CN107270427A - 一种带热回收功能的新型溶液调湿新风机组 - Google Patents
一种带热回收功能的新型溶液调湿新风机组 Download PDFInfo
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Abstract
本发明涉及一种带热回收功能的新型溶液调湿新风机组,主要包括溶液模块、制冷系统、全热回收单元、加湿模块。该装置最大特点是无需外接冷热源,仅需补充自来水,不仅可以提供室内需要的新风,而且新风还承担室内的湿负荷和部分显热负荷;并且利用盐溶液高效杀菌的特点,为室内提供干净新风;等焓除湿过程,提高制冷效率。
Description
技术领域
本发明涉及一种溶液式空气处理装置,尤其是涉及一种带热回收功能的新型溶液调湿新风机组。
背景技术
人类至少70%以上的时间在室内度过,但是室内空气污染物的浓度一般是室外污染物浓度的2-5倍,在某些情况下是室外污染物的几十甚至上百倍。这些污染物是呼吸道疾病、肺癌、哮喘等疾病的诱因。室内污染已成为了人们身边潜伏的隐形杀手。
目前市面上的新风机组只有过滤PM2.5和热交换的功能,不具备杀菌和除(加)湿功能,而且静电杀菌会产生臭氧,降低室内空气品质,对室内温湿度控制精度低。
现有的溶液调湿空调中,目前技术比较成熟、应用范围比较广的是热泵式溶液调湿空调,然而热泵式溶液调湿空调机组结构复杂,造价高,体积庞大,对机房要求较高,安装不够灵活,不适用于小空间建筑项目。
发明内容
为解决上述技术问题,本发明的目的是提供本发明的目的在于提供一种新型带热回收的溶液调湿新风机组,属于调湿空调领域,尤其是溶液式空气处理装置领域。
本发明的技术方案如下:
一种带热回收功能的新型溶液调湿新风机组,其特征在于:包括溶液模块、制冷系统、全热回收单元、加湿模块;
所述溶液模块包括再生溶液模块、除湿溶液模块;
所述制冷系统包括制冷系统Ⅰ及制冷系统Ⅱ,
其中制冷系统Ⅰ包括压缩机Ⅰ、冷凝器Ⅰ、膨胀阀Ⅰ、蒸发器Ⅰ,其中所述蒸发器Ⅰ和冷凝器Ⅰ通过两条管路相连,所述膨胀阀Ⅰ设置在其中一条管路上,所述压缩机Ⅰ设置在另一条管路上;
制冷系统Ⅱ包括压缩机Ⅱ、水-板式换热器、冷凝器Ⅱ、膨胀阀Ⅱ及蒸发器Ⅱ,其中所述蒸发器Ⅱ和冷凝器Ⅱ通过两条管路相连,所述膨胀阀Ⅱ设置在其中一条管路上,所述水-板式换热器和压缩机Ⅱ设置在另一条管路上,所述压缩机Ⅱ靠近所述蒸发器Ⅱ设置;
所述全热回收单元包括全热回收型转轮热交换器;所述加湿模块包括水加湿模块;
所述全热回收型转轮热交换器、所述蒸发器Ⅰ、蒸发器Ⅱ、所述除湿溶液模块形成室外新风通道,室外新风依次经过所述全热回收型转轮热交换器、所述蒸发器Ⅰ、蒸发器Ⅱ、所述除湿溶液模块进入室内;
所述全热回收型转轮热交换器、所述冷凝器Ⅰ、所述再生溶液模块、所述水加湿模块、所述冷凝器Ⅱ形成排风通道,室内回风依次经过所述全热回收型转轮热交换器、所述冷凝器Ⅰ、所述再生溶液模块、所述水加湿模块、所述冷凝器Ⅱ排出。
进一步的,所述溶液模块还包括与再生溶液模块、除湿溶液模块配套的溶液泵、溶液槽和管路,所述再生溶液模块的底部再生溶液槽内的溶液通过管路流到溶液槽,利用第一溶液泵与安装在再生溶液模块上部的第一布液管相连;所述除湿溶液模块的底部除湿溶液槽通过第二溶液泵与安装在除湿溶液模块上部的第二布液管相连;所述溶液槽、除湿溶液槽的溶液通过第三溶液泵进行循环。
进一步的,在制冷系统中,其中制冷系统Ⅰ所述压缩机Ⅰ中的制冷剂依次流经压缩机Ⅰ、冷凝器Ⅰ、膨胀阀Ⅰ、蒸发器Ⅰ,然后回到压缩机Ⅰ,完成循环;所述蒸发器Ⅰ内的制冷剂循环通路的出口通过管路与压缩机Ⅰ的入口相连,压缩机Ⅰ的出口通过管路与所述冷凝器Ⅰ的制冷剂循环通路的入口相连,所述冷凝器Ⅰ的制冷剂循环通路的出口通过管路与膨胀阀Ⅰ的入口相连,膨胀阀Ⅰ的出口通过管路与所述蒸发器Ⅰ的制冷剂循环通路的入口相连。制冷系统Ⅱ所述压缩机Ⅱ中的制冷剂依次流经压缩机Ⅱ、水-板式换热器、冷凝器Ⅱ、膨胀阀Ⅱ、蒸发器Ⅱ,然后回到压缩机Ⅱ,完成循环;所述蒸发器Ⅱ内的制冷剂循环通路的出口通过管路与压缩机Ⅱ的入口相连,压缩机Ⅱ的出口通过管路与所述水-板式换热器及冷凝器Ⅱ的制冷剂循环通路的入口相连,所述水-板式换热器及冷凝器Ⅱ的制冷剂循环通路的出口通过管路与膨胀阀Ⅱ的入口相连,膨胀阀Ⅱ的出口通过管路与所述蒸发器Ⅱ的制冷剂循环通路的入口相连。
进一步的,在全热回收单元中,所述全热回收型转轮热交换器与室内回风进行热质交换,转轮吸收室内回风的冷量并将水分排到排风中,之后旋转至新风侧,与新风进行热质交换,对新风进行预冷预除湿;而与转轮进行过热质交换的排风则被排出。
进一步的,所述加湿模块中,利用循环水带走水-板式换热器的冷凝热,经过水-板式换热器的水利用水加湿模块对经过再生模块后的室内回风进行降温加湿处理,水加湿模块工作的时候,需要对水加湿模块的水槽进行补水。
进一步的,所述再生溶液模块和除湿溶液模块利用盐溶液表面与空气中的水蒸气分压力差进行热湿交换,利用不同浓度溶液的吸湿特性实现对空气的除湿处理;高温潮湿的室外新风首先经过所述全热回收型转轮热交换器与低温低湿的室内回风进行全热交换,新风空气被降温除湿,经过降温除湿过程后的室外新风再经过所述蒸发器Ⅰ、蒸发器Ⅱ进一步的进行深度的降温除湿;最后,经过深度降温除湿的新风经过所述溶液除湿模块进行等焓升温除湿,已到满足室内送风要求状态点;低温低湿的室内回风依次经过所述全热回收型转轮热交换器,空气被升温加湿,经过升温加湿的室内回风经过所述冷凝器Ⅰ,吸收冷凝器Ⅰ排放的冷凝热,温度升高,然后经过所述溶液再生模块进行等焓降温加湿,再经过所述水加湿模块进行降温加湿、最后室内回风吸收所述冷凝器Ⅱ排放的冷凝热,温度升高,而后排出。
进一步的,所述再生溶液模块、除湿溶液模块及水加湿模块结构一致,里面填料均由无纺布和ABS材料高温融合而成,采用瓦楞形状叠加在一起,保证溶液及水不被风带出来;外框使用ABS材料,模具一体化成型;里面循环的盐溶液采用水溴化锂、氯化钙或者氯化锂,循环亦可采用水。
借由上述方案,本发明至少具有以下优点:
除湿效率高,灭杀空气中有害病菌,结构紧凑,造价低,体积较小,较传统的热泵式溶液调试新风机组在施工安装等方面更有优势。
附图说明
图1、本发明的主要结构示意图。
具体实施方式
下面结合附图和实施例,对本发明的具体实施方式作进一步详细描述。以下实施例用于说明本发明,但不用来限制本发明的范围。
如图1所示,所述新型带热回收的溶液调湿新风机组,以其典型形式为例,主要含有溶液模块、制冷系统、全热回收单元、加湿模块。所述溶液模块包括再生溶液模块8、除湿溶液模块4与之配套的第一溶液泵17、第二溶液泵21、第三溶液泵16、溶液槽18和管路;所述制冷系统包括制冷系统Ⅰ及制冷系统Ⅱ,其中制冷系统Ⅰ包括压缩机Ⅰ12、冷凝器Ⅰ7、膨胀阀Ⅰ13、蒸发器Ⅰ2;制冷系统Ⅱ包括压缩机Ⅱ14、水-板式换热器20、冷凝器Ⅱ10、膨胀阀Ⅱ15及蒸发器Ⅱ3及与之配套的管路。
室外新风首先通过全热回收型转轮热交换器1进行全热交换,对新风进行预冷除湿,之后经过蒸发器Ⅰ2与蒸发器Ⅱ3,进一步的进行深度的降温除湿,经过深度降温除湿的新风再经过所述溶液除湿模块4进行等焓升温除湿,已到满足室内送风要求状态点;由离心式送风机5送入室内;低温低湿的室内回风由回风机6吸入,依次经过所述全热回收型转轮热交换器1,空气被升温加湿,经过升温加湿的室内回风经过所述冷凝器Ⅰ7,吸收冷凝器Ⅰ7排放的冷凝热,温度升高,然后经过所述溶液再生模块8进行等焓降温加湿,再经过所述水加湿模块9进行降温加湿、最后室内回风吸收所述冷凝器Ⅱ10排放的冷凝热,温度升高,而后排出。
所述溶液模块主要由再生溶液模块8、除湿溶液模块4与之配套的第一溶液泵17、第二溶液泵21、第三溶液泵16、溶液槽18和管路组成;室外新风首先通过全热回收型转轮热交换器1进行全热交换,对新风进行预冷除湿,之后经过蒸发器Ⅰ2与蒸发器Ⅱ3,进一步的进行深度的降温除湿,经过深度降温除湿的新风再经过所述溶液除湿模块4进行等焓升温除湿,已到满足室内送风要求状态点;低温低湿的室内回风由回风机6吸入,依次经过所述全热回收型转轮热交换器1,空气被升温加湿,经过升温加湿的室内回风经过所述冷凝器Ⅰ7,吸收冷凝器Ⅰ7排放的冷凝热,温度升高,然后经过所述溶液再生模块8,将被稀释的溶液浓缩再生,变成高温高湿的空气,而后排出;再生溶液模块8的底部再生溶液槽8-1内的溶液通过管路流到溶液槽18,利用第一溶液泵17与安装在再生溶液模块上部的第一布液管8-2相连;除湿溶液模块4底部除湿溶液槽4-1通过管路及第二溶液泵21与安装在除湿溶液模块上部的布液管4-3相连;再生溶液模块8底部再生溶液槽8-2通过管路使溶液流入溶液槽18,第三溶液泵16将溶液槽18内的溶液与除湿溶液槽4-1内的溶液进行循环。
所述冷系统中,其中制冷系统Ⅰ所述压缩机Ⅰ12中的制冷剂依次流经压缩机Ⅰ12、冷凝器Ⅰ7、膨胀阀Ⅰ13、蒸发器Ⅰ2,然后回到压缩机Ⅰ12,完成循环;所述蒸发器Ⅰ2内的制冷剂循环通路的出口通过管路与压缩机Ⅰ12的入口相连,压缩机Ⅰ12的出口通过管路与所述冷凝器Ⅰ7的制冷剂循环通路的入口相连,所述冷凝器Ⅰ7的制冷剂循环通路的出口通过管路与膨胀阀Ⅰ13的入口相连,膨胀阀Ⅰ13的出口通过管路与所述蒸发器Ⅰ2的制冷剂循环通路的入口相连。制冷系统Ⅱ所述压缩机Ⅱ14中的制冷剂依次流经压缩机Ⅱ14、水-板式换热器20、冷凝器Ⅱ10、膨胀阀Ⅱ15、蒸发器Ⅱ3,然后回到压缩机Ⅱ14,完成循环;所述蒸发器Ⅱ3内的制冷剂循环通路的出口通过管路与压缩机Ⅱ14的入口相连,压缩机Ⅱ14的出口通过管路与所述水-板式换热器20及冷凝器Ⅱ10的制冷剂循环通路的入口相连,所述水-板式换热器20及冷凝器Ⅱ10的制冷剂循环通路的出口通过管路与膨胀阀Ⅱ15的入口相连,膨胀阀Ⅱ15的出口通过管路与所述蒸发器Ⅱ3的制冷剂循环通路的入口相连。
本发明至少具有以下优点:
除湿效率高,灭杀空气中有害病菌,结构紧凑,造价低,体积较小,较传统的热泵式溶液调试新风机组在施工安装等方面更有优势。
以上所述仅是本发明的优选实施方式,并不用于限制本发明,应当指出,对于本技术领域的普通技术人员来说,在不脱离本发明技术原理的前提下,还可以做出若干改进和变型,这些改进和变型也应视为本发明的保护范围。
Claims (7)
1.一种带热回收功能的新型溶液调湿新风机组,其特征在于:包括溶液模块、制冷系统、全热回收单元、加湿模块;
所述溶液模块包括再生溶液模块、除湿溶液模块;
所述制冷系统包括制冷系统Ⅰ及制冷系统Ⅱ,
其中制冷系统Ⅰ包括压缩机Ⅰ、冷凝器Ⅰ、膨胀阀Ⅰ、蒸发器Ⅰ,其中所述蒸发器Ⅰ和冷凝器Ⅰ通过两条管路相连,所述膨胀阀Ⅰ设置在其中一条管路上,所述压缩机Ⅰ设置在另一条管路上;
制冷系统Ⅱ包括压缩机Ⅱ、水-板式换热器、冷凝器Ⅱ、膨胀阀Ⅱ及蒸发器Ⅱ,其中所述蒸发器Ⅱ和冷凝器Ⅱ通过两条管路相连,所述膨胀阀Ⅱ设置在其中一条管路上,所述水-板式换热器和压缩机Ⅱ设置在另一条管路上,所述压缩机Ⅱ靠近所述蒸发器Ⅱ设置;
所述全热回收单元包括全热回收型转轮热交换器;所述加湿模块包括水加湿模块;
所述全热回收型转轮热交换器、所述蒸发器Ⅰ、蒸发器Ⅱ、所述除湿溶液模块形成室外新风通道,室外新风依次经过所述全热回收型转轮热交换器、所述蒸发器Ⅰ、蒸发器Ⅱ、所述除湿溶液模块进入室内;
所述全热回收型转轮热交换器、所述冷凝器Ⅰ、所述再生溶液模块、所述水加湿模块、所述冷凝器Ⅱ形成排风通道,室内回风依次经过所述全热回收型转轮热交换器、所述冷凝器Ⅰ、所述再生溶液模块、所述水加湿模块、所述冷凝器Ⅱ排出。
2.根据权利要求1所述的带热回收功能的新型溶液调湿新风机组,其特征在于:所述溶液模块还包括与再生溶液模块、除湿溶液模块配套的溶液泵、溶液槽和管路,所述再生溶液模块的底部再生溶液槽内的溶液通过管路流到溶液槽,利用第一溶液泵与安装在再生溶液模块上部的第一布液管相连;所述除湿溶液模块的底部除湿溶液槽通过第二溶液泵与安装在除湿溶液模块上部的第二布液管相连;所述溶液槽、除湿溶液槽的溶液通过第三溶液泵进行循环。
3.根据权利要求1所述的带热回收功能的新型溶液调湿新风机组,其特征在于:在制冷系统中,其中制冷系统Ⅰ所述压缩机Ⅰ中的制冷剂依次流经压缩机Ⅰ、冷凝器Ⅰ、膨胀阀Ⅰ、蒸发器Ⅰ,然后回到压缩机Ⅰ,完成循环;所述蒸发器Ⅰ内的制冷剂循环通路的出口通过管路与压缩机Ⅰ的入口相连,压缩机Ⅰ的出口通过管路与所述冷凝器Ⅰ的制冷剂循环通路的入口相连,所述冷凝器Ⅰ的制冷剂循环通路的出口通过管路与膨胀阀Ⅰ的入口相连,膨胀阀Ⅰ的出口通过管路与所述蒸发器Ⅰ的制冷剂循环通路的入口相连。制冷系统Ⅱ所述压缩机Ⅱ中的制冷剂依次流经压缩机Ⅱ、水-板式换热器、冷凝器Ⅱ、膨胀阀Ⅱ、蒸发器Ⅱ,然后回到压缩机Ⅱ,完成循环;所述蒸发器Ⅱ内的制冷剂循环通路的出口通过管路与压缩机Ⅱ的入口相连,压缩机Ⅱ的出口通过管路与所述水-板式换热器及冷凝器Ⅱ的制冷剂循环通路的入口相连,所述水-板式换热器及冷凝器Ⅱ的制冷剂循环通路的出口通过管路与膨胀阀Ⅱ的入口相连,膨胀阀Ⅱ的出口通过管路与所述蒸发器Ⅱ的制冷剂循环通路的入口相连。
4.根据权利要求1所述的带热回收功能的新型溶液调湿新风机组,其特征在于:在全热回收单元中,所述全热回收型转轮热交换器与室内回风进行热质交换,转轮吸收室内回风的冷量并将水分排到排风中,之后旋转至新风侧,与新风进行热质交换,对新风进行预冷预除湿;而与转轮进行过热质交换的排风则被排出。
5.根据权利要求1所述的带热回收功能的新型溶液调湿新风机组,其特征在于:所述加湿模块中,利用循环水带走水-板式换热器的冷凝热,经过水-板式换热器的水利用水加湿模块对经过再生模块后的室内回风进行降温加湿处理,水加湿模块工作的时候,需要对水加湿模块的水槽进行补水。
6.根据权利要求2所述的带热回收功能的新型溶液调湿新风机组,其特征在于:所述再生溶液模块和除湿溶液模块利用盐溶液表面与空气中的水蒸气分压力差进行热湿交换,利用不同浓度溶液的吸湿特性实现对空气的除湿处理;高温潮湿的室外新风首先经过所述全热回收型转轮热交换器与低温低湿的室内回风进行全热交换,新风空气被降温除湿,经过降温除湿过程后的室外新风再经过所述蒸发器Ⅰ、蒸发器Ⅱ进一步的进行深度的降温除湿;最后,经过深度降温除湿的新风经过所述溶液除湿模块进行等焓升温除湿,已到满足室内送风要求状态点;低温低湿的室内回风依次经过所述全热回收型转轮热交换器,空气被升温加湿,经过升温加湿的室内回风经过所述冷凝器Ⅰ,吸收冷凝器Ⅰ排放的冷凝热,温度升高,然后经过所述溶液再生模块进行等焓降温加湿,再经过所述水加湿模块进行降温加湿、最后室内回风吸收所述冷凝器Ⅱ排放的冷凝热,温度升高,而后排出。
7.根据权利要求1所述的带热回收功能的新型溶液调湿新风机组,其特征在于:所述再生溶液模块、除湿溶液模块及水加湿模块结构一致,里面填料均由无纺布和ABS材料高温融合而成,采用瓦楞形状叠加在一起,保证溶液及水不被风带出来;外框使用ABS材料,模具一体化成型;里面循环的盐溶液采用水溴化锂、氯化钙或者氯化锂,循环亦可采用水。
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