CN1181903C - 一种三导向阀塔盘 - Google Patents

一种三导向阀塔盘 Download PDF

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CN1181903C
CN1181903C CNB021599289A CN02159928A CN1181903C CN 1181903 C CN1181903 C CN 1181903C CN B021599289 A CNB021599289 A CN B021599289A CN 02159928 A CN02159928 A CN 02159928A CN 1181903 C CN1181903 C CN 1181903C
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潘国昌
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Beijing Zehua Chemical Engineering Co ltd
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BEIJING ZEHUA CHEMICAL ENGINEERING Co Ltd
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Abstract

一种三导向阀塔盘,涉及炼油、化工设备技术领域。本发明的特征是浮阀或固定阀在塔板上的布置为:每排阀体的中心连线均与进口堰平行,靠近进口堰的第一排阀的舌孔的喷射方向一致且进口堰平行,第二排阀的舌孔喷射方向与第一排相反,第三排阀的舌孔喷射方向指向降液管方向,然后依次类推。本发明与传统的塔盘相比其优点是:该塔盘可使从阀喷出的部分气流除推动液体向降液管方向运动以外,还交错地推动液体向左右两侧运动并防止其对冲,因而增加了液体在塔板上的停留时间;加强垂直于液流方向上液体的混和与交换;消除塔板上液体的停滞区、回流区,使塔板上喷动的液层高度均匀,减少液沫夹带,提高塔板的气速上限,从而具有高效率与高生产能力。

Description

一种三导向阀塔盘
技术领域
本发明涉及一种用于炼油、石化、化学工业等领域中蒸馏、吸收过程的重要设备—塔盘,特别涉及一种三导向阀塔盘的结构设计。
背景技术
在炼油、石化、化学等工业中,塔盘是分离混合物的重要设备、对其产品的产量、质量、能耗、成本等起重要作用。目前,国内外应用最广泛的塔盘技术是传统的F1(V1)型塔盘(如图1所示),但它已不能满足目前增产、提质、降耗等要求,该种塔盘存在的问题有:①当提高负荷时,阀孔间的气流对冲后向上喷射,使液沫夹带增加,效率下降;控制了生产能力的提高;②气流向阀四周辐射,使液体返混增加,使效率下降;③液体自弓形降液管流入塔盘后,分布很不均匀,中部流速高,两侧弧形区形成回流和停滞区域,降低了塔板效率;④液体入口区易漏液,塔板上液面不均;⑤浮阀易旋转、脱落而严重影响塔板上的操作。凡此种种都影响到塔盘的通量与效率,对分离过程产生不利影响。
近年来,为了克服以上缺点,国内曾提出了导向浮阀的概念,它利用阀体喷出气流的动能,定向地推动液体向降液管方向运动,从而可以降低塔板上的液层高度,减少返混,使塔板性能得到一定程度的提高,但是过度推液将使塔板上液面出现负梯度,甚至高气速下将液体抛向空中,液体在塔板上停留时间减少,效率下降,而且均匀的推液作用对塔板上液体流动的不均匀性减少不大,所以现有技术中各种导向浮阀对塔盘的通量与效率提高不多。
发明内容
针对现有技术存在的问题,本发明的目的是提供一种三导向阀塔盘,该塔盘可使从阀喷出的部分气流除推动液体向降液管方向运动以外,还交错地推动液体向左右两侧运动并防止其对冲,使液体在塔板上的停留时间增加,加强垂直于液流方向上液体的混和与交换、消除回流区、减少液沫夹带,从而进一步提高塔盘的通量、效率和生产能力。
本发明是通过如下技术方案实现的:一种三导向阀塔盘,它主要由塔板、设置在塔板上的多排圆形浮阀或固定阀、阀孔、降液管、受液盘以及进口堰组成,在所述阀的阀面上冲有1~3个舌孔,其特征在于:所述多排阀在塔板上的排列及布置如下:每排阀体的中心连线均与进口堰平行,靠近进口堰的第一排阀的舌孔喷射方向一致且与进口堰平行,第二排阀的舌孔喷射方向与第一排相反,第三排阀的舌孔喷射方向指向降液管方向,第四排舌孔喷射方向同第一排,第五排舌孔喷射方向同第二排,第六排舌孔喷射方向同第三排,然后依次类推。
本发明所述的浮阀阀面为圆形,有两个垂直于阀面且其宽度不相等的阀腿;所述的阀孔为圆形,其两侧各有一个用于放置阀腿的宽缺口和窄缺口,所述的每排阀孔上的窄缺口的排列方向与所对应的浮阀上的舌孔喷射方向一致。所述的宽阀腿的宽度为10~12mm,高度10~20mm,窄阀腿的宽度较宽阀腿的宽度窄5~6mm,高度高0~4mm,所述的窄阀腿所在位置与舌孔喷射方向一致。
本发明所述的浮阀还可设置3个阀腿,即设置一个宽阀腿和两个相等的窄阀腿,宽阀腿的宽度较两个窄阀腿宽5~10mm,高度小0~5mm;所述宽阀腿所在位置与所述浮阀上的舌孔喷射方向相反;该阀所对应的阀孔为园形,在阀孔上设有限制阀转动的两个突起,该突起位置与所述阀面上舌孔喷射方向一致;所述两个突起的排列位置为:靠近进口堰的第一排阀孔的突起位置指向与进口堰方向平行,第二排阀孔的突起位置与第一排位置相反,第三排阀孔的突起位置指向降液管,第四排同第一排,第五排同第二排,第六排同第三排,然后依次类推。
本发明所述的阀可以是固定阀,所述的固定阀的阀体为圆形,阀面上有1~3个舌孔,均由塔板冲制而成,阀上有2个宽度不相等的阀腿且与塔板固定,宽阀腿的宽度为10~12mm,窄阀腿的宽度较宽阀腿窄5~6mm,高度高0~4mm,所述的窄阀腿的位置与所述固定阀上的舌孔喷射方向一致。
上述固定阀还可设置3个阀腿,即一个宽阀腿和两个相等的窄阀腿,所述阀腿与塔板固定,宽阀腿的宽度较两个窄阀腿宽5~6mm,高度小0~4mm,所述宽阀腿所在的位置与所述固定阀上的舌孔喷射方向相反。
本发明与现有塔盘相比,具有以下优点及突出性进步:①增加了液体在塔板上的停留时间,有利于提高塔板效率;②加强了垂直于液流方向上液体的混和与交换,使液体在塔板上的停留时间均匀;③消除塔板上液体的停滞区域,消除回流区;④使塔板上喷动的液层高度均匀,从而可以减少液沫夹带,提高塔板的气速上限,从而具有较高效率与高生产能力。
附图说明
图1为传统的F1浮阀立体图。
图2为F1浮阀塔盘上液流分布示意图。
图3为本发明提供的三导向阀塔盘原理示意图。
图4为三导向圆形浮阀塔盘上阀孔及阀面的排列布置图。
图5为本发明的一个实施例的结构示意图,即浮阀有一个舌孔、两个宽窄不等的阀腿,阀孔两侧各有一个缺口。
图6为本发明的另一个实施例的结构示意图,浮阀有3个舌孔、3个阀腿,阀孔两侧各有一个突起。
图7为三导向3腿浮阀塔盘的阀面及阀孔的排列布置图。
图8为本发明采用固定阀的三导向阀塔盘的一个实施例的结构示意图。
图9为三导向3腿浮阀(3D-ADV+)与F1浮阀的夹带率ev%比较图。
图10为三导向3腿浮阀(3D-ADV+)与F1浮阀上限负荷因子Cb的比较图。
图11为三导向浮阀与F1塔盘的压强Δp比较图。
图12为三导向浮阀与F1盘的氧解吸收率比较图。
具体实施方式
下面结合附图对本发明做进一步的说明。
图3为本发明提供的三导向阀塔盘原理示意图,它主要由塔板1、降液管2、受液盘3、进口堰4,设置在塔板上的多排圆形浮阀或固定阀6及阀孔5组成,多排阀在塔板1上的排列及布置如下:每排阀体的中心连线均与进口堰4平行,靠近进口堰的第一排阀的舌孔的喷射方向一致且与进口堰4平行,第二排阀的舌孔喷射方向与第一排相反,第三排阀的舌孔喷射方向指向降液管方向,第四排舌孔喷射方向同第一排,第五排同第二排,第六排同第三排,然后依次类推。液体从受液盘3经过进口堰(或鼓泡促进器)4进入塔板1,在塔板上与阀孔5上升的气流接触形成鼓泡层,气流经浮阀的作用部分动能推动液体向左右(7、8)方向运动,另有部分浮阀推动液体向降液管2方向流动,从而形成三导向阀塔盘。
图4为三导向圆形浮阀塔盘上阀孔及阀面的排列布置图,图中每排三导向阀的中心连线与进口堰4(鼓泡促进器)平行,沿进口堰4的第一排51的阀孔的窄缺口48向右,而与之相邻的第二排52的窄缺口向左;相应地,阀面上舌片45的指向和窄缺口48一致,即以上两排阀的推液方向分别导向塔盘的左右侧,第三排阀53的窄缺口48指向降液管2的方向,它推动液体向降液管2方向流动,其余依次类推。
图5为本发明三导向浮阀的一个实施例,直径为25~50mm的圆形阀面41上设有一个舌片45,其一端和阀面41相连,舌片高于阀面1~5mm,阀体两侧各有一个垂直于阀面且宽度不相等的阀腿42、43,宽阀腿42的宽度为10~12mm,高度10~20mm,窄阀腿43的宽度较宽阀腿42的宽度窄5~6mm,高度高0~4mm。阀孔49为圆形,阀孔两侧各有一个放置阀腿的缺口47、48,缺口宽度较阀腿宽1~2mm。安装时将两个阀腿分别置于两个缺口内,窄阀腿43弯折90°,将阀体安装在阀孔中,窄阀腿所在位置应与舌孔喷射方向一致;阀体可以上下浮动而不能旋转,该浮阀的部分气流将推动液流向窄腿43方向流动,即气流的推液方向与小缺口48的方向一致。
图6为本发明的另一个实施例的结构示意图,浮阀设有3个舌孔,3个阀腿,阀孔两侧各有一个突起。阀面61为圆形,有一个宽阀腿62,两个较窄的阀腿63,其中宽阀腿的宽度较其它两个窄阀腿宽5~10mm,高度小0~5mm。阀面上设有三个舌片65和相应的舌孔64,所述宽阀腿所在位置与所述浮阀上的舌孔喷射方向相反,舌片起导流作用。阀孔68为圆形,两侧(与窄阀腿相邻处)各有一个突起67,突起的作用是放置阀面旋转,同时有定向作用,即保证每排阀的舌片65的方向一致。
图7为上述三导向浮阀塔盘的阀面61及阀孔68的排列布置图。靠近进口堰4的第一排71阀孔的突起67的位置与所述浮阀上的舌孔喷射方向一致且与进口堰平行,即沿74所示的方向;第二排阀孔的突起位置与第一排位置相反,即沿75所指的方向;第三排73阀孔的突起位置指向降液管2的方向76,第四排同第一排,第五排同第二排,第六排同第三排,然后依次类推。
图8为本发明采用固定阀的三导向阀塔盘的一个实施例的结构示意图,它的阀面81与三导向浮阀相同,也有1~3各舌片85和舌孔84,该固定阀的阀面81是由塔板本身冲出,阀上有2个宽度不相等的阀腿82、83,也是由塔板冲出,阀面81通过阀腿82、83与塔板1连接在一起。宽阀腿的宽度为10~12mm,窄阀腿的宽度较宽阀腿窄5~6mm,高度高0~4mm,所述的窄阀腿的位置与所述固定阀上的舌孔喷射方向一致。气流由阀孔87冲出,经舌片、阀腿和阀面的作用,也有部分气流推动液体向舌孔方向86流动。
本发明中的固定阀还可设置3各阀腿,即一个宽阀腿和两个相等的窄阀腿,宽阀腿的宽度较两个窄阀腿宽5~10mm,高度小0~5mm,所述宽阀腿所在的位置与所述固定阀上的舌孔喷射方向相反。
实施例
直径1.2mm的试验塔,内有三块塔板,下层为气体分布板,中层为试验板,上层为液沫夹带收集板。试验板为三导向3腿浮阀塔盘及F1型浮阀塔盘。技术参数如下:弓形降液管宽200mm,降液管占塔截面11%;出口堰长890mm,堰高50mm;三导向浮阀开孔率17.7%;空气速度0.8~3.6m/s;水流量:8~112m3/h;
对二种塔盘在同样条件下进行了对比试验,测定其液沫夹带率,压降以及氧解吸效率,对比实验数据如图9、图10、图11和图12。
由以上曲线图可以看出,三导向3腿浮阀塔盘的生产能力(即上限负荷因子Cb)较F1浮阀塔盘平均提高了30%~40%,压降平均下降了28%,泄漏下降了30%,效率平均提高了20%。

Claims (5)

1.一种三导向阀塔盘,它主要由塔板(1)、设置在塔板上的多排圆形浮阀或固定阀(6)、阀孔(5)、降液管(2)、受液盘(3)以及进口堰(4)组成,在所述阀的阀面上冲有1~3个舌孔,其特征在于:所述的多排阀在塔板上的排列及布置如下:每排阀体的中心连线均与进口堰(4)平行,靠近进口堰的第一排阀的舌孔喷射方向一致且与进口堰平行,第二排阀的舌孔喷射方向与第一排相反,第三排阀的舌孔喷射方向指向降液管方向,第四排舌孔喷射方向同第一排,第五排舌孔喷射方向同第二排,第六排舌孔喷射方向同第三排,然后依次类推。
2.按照权利要求1所述的三导向阀塔盘,其特征在于:所述的浮阀有两个垂直于阀面且其宽度不相等的阀腿;所述的宽阀腿的宽度为10~12mm,高度10~20mm,窄阀腿的宽度较宽阀腿的宽度窄5~6mm,高度高0~4mm,所述的窄阀腿所在位置与舌孔喷射方向一致;所述的阀孔为圆形,其两侧各有一个用于放置该阀腿的宽缺口和窄缺口,所述的每排阀孔上的窄缺口的排列方向与所述浮阀上的舌孔喷射方向一致。
3.按照权利要求1所述的三导向阀塔盘,其特征在于:所述的圆形浮阀设有一个宽阀腿和两个相等的窄阀腿,所述的宽阀腿的宽度较其它两个窄阀腿宽5~6mm,高度小0~4mm;所述宽阀腿所在位置与所述浮阀上的舌孔喷射方向相反;所述的阀孔为圆形,在阀孔上设有限制阀转动的两个突起,该突起位置与所述阀面上舌孔喷射方向一致;所述两个突起的排列位置为:靠近进口堰的第一排阀孔的突起位置指向与进口堰方向平行,第二排阀孔的突起位置与第一排位置相反,第三排阀孔的突起位置指向降液管,第四排同第一排,第五排同第二排,第六排同第三排,然后依次类推。
4.按照权利要求1所述的三导向阀塔盘,其特征在于:所述的固定阀的阀体是由塔板冲制而成,阀上有2个宽度不相等的阀腿且与塔板固定,宽阀腿的宽度为10~12mm,窄阀腿的宽度较宽阀腿窄5~6mm,高度高0~4mm,所述的窄阀腿的位置与所述固定阀上的舌孔喷射方向一致。
5.按照权利要求1所述的三导向阀塔盘,其特征在于:所述的固定阀的阀体是由塔板冲制而成,阀上设有一个宽阀腿和两个相等的窄阀腿,所述阀腿与塔板固定,宽阀腿的宽度较两个窄阀腿宽5~10mm,高度小0~5mm,所述宽阀腿所在的位置与所述固定阀上的舌孔喷射方向相反。
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