In the case shown, flow velocity of 350 m/s (cell C7) will give rise to Pitot tube reading of 198845 Pa (cell C26). Consider a Pitot tube reading of 275000 Pa for which we need to determine flow velocity. A two or three step iteration will be needed.A B C D E F 1 2 Table 2: Supersonic Pitot Tube 3\par
Step 1\par
Step 2\par
Step   {\ref 2} depicts values that one will see in column C). The value in column C26 will now read 280029 which is somewhat different from the desired value of 275000. Repeat the iteration and we get the value of 274774 in cell C26 (as depicted in cell E26 in Table  {\ref 2}). One more iteration gives value of 275000 (the desired figure) in cell C26 and the corresponding figure of velocity V 1 (441.5 m/s) in cell C7 (as depicted in cell F7 in Table  {\ref 2}). Thus a reading Pa (equivalent to 2.714 atm) corresponds to V 1 = 441.5 m/s. Sonic velocity upstream shock is calculated as 339.6 m/s and downstream of shock as 370.6 m/s. Mach numbers upstream and downstream of shock are 1.300 and 0.786 respectively.\par
Another example is shown in Table \hyperref[tab_3]{3}. It can be seen that Pitot tube reading of 1221980 Pa (12.06 atm) represents a velocity upstream of shock as 1018.7 m/s. Sonic velocity upstream of shock is calculated as 339.6 m/s and downstream of shock as 555.8 m/s. Mach numbers upstream and downstream of shock are 3.0 and 0.475 respectively. Complete information about the example like downstream velocity, pressure, temperature and density is available in the spreadsheet. There never was a need to refer to any tables.  V.A B C D E F 1 
\section[{Flow Through Nozzles}]{Flow Through Nozzles}\par
The spreadsheet solution of compressible flow  
\section[{Continuity equation: ?}]{Continuity equation: ?}1 A 1 V 1 = ? 2 A 2 V 2 or ? 1 /? 2 ) = (A 2 /A 1 ) (V 2 /V 1 ) (A 1\par
and A 2 are cross sectional areas of two locations in the nozzle and V 1 and V 2 are velocities at these locations respectively. Location 2 could be anywhere in the nozzle between inlet and exit). 
\section[{From equation of state:}]{From equation of state:}\par
Steady state energy equation (neglecting potential energy):\par
Or where Z = 2?R/ (?-1) =2009 for air.\par
For isentropic flow: 
\section[{Or}]{Or}\par
From equations 1, 2 and 3, Velocity V 2 at the downstream location can be calculated from value of A 2 since all other information pertains to upstream and is known.  Pressure P 2 at the downstream location can be calculated from eqn (17) and temperature T 2 can be calculated from eqn (15). All the information is available to determine the density at the downstream location. Table \hyperref[tab_4]{4} is a sample of the nozzle flow analysis. It may be noted that column C is for parameters at the first section and column D is for second section where areas A 1 = 0.00785 sq m and A 2 = 0.00385 sq m. Also this table represents data for the subsonic solution of the problem. A second solution exists for the supersonic section of the problem. To arrive at the supersonic section of the solution, give a large value (say 1000) of V 2 (row 14) as the initial guess of V 2 and solve the problem through 'What-if-Analysis'. 
\section[{VI.}]{VI.} 
\section[{Conclusion}]{Conclusion}\par
It is shown that compressible flow can be analyzed without going through the step of referring to pre-calculated tables. Use of spreadsheet makes it possible. In general, the reading of Mach number M may lie between two values and interpolation is required; interpolated value could be in error. Also the complete problem is solved in one step, i.e. all parameters are determined in one step.\begin{figure}[htbp]
\noindent\textbf{}\includegraphics[]{image-2.png}
\caption{\label{fig_0}}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{}\includegraphics[]{image-3.png}
\caption{\label{fig_1}}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{2}\includegraphics[]{image-4.png}
\caption{\label{fig_2}Fig. 2 :}\end{figure}
  \begin{figure}[htbp]
\noindent\textbf{1} \par 
\begin{longtable}{P{0.11691449814126394\textwidth}P{0.22750929368029738\textwidth}P{0.27806691449814125\textwidth}P{0.22750929368029738\textwidth}}
\tabcellsep \multicolumn{3}{l}{gives one example of solution of a}\\
\multicolumn{3}{l}{normal shock wave problem.}\tabcellsep \\
A\tabcellsep B\tabcellsep C\tabcellsep D\\
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2\tabcellsep \tabcellsep Case 1\tabcellsep Case 2\\
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6\tabcellsep T1, K\tabcellsep 288\tabcellsep 288\\
7\tabcellsep P1,Pa\tabcellsep 101320\tabcellsep 101320\\
8\tabcellsep P1,atm\tabcellsep 1\tabcellsep 1\\
9\tabcellsep Ro1, kg/m3\tabcellsep 1.226\tabcellsep 1.226\\
10\tabcellsep Z\tabcellsep 2009.000\tabcellsep 2009.000\\
11\tabcellsep RHS\tabcellsep 2.251\tabcellsep 2.251\\
12\tabcellsep a\tabcellsep -6.000\tabcellsep -6.000\\
13\tabcellsep b\tabcellsep \multicolumn{2}{l}{0.012134236 0.012134236}\\
14\tabcellsep V2\tabcellsep 680.042\tabcellsep 255.139\\
15\tabcellsep LHS\tabcellsep 2.251\tabcellsep 2.251\\
16\tabcellsep c\tabcellsep 288.018\tabcellsep 108.059\\
17\tabcellsep d\tabcellsep 1611.351\tabcellsep 226.816\\
18\tabcellsep e\tabcellsep 1611.250\tabcellsep 604.512\\
19\tabcellsep T2, K\tabcellsep 287.917\tabcellsep 485.755\\
20\tabcellsep P2, Pa\tabcellsep 101284.592\tabcellsep 455460.903\\
21\tabcellsep P2, atm\tabcellsep 1.000\tabcellsep 4.495\\
22\tabcellsep Ro2, kg/m3\tabcellsep 1.226\tabcellsep 3.267\\
23\tabcellsep c1\tabcellsep 340.174\tabcellsep 340.174\\
24\tabcellsep c2\tabcellsep 340.125\tabcellsep 441.788\\
25\tabcellsep M1\tabcellsep 1.999\tabcellsep 1.999\\
26\tabcellsep M2\tabcellsep 1.999\tabcellsep 0.578\\
27\tabcellsep P01, atm\tabcellsep 3.797\tabcellsep 3.797\\
28\tabcellsep P02, atm\tabcellsep 3.797\tabcellsep 5.545\end{longtable} \par
 
\caption{\label{tab_0}Table 1}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{1} \par 
\begin{longtable}{P{0.85\textwidth}}
( ) Volume Xx X Issue I V ersion I D\\
of Researches in Engineering\\
Global Journal\end{longtable} \par
 
\caption{\label{tab_1}Table 1}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{} \par 
\begin{longtable}{P{0.09770114942528735\textwidth}P{0.05536398467432949\textwidth}P{0.16446360153256703\textwidth}P{0.13759578544061302\textwidth}P{0.1310823754789272\textwidth}P{0.1310823754789272\textwidth}P{0.13271072796934866\textwidth}}
\tabcellsep \tabcellsep \multicolumn{4}{l}{Compressible Flow Analysis through Spreadsheet}\tabcellsep \\
\multicolumn{2}{l}{Under Data-}\tabcellsep \tabcellsep (13)\tabcellsep \tabcellsep \tabcellsep \\
\tabcellsep \tabcellsep \tabcellsep (14)\tabcellsep \tabcellsep \tabcellsep \\
Year 2020\tabcellsep \tabcellsep \tabcellsep \tabcellsep \tabcellsep \tabcellsep \\
( ) Volume Xx X Issue I V ersion I D\tabcellsep 4 5 6 7 8 9\tabcellsep cp, J/kg.K ? R, J/kg.K V1, m/s T1, K P1,Pa\tabcellsep 1004.5 1.4 287 350.0 287 101320\tabcellsep 1004.5 1.4 287 446.8 287 101320\tabcellsep 1004.5 1.4 287 441.3 287 101320\tabcellsep 3 1004.5 1.4 287 441.5 287 101320\\
of Researches in Engineering\tabcellsep 10 11 12 13 14 15 16 17 18 19\tabcellsep P1,atm Ro1, kg/m3 Z RHS a b V2, m/s LHS c d\tabcellsep 1 1.230 2009 5.707 -6.000 0.033448 332.9 5.707 272.959 386.088\tabcellsep 1 1.230 2009 3.889 -6.000 0.022135 289.7 3.890 186.133 292.512\tabcellsep 1 1.230 2009 3.961 -6.000 0.022572 291.4 3.961 189.493 295.794\tabcellsep 1 1.230 2009 3.958 -6.000 0.022552 291.4 3.958 189.387 295.794\\
Global Journal\tabcellsep 20 21 22 23 24\tabcellsep e T2, K P2, Pa P2, atm Ro2, kg/m3\tabcellsep 405.948 292.8 108692 1.073 1.293\tabcellsep 451.028 344.6 187607 1.852 1.897\tabcellsep 448.000 341.7 182703 1.803 1.863\tabcellsep 448.252 341.8 182884 1.805 1.864\\
\tabcellsep 25\tabcellsep T02, K\tabcellsep 348.0\tabcellsep 386.4\tabcellsep 384.0\tabcellsep 384.1\\
\tabcellsep 26\tabcellsep P02, Pa\tabcellsep 198845\tabcellsep 280029\tabcellsep 274774\tabcellsep 275000\\
\tabcellsep 27\tabcellsep P02,atm\tabcellsep 1.962\tabcellsep 2.764\tabcellsep 2.712\tabcellsep 2.714\\
\tabcellsep 28\tabcellsep c1, m/s\tabcellsep 339.6\tabcellsep 339.6\tabcellsep 339.6\tabcellsep 339.6\\
\tabcellsep 29\tabcellsep c2, m/s\tabcellsep 343.0\tabcellsep 372.1\tabcellsep 370.5\tabcellsep 370.6\\
\tabcellsep 30\tabcellsep M1\tabcellsep 1.031\tabcellsep 1.316\tabcellsep 1.300\tabcellsep 1.300\\
\tabcellsep 31\tabcellsep M2\tabcellsep 0.970\tabcellsep 0.779\tabcellsep 0.786\tabcellsep 0.786\\
© 2020 Global Journals\tabcellsep \tabcellsep \tabcellsep \tabcellsep \tabcellsep \tabcellsep \end{longtable} \par
 
\caption{\label{tab_2}}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{3} \par 
\begin{longtable}{P{0.053593947036569986\textwidth}P{0.14791929382093316\textwidth}P{0.18221941992433796\textwidth}P{0.15542244640605296\textwidth}P{0.15542244640605296\textwidth}P{0.15542244640605296\textwidth}}
2\tabcellsep \tabcellsep \tabcellsep Step 1\tabcellsep Step 2\tabcellsep Step 3\\
3\tabcellsep cp, J/kg.K\tabcellsep 1004.5\tabcellsep 1004.5\tabcellsep 1004.5\tabcellsep 1004.5\\
4\tabcellsep ?\tabcellsep 1.4\tabcellsep 1.4\tabcellsep 1.4\tabcellsep 1.4\\
5\tabcellsep R, J/kg.K\tabcellsep 287\tabcellsep 287\tabcellsep 287\tabcellsep 287\\
6\tabcellsep V1, m/s\tabcellsep 350.0\tabcellsep 1034.3\tabcellsep 1019.0\tabcellsep 1018.7\\
7\tabcellsep T1, K\tabcellsep 287\tabcellsep 287\tabcellsep 287\tabcellsep 287\\
8\tabcellsep P1,Pa\tabcellsep 101320\tabcellsep 101320\tabcellsep 101320\tabcellsep 101320\\
9\tabcellsep P1,atm\tabcellsep 1\tabcellsep 1\tabcellsep 1\tabcellsep 1\\
10\tabcellsep Ro1, kg/m3\tabcellsep 1.230\tabcellsep 1.230\tabcellsep 1.230\tabcellsep 1.230\\
11\tabcellsep Z\tabcellsep 2009\tabcellsep 2009\tabcellsep 2009\tabcellsep 2009\\
12\tabcellsep RHS\tabcellsep 5.707\tabcellsep 1.539\tabcellsep 1.555\tabcellsep 1.556\\
13\tabcellsep a\tabcellsep -6.000\tabcellsep -6.000\tabcellsep -6.000\tabcellsep -6.000\\
14\tabcellsep b\tabcellsep \multicolumn{4}{l}{0.033448 0.007289 0.007414 0.007417}\\
15\tabcellsep V2, m/s\tabcellsep 332.9\tabcellsep 265.4\tabcellsep 264.1\tabcellsep 264.1\\
16\tabcellsep LHS\tabcellsep 5.707\tabcellsep 1.540\tabcellsep 1.555\tabcellsep 1.555\\
17\tabcellsep c\tabcellsep 272.959\tabcellsep 73.649\tabcellsep 74.377\tabcellsep 74.400\\
18\tabcellsep d\tabcellsep 386.088\tabcellsep 245.443\tabcellsep 243.002\tabcellsep 243.002\\
19\tabcellsep e\tabcellsep 405.948\tabcellsep 956.451\tabcellsep 937.674\tabcellsep 937.393\\
20\tabcellsep T2, K\tabcellsep 292.8\tabcellsep 784.7\tabcellsep 769.0\tabcellsep 768.8\\
21\tabcellsep P2, Pa\tabcellsep 108692\tabcellsep 1079458\tabcellsep 1047631\tabcellsep 1046964\\
22\tabcellsep P2, atm\tabcellsep 1.073\tabcellsep 10.654\tabcellsep 10.340\tabcellsep 10.333\\
23\tabcellsep Ro2, kg/m3\tabcellsep 1.293\tabcellsep 4.793\tabcellsep 4.746\tabcellsep 4.745\\
24\tabcellsep T02, K\tabcellsep 348.0\tabcellsep 819.7\tabcellsep 803.8\tabcellsep 803.5\\
25\tabcellsep P02, Pa\tabcellsep 198845\tabcellsep 1257929\tabcellsep 1222696\tabcellsep 1221980\\
26\tabcellsep P02,atm\tabcellsep 1.962\tabcellsep 12.415\tabcellsep 12.067\tabcellsep 12.060\\
27\tabcellsep c1, m/s\tabcellsep 339.6\tabcellsep 339.6\tabcellsep 339.6\tabcellsep 339.6\\
28\tabcellsep c2, m/s\tabcellsep 343.0\tabcellsep 561.5\tabcellsep 555.9\tabcellsep 555.8\\
29\tabcellsep M1\tabcellsep 1.031\tabcellsep 3.046\tabcellsep 3.001\tabcellsep 3.000\\
30\tabcellsep M2\tabcellsep 0.970\tabcellsep 0.473\tabcellsep 0.475\tabcellsep 0.475\end{longtable} \par
 
\caption{\label{tab_3}Table 3 :}\end{figure}
 \begin{figure}[htbp]
\noindent\textbf{4} \par 
\begin{longtable}{P{0.06915254237288135\textwidth}P{0.29101694915254234\textwidth}P{0.3659322033898305\textwidth}P{0.12389830508474577\textwidth}}
2\tabcellsep \tabcellsep \tabcellsep \\
3\tabcellsep cp\tabcellsep 1004.5\tabcellsep 1004.5\\
4\tabcellsep ?\tabcellsep 1.4\tabcellsep 1.4\\
5\tabcellsep R\tabcellsep 287\tabcellsep 287\\
6\tabcellsep A1\tabcellsep \multicolumn{2}{l}{0.007854 0.00785398}\\
7\tabcellsep P1, atm\tabcellsep 1\tabcellsep 1\\
8\tabcellsep P1, Pa\tabcellsep 1.01E+05\tabcellsep 1.01E+05\\
9\tabcellsep T1, K\tabcellsep 313\tabcellsep 313\\
10\tabcellsep V1, m/s\tabcellsep 100\tabcellsep 100\\
11\tabcellsep Ro1, kg/m3\tabcellsep 1.13E+00\tabcellsep 1.13E+00\\
12\tabcellsep Z\tabcellsep 2009\tabcellsep 2009\\
13\tabcellsep RHS\tabcellsep 63.8817\tabcellsep 63.8817\\
14\tabcellsep \multicolumn{3}{l}{V2, m/s 99.999787 258.772587}\\
15\tabcellsep V2/V1\tabcellsep \multicolumn{2}{l}{0.9999979 2.58772587}\\
16\tabcellsep A2\tabcellsep \multicolumn{2}{l}{0.007854 0.00384845}\\
17\tabcellsep A1/A2\tabcellsep \multicolumn{2}{l}{0.9999977 2.04081633}\\
18\tabcellsep LHS\tabcellsep \multicolumn{2}{l}{63.88169 63.8808525}\\
19\tabcellsep P2, Pa\tabcellsep 1.01E+05\tabcellsep 7.27E+04\\
20\tabcellsep P2, atm\tabcellsep 1.00E+00\tabcellsep 7.17E-01\\
21\tabcellsep P1/P2\tabcellsep 1.00E+00\tabcellsep 1.39E+00\\
22\tabcellsep T2, K\tabcellsep \multicolumn{2}{l}{312.99997 284.641749}\\
23\tabcellsep T1/T2\tabcellsep \multicolumn{2}{l}{1.0000001 1.09962787}\\
24\tabcellsep Ro2, kg/m3\tabcellsep 1.13E+00\tabcellsep 8.90E-01\\
25\tabcellsep \multicolumn{2}{l}{Ro1/Ro2 1.00E+00}\tabcellsep 1.27E+00\\
26\tabcellsep \multicolumn{3}{l}{c1, m/s 354.63136 354.631358}\\
27\tabcellsep \multicolumn{3}{l}{c2, m/s 354.63134 338.184941}\\
28\tabcellsep M1\tabcellsep \multicolumn{2}{l}{0.281983 0.28198296}\\
29\tabcellsep M2\tabcellsep \multicolumn{2}{l}{0.2819824 0.76518069}\end{longtable} \par
 
\caption{\label{tab_4}Table 4 :}\end{figure}
 			\footnote{© 2020 Global Journals} 		 		\backmatter  			  				\begin{bibitemlist}{1}
\bibitem[Anderson and Hill]{b0}\label{b0} 	 		\textit{},  		 			John D Anderson 		,  		 			Mcgraw Hill 		.  		 	 
\bibitem[Gill (2020)]{b1}\label{b1} 	 		‘Equations for isentropic compressible flow through variable area ducts’.  		 			B S Gill 		.  	 	 		\textit{International Journal of Aerospace and Mechanical Engineering}  		May 2020. 7  (2)  p. .  	 
\end{bibitemlist}
 			 		 	 
\end{document}
