CN203586377U - Compressed heat exchange unit - Google Patents
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Abstract
本实用新型涉及一种压缩式换热机组,其特征在于,该换热机组包括压缩式热泵、一个以上水-水换热器以及连接管路;所述连接管路分为一次侧管路和二次侧管路两部分:所述一次侧管路采用逐级顺序串联的连接方式,即所述一次侧管路依次经过各所述水-水换热器和所述压缩式热泵的蒸发器;所述二次侧管路采用先并联后串联、逐级顺序串联或独立分开的连接方式连通到热用户。本实用新型能够将一次网热水的热量梯级利用,从而大幅度增大了集中供热系统一次网热水的供、回水温差,因此可以的大大减少管路系统的初投资和水泵运行电耗,为利用热源低品位热能甚至废热余热等创造了条件,提高系统综合能源利用效率,降低供热成本。
The utility model relates to a compression heat exchange unit, which is characterized in that the heat exchange unit includes a compression heat pump, more than one water-water heat exchanger and a connecting pipeline; the connecting pipeline is divided into a primary side pipeline and a Two parts of the secondary side pipeline: the primary side pipeline is connected in series step by step, that is, the primary side pipeline passes through each of the water-water heat exchangers and the evaporator of the compression heat pump in sequence ; The secondary side pipeline is connected to the heat user in the connection mode of parallel connection first and then series connection, step-by-step sequential series connection or independent separation. The utility model can use the heat of the hot water in the primary network in steps, thereby greatly increasing the temperature difference between the supply and return water of the hot water in the primary network of the central heating system, and thus can greatly reduce the initial investment of the pipeline system and the running power of the water pump. It creates conditions for the use of low-grade heat energy from heat sources or even waste heat and waste heat, improves the overall energy utilization efficiency of the system, and reduces heating costs.
Description
技术领域technical field
本实用新型涉及一种用于采暖、供热水的换热机组,具体涉及一种能够使集中供The utility model relates to a heat exchange unit for heating and hot water supply, in particular to a heat exchange unit capable of centrally supplying
热系统一次网热水供、回水温差大幅增大的压缩式换热机组,属于能源技术领域。The utility model relates to a compression heat exchange unit with a greatly increased temperature difference between primary network hot water supply and return water of a heating system, belonging to the field of energy technology.
背景技术Background technique
随着城市集中供暖规模的不断增加,集中热源产生的高温热水往往要经过较长距离的输送才能达到热用户处。为扩大供暖面积,降低输送成本,并为回收电厂余热创造条件,清华大学付林等提出了专利号为:ZL200810101064.5,发明名称为:“一种热泵型换热机组”的发明专利。该专利采用换热与热水驱动的吸收式热泵复合技术解决以上问题,并且在越来越多的项目上得到应用。然而在推广和应用中,发现该专利存在如下问题:As the scale of urban central heating continues to increase, the high-temperature hot water generated by centralized heat sources often has to be transported over a long distance to reach the heat user. In order to expand the heating area, reduce transportation costs, and create conditions for the recovery of waste heat from power plants, Fu Lin of Tsinghua University and others proposed an invention patent with the patent number: ZL200810101064.5 and the invention name: "A heat pump heat exchange unit". This patent uses heat exchange and hot water driven absorption heat pump composite technology to solve the above problems, and has been applied in more and more projects. However, in the promotion and application, it was found that the patent has the following problems:
1)受到热网供水温度的限制:某些供热系统由于设计温度或运行年限的限制,一次网不能输送超过115℃的热水,导致进入吸收式热泵换热机组发生器的水温较低,对于吸收式热泵会造成驱动力不足,因此吸收式热泵换热机组的出水温度很难降到35℃以下,从而限制了供、回水温差的扩大,使得供热能力不足。而管网改造受到建设环境、成本、市容等得诸多限制在很多时候是无法进行的。1) Restricted by the water supply temperature of the heating network: Due to the design temperature or operating years of some heating systems, the primary network cannot deliver hot water exceeding 115°C, resulting in low water temperature entering the generator of the absorption heat pump heat exchange unit. For the absorption heat pump, the driving force will be insufficient, so the outlet water temperature of the absorption heat pump heat exchange unit is difficult to drop below 35°C, which limits the expansion of the temperature difference between the supply and return water, and makes the heating capacity insufficient. However, the transformation of the pipeline network is often impossible due to many constraints such as the construction environment, cost, and city appearance.
2)由于回水温度太高,回水输送回集中热源后,导致无法有效回收余热源的余热资源,造成供热量减少。2) Since the return water temperature is too high, after the return water is transported back to the centralized heat source, the waste heat resources of the waste heat source cannot be effectively recovered, resulting in a reduction in heat supply.
因此在这样集中供热的应用场所,采用新的技术手段降低高温热水的回水温度以进一步增大其供、回水温差,将对扩大集中供热的供热半径,节约供热能耗,降低供热成本产生深远的意义。Therefore, in such central heating application places, adopting new technical means to reduce the return water temperature of high-temperature hot water to further increase the temperature difference between the supply and return water will expand the heating radius of central heating and save heating energy consumption. , Reducing the cost of heating has far-reaching significance.
发明内容Contents of the invention
针对上述问题,本实用新型的目的是提供一种能够使集中供热系统一次网热水供、回水温差大幅增大的压缩式换热机组。In view of the above problems, the purpose of this utility model is to provide a compression heat exchange unit that can greatly increase the temperature difference between the hot water supply and return water in the central heating system.
为实现上述目的,本实用新型采取以下技术方案:一种压缩式换热机组,其特征在于,该换热机组包括压缩式热泵、一个以上水-水换热器以及连接管路;所述连接管路分为一次侧管路和二次侧管路两部分:所述一次侧管路采用逐级顺序串联的连接方式,即所述一次侧管路依次经过各所述水-水换热器和所述压缩式热泵的蒸发器;所述二次侧管路采用先并联后串联的连接方式,即两路以上所述二次侧管路分别经过所述压缩式热泵的冷凝器和若干所述水-水换热器后汇合成一路,再直接连通到热用户或经过其余所述水-水换热器后连通到热用户。In order to achieve the above purpose, the utility model adopts the following technical solutions: a compression heat exchange unit, which is characterized in that the heat exchange unit includes a compression heat pump, more than one water-water heat exchanger and connecting pipelines; the connection The pipeline is divided into two parts: the primary side pipeline and the secondary side pipeline: the primary side pipeline is connected in series step by step, that is, the primary side pipeline passes through each of the water-water heat exchangers in sequence and the evaporator of the compression heat pump; the secondary side pipelines are connected in parallel first and then in series, that is, more than two secondary side pipelines respectively pass through the condenser of the compression heat pump and several The above-mentioned water-water heat exchangers are combined into one road, and then directly connected to the heat user or connected to the heat user after passing through the other water-water heat exchangers.
在一个优选的实施例中,所述压缩式热泵是单台或串联/并联的多台,且所述压缩式热泵为容积式压缩机或离心式压缩机。In a preferred embodiment, the compression heat pump is a single unit or multiple units connected in series/parallel, and the compression heat pump is a displacement compressor or a centrifugal compressor.
在一个优选的实施例中,所述换热机组安装在集中供热系统的一次网与二次网换热站中,采暖末端采用地板采暖、风机盘管或暖气片。In a preferred embodiment, the heat exchange unit is installed in the heat exchange station between the primary network and the secondary network of the central heating system, and the heating end adopts floor heating, fan coil or radiator.
一种压缩式换热机组,其特征在于,该换热机组包括压缩式热泵、一个以上水-水换热器以及连接管路;所述连接管路分为一次侧管路和二次侧管路两部分:所述一次侧管路采用逐级顺序串联的连接方式,即所述一次侧管路依次经过各所述水-水换热器和所述压缩式热泵的蒸发器;所述二次侧管路也采用逐级顺序串联的连接方式,即所述二次侧管路依次经过所述压缩式热泵的冷凝器和各所述水-水换热器后连通到热用户。A compression heat exchange unit, characterized in that the heat exchange unit includes a compression heat pump, more than one water-water heat exchanger and a connecting pipeline; the connecting pipeline is divided into a primary side pipeline and a secondary side pipeline There are two parts of the pipeline: the primary side pipeline is connected in series step by step, that is, the primary side pipeline passes through each of the water-water heat exchangers and the evaporator of the compression heat pump in turn; the two The secondary side pipelines are also connected in series step by step, that is, the secondary side pipelines are connected to heat users after passing through the condenser of the compression heat pump and each of the water-water heat exchangers in sequence.
在一个优选的实施例中,所述压缩式热泵是单台或串联/并联的多台,且所述压缩式热泵为容积式压缩机或离心式压缩机。In a preferred embodiment, the compression heat pump is a single unit or multiple units connected in series/parallel, and the compression heat pump is a displacement compressor or a centrifugal compressor.
在一个优选的实施例中,所述换热机组安装在集中供热系统的一次网与二次网换热站中,采暖末端采用地板采暖、风机盘管或暖气片。In a preferred embodiment, the heat exchange unit is installed in the heat exchange station between the primary network and the secondary network of the central heating system, and the heating end adopts floor heating, fan coil or radiator.
一种压缩式换热机组,其特征在于,该换热机组包括压缩式热泵、一个以上水-水换热器以及连接管路;所述连接管路分为一次侧管路和二次侧管路两部分:所述一次侧管路采用逐级顺序串联的连接方式,即所述一次侧管路依次经过各所述水-水换热器和所述压缩式热泵的蒸发器;所述二次侧管路采用独立分开的连接方式,即所述二次侧管路经过所述压缩式热泵的冷凝器和所述水-水换热器后分别直接连通到热用户。A compression heat exchange unit, characterized in that the heat exchange unit includes a compression heat pump, more than one water-water heat exchanger and a connecting pipeline; the connecting pipeline is divided into a primary side pipeline and a secondary side pipeline There are two parts of the pipeline: the primary side pipeline is connected in series step by step, that is, the primary side pipeline passes through each of the water-water heat exchangers and the evaporator of the compression heat pump in turn; the two The secondary side pipeline adopts an independent and separate connection mode, that is, the secondary side pipeline is directly connected to the heat user after passing through the condenser of the compression heat pump and the water-water heat exchanger.
在一个优选的实施例中,所述压缩式热泵是单台或串联/并联的多台,且所述压缩式热泵为容积式压缩机或离心式压缩机。In a preferred embodiment, the compression heat pump is a single unit or multiple units connected in series/parallel, and the compression heat pump is a displacement compressor or a centrifugal compressor.
在一个优选的实施例中,所述换热机组安装在集中供热系统的一次网与二次网换热站中,采暖末端采用地板采暖、风机盘管或暖气片。In a preferred embodiment, the heat exchange unit is installed in the heat exchange station between the primary network and the secondary network of the central heating system, and the heating end adopts floor heating, fan coil or radiator.
本实用新型由于采取以上技术方案,其具有以下优点:1、由于本实用新型的换热机组包括压缩式热泵和水-水换热器,使得一次网热水依次经过水-水换热器和压缩式热泵的蒸发器,将一次网热水的热量梯级利用,从而大幅度增大了集中供热系统一次网热水的供、回水温差,从而可以的大大减少管路系统的初投资和水泵运行电耗,为利用热源低品位热能甚至废热余热等创造了条件,提高系统综合能源利用效率,降低供热成本。另外,本实用新型可以使一次网热水回水温度低于二次网热水进水温度,这对常规换热器而言是无法实现的。2、本实用新型采用换热与压缩式热泵复合技术,相对于采用换热与吸收式热泵复合技术的换热机组,由于不需要采用高温热水作为驱动源,因此对于一次网热水进水温度的要求可以降低,在诸如旧一次管网改造等不能输送超过115℃高温热水的场所,可以在原有管网条件不变的情况下,有效的扩大供暖面积,缓解管网供热能力不足的矛盾。此外,由于送往集中热源的一次网热水回水温度可以降得更低,对于集中热源的余热回收更加有利,更多回收的余热足以抵消压缩式热泵的能源消耗。同时,由于换热器和压缩式热泵的二次侧管路采用串联或并联的方式,使得压缩式热泵的出水温度可以低于二次网热水回水温度,进一步的减少了压缩式热泵的能源消耗。3、本实用新型可以将一次网热水回水温度降低至15℃或以下,从而可以扩大余热的来源,增大余热回收量,提高整个系统的供热能力。例如在湿冷型热电厂或工业余热回收领域,大量的余热分布在15℃-30℃的区间。由此可见,本实用新型采用换热与压缩式热泵复合技术的换热机组对于提高管网输送能力,有效回收余热资源,扩大集中供热的供热半径,节约供热能耗,降低供热成本能够产生深远的意义。Because the utility model adopts the above technical scheme, it has the following advantages: 1. Since the heat exchange unit of the utility model includes a compression heat pump and a water-water heat exchanger, the hot water of the primary network passes through the water-water heat exchanger and the water-water heat exchanger successively. The evaporator of the compression heat pump uses the heat of the hot water in the primary network in stages, thereby greatly increasing the temperature difference between the supply and return water of the hot water in the central heating system, thereby greatly reducing the initial investment and cost of the pipeline system. The power consumption of water pump operation creates conditions for the use of low-grade heat energy from heat sources and even waste heat, which improves the overall energy utilization efficiency of the system and reduces heating costs. In addition, the utility model can make the return water temperature of the primary network hot water lower than the secondary network hot water inlet temperature, which cannot be realized for conventional heat exchangers. 2. The utility model adopts the compound technology of heat exchange and compression heat pump. Compared with the heat exchange unit adopting the compound technology of heat exchange and absorption heat pump, since it does not need to use high-temperature hot water as the driving source, the hot water inflow to the primary network The temperature requirement can be reduced. In places where hot water exceeding 115°C cannot be transported, such as the old pipeline network renovation, the heating area can be effectively expanded and the heating capacity of the pipeline network can be alleviated while the original pipeline network conditions remain unchanged. contradiction. In addition, since the return temperature of the primary network hot water sent to the centralized heat source can be lowered, it is more beneficial to the recovery of waste heat from the centralized heat source, and more recovered waste heat is enough to offset the energy consumption of the compression heat pump. At the same time, since the heat exchanger and the secondary side pipeline of the compression heat pump are connected in series or in parallel, the outlet water temperature of the compression heat pump can be lower than the hot water return temperature of the secondary network, which further reduces the pressure of the compression heat pump. Energy consumption. 3. The utility model can reduce the return temperature of primary network hot water to 15°C or below, thereby expanding the source of waste heat, increasing the amount of waste heat recovery, and improving the heat supply capacity of the entire system. For example, in the field of wet-cooled thermal power plants or industrial waste heat recovery, a large amount of waste heat is distributed in the range of 15°C-30°C. It can be seen that the utility model adopts the combined technology of heat exchange and compression heat pump to improve the transportation capacity of the pipeline network, effectively recover waste heat resources, expand the heating radius of centralized heating, save heating energy consumption, and reduce heating energy consumption. Costs can have profound implications.
附图说明Description of drawings
以下结合附图来对本实用新型进行详细的描绘。然而应当理解,附图的提供仅为了更好地理解本实用新型,它们不应该理解成对本实用新型的限制。The utility model is described in detail below in conjunction with accompanying drawing. However, it should be understood that the drawings are only provided for better understanding of the utility model, and they should not be construed as limiting the utility model.
图1为本实用新型实施例1的换热机组示意图;Fig. 1 is the schematic diagram of the heat exchanger unit of the utility model embodiment 1;
图2为本实用新型实施例2的换热机组示意图;Fig. 2 is the schematic diagram of the heat exchange unit of the
图3为本实用新型实施例3的换热机组示意图;Fig. 3 is the schematic diagram of the heat exchange unit of the utility model embodiment 3;
图4为本实用新型实施例4的换热机组示意图。Fig. 4 is a schematic diagram of the heat exchange unit in Embodiment 4 of the present utility model.
具体实施方式Detailed ways
下面结合附图和实施例对本实用新型进行详细的描述。Below in conjunction with accompanying drawing and embodiment the utility model is described in detail.
图1显示了根据本实用新型实施1提供的换热机组10,该换热机组10包括压缩式热泵1、水-水换热器2以及连接管路。其中,连接管路分为一次侧管路31和二次侧(用户侧)管路32两部分:一次侧管路31采用逐级顺序串联的连接方式,即一次侧管路31依次经过水-水换热器2和压缩式热泵1的蒸发器;二次侧管路32采用并联的连接方式,即二次侧管路32分为两路,一路经过压缩式热泵机组1的冷凝器,另一路经过水-水换热器2,然后这两路管路汇合成一路连通到热用户。Fig. 1 shows a
图2显示了根据本实用新型实施2提供的换热机组20,该换热机组20与实施例1中的换热机组10结构相似,区别仅在于二次侧管路32采用独立分开的两路,即一路经过压缩式热泵1的冷凝器后直接连通到热用户,另一路经过水-水换热器2后直接连通到热用户。此时,换热机组20可以输出两种参数的热水,即经过压缩式热泵1的二次网热水参数和经过水-水换热器器2的二次网热水参数可以不相同,分别通过各自的二次侧管路32输送到不同的热用户。Figure 2 shows the heat exchange unit 20 provided according to
图3显示了根据本实用新型实施3提供的换热机组30,该换热机组30与实施例1中的换热机组10结构相似,区别仅在于二次侧管路32也采用逐级顺序串联的连接方式,即二次侧管路32依次经过压缩式热泵1的冷凝器和水-水换热器3后连通到热用户。Fig. 3 shows the
图4显示了根据本实用新型实施4提供的换热机组40,该换热机组40包括两级水-水换热器(仅以此为例,并不限于此),即一级水-水换热器2a和二级水-水换热器2b。该换热机组40的一次侧管路31仍然采用逐级顺序串联的连接方式,但二次侧管路32采用先并联后串联的连接方式,即二次侧管路32分为两路,一路经过压缩式热泵1的冷凝器,另一路经过一级水-水换热器2a,然后这两路管路汇合成一路再经过水-水换热器2b后连通到热用户。Fig. 4 shows the
在一个优选的实施例中,压缩式热泵1可以是单台,也可以是串联或并联的多台。对于压缩式热泵1,可以是容积式压缩机或离心式压缩机。In a preferred embodiment, the compression heat pump 1 can be a single unit, or multiple units connected in series or in parallel. For the compression heat pump 1, it can be a displacement compressor or a centrifugal compressor.
下面结合实施例1提供的换热机组10和实施例4提供的换热机组40分别说明本实用新型在某集中供热系统中应用的流程。The process of applying the utility model in a central heating system will be described below in conjunction with the
实施例1:如图1所示,在实际运行中,由集中热源输出的110℃一次网热水进水首先进入水-水换热器2作为加热热源,加热二次网热水;放热降温至50℃左右后从水-水换热器2中流出,再进入压缩式热泵1的蒸发器作为低品位热源,放热降温至至15℃左右后流出,返回集中热源,如此循环。Example 1: As shown in Figure 1, in actual operation, the 110°C primary network hot water output from the centralized heat source first enters the water-
由热用户输出的45℃二次网热水回水分为两路进入换热机组10:一路进入压缩式热泵1的冷凝器中吸收热量,被加热至60℃左右后流出;另一路进入水-水换热器2中与一次网热水进行换热,被加热到60℃左右后流出,两路60℃热水汇合在一起后送往热用户。由此可见,本实施例提供的换热机组10采用热泵-换热器组合的方式能够有效的进行高温热水的梯级利用,实现了95℃的供、回水温差,并能够产生出满足使用要求的采暖或生活热水。该换热机组10一般安装在大型集中供热系统的各热力站中,特别是一次网与二次网换热站用,采暖末端可采用地板采暖、风机盘管或暖气片等形式。The 45°C secondary network hot water return water output by the heat user is divided into two paths and enters the heat exchange unit 10: one path enters the condenser of the compression heat pump 1 to absorb heat, and flows out after being heated to about 60°C; the other path enters the water- The
实施例4:如图4所示,在实际运行中,由集中热源输出的110℃一次网热水进水首先进入二级水-水换热器2b作为加热热源,加热二次网热水;放热降温至65℃左右后流出,再进入一级水-水换热器2a加热二次网热水;放热降温至50℃左右后流出,再进入压缩式热泵1的蒸发器作为低位热源,放热降温至15℃左右后流出,返回集中热源,如此循环。Embodiment 4: As shown in Figure 4, in actual operation, the 110°C primary network hot water output from the centralized heat source first enters the secondary water-
由热用户输出的45℃二次网热水回水分为两路进入换热机组40:一路进入压缩式热泵1的冷凝器中吸收热量,被加热至60℃左右后流出;另一路进入一级水-水换热器2a中与一次网热水进行换热,被加热到60℃左右后流出;两路60℃热水汇合在一起后进入二级水-水换热器2b中再次与一次网热水进行换热,被加热到70℃左右后送往热用户。由此可见,本实施例提供的换热机组40采用热泵-两级换热器组合的方式能够有效进行高温热水的梯级利用,实现95℃的供、回水温差,并能够产生出品质较高的采暖或生活热水。该换热机组40一般安装在大型集中供热系统的各热力站中,特别是一次网与二次网换热站用,采暖末端采用暖气片形式。The 45°C secondary network hot water return water output by the heat user is divided into two paths and enters the heat exchange unit 40: one path enters the condenser of the compression heat pump 1 to absorb heat, and flows out after being heated to about 60°C; the other path enters the first stage The water-
上述各实施例仅用于对本实用新型的目的、技术方案和有益效果进行了进一步详细说明,并不用于限制本实用新型,凡在本实用新型的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本实用新型的保护范围之内。The above-mentioned embodiments are only used to further describe the purpose, technical solutions and beneficial effects of the utility model in further detail, and are not used to limit the utility model. Any modifications made within the spirit and principles of the utility model, Equivalent replacements, improvements, etc., should all be included within the protection scope of the present utility model.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103673059A (en) * | 2013-11-08 | 2014-03-26 | 清华大学 | Compression-type heat exchanger unit |
| GB2527530A (en) * | 2014-06-24 | 2015-12-30 | Thermal Integration Ltd | Fluid-heating apparatus |
| CN107224824A (en) * | 2017-07-14 | 2017-10-03 | 河南省德耀节能科技股份有限公司 | A kind of drying materials system |
| CN110500638A (en) * | 2019-09-18 | 2019-11-26 | 临沂智慧新能源科技有限公司 | One kind energy-saving secondary station heat pump unit Internet-based and control method |
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2013
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103673059A (en) * | 2013-11-08 | 2014-03-26 | 清华大学 | Compression-type heat exchanger unit |
| GB2527530A (en) * | 2014-06-24 | 2015-12-30 | Thermal Integration Ltd | Fluid-heating apparatus |
| CN107224824A (en) * | 2017-07-14 | 2017-10-03 | 河南省德耀节能科技股份有限公司 | A kind of drying materials system |
| CN110500638A (en) * | 2019-09-18 | 2019-11-26 | 临沂智慧新能源科技有限公司 | One kind energy-saving secondary station heat pump unit Internet-based and control method |
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