CN115217622A - 一种基于反应活性调控的氨氢融合燃料控制系统 - Google Patents
一种基于反应活性调控的氨氢融合燃料控制系统 Download PDFInfo
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- CN115217622A CN115217622A CN202210830675.3A CN202210830675A CN115217622A CN 115217622 A CN115217622 A CN 115217622A CN 202210830675 A CN202210830675 A CN 202210830675A CN 115217622 A CN115217622 A CN 115217622A
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- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 236
- 239000001257 hydrogen Substances 0.000 title claims abstract description 236
- 239000000446 fuel Substances 0.000 title claims abstract description 131
- 230000004927 fusion Effects 0.000 title claims abstract description 52
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 21
- 230000000694 effects Effects 0.000 title claims abstract description 21
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 173
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 166
- 238000002485 combustion reaction Methods 0.000 claims abstract description 90
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 77
- 238000004519 manufacturing process Methods 0.000 claims abstract description 30
- 238000002347 injection Methods 0.000 claims abstract description 26
- 239000007924 injection Substances 0.000 claims abstract description 26
- 239000007789 gas Substances 0.000 claims abstract description 25
- 230000002000 scavenging effect Effects 0.000 claims abstract description 25
- 230000001276 controlling effect Effects 0.000 claims abstract description 13
- 230000001105 regulatory effect Effects 0.000 claims abstract description 13
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 238000003860 storage Methods 0.000 claims description 14
- 238000000034 method Methods 0.000 claims description 8
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- 238000005507 spraying Methods 0.000 claims description 6
- 230000009257 reactivity Effects 0.000 claims description 4
- 239000007921 spray Substances 0.000 claims description 4
- 238000005485 electric heating Methods 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 238000002360 preparation method Methods 0.000 claims description 3
- 239000002918 waste heat Substances 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 11
- 238000005516 engineering process Methods 0.000 description 6
- 230000008859 change Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 230000000087 stabilizing effect Effects 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
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- 238000011160 research Methods 0.000 description 2
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- 150000001298 alcohols Chemical class 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000003763 carbonization Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
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- 230000009466 transformation Effects 0.000 description 1
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- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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Abstract
本发明公开了一种基于反应活性调控的氨氢融合燃料控制系统,包括车载氨氢燃料供给系统、氨氢融合燃料预混燃烧发动机和ECU;所述ECU用于调控待进入氨氢融合燃料预混燃烧发动机的氨燃料和氢气的喷气量及压力值;所述车载氨氢燃料供给系统包括低压液氨供给单元和车载制氢单元,用于向所述氨氢融合燃料预混燃烧发动机提供制备的低压氨燃料和氢气;所述氨氢融合燃料预混燃烧发动机包括带有预燃室的湍流射流点火装置;所述进气通道上分别设置有朝向所述缸盖的氨喷射器和第一氢气喷射器,所述湍流射流点火装置用于实现空气和燃料单独喷射的双喷射模式和空气单独喷射的扫气模式,或空气和氢气混合喷射模式以及利用氢气/空气混合气喷射的扫气模式。
Description
技术领域
本发明属于内燃机技术领域,具体涉及一种基于反应活性调控的氨氢融合燃料控制系统。
背景技术
随着传统能源需求的持续上升和全球变暖问题的突显,世界主要汽车生产国纷纷加快部署,将发展清洁能源汽车作为国家战略,发展无碳燃料成为降低碳排放的重要解决方案。大时代背景驱使着传统内燃机向高效清洁燃烧的技术路线发展。近几年,内燃机技术的不断成熟,热效率不断攀升。然而内燃机的碳排放和污染物排放的根源在于燃料本身元素组成。因此,内燃机燃料的低碳、碳中性和零碳化将是内燃机的未来之路。
内燃机零碳技术的本质是燃烧碳中和燃料实现全生命周期的零碳排放。氢能由于良好的燃烧性能、近零的污染物排放以及可由可再生能源生产的性质而备受关注,发展氢能产业是实施“双碳”战略的重要抓手,然而氢气储运难和安全性差等问题制约了其产业化发展。研究发现,氨作为高效储氢介质,具有高能量密度、易液化储运、安全性高和无碳排放等优势,可以用可再生能源生产氢,再将氢转换为氨,运输到目的地,可以极大降低氢的运输成本,并且提高运输的安全性能。氨既是氢能载体,又是零碳燃料,对一定体积的液氨,其含氢量和能量密度分别为相同体积液态氢的1.7和1.5倍。此外,氨还可以通过可再生能源太阳能、电能等利用空气和水合成,整个制备过程无碳排放。我国幅员辽阔,有着十分丰富的太阳能资源、风能等可再生能源。良好的工业生产基础有利于逐步实现化石能源向可再生氨能源的转型。目前国内已有多家科研单位以及企业开始谋划布局氢氨产业链,国内福建、宁夏等地以及国家能源集团纷纷成立相关联盟组织研讨会,抢占先机。因此,发展氨氢融合燃料动力切合我国能源格局现状以及未来的战略调整。
氨气作为发动机燃料开发工作面临的主要挑战来自于氨的不良燃烧特性,如高自燃温度、低火焰速度及高的汽化潜热,较差的自燃能力和燃烧稳定性导致其作为发动机燃料时需要高反应活性的点火源引燃。着火和燃烧不稳定直接导致发动机动力性能和排放性能变差,并造成氨泄漏。而氨气具有腐蚀性和弱毒性,一旦泄漏,将腐蚀损伤发动机零部件、危及人员安全。因此,缸内稳定的着火与火焰传播过程对发动机燃烧过程优化、排放控制、安全性保障均具有重要意义。如何实现氨燃料稳定着火及高效燃烧是目前氨燃料发动机研制面临的关键技术之一。由于氨容易制备氢气,而氢气的燃烧速度快(3m/s),通过车载制氢与氨气形成氢氨融合燃料,根据发动机负荷和转速的变化,实时调控燃料比例,可实现高效清洁燃烧。因此,车载氨裂解制氢技术和氨氢燃料混合比控制技术是氨燃料重型内燃机性能的关键技术。
发明内容
本发明的目的在于提供一种基于反应活性调控的氨氢融合燃料控制系统,通过车载氨氢燃料供给系统在进气形成过程低压喷射氢气与氨燃料并形成反应活性可控的氢氨融合燃料,最终实现内燃机实现高效燃烧的同时实现零碳排放。本发明的目的是通过以下技术方案实现的:
本发明公开了一种基于反应活性调控的氨氢融合燃料控制系统,包括车载氨氢燃料供给系统、氨氢融合燃料预混燃烧发动机和ECU;
所述ECU用于控制氨氢融合燃料预混燃烧发动机和车载氨氢燃料供给系统,调控待进入氨氢融合燃料预混燃烧发动机的氨燃料和氢气的喷气量及压力值;
所述车载氨氢燃料供给系统包括低压液氨供给单元和车载制氢单元,用于向所述氨氢融合燃料预混燃烧发动机提供制备的低压氨燃料和氢气;其中所述低压液氨供给单元用于提供压力范围为0.5~1MPa的氨燃料,所述车载制氢单元用于提供压力范围为1.0~2.0MPa的氢气;
所述氨氢融合燃料预混燃烧发动机包括发动机缸盖、缸套、活塞、主燃烧室、进气通道、排气通道,还包括设置在缸盖上带有预燃室的湍流射流点火装置;其中,所述进气通道上分别设置有朝向所述缸盖的氨喷射器和第一氢气喷射器,喷入进气通道的氨燃料和氢气在进气通道内形成氨氢融合燃料;所述湍流射流点火装置用于实现空气和氢气单独喷射的双喷射模式和空气单独喷射的扫气模式,或氢气-空气混合气喷射的夹气喷射模式以及利用氢气-空气混合气喷射的扫气模式;
所述控制系统的工作过程包括:低压液氨供给单元在ECU的调控下生成压力为0.5~1.0MPa的氨燃料,随后制备的氨燃料分为两路,一部分经管道进入氨喷射器,一部分进入车载制氢单元参与制取氢气;所述车载制氢单元在ECU调控下生成压力为1.0~2.0MPa的氢气,随后氢气分为两路,一部分由所述第一氢气喷射器喷入进气通道,进气通道喷射的氢气与氨燃料混合后在进气通道内形成氨氢融合燃料,其中第一氢气喷射器的喷氢量由ECU调控,从而在进气通道内实现反应活性可调控的氨氢融合燃料;另一部分供给至湍流射流点火装置,并在预燃室内腔中被火花塞点燃,在主燃烧室中形成射流火焰,而后在主燃烧室内点燃氨氢融合燃料,完成燃烧做功。
进一步的,所述低压液氨供给单元包括依次连接的氨存储罐、加热器、稳压罐和压力控制器,所述氨存储罐中装有液氨;所述车载制氢单元包括依次连接的车载制氢装置、高压储氢罐和压力控制器。
进一步的,一进气阀设置在进气通道内,一排气阀设置在排气通道内,且进气阀和排气阀分别设置在缸盖的左右两侧,所述进气阀和排气阀用于结合发动机的节气门装置,改变进气量。
进一步的,所述湍流射流点火装置包括预燃室内腔、火花塞、空气喷射器和第二氢气喷射器;所述空气喷射器的喷嘴伸入预燃室内腔用于向预燃室内腔喷射空气,所述第二氢气喷射器的喷嘴伸入预燃室内腔用于向预燃室内腔喷射氢气;所述火花塞、所述空气喷射器的喷嘴和第二氢气喷射器的喷嘴设置在所述预燃室的同一侧;所述湍流射流点火装置底部开有射流孔,所述预燃室内腔与主燃烧室通过射流孔相通;所述湍流射流点火装置具有两种工作模式,分别是双喷射模式和扫气模式;
当所述ECU控制所述湍流射流点火装置为双喷射模式时,所述空气喷射器和第二氢气喷射器分别向所述预燃室内腔喷射新鲜空气和氢气,用于在预燃室内部形成当量混合气;
当所述ECU控制所述湍流射流点火装置为扫气模式时,只有所述空气喷射器向预燃室内腔喷射新鲜空气,对预燃室进行扫气。
进一步的,所述湍流射流点火装置包括预燃室内腔、火花塞、第二氢气喷射器;所述第二氢气喷射器向下依次安装有高压预混腔和电磁阀,所述电磁阀底部的喷嘴伸入预燃室内腔用于向预燃室内腔喷射氢气-空气混合气;所述高压预混腔侧壁连通一进气口,用于将高压空气与来自第二氢气喷射器的氢气在其中进行预混;所述火花塞的喷嘴伸入所述预燃室内腔中;所述湍流射流点火装置底部开有射流孔,所述预燃室内腔与主燃烧室通过射流孔相通;所述湍流射流点火装置具有两种工作模式,分别是夹气喷射模式和扫气模式;
所述ECU控制所述湍流射流点火装置为夹气喷射模式时,所述第二氢气喷射器中氢气和高压空气在高压预混腔内混合后由电磁阀喷射空气和氢气的混合气,用于在预燃室内部形成当量混合气;
所述ECU控制所述湍流射流点火装置为扫气模式时,所述电磁阀喷射两次,第一次向预燃室内腔喷射新鲜空气,对预燃室进行扫气;而后,第二氢气喷射器中氢气和高压空气在高压预混腔内混合后形成混合气,由电磁阀第二次喷射进入预燃室。
进一步的,所述氨喷射器为液氨低压喷射器,所述第一氢气喷射器具有一氢气低压喷嘴。
进一步的,所述车载氨制氢装置由所述氨氢融合燃料预混燃烧发动机的发动机余热加热,或是单独安装电加热装置进行热量供给。
与现有技术相比,本发明的技术方案所带来的有益效果是:
1.本发明在进气通道安装两个喷射器,通过ECU的调控实现在进气通道形成反应活性可调控的氨氢融合燃料,根据发动机的实际运行工况调节氨氢融合燃料燃烧反应速率,解决氨燃烧火焰传播速度慢的问题,提高发动机的燃烧稳定性;
2.本发明提供整合的车载氨氢燃料供给系统,能够制备低压氨燃料及低压氢燃料;且所述车载氨氢燃料供给系统产生的氢气用于湍流射流点火装置,可大幅提高发动机点火能力;
3.所述湍流射流点火装置提供两种工作模式,其扫气模式通过在预燃室喷氢从而提高射流点火强度,解决氨燃烧点火难的问题,并进一步提高氨燃料火焰传播速度,使氨燃料内燃机一直在高效区工作,并实现二氧化碳零排放。
同时本发明可以扩展到其它氢基燃料,如醇类、醚类等。
附图说明
图1是一种基于反应活性调控的氨氢融合燃料控制系统的示意图;
图2是实施例1的氨氢融合燃料发动机的结构示意图;
图3是实施例1的射流点火装置剖面图;
图4是实施例2的射流点火装置剖面图。
图中:
1:活塞 2:主燃烧室 3:进气阀
4:氨喷射器 5:第一氢气喷射器 6:湍流射流点火装置
7:射流火焰 8:排气阀 9:缸盖
10:缸套 11,21:预燃室内腔 12,16:火花塞
13:空气喷射器 14:压紧螺栓 15,17:第二氢气喷射器
18:高压预混腔 19:进气口 20:电磁阀
具体实施方式
为使本发明实施例的目的、技术方案、有益效果及显著进步更加清楚,下面结合本发明实例中所提供的附图,对本发明实施例中的技术方案进行清楚、完整的描述,显然,所有描述的这些实施例仅是本发明的部分实施例,而不是全部的实施例;基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。
本发明提出的一种基于反应活性调控的氨氢融合燃料控制系统,通过在进气道喷射氨燃料和氢气,在气缸内形成氨氢融合燃料,并通过控制氢气喷射量来调控氨氢融合燃料的反应活性。所述装置所需的氢气来源于车载制氢装置,由氨燃料制备。同时,所制备的氢气可供给预燃室,作为预燃室燃料,配合湍流射流点火装置,形成射流火焰点燃主燃烧室混合气,实现发动机点火性能提升。下面结合附图对该装置的工作过程作进一步说明。
如图1所示,一种基于反应活性调控的氨氢融合燃料控制系统,包括车载氨氢燃料供给系统、氨氢融合燃料预混燃烧发动机和ECU。
所述车载氨氢燃料供给系统包括低压液氨供给单元和车载制氢单元,其中所述低压液氨供给单元用于提供压力范围为0.5~1MPa的低压氨燃料,包括依次连接的氨存储罐、加热器、稳压罐和压力控制器,所述氨存储罐中装有液氨;所述车载制氢单元用于提供压力范围为1.0~2.0MPa的低压氢气,包括依次连接的车载制氢装置、高压储氢罐和压力控制器;所述压力控制器用控制氨燃料/氢气的压力,优选低压液氨供给单元输出的压力值为0.8MPa,优选车载制氢单元输出的压力值为1.0MPa。制备的低压氨燃料(可以是氨气或是液氨)一路流入所述氨氢融合燃料预混燃烧发动机的氨喷射器4中,另一路流入车载制氢单元用于制氢;制备的低压氢气分为两路送入所述氨氢融合燃料预混燃烧发动机中,一路送入第一氢气喷射器5参与燃烧做功,另一路送入湍流射流点火装置6用于预燃室中参与预燃。
所述ECU用于控制氨氢融合燃料预混燃烧发动机、车载制氢装置和压力控制器,调控待进入氨氢融合燃料发动机的氨燃料和氢气的喷气量及压力值。
如图2所示,所述氨氢融合燃料预混燃烧发动机包括缸套10和设置在缸套10顶部的发动机缸盖9,所述发动机缸盖9顶部设置有进气阀3、排气阀8以及湍流射流点火装置6;所述进气阀3设置在进气通道内,所述排气阀8设置在排气通道内,且进气阀3和排气阀8分别设置在缸盖的左右两侧;所述缸套10内设置有活塞1;所述进气阀3和排气阀8用于结合氨氢融合燃料预混燃烧发动机的节气门装置,改变进气量。发动机缸盖与湍流射流点火装置6和活塞1共同组成主燃烧室2,且所述湍流射流点火装置6位于主燃烧室正上方。其中,所述进气通道上分别设置有朝向所述进气阀3的氨喷射器4和第一氢气喷射器5,喷入进气通道的氨气和氢气在进气通道内形成氨氢融合燃料,且该氨氢融合燃料反应活性由位于进气通道的第一氢气喷射器5调整喷氢量实现,当喷氢量增加,氨氢融合燃料反应活性提高,反之,氨氢融合燃料反应活性降低。所述第一氢气喷射器5由ECU和发动机燃料喷射系统配合控制调控。
其中,所述氨喷射器4为液氨低压喷射器,所述第一氢气喷射器5具有一氢气低压喷嘴。
如图3所示,所述湍流射流点火装置6为配置双喷式预燃室形成带有扫气功能的湍流射流点火装置,具有两种工作模式,分别是双喷射模式和扫气模式。所述湍流射流点火装置6包括一壳体,所述壳体底部通过螺纹安装于发动机缸盖9上;所述壳体内部安装有竖直设置的空气喷射器13和第二氢气喷射器15,所述空气喷射器13和第二氢气喷射器15分别通过一个压紧螺栓14固定于所述壳体上,所述压紧螺栓具有通孔且两端均具有螺纹,一端通过螺纹与壳体连接,用于固定空气喷射器13或第二氢气喷射器15,另一端用于连接气路,所述压紧螺栓的通孔用于将空气送入空气喷射器13或是将氢气送入第二氢气喷射器15。所述壳体下部形成一预燃室内腔11,一火花塞12安装在所述预燃室内腔顶部且火花塞12的电极伸入预燃室中;所述火花塞、所述空气喷射器的喷嘴和第二氢气喷射器的喷嘴设置在所述预燃室的同一侧;所述壳体底部开有射流孔,且所述预燃室与主燃烧室通过射流孔相通。所述空气喷射器和第二氢气喷射器通过ECU和发动机燃料喷射系统配合控制调控。所述射流孔用于实现火焰加速传播,提高燃烧速率,进而提高发动机的经济性。
结合图1,其工作过程为:
氨存储罐中的氨燃料依次流经加热器、稳压罐和压力控制器,ECU用于调控压力控制器中氨燃料的压力为0.5~1.0MPa,随后氨燃料分为两路,一部分经管道进入氨喷射器4,一部分进入车载制氢单元中的车载制氢装置。车载制氢装置制备的氢气依次流经高压储氢罐和压力控制器,ECU调控压力控制器中氢气的压力为1.0~2.0MPa,随后氢气分为两路,一部分由所述第一氢气喷射器5喷入进气通道,进气通道喷射的氢气与氨燃料混合后在主燃烧室形成氨氢融合燃料,其中第一氢气喷射器5的喷氢量由ECU调控,从而在进气通道内实现反应活性可调控的氨氢融合燃料;另一部分供给至湍流射流点火装置6,即由第二氢气喷射器15喷入预燃室内腔11,所述空气喷射器和第二氢气喷射器分别向所述预燃室内腔喷射新鲜空气和氢气,在预燃室内部形成当量混合气,而后由火花塞12点燃,在主燃烧室2中形成射流火焰7,而后点燃主燃烧室2氨氢融合燃料,完成燃烧做功。其中,当所述ECU控制所述湍流射流点火装置为双喷射模式时,空气喷射器13向预燃室内腔11中喷射新鲜空气,同时,当所述ECU控制所述湍流射流点火装置为扫气模式时,只有所述空气喷射器13向预燃室内腔喷射新鲜空气,对预燃室进行扫气。在主燃烧室2混合气过浓或者发动机工作在高EGR率工况时,该扫气过程可消除主燃烧室2中氨气或废气对预燃室氢气/空气混合气着火及燃烧的影响,进而保证射流点火强度,最终实现发动机稳定着火。
同时发动机余热用于向车载氨制氢装置供热,也可以通过安装的电加热装置进行热量供给。图1中虚线表示ECU接收或发出的信号的传递路线。
实施例2
与实施例1结构类似,只是所述湍流射流点火装置6结构略有不同。以下只描述其区别特征。
所述湍流射流点火装置6配置夹气喷射预燃室形成具有扫气过程的湍流射流点火装置,具有两种工作模式,分别是夹气喷射模式和扫气模式。所述湍流射流点火装置包括火花塞16,第二氢气喷射器17,高压预混腔18,进气口19,电磁阀20,和预燃室内腔21。如图4所示,包括一壳体,所述壳体底部通过螺纹安装于发动机缸盖9上;所述壳体内部从上至下依次安装有第二氢气喷射器17、高压预混腔18和电磁阀20;所述高压预混腔18侧壁连通一进气口19,用于将高压空气与来自第二氢气喷射器17的氢气在其中进行预混;所述壳体下部形成一预燃室内腔21,一火花塞16安装在壳体内,所述火花塞16的电极及所述电磁阀20底部的出口伸入预燃室内腔中;所述壳体底部开有射流孔,所述射流孔用于实现火焰加速传播,提高燃烧速率,进而提高发动机的经济性。
其工作过程为:所述ECU控制所述湍流射流点火装置为夹气喷射模式时,车载制氢装置制备的氢气一部分由所述第一氢气喷射器5喷入进气通道,另一部分供给第二氢气喷射器17,来自所述第二氢气喷射器17的氢气与来自进气口19的高压空气在所述高压预混腔18内进行预混,形成当量均质预混气,而后均质预混气由电磁阀20喷入预燃室内腔21,而后由火花塞16点燃,在主燃烧室2中形成射流火焰7,而后点燃主燃烧室2氨氢融合燃料,完成燃烧做功。所述ECU控制所述湍流射流点火装置为扫气模式时,所述电磁阀喷射两次,第一次向预燃室内腔21喷射新鲜空气,对预燃室内腔21进行扫气;而后,第二氢气喷射器17中氢气和高压空气在高压预混腔18内混合后形成混合气,由电磁阀第二次喷射进入预燃室内腔21。
以上实施例仅用以说明本发明的技术方案,而非是对其的限制,尽管参照前述各实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解,其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分或者全部技术特征进行等同替换,而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的范围,本领域技术人员根据本说明书内容所做出的非本质改进和调整或者替换,均属本发明所要求保护的范围。
Claims (7)
1.一种基于反应活性调控的氨氢融合燃料控制系统,其特征在于,包括车载氨氢燃料供给系统、氨氢融合燃料预混燃烧发动机和ECU;
所述ECU用于控制氨氢融合燃料预混燃烧发动机和车载氨氢燃料供给系统,调控待进入氨氢融合燃料预混燃烧发动机的氨燃料和氢气的喷气量及压力值;
所述车载氨氢燃料供给系统包括低压液氨供给单元和车载制氢单元,用于向所述氨氢融合燃料预混燃烧发动机提供制备的低压氨燃料和氢气;其中所述低压液氨供给单元用于提供压力范围为0.5~1MPa的氨燃料,所述车载制氢单元用于提供压力范围为1.0~2.0MPa的氢气;
所述氨氢融合燃料预混燃烧发动机包括发动机缸盖(9)、缸套(10)、活塞(1)、主燃烧室(2)、进气通道、排气通道,还包括设置在缸盖上带有预燃室的湍流射流点火装置(6);其中,所述进气通道上分别设置有朝向所述缸盖(9)的氨喷射器(4)和第一氢气喷射器(5),喷入进气通道的氨燃料和氢气在进气通道内形成氨氢融合燃料;所述湍流射流点火装置(6)用于实现空气和氢气单独喷射的双喷射模式和空气单独喷射的扫气模式,或氢气-空气混合气喷射的夹气喷射模式以及利用氢气-空气混合气喷射的扫气模式;
所述控制系统的工作过程包括:低压液氨供给单元在ECU的调控下生成压力为0.5~1.0MPa的氨燃料,随后制备的氨燃料分为两路,一部分经管道进入氨喷射器(4),一部分进入车载制氢单元参与制取氢气;所述车载制氢单元在ECU调控下生成压力为1.0~2.0MPa的氢气,随后氢气分为两路,一部分由所述第一氢气喷射器(5)喷入进气通道,进气通道喷射的氢气与氨燃料混合后在进气通道内形成氨氢融合燃料,其中第一氢气喷射器(5)的喷氢量由ECU调控,从而在进气通道内实现反应活性可调控的氨氢融合燃料;另一部分供给至湍流射流点火装置(6),并在预燃室内腔(11)中被火花塞(12)点燃,在主燃烧室(2)中形成射流火焰(7),而后在主燃烧室(2)内点燃氨氢融合燃料,完成燃烧做功。
2.根据权利要求1所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,所述低压液氨供给单元包括依次连接的氨存储罐、加热器、稳压罐和压力控制器,所述氨存储罐中装有液氨;所述车载制氢单元包括依次连接的车载制氢装置、高压储氢罐和压力控制器。
3.根据权利要求1所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,一进气阀(3)设置在进气通道内,一排气阀(8)设置在排气通道内,且进气阀和排气阀分别设置在缸盖(9)的左右两侧,所述进气阀(3)和排气阀(8)用于结合发动机的节气门装置,改变进气量。
4.根据权利要求2所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,所述湍流射流点火装置(6)包括预燃室内腔(11)、火花塞(12)、空气喷射器(13)和第二氢气喷射器(15);所述空气喷射器(13)的喷嘴伸入预燃室内腔(11)用于向预燃室内腔(11)喷射空气,所述第二氢气喷射器(15)的喷嘴伸入预燃室内腔(11)用于向预燃室内腔(11)喷射氢气;所述火花塞、所述空气喷射器的喷嘴和第二氢气喷射器的喷嘴设置在所述预燃室的同一侧;所述湍流射流点火装置(6)底部开有射流孔,所述预燃室内腔与主燃烧室通过射流孔相通;所述湍流射流点火装置(6)具有两种工作模式,分别是双喷射模式和扫气模式;
当所述ECU控制所述湍流射流点火装置(6)为双喷射模式时,所述空气喷射器(13)和第二氢气喷射器分别向所述预燃室内腔(11)喷射新鲜空气和氢气,用于在预燃室内部形成当量混合气;
当所述ECU控制所述湍流射流点火装置(6)为扫气模式时,只有所述空气喷射器向预燃室内腔(11)喷射新鲜空气,对预燃室进行扫气。
5.根据权利要求2所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,所述湍流射流点火装置(6)包括预燃室内腔(21)、火花塞(16)、第二氢气喷射器(17);所述第二氢气喷射器(17)向下依次安装有高压预混腔(18)和电磁阀(20),所述电磁阀(20)底部的喷嘴伸入预燃室内腔(21)用于向预燃室内腔(21)喷射氢气;所述高压预混腔(18)侧壁连通一进气口(19),用于将高压空气与来自第二氢气喷射器(17)的氢气在其中进行预混;所述火花塞的喷嘴伸入所述预燃室内腔(21)中;所述湍流射流点火装置(6)底部开有射流孔,所述预燃室内腔(21)与主燃烧室通过射流孔相通;所述湍流射流点火装置(6)具有两种工作模式,分别是夹气喷射模式和扫气模式;
所述ECU控制所述湍流射流点火装置(6)为夹气喷射模式时,所述第二氢气喷射器中氢气和高压空气在高压预混腔(18)内混合后由电磁阀喷射空气和氢气的混合气,用于在预燃室内部形成当量混合气;
所述ECU控制所述湍流射流点火装置(6)为扫气模式时,所述电磁阀喷射两次,第一次向预燃室内腔喷射新鲜空气,对预燃室进行扫气;而后,第二氢气喷射器中氢气和高压空气在高压预混腔内混合后形成混合气,由电磁阀第二次喷射进入预燃室。
6.根据权利要求1所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,所述氨喷射器(4)为液氨低压喷射器,所述第一氢气喷射器(5)具有一氢气低压喷嘴。
7.根据权利要求2所述的基于反应活性调控的氨氢融合燃料控制系统,其特征在于,所述车载氨制氢装置由所述氨氢融合燃料预混燃烧发动机的发动机余热加热,或是单独安装电加热装置进行热量供给。
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