CN100552311C - 节能型空调除湿系统 - Google Patents
节能型空调除湿系统 Download PDFInfo
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- CN100552311C CN100552311C CNB2008100239017A CN200810023901A CN100552311C CN 100552311 C CN100552311 C CN 100552311C CN B2008100239017 A CNB2008100239017 A CN B2008100239017A CN 200810023901 A CN200810023901 A CN 200810023901A CN 100552311 C CN100552311 C CN 100552311C
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- 238000004378 air conditioning Methods 0.000 title claims abstract description 19
- VSCWAEJMTAWNJL-UHFFFAOYSA-K Aluminium chloride Chemical compound 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Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 claims abstract description 22
- 238000001816 cooling Methods 0.000 claims abstract description 14
- 238000009833 condensation Methods 0.000 claims abstract description 13
- 230000005494 condensation Effects 0.000 claims abstract description 13
- 238000007906 compression Methods 0.000 claims abstract description 11
- 239000003463 adsorbent Substances 0.000 claims abstract description 5
- 238000000034 method Methods 0.000 claims description 11
- 238000001704 evaporation Methods 0.000 claims description 6
- 238000007791 dehumidification Methods 0.000 abstract description 11
- 230000008929 regeneration Effects 0.000 abstract description 6
- 238000011069 regeneration method Methods 0.000 abstract description 6
- 238000010438 heat treatment Methods 0.000 abstract description 2
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- 241000894006 Bacteria Species 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N Triethylene glycol Chemical compound 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- UXVMQQNJUSDDNG-UHFFFAOYSA-L cacl2 Chemical compound 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[Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- 238000009795 derivation Methods 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000000630 rising Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N silicium dioxide Chemical compound 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Abstract
本发明公开了一种节能型空调除湿系统，包括全热交换器、氯化锂转轮和压缩子系统；压缩子系统由低温环路热泵系统和高温环路热泵系统串联而成；室外新风经过全热交换器降低温度后除湿，然后与另一部分室内回风混合，再经蒸发器，温度降低后，送入室内；另一室外新风经过低温环路热泵系统的冷凝器加热后，一路经高温环路热泵系统的蒸发器降温后排入室外的大气中；另一路经高温环路热泵系统的冷凝器再次加热后，作为氯化锂转轮的吸附剂再生热源。低温环路冷凝热作为高温环路热泵的热源。高温环路热泵的冷凝热作为除湿模块所需的再生热源。使热源和热汇的能量都得到充分利用，简化了系统结构，使控制更加简单，降低了热污染。
Description
节能型空调除湿系统
技术领域
本发明涉及一种空调除湿设备，具体说是一种节能型空调除湿系统。 背景技术
夏季，空调室内通入的冷却水温度一般都低于室内空气的露点温度，很容 易造成室内水蒸气凝结。为了防止结露，空调室内都需要除湿。家用空调器没 有除湿装置，依靠冷风制冷，室内处于紊流状态，室内不易结露。但蒸发器盘 管处会有凝水出现， 一般是用一根水管将其导出室外。大型空调机组中都有除 湿段。 一般中央空调由新风段、混合段、冷却段、除湿段、加压段组成。冷却
除湿空调系统依靠冷水机组实现供冷和除湿。冷水机组的供水温度为7'C左右， 低于空气的露点温度，使得被处理空气中水蒸气凝结而除湿。冷却除湿在空调 中称为表冷段。转轮除湿或液体除湿的空调系统则是温湿度独立控制系统，冷 水机组只有制冷功能，供热系统提供高温再生热源，供给转轮或液体再生持续 除湿。冷水机组制冷为冷却段，液体或转轮除湿为除湿段。
上述三种除湿方式中，冷却除湿热湿负荷同时处理，形式最简单，施工方 便，但受到冷冻水温度的限制不能达到较低的湿度，而且表冷器在湿工况下运 行，容易滋生细菌和病毒，影响室内空气品质。此外，这种系统中冷水机组需 要提供较低的冷水温度，因此，机组的COP较低，能源利用率低。再有，经过 冷却除湿的空气温度较低，不能满足人体舒适度要求，还必须加热使其温度升 高，达到室内送风状态点后才能送入室内。固体千燥剂除湿系统与液体干燥剂 除湿系统对空气的除湿与制冷分开处理。固体干燥剂除湿通常釆用转轮式除湿 器，利用多孔材料如硅胶、活性炭、分子筛以及氯化锂晶体等盐类吸湿能力强 的特性，将空气处理到低含湿量。空气在处理过程中近似为等焓过程。新风的温度会有所上升。液体干燥剂除湿系统利用三甘醇、氯化锂、氯化钙以及溴化 锂等水溶液强烈的吸湿特性对空气进行除湿。新风在处理过程近似为等温处理 过程。后两种除湿过程中，温湿度独立控制，冷水机组只承担室内显热负荷，
供水温度20。C左右，与冷却除湿相比，机组COP较高，能源利用率高，且除湿 过程没有露点温度限制，可以将新风的含湿量处理到很低，是很好的除湿方式。 但必须有髙温的热源提供再生温度，除湿才得以往复。因此，这两种除湿系统 都有一套专门的热源系统，如太阳能系统，地热系统或者燃气系统等来提供较 高温度的热量驱动系统运转。太阳能系统和地热系统虽然利用了天然能源，比 较环保和节能，但系统比较复杂，初投资比较大。燃气系统则运行费用较高， 因此，寻找合适的高温热源是实现固体除湿的关键技术。而寻求再生高温能源 的过程中，人们却忽视了被白白浪费掉的系统自身所产生这部分热量。 发明内容
本发明所要解决的技术问题，在于克服现有技术存在的技术缺陷，提供一 种节能型空调除湿系统。在既需要冷量又需要除湿的室内，使用低温环路热泵 提供室内制冷所需冷负荷。低温环路冷凝热作为高温环路热泵的热源。高温环 路热泵的冷凝热作为除湿转轮吸附剂再生所需的高温热源。
本发明节能型空调除湿系统，包括全热交换器A、氯化锂转轮B和压缩子系 统；其特征是：
压缩子系统由低温环路热泵系统13和高温环路热泵系统14串联而成； 低温环路热泵系统13由蒸发器Cl、压缩机Fl、冷凝器Dl和节流阀El依 次串联构成；
高温环路热泵系统14由蒸发器C2、压缩机F2、冷凝器D2和节流阀E2依 次串联构成；
室外新风1先经过全热交换器A，与一部分窒内回风3进行能量交换，温度降低后进入氯化锂转轮B除湿，然后与另一部分室内回风31混合，再进入压缩 子系统中低温环路热泵系统13的蒸发器C1，温度降低后，送入室内；另一室外 新风100经过低温环路热泵系统13的冷凝器Dl被冷凝热加热后，分为三路： 一路经高温环路热泵系统14的蒸发器C2降温后排入室外的大气中；另一路经 高温环路热泵系统14的冷凝器D2，被冷凝热再次加热后，作为氯化锂转轮B的 吸附剂再生热源；再一路为多余气体直接通过管路15排入室外大气中。
低温环路热泵系统的工况为：蒸发温度：18。C士3。C;冷凝热温度：50°C ±3°C。
高温环路热泵系统的工况为：蒸发温度：43°C±5;冷凝热温度：76°C±5°C 本发明节能型空调除湿系统，在既需要冷量又需要除湿的室内，使用低温 环路热泵提供室内制冷所需冷负荷。低温环路冷凝热作为高温环路热泵的热源。 高温环路热泵的冷凝热作为除湿模块所需的再生热源。使热源和热汇的能量都 得到充分利用，简化了系统构建，使控制更加简单，消除了冷水机组的热污染， 是 一 种既节能又环保的系统形式。 附图说明
图1为本发明节能型空调除湿系统结构框图。 具体实施方式
下面结合附图和实施例，对本发明作进一步详细说明。
实施例：如图1所示，节能型空调除湿系统，包括全热交换器A、氯化锂转
轮B和压缩子系统；
压縮子系统由低温环路热泵系统13和高温环路热泵系统14串联而成； 低温环路热泵系统13由蒸发器Cl、压缩机Fl、冷凝器Dl和节流阀El依
次串联构成；低温环路热泵系统的工况为：蒸发温度：18。C士3。C;冷凝温度：50。C ±3°C。
高温环路热泵系统14由蒸发器C2、压缩机F2、冷凝器D2和节流阀E2依 次串联构成；高温环路热泵系统的工况为：蒸发温度：43。C±5;冷凝温度：76 。C ±5。
室外新风1先经过全热交换器A，与一部分室内回风3进行能量交换，温 度降低后进入氯化锂转轮B除湿，除湿后与另一部分室内回风31混合，再进入 压缩子系统中低温环路热泵系统13的蒸发器C1，被冷却降温至20士3。C后，经 管路2送入室内；经过全热交换器进行过能量交换的室内回风3，经排气口 7排 出室外；另一部分室外新风IOO经过低温环路热泵系统13的冷凝器D1被冷凝 热加热，它作为冷凝器的热汇，吸收冷凝器的热量，温度升高至45。C土3。C,然 后分为三路： 一路经管路IO，作为高温环路热泵系统14的热源，经高温环路热 泵系统14的蒸发器C2降温后由管路71排入室外的大气中；另一路管路9到高 温环路热泵系统14的冷凝器D2，作为高温环路热泵系统14冷凝器侧的热汇， 吸收冷凝器D2所放出的高温冷凝热，被冷凝热再次加热，温度升高至7(TC以 上后，作为氯化锂转轮B的吸附剂的再生热源，通过转轮B后携带了大量水蒸 气，由管路72被排入室外大气中；还有一路将多余气体经管路73被直接排入 室外大气中。
Claims (3)
1、节能型空调除湿系统，包括全热交换器(A)、氯化锂转轮(B)和压缩子系统；其特征是： 压缩子系统由低温环路热泵系统(13)和高温环路热泵系统(14)串联而成； 低温环路热泵系统(13)由蒸发器(C1)、压缩机(F1)、冷凝器(D1)和节流阀(E1)依次串联构成； 高温环路热泵系统(14)由蒸发器(C2)、压缩机(F2)、冷凝器(D2)和节流阀(E2)依次串联构成； 室外新风(1)先经过全热交换器(A)，与一部分室内回风(3)进行能量交换，温度降低后进入氯化锂转轮(B)除湿，然后与另一部分室内回风(31)混合，再进入压缩子系统中低温环路热泵系统(13)的蒸发器(C1)，温度降低后，送入室内；另一室外新风(100)经过低温环路热泵系统(13)的冷凝器(D1)被冷凝热加热后，分为三路：一路经高温环路热泵系统(14)的蒸发器(C2)降温后排入室外的大气中；另一路经高温环路热泵系统(14)的冷凝器(D2)，被冷凝热再次加热后，作为氯化锂转轮(B)的吸附剂再生热源；再一路直接通过管路(15)排入室外大气中。
2、 根据权利要求l所述节能型空调除湿系统，其特征是：所述低温环路热 泵系统的工况为：蒸发温度：18°C±3°C;冷凝温度：50°C±3°C。
3、 根据权利要求1或2所述节能型空调除湿系统，其特征是：所述高温环 路热泵系统的工况为：蒸发温度：43°C±5;冷凝温度：76°C±5°C。
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