烟气再循环联合循环中燃气轮机温度控制方案
Temperature Control Scheme for Gas Turbine of Combined Cycles with Exhaust Gas Recirculation
通讯作者: 张士杰,研究员,博士生导师;E-mail:zhangsj@mail.etp.ac.cn.
责任编辑: 王一凡
收稿日期: 2023-04-11 修回日期: 2023-06-9 接受日期: 2023-06-12
基金资助: |
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Received: 2023-04-11 Revised: 2023-06-9 Accepted: 2023-06-12
作者简介 About authors
李柯颖(1993-),博士生,从事先进燃气轮机循环研究.
在部分负荷工况下,采用余热锅炉排气再循环与压气机进口导叶调节联合应用(EGR-IGVC)策略,可有效改善燃气轮机联合循环性能.但此策略若配合联合循环电站部分负荷工况中燃气轮机常采用的等T3(透平入口温度)-T4m(透平排气温度最大允许值)温控方案,在较低负荷下会造成较大的底循环㶲损失,底循环做功能力下降明显.提出了一种更适用于EGR-IGVC策略的等T3-T4m-T4d(透平排气温度设计值)温控方案,以PG9351FA型燃气轮机联合循环为研究对象,采用能量与㶲分析方法,对比研究了EGR-IGVC策略配合两种温控方案时的联合循环部分负荷性能.研究结果表明,当环境温度为15 ℃,部分负荷率在80%负荷以上时,EGR-IGVC策略配合等T3-T4m方案效果仍为最佳;在30%~80%负荷时,与配合等T3-T4m方案相比,EGR-IGVC策略配合等T3-T4m-T4d方案可使燃气轮机效率提高0.15~0.47个百分点,余热锅炉㶲损失减少0.51%(2.15 MW)以上.研究亦表明,当环境温度在0~40 ℃间变化时,采用等T3-T4m-T4d方案总能获得更高的联合循环效率,且随环境温度上升,部分负荷效率增幅更为明显.
关键词:
Under partial-load conditions, the combined application of exhaust gas recirculation of heat recovery steam generator and compressor inlet guide vane adjustment (EGR-IGVC) can effectively improve the performance of gas turbine combined cycle. However, if this strategy is combined with the temperature control scheme of constant T3(turbine inlet temperature)-T4m(maximum allowable turbine exhaust temperature), which is often adopted in gas turbine combined cycles under part-load conditions, it would cause a large bottoming cycle exergy destruction and a significant decrease in bottoming cycle power output at relatively lower loads. In this paper, a constant T3-T4m-T4d (the design value of turbine exhaust temperature) scheme suitable for the EGR-IGVC strategy is proposed, the PG9351FA gas turbine combined cycle unit is taken as the research object, and the partial-load performance of combined cycle under the two temperature control schemes is compared and investigated based on energy and exergy analysis. The results show that the combination of the EGR-IGVC strategy with the constant T3-T4m scheme is still the best at the ambient temperature of 15 ℃ and the partial-load rate of above 80%. At a load of 30%—80%, compared with the constant T3-T4m scheme, the EGR-IGVC strategy combined with the constant T3-T4m-T4d scheme can increase the gas turbine efficiency by 0.15%—0.47%, and decrease the exergy destruction of the heat recovery steam generator by more than 0.51%(2.15 MW). The results also show that adopting the constant T3-T4m-T4d scheme can always obtain higher combined cycle efficiency when the ambient temperature varies between 0 and 40 ℃. In addition, the increase in partial-load efficiency becomes more evident with the rise of ambient temperature.
Keywords:
本文引用格式
李柯颖, 陈鲲, 江泽鹏, 李超, 郭孝国, 张士杰.
LI Keying, CHEN Kun, JIANG Zepeng, LI Chao, GUO Xiaoguo, ZHANG Shijie.
燃气轮机联合循环(Gas Turbine Combined Cycle, GTCC)机组能够实现能量的梯级利用,具有高效率、低污染等优势.随着重型燃气轮机技术的发展,目前最先进的重型燃气轮机联合循环设计工况时效率已达60%以上[1].但随着可再生能源发电比例的提高,在实际应用中,联合循环常作为调峰机组使用[2],其年平均负荷一般仅维持在70%~80%左右[3],国内某发电厂联合循环机组在夜间的负荷仅为35%[4].而随负荷降低,联合循环效率下降明显.对于某F级燃气轮机联合循环,当负荷由100%降至40%时,循环效率会下降14个百分点以上[5].因而,研究如何改善部分负荷条件下的联合循环机组性能十分必要.
在部分负荷条件下,联合循环电站通常采用压气机进口导叶角度控制(Inlet Guide Vane Control, IGVC)策略,以防止燃气轮机透平入口温度的过快下降,从而增大底循环做功量,改善联合循环部分负荷性能.但对于重型燃气轮机而言,压气机进口导叶(IGV)角度可调节程度有限[6],且IGV角度调节会造成压气机效率下降.因此,IGVC策略对联合循环部分负荷性能的改善效果受到一定限制.近年来,烟气再循环(Exhaust Gas Recirculation, EGR)作为改善联合循环部分负荷性能的手段之一被提出[7].通过烟气再循环,压气机入口空气被加热,进入燃气轮机的空气质量流量减少,从而达到与IGV角度调节相同的效果[8].因此,EGR与IGV联合使用可有效拓宽压气机入口空气可被调节的质量流量范围.已有研究表明,在负荷下降过程中,联合循环电站先采用EGRC再采用IGVC(EGR-IGVC策略)可以获得比单纯的IGVC策略更高的循环效率[9].
目前,IGVC策略通常配合燃气轮机等T3(透平入口温度)-T4m(透平排气温度最大允许值)温控方案[10-11]使用,即在降负荷过程中,先控制燃气轮机透平入口温度维持在设计值不变(透平排气温度会随负荷降低不断升高),然后将透平排气温度维持在最大允许值不变[12].但对于EGR-IGVC策略,若仍配合常用的等T3-T4m方案,由于在更宽负荷范围内燃气轮机透平排气温度均维持在最大允许值,余热锅炉主蒸汽与再热蒸汽超温问题变得更为严重[13].虽然蒸汽超温问题可通过喷水冷却的方式来解决,但这势必会造成更大的底循环㶲损失,底循环做功能力下降明显[14].因而,EGR-IGVC策略下是否有更为合理的燃气轮机温控方案,是一个值得研究的问题.
本文以S109FA联合循环机组为研究对象,提出了一种适用于EGR-IGVC策略的燃气轮机等T3-T4m-T4d(透平排气温度设计值)温控方案.通过建立燃气-蒸汽联合循环变工况系统模型,基于能量与㶲分析方法,研究了EGR-IGVC策略配合该温控方案时的顶循环、底循环与联合循环部分负荷性能,并在不同环境温度下与传统的等T3-T4m温控方案进行了对比.
1 研究对象
采用基于烟气再循环的燃气轮机联合循环(EGR-GTCC)系统,结构如图1所示.
图1
表1 设计工况下联合循环系统运行与性能参数
Tab.1
系统 | 参数 | 设计值 |
---|---|---|
环境 | 环境温度/℃ | 15.00 |
环境压力/bar | 1.01 | |
环境相对湿度/% | 60.00 | |
燃气轮机 | 入口空气质量流量/(kg·s-1) | 635.00 |
燃料质量流量/(kg·s-1) | 14.74 | |
透平入口温度/℃ | 1 328.00 | |
燃气轮机排气温度/℃ | 615.00 | |
燃气轮机做功/MW | 253.20 | |
余热锅炉 | 高压蒸汽温度/℃ | 565.00 |
中压蒸汽温度/℃ | 297.00 | |
低压蒸汽温度/℃ | 295.00 | |
高压蒸汽压力/bar | 98.80 | |
中压蒸汽压力/bar | 24.00 | |
低压蒸汽压力/bar | 4.00 | |
蒸汽轮机 | 高压入口压力/bar | 98.80 |
中压入口压力/bar | 24.00 | |
低压入口压力/bar | 4.00 | |
蒸汽轮机做功/MW | 139.80 | |
联合循环 | 联合循环做功/MW | 393.00 |
联合循环效率/% | 56.14 |
在部分负荷条件下,为避免主蒸汽与再热蒸汽超温,余热锅炉在高压过热器与再热器处添加减温器.考虑到机组运行性能与安全性,在45%负荷以上,蒸汽轮机设置为滑压运行模式,45%负荷以下设置为定压运行模式[16].
2 运行策略与温控方案
表2 3种运行策略的描述
Tab.2
运行策略 | 方案 | 控制参数 | 描述 | 负荷范围/% |
---|---|---|---|---|
IGVC | 等T3-T4m | Δa, qm | 维持透平入口温度为设计工况值 | 82.5~100 |
Δa, qm | 维持透平排气温度为最大值 | 82.5~43.7 | ||
qm | 透平入口与排气温度迅速下降 | 43.7~30 | ||
EGR-IGVC | 等T3-T4m | EGRR, qm | 维持透平入口温度为设计工况值 | 89.1~100 |
EGRR, qm | 维持透平排气温度为最大值 | 81.8~89.1 | ||
Δa, qm | 维持透平排气温度为最大值 | 36.7~81.8 | ||
qm | 透平入口与排气温度迅速下降 | 30~36.7 | ||
等T3-T4m-T4d | EGRR, qm | 维持透平入口温度为设计工况值 | 89.1~100 | |
EGRR, qm | 维持透平排气温度为最大值 | 81.8~89.1 | ||
qm | 透平入口与排气温度逐渐下降 | 75.7~81.8 | ||
Δa, qm | 维持透平排气温度为设计工况值 | 33.0~75.7 | ||
qm | 透平入口与排气温度迅速下降 | 30~33.0 |
3 联合循环系统计算模型
3.1 模型建立
图2
对于EGR-IGVC策略配合相应的温度控制方案, 在调节燃料量的同时,先增大EGRR提升压气机入口空气温度,当EGRR达到最大值,再调节Δa直至极限,以获得目标负荷下联合循环出功量的同时保证透平入口与排气温度在相应控制水平(见表2).当目标负荷、控制策略以及温度控制方案确定后,即可获得EGRR与Δa.
对于PG9351FA型燃气轮机,IGV角度的最大变化量为39°.相应地,IGV可调节的空气质量流量比例为40%[14].根据这两个参数,确定IGV对压气机入口空气质量流量的调节能力.
为评价EGR-GTCC系统性能,引入燃气轮机与底循环做功量,燃气轮机与联合循环效率进行能量分析,以及引入物流㶲,主要部件与底循环㶲损失比例进行㶲分析.基本计算公式详见文献[20],主要部件与底循环㶲损失比例计算公式如下:
式中: Ii为第i个部件㶲损失; Ef,EGT-out分别为燃料㶲与燃气轮机出口㶲;χi,χBot分别为第i个部件与底循环㶲损失比例;WST为蒸汽轮机出功量.
3.2 模型验证
图3
图3
IGVC策略下燃气轮机与联合循环部分负荷效率的模拟结果与文献对比
Fig.3
Comparison between simulation and results in literature of partial-load efficiency of gas turbine and combined cycle under IGVC strategy
4 结果分析
4.1 部分负荷下EGR-GTCC系统的能量分析
图4
图4
烟气再循环比例与IGV角度变化量
Fig.4
Recirculation ratio of exhaust gas and variation of inlet guide vane angle
图5
图6
在30%~90%负荷范围内,3种工况下的顶循环性能参数如表3所示.
表3 顶循环性能参数
Tab.3
项目 | 策略 | 方案 | 压比 | 燃气轮机做功/MW | 燃气轮机效率/% |
---|---|---|---|---|---|
90%负荷 | IGVC | 等T3-T4m | 14.08 | 226.09 | 35.05 |
EGR-IGVC | 等T3-T4m | 13.88 | 223.25 | 35.01 | |
等T3-T4m-T4d | |||||
80%负荷 | IGVC | 等T3-T4m | 12.81 | 193.22 | 33.05 |
EGR-IGVC | 等T3-T4m | 12.75 | 191.77 | 33.45 | |
等T3-T4m-T4d | 12.95 | 192.56 | 33.82 | ||
70%负荷 | IGVC | 等T3-T4m | 11.71 | 163.95 | 31.28 |
EGR-IGVC | 等T3-T4m | 11.54 | 164.55 | 31.88 | |
等T3-T4m-T4d | 12.02 | 166.62 | 32.34 | ||
60%负荷 | IGVC | 等T3-T4m | 10.55 | 135.61 | 29.26 |
EGR-IGVC | 等T3-T4m | 10.39 | 137.04 | 30.00 | |
等T3-T4m-T4d | 10.82 | 138.87 | 30.47 | ||
50%负荷 | IGVC | 等T3-T4m | 9.31 | 107.73 | 26.92 |
EGR-IGVC | 等T3-T4m | 9.13 | 110.36 | 27.94 | |
等T3-T4m-T4d | 9.51 | 111.63 | 28.33 | ||
40%负荷 | IGVC | 等T3-T4m | 8.29 | 82.61 | 24.58 |
EGR-IGVC | 等T3-T4m | 7.75 | 84.36 | 25.53 | |
等T3-T4m-T4d | 8.11 | 85.59 | 25.90 | ||
30%负荷 | IGVC | 等T3-T4m | 7.88 | 61.36 | 22.13 |
EGR-IGVC | 等T3-T4m | 6.96 | 61.37 | 23.08 | |
等T3-T4m-T4d | 6.98 | 62.52 | 23.23 |
由表3可见,在80%负荷以下,由于EGR减少了燃烧室㶲损失[14],改善了燃气轮机性能[22],所以EGR-IGVC策略下的燃气轮机效率明显高于IGVC策略.EGR-IGVC策略配合等T3-T4m-T4d方案时,燃气轮机效率高于等T3-T4m方案.增大EGRR与减小IGV角度,压气机特性曲线中工况点会向左下角移动,更低的压气机入口空气质量流量对应的压比也越低.等T3-T4m-T4d方案下的压气机入口空气质量流量较等T3-T4m方案更大,压比与燃气轮机做功量也更高.EGR-IGVC策略配合等T3-T4m-T4d方案时,燃气轮机效率较配合等T3-T4m方案提升0.15~0.47个百分点,较IGVC策略则可提升0.77~1.41个百分点.
图7
图8
图9所示为3种工况下的联合循环效率及EGR-IGVC策略采用等T3-T4m-T4d与等T3-T4m方案相比的效率增幅随负荷变化情况.
图9
图9
联合循环效率及EGR-IGVC策略采用等T3-T4m-T4d方案与等T3-T4m方案相比的效率增幅
Fig.9
Efficiency of combined cycle and increase efficiency under constant T3-T4m-T4d scheme compared with those of constant T3-T4m scheme of EGR-IGVC strategy
由图9可见,尽管对于EGR-IGVC策略配合等T3-T4m-T4d方案,底循环做功量更低,但在80%负荷以下,联合循环效率仍略高于等T3-T4m方案.在30%负荷下,联合循环效率可比EGR-IGVC策略配合等T3-T4m方案高0.15个百分点,比IGVC策略配合等T3-T4m方案高2.48个百分点.但仅能量分析并不能解释这一现象,需进一步进行㶲分析.
4.2 部分负荷下EGR-GTCC系统的㶲分析
㶲分析是一种定量分析方法,可以揭示热力系统产生㶲损失的位置和大小,对提高系统能源利用效率具有重要意义.以50%负荷为例,3种工况下得到的联合循环系统㶲流桑基图如图10所示.其中,燃料㶲设置为100,其余物流㶲与各部件㶲损失定义为其占燃料㶲的比例的100倍.
图10
图10
联合循环系统的㶲流桑基图(50%负荷)
Fig.10
Sankey diagram of the exergy flow for the combine cycle system (50% load)
从㶲流图中可看出,在50%负荷工况时,与IGVC策略相比,EGR-IGVC策略配合等T3-T4m方案,燃气轮机排气㶲占燃料㶲的比例可增大3.05%,但却导致余热锅炉出现更大的㶲损失.这说明EGR-IGVC策略下,配合等T3-T4m方案虽有更多㶲流进入底循环,但这部分㶲在底循环中并没有得到充分利用.而配合等T3-T4m-T4d方案则可解决这一问题,如图10(c)所示,与配合等T3-T4m方案比,余热锅炉㶲损失占燃料㶲的比例可减少0.51%(2.15 MW),底循环㶲损失比例相应可减少0.66%.
图11所示为70%与50%负荷下,EGR-IGVC策略采用两种温度控制方案时的联合循环各部件㶲损失比例.
图11
图11
EGR-IGVC策略下70%与50%负荷时的联合循环各部件㶲损失比例
Fig.11
Proportion of exergy destructions for combined cycle of various components under the EGR-IGVC strategy at plant loads of 70% and 50%
从图11中可看出,随着负荷的降低,配合等T3-T4m-T4d方案时余热锅炉㶲损失减小幅度增大.因而,在80%负荷以下,底循环㶲损失降幅较大,EGR-IGVC策略配合等T3-T4m-T4d方案得到的联合循环效率就高于等T3-T4m方案.
4.3 考虑环境温度变化时EGR-GTCC系统部分负荷性能
环境温度的变化对压气机入口空气参数有较大影响,且EGR-IGVC策略的本质也是通过改变压气机入口空气参数,实现对透平入口与排气温度的控制.因而,对等T3-T4m-T4d方案的研究还必须考虑到环境温度对联合循环部分负荷性能带来的影响.以50%负荷为例,在不同环境温度下分别采用等T3-T4m方案与等T3-T4m-T4d方案,EGR-IGVC策略下得到的联合循环效率随环境温度变化如图12所示.
图12
图12
EGR-IGVC配合等T3-T4m方案与等T3-T4m-T4d方案时的联合循环效率对比
Fig.12
Comparison of efficiency of combined cycle of EGR-IGVC combined with constant T3-T4m scheme and constant T3-T4m-T4d scheme
从图12中可看出,在环境温度高于0 ℃时,EGR-IGVC策略配合等T3-T4m-T4d方案下的联合循环效率明显高于等T3-T4m方案.随环境温度上升,联合循环效率增幅逐渐增大.当环境温度由 -20 ℃上升至40 ℃时,燃气轮机效率增幅由0.31个百分点增大至0.49个百分点,底循环㶲损失占燃料㶲的比例减小了2.80~3.03 MW.
5 结论
本文提出了适用于EGR-IGVC策略的燃气轮机等T3-T4m-T4d温控方案,通过能量分析与㶲分析方法,研究了EGR-IGVC策略配合该温控方案时,顶循环、底循环与联合循环的部分负荷性能,并将其与EGR-IGVC策略配合燃气轮机等T3-T4m温控方案,以及传统IGVC策略配合燃气轮机等T3-T4m温控方案进行了对比,得到的主要结论如下:
(1) 环境温度为15 ℃时,在约80%~100%负荷范围内,EGR-IGVC策略配合等T3-T4m方案仍为最佳,获得的燃气轮机与联合循环效率略高于IGVC策略.但在80%负荷以下,配合等T3-T4m则导致底循环㶲损失明显大于IGVC策略.且随负荷降低,底循环㶲损失增幅逐渐增大.
(2) 环境温度为15 ℃时,在30%~80%负荷范围内,与配合等T3-T4m方案相比,EGR-IGVC策略配合等T3-T4m-T4d方案可使燃气轮机效率进一步提高0.15~0.47个百分点,且由于底循环运行工况得到改善,高压过热器与再热器㶲损失减小,余热锅炉总㶲损失减少0.51%(2.15 MW)以上,联合循环效率更高.
(3) 随环境温度上升,与配合等T3-T4m方案相比,由于燃气轮机效率提升及底循环㶲损失减小幅度相近,EGR-IGVC策略配合等T3-T4m-T4d方案对联合循环部分负荷效率的提升效果更加明显.在50%负荷工况时,环境温度由 -20 ℃ 上升至40 ℃时,燃气轮机效率可提升0.31~0.49个百分点,底循环㶲损失可减小2.80~3.03 MW.
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