gas turbine surge compressor


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  1. ABSTRACT
  2. In this work, the transient process of surge has been investigated numerically in a gas turbine engine. A one-dimensional
  3. stage-by-stage mathematical model has been developed which can describe the system behavior during aerodynamic
  4. instabilities. It is demonstrated that, these instabilities can be stabilized by the use of active control strategies, such as air
  5. bleeding and air injection. Both steady and unsteady active control systems were considered. In the steady case, mass is
  6. removed at a fixed rate from the diffuser, or mass is injected at a fixed rate into the first stage of the compressor. In
  7. unsteady control, the rate of bleeding or injection is linked with the amplitude and the frequency of the upstream pressure
  8. disturbances. Results show that both steady and unsteady strategies eliminate surge disturbances and suppress the
  9. instabilities. Therefore, they extend the stable operating range of compressor. It is also shown that smaller amount of
  10. compressed air needs to be removed in the unsteady control case. Also, a variable area diffuser is shown to be able of
  11. suppressing surge instabilities. Active control of i
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  42. 1- PhD Student (Corresponding Author): khaleghi@aut.ac.ir
  43. 2- Assistant Prof.
  44. 3- Assistant Prof.
  45. www.SID.ir
  46. Archive of SID
  47. 98 Mech. & Aerospace Eng. J. Vol. 2, No. 2, Nov. 2006
  48. NOMENCLATURE
  49. A = Area
  50. Am = Amplitude of Surge Disturbance
  51. Cf = Friction Factor
  52. DH = Hydraulic Diameter
  53. DA = Diffuser Area
  54. E = Internal Energy Per Unit mass
  55. Fx = Axial Force
  56. f = Frequency of Surge Disturbance
  57. fdis =
  58. Frequency of Inlet Total Pressure
  59. Perturbation
  60. K1-K5 = Constants
  61. mB = Mass Flow Rate of Bleed or Injected air
  62. p = Static Pressure
  63. Q = Heat Production
  64. t = Time
  65. U = Axial Velocity
  66. UBX = Axial Velocity of Bleed or injected air
  67. W = Work
  68. 5 =
  69. Density
  70. Introduction
  71. Turbo machines are used in a wide variety of
  72. engineering applications for power generation and
  73. propulsion. There are two major fluid dynamic
  74. instabilities in compression systems, known as
  75. rotating stall and surge. Surge is a large amplitude
  76. oscillation of the total annulus averaged flow through
  77. the compressor; whereas in rotating stall, one can
  78. finds from one to several cells of severely stalled flow
  79. rotating around the circumference, although the
  80. annulus averaged mass flow remains constant in time
  81. once the pattern is fully developed. Therefore,
  82. rotating stall is the two-dimensional or threedimensional
  83. disturbance localized to the compressor
  84. and characterized by regions of reduced or reversed
  85. flow that rotate around the annulus of the compressor
  86. [1-4]. To avoid these dangers, compressors have been
  87. designed to operate away from the peak operating
  88. point.
  89. A compression system mathematical model was
  90. developed using lumped-volume techniques which
  91. make certain assumptions about compressibility
  92. within the system.
  93. The lumped volume model uses an isentropic
  94. relationship to relate the time-dependant change in
  95. density to a time-dependant change in total pressure,
  96. and uses a steady-state form of the energy equation
  97. [5]. A stage-by-stage mathematical model was
  98. presented by Davis [6] which removed assumptions
  99. inherent in lumped-volume models. A one
  100. dimensional model developed by Garrard and Davis
  101. [7-10] was found to predict the flow oscillations of
  102. surge cycles due to perturbations of fuel flow rate. A
  103. one dimensional model was developed to predict
  104. surge disturbance propagation and engine response
  105. during surge and surge recovery, due to perturbation
  106. of total pressure and temperature, and exit nozzle area
  107. [11]. Moore and Greitzer [12] developed a 2-D model
  108. for rotating stall and surge. Their analysis was
  109. extended to the compressible flow regime by
  110. Bonnaure [13] and Hendricks [14]. It also was further
  111. modified to include actuation by Feulner [15], who
  112. also converted the model to a form compatible with
  113. control theory. Paduano used controllable inlet guide
  114. vanes for elimination of rotating stall [16,17]. Pinsley
  115. [18] studied centrifugal surge control using throttle
  116. valves as actuators. The effect of bleeding on the
  117. control of instabilities was studied by Eveker [19],
  118. Yeung [20] and Murray [21]. The reported amounted
  119. of bleeding by Yeung to achieve operating
  120. enhancements ranges from 1 to 10 percent based on
  121. the mean flow. Niazi and Stein [22] developed a
  122. three-dimensional viscous flow solver and studied the
  123. fluid dynamic phenomena that lead to the onset of
  124. instabilities in centrifugal and axial compressors and
  125. the effect of bleeding on the control of instabilities.
  126. The next section of this study contains the model
  127. description. In the third section, the results of using
  128. steady and unsteady control for uniform inlet flow are
  129. presented. Air bleeding, air injection and variable
  130. area diffuser are used as control systems. Although
  131. one-dimensional models are not able to simulate
  132. rotating stall, they are shown to properly enable
  133. simulation of surge instability and study of active
  134. control. In the fourth section, the results of using
  135. steady and unsteady control for inlet flow with total
  136. pressure perturbation are presented.
  137. Modeling
  138. Figure 1 shows the engine geometry consisting of
  139. compressor, a diffuser, a combustion chamber, a two
  140. stage turbine and an exhaust duct with a convergent
  141. nozzle. Dimensions are given in mm. The compressor
  142. geometry and characteristics are taken from Rolls-
  143. Royce C-141, which its geometry and experimental
  144. data were available in house.
  145. www.SID.ir
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  148. Fig. 2 Compressor characteristic performance of the
  149. third stage.
  150. Fig. 1Geometry of the engine.
  151. Governing Equations
  152. The governing equations are the unsteady, onedimensional
  153. equations of continuity, momentum and
  154. energy. These equations for an inviscid flow are
  155. expressed in the conservative form (Equations 1 to 4).
  156. It must be noted that these 1-D equations are used for
  157. simulation of compressor and turbine flows and not
  158. for the combustion chamber. The combustion
  159. chamber is considered as a zero dimensional
  160. component which energy release is modeled by an
  161. increase in total temperature as:
  162. (1)
  163. (2)
  164. (3)
  165. (4)
  166. Component Characteristics
  167. To provide stage force (FX) and shaft work (Wshaft)
  168. input to the momentum and energy equations, a set of
  169. quasi-steady stage characteristics must be available
  170. for closure. The stage characteristics provide the
  171. pressure and temperature variation across each stage
  172. as a function of normalized corrected mass flow rate.
  173. The compressor has four stages and an inlet guide
  174. vane (IGV) with different pressure and temperature
  175. characteristics. During transition to surge, the steady
  176. stage forces derived from the steady characteristics
  177. are modified for dynamic behavior via a first-order
  178. time lag equation. Appropriate time constants must be
  179. used for each stage to provide the correct transient
  180. behavior. The pressure and temperature
  181. characteristics of the third stage are given in Fig.2.
  182. Characteristics of other stages are also modified for
  183. dynamic behavior.
  184. Burner is considered as a zero dimensional
  185. component. The energy release from the combustion
  186. chamber is considered by an increase in total
  187. temperature. The air-fuel ratio and combustion
  188. chamber loss of a typical engine are used in the
  189. model. The ratio of exit to inlet total pressure of
  190. combustion chamber is 0.96. Turbine stages
  191. characteristics, with specified power rating, were
  192. obtained in order to take the matching condition into
  193. account.
  194. Numerical Scheme and Boundary Conditions
  195. The method of characteristics is used as the
  196. Numerical scheme to solve the governing equations.
  197. A variable time step is used to satisfy the Courant
  198. condition. For more details of MOC one may refer to
  199. reference [23].
  200. Specified total pressure and temperature during
  201. normal forward flow is the inlet boundary conditions.
  202. The exit boundary condition is the specification of
  203. S ,
  204. x
  205. N
  206. t
  207. M =
  208. 
  209. 
  210. +
  211. 
  212. 
  213. ,
  214.   
  215. 
  216. 
  217.   
  218. 
  219. =
  220. e
  221. M U
  222. 2 ,
  223.   
  224. 
  225. 
  226.   
  227. 
  228. +
  229. = +
  230. Ue pU
  231. U p
  232. U
  233. N
  234. ( )
  235. ( )
  236. .
  237. 2 1
  238. 2
  239. ln
  240. 2
  241. 2
  242.       
  243. 
  244. 
  245.       
  246. 
  247. +
  248. 
  249. 
  250. 
  251.  
  252. 
  253. +
  254. +
  255. =
  256. Adx
  257. dm
  258. e p
  259. dx
  260. U p dA
  261. A
  262. U
  263. Adx
  264. W
  265. Adx
  266. Q t
  267. Adx
  268. dm U
  269. D
  270. U U
  271. C
  272. Adx
  273. FX
  274. dx
  275. dA
  276. A
  277. U
  278. Adx
  279. dm
  280. dx
  281. U d A
  282. S
  283. B
  284. B
  285. shaft
  286. B Bx
  287. H
  288. f
  289. B
  290. & &
  291. &
  292. &
  293. 
  294.  
  295. 
  296. www.SID.ir
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  298. Mech. & Aerospace Eng. J. Vol. 2, No. 2, Nov. 2006 100
  299. exit Mach number or static pressure. During
  300. reverse flow the inlet is converted to an exit boundary
  301. with the specification of the ambient static pressure.
  302. Therefore, both the inlet an exit boundaries function
  303. as exit boundaries during a surge cycle. The boundary
  304. conditions are properly applied to the combustor to
  305. take the zero dimensional modeling into account. The
  306. initial values are determined for the boundary
  307. conditions at some specified compressor operating
  308. points.
  309. Control Strategies
  310. In this study, two types of active control systems are
  311. considered: steady and unsteady. In steady control,
  312. including steady air bleeding and air injection, a fixed
  313. fraction of mass flow rate is removed from or injected
  314. to the compression system. In unsteady case, the mass
  315. flow rate of removed or injected air is linked to the
  316. pressure fluctuation upstream of compressor during
  317. instabilities. Figure 3 illustrates the schematic of the
  318. unsteady control system which is used in the present
  319. study.
  320. Fig. 3 Schematic of the unsteady control system.
  321. The Validation of Results
  322. To obtain the stable operating conditions, the
  323. equations are solved by a time marching technique.
  324. To validate the results, the predicted overall
  325. characteristic of the compressor (for stable
  326. conditions) is compared with the experimental data in
  327. Fig.4. Close agreement between the model steady
  328. state results and experimental data, especially near the
  329. surge point, is obtained. Table 1 shows the
  330. comparison between the surge point obtained from
  331. the model and the experimental surge point. As
  332. shown in figure 4 the experimental curve is
  333. sufficiently close to the theoretical curve near the
  334. surge point. Such results can be attributed to the fact
  335. that one-dimensional modeling is quite close to the
  336. nature of surge.
  337. Tab. 1 Experimental and computational surge
  338. point of compressor.
  339. Fig. 4 Compressor overall characteristics.
  340. Uniform Inlet Flow
  341. In steady control, a fixed fraction of the mass flow
  342. rate is removed through a valve which can be placed
  343. at the diffuser or at the interstage of compression
  344. system, or a fixed fraction of the mass flow rate is
  345. injected into the first stage of the compressor. Figure
  346. 5 shows the static pressure at the compressor face
  347. versus time. Steady bleeding from diffuser, equal to
  348. 4.3% of mean mass flow rate was applied to the
  349. unstable operating condition at point B (shown in
  350. Fig.6). As shown, this amount of bleeding can
  351. remove surge disturbance.
  352. Fig. 5 Inlet static pressure fluctuation.
  353. www.SID.ir
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  356. To study the effect of bleeding, steady bleeding from
  357. diffuser and also interstage (second stage) was
  358. considered. Bleeding equal to 3 % and 4.3 % of mean
  359. flow rate was applied to the unstable condition at
  360. point B. For 70 % and 100 % of bleeding which is
  361. equal to 3 % and 4.3 % of mean flow rate
  362. respectively, the stable controlled operating points are
  363. shown as points C and D in Fig.6. In Fig.6, the
  364. horizontal axis is the mass flow rate after bleed valve
  365. and the vertical axis is the static pressure ratio of the
  366. compressor. For 70 % of bleeding (3 % of mean flow
  367. rate), the computed mass flow rate is 15.75 kg/s and
  368. the corresponding overall static pressure ratio is 2.37.
  369. For 100 % of bleeding (4.3 % of mean flow rate), the
  370. mass flow rate is 15.65 kg/s and the static pressure
  371. ratio is 2.35. This reduction of static pressure ratio is
  372. due to removing more compressed air in 100 %
  373. bleeding.
  374. To investigate the effect of interstage bleeding,
  375. the same amount of bleeding (4.3 % of mean flow
  376. rate) was applied to the unstable condition at point B.
  377. Mass is removed from the interstage (second stage)
  378. and the new operating point is shown as point E
  379. which has the mass flow rate of 15.6 kg/s and static
  380. pressure ratio of 2.38. As illustrated, interstage
  381. bleeding results in higher pressure ratio.
  382. 3.3 % of the mean flow rate was injected into the
  383. first stage, during the unstable condition at point B, to
  384. study the effect of injection on the performance of the
  385. compressor. The new stable operating condition is
  386. point F in Fig.6. The mass flow rate of point F is
  387. 15.85 and the corresponding pressure ratio is 2.5.
  388. Fig. 6 Compressor characteristic performance for
  389. steady control
  390. The steady bleeding is inefficient and must be turned
  391. off during design operation. In unsteady control, the
  392. removed mass flow rate is linked to the pressure
  393. fluctuation upstream of the compressor. Although
  394. such strategy is not possible in one-dimensional
  395. analysis, using periodic functions for bleeding mass
  396. flow rate is shown to improve the stable operating
  397. range. The amount of mass, which is removed from
  398. diffuser, is linked to the amplitude and frequency of
  399. surge disturbance. The amplitude and frequency of
  400. pressure fluctuation during surge is found to be 12
  401. Kpa and 80 Hz from Fig.5.
  402. Three forms of periodic functions are used for
  403. bleeding control. In the following equations, K1 , K2 ,
  404. K3 ,  are chosen to be 1, 0.9, 0.5 and I/4
  405. respectively:
  406. (5)
  407. (6)
  408. (7)
  409. In the above equations, "P1", "t", "Am", "f" and ""
  410. are respectively ambient pressure, time, amplitude,
  411. frequency of the fluctuations and the phase lag. The
  412. constants K1, K2, K3 are chosen to ensure the bleed
  413. rate is less than 3 % of mean flow rate. The parameter
  414. m& B is averaged mass flow rate and is set to be 2.3 %
  415. of the mean mass flow rate. Figure 7 is given for
  416. better understanding the trend of control function.
  417. Results are shown in figure 8. Point G, H and I are
  418. new stable operating points corresponding to equation
  419. 5-7 respectively. For point G the computed mass flow
  420. rate is 15.6 kg/s and the static pressure ratio is 2.4.
  421. Point H has mass flow rate of 15.7 kg/s and static
  422. pressure ratio of 2.37. Point I has the minimum mass
  423. flow rate equal to 15.5 kg/s with the static pressure
  424. ratio of 2.37. The minimum mass flow rate obtained
  425. is related to the equation 7 and the maximum pressure
  426. ratio is related to equation 5. This behavior may be
  427. attributed to the effect of different shapes of the
  428. equations shown in figure 7. The similar shapes to the
  429. nature of surge may lead to higher pressure ratios or
  430. lower mass flow rates. As shown, smaller amount of
  431. compressed air need to be removed in unsteady
  432. control, and also it leads to operating point with
  433. = +    [ (t f + )]
  434. P
  435. m m m K Am B B B sin 2 . .
  436. 1
  437. 1 & & &
  438. ( )
  439. ( )
  440. 
  441. 
  442. +
  443. + +
  444. = +   
  445.  
  446.  
  447. t f
  448. t f
  449. P
  450. m m m K Am B B B cos 2 . .
  451. sin 2 . .
  452. 2
  453. 1
  454. 2 & & &
  455. ( )
  456. ( )
  457. ( ) 
  458. 
  459. 
  460. 
  461. 
  462.    
  463. +
  464. + +
  465. + +
  466. = +   
  467.  
  468.  
  469.  
  470. t f
  471. t f
  472. t f
  473. P
  474. m m m K Am B B B
  475. cos 2 . .
  476. cos 2 . .
  477. sin 2 . .
  478. 3
  479. 2
  480. 1
  481. 3 & & &
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  485. higher pressure ratio.
  486. Fig. 7 Schematic shape of three control functions.
  487. Fig. 8 Compressor characteristic performance
  488. for unsteady control
  489. Variable Area Diffuser
  490. To study the effect of variable area diffuser, which is
  491. located before the burner, the area of the diffuser is
  492. changed with time. The area variation is linked to the
  493. amplitude and frequency of surge disturbance. The
  494. following periodic control law was chosen in this
  495. study:
  496. (8)
  497. DAd is the design area of the diffuser. Constants K4
  498. and K5 are chosen to be 0.2 and 0.1 respectively so
  499. that the area variation does not exceed 2.5% of the
  500. design area.
  501. This control law was applied to the unstable
  502. operating condition at point B shown in figure 6.
  503. Figure 9 shows the inlet mass flow rate versus time.
  504. As illustrated, using an appropriate form of diffuser
  505. area variation eliminates the surge instability and
  506. leads to stable controlled condition.
  507. The area of diffuser decreases periodically by
  508. using the above control law. As a result, compressor
  509. back pressure decreases periodically. Reduction of
  510. back pressure has the same effect of bleeding.
  511. Therefore, variable area diffuser is capable of
  512. eliminating compressor instabilities.
  513. Fig. 9 Inlet mass flow rate (variable area
  514. diffuser).
  515. Intel Total Pressure Perturbation
  516. Instabilities Due to Inlet Total Pressure Perturbation
  517. As mentioned in the previous sections, Transient
  518. interaction of shock waves and boundary layer at the
  519. entry may lead to sinusoidal variations of pressure
  520. that can affect compressor instabilities. AS suggested
  521. by Tesch and Steenken [24], the following form for
  522. modeling of the perturbation was considered:
  523. (9)
  524. In the above equation, (PT) SS is the steady state inlet
  525. total pressure, "t" is time and "fdis" is the perturbation
  526. frequency. Instead of amplitude, a parameter named
  527. amplitude-percent was used.
  528. To study the engine response, we first applied the
  529. above sinusoidal perturbation with the amplitudepercent
  530. of 5 and frequency of 10 Hz to the stable
  531. condition at surge point. Since no surge disturbance
  532. was observed, we increased the frequency at constant
  533. amplitude-percent. The first surge disturbance, with
  534.  (  +  )
  535.  
  536. =
  537. 1 5
  538. 4
  539. 1 / P sin 2f K.t . .
  540. DA K Am
  541. DA DA d
  542. d
  543. ( ) ( ) ( )
  544. Amplitude _ Percent Sifn(2 t ).
  545. P P P
  546. dis
  547. T T SS T SS
  548.    
  549. = + 
  550. 
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  554. Fig. 12 Compressor overall characteristics
  555. the frequency of 25 Hz, was captured when the
  556. frequency of perturbation was increased to 30 Hz.
  557. The inlet mass flow rate versus time is given in
  558. Fig.10.
  559. Fig. 10 Inlet mass flow rate (pressure
  560. perturbation)
  561. Fig.11 Minimum frequency of the perturbations
  562. that leads to surge
  563. The same methodology was applied to the stable
  564. operating condition at surge point for other
  565. magnitudes of amplitude-percent. Figure 11 shows
  566. the minimum frequency of the perturbations that
  567. leads to surge for various amplitude-percent
  568. magnitudes. It also indicates the surge frequency.
  569. Steady Control Results
  570. To study the effect of steady bleeding, 4 % of the
  571. mean mass flow rate was extracted from the diffuser.
  572. This amount of bleeding was applied to the stable
  573. operating condition at point A which has been
  574. destabilized with inlet perturbation of total pressure
  575. of amplitude percent of 5 and frequency of 30 Hz. As
  576. shown in Fig.11 this perturbation is capable of
  577. destabilizing the stable condition at point A which is
  578. closed to the surge point (Fig.12). Fig.13 shows the
  579. inlet mass flow rate versus time for this case. As
  580. illustrated, this amount of bleeding can remove surge
  581. disturbance completely.
  582. Fig. 13 Inlet mass flow rate (Steady bleeding).
  583. Table. 2 Minimum amount of required steady
  584. bleeding for various inlet perturbations.
  585. To obtain the minimum mass flow rate
  586. needed to be removed for stabilizing the instabilities,
  587. we reduce the steady removed mass. Bleeding equal
  588. to 2.2 % of mean mass flow rate was found to be
  589. optimum. The same methodology was used in the
  590. case of perturbations of higher amplitude percent. The
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  594. frequency of perturbations was chosen from Fig.11 to
  595. ensure that the inlet perturbations can destabilize the
  596. compressor. Table.2 shows the minimum amount of
  597. steady bleeding needed for various amplitude percent
  598. magnitudes. As the amplitude percent increases,
  599. higher amount of mass flow rate is needed to be
  600. removed in order to stabilize the instabilities.
  601. Unsteady Control Results
  602. The frequency of surge disturbance is chosen from
  603. Fig.11 and the pressure fluctuation during surge is
  604. also obtained from computations for each case. As
  605. discussed, unsteady one dimensional bleeding with
  606. periodic forms, can reduce the amount of bleeding.
  607. Therefore, it is more efficient. A sinusoidal form
  608. (equation 10) is used to consider periodic bleeding.
  609. (10)
  610. In equation 10, P1, t, Am, and f are the ambient
  611. pressure, time, the amplitude and the frequency of the
  612. fluctuations, respectively. "" is the phase lag and is
  613. chosen to be /4. mB is the averaged mass flow rate
  614. which is needed to be removed. The constant K4 is
  615. chosen to ensure that the bleed rate does not exceed
  616. 20 % of the averaged removed mass flow rate. The
  617. above control law was applied to the same operating
  618. conditions in steady part. Tab.3 shows the minimum
  619. averaged mass flow rate needed to be removed in
  620. order to stabilize the instabilities. As shown, smaller
  621. amount of compressed air need to be removed in
  622. unsteady control, as compared to steady case.
  623. CONCLUSION
  624. A one-dimensional unsteady computer code has been
  625. developed which enables simulation of surge
  626. disturbance propagation through entire jet engines.
  627. The effect of active control on the instabilities was
  628. studied and the following observations and lower
  629. conclusions were obtained:
  630. 1- steady control can eliminate surge disturbance. If
  631. the amount of bleeding air increases, the new stable
  632. operating point has lower mass flow rate and pressure
  633. ratio.
  634. 2- using air injection, as the control system, the new
  635. operating point has higher pressure ratio and also
  636. higher mass flow rate, as compared to air bleeding.
  637. 3- if the bleeding air is injected into the first stage of
  638. the compressor, the required amount of bleeding
  639. reduces.
  640. 4- Interstage bleeding leads to a new stable operating
  641. point with higher pressure ratios compared to
  642. bleeding from the diffuser, so it is more efficient.
  643. 5- smaller amount of compressed air need to be
  644. removed in unsteady control. This leads to a new
  645. operating point with higher pressure ratio.
  646. 6- compressor back pressure reduces as the diffuser
  647. area decreases. Therefore, variable area diffuser can
  648. be used to stabilize compressor instabilities.
  649. 7- inlet perturbations can destabilize the stable
  650. operating condition at design point.
  651. Acknowledgment
  652. This research was supported by Amirkabir University
  653. of Technology, Iran, Tehran, which in greately
  654. appreciated.
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