CN102826620B - Energy-saving water distiller - Google Patents
Energy-saving water distiller Download PDFInfo
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- CN102826620B CN102826620B CN201210359981XA CN201210359981A CN102826620B CN 102826620 B CN102826620 B CN 102826620B CN 201210359981X A CN201210359981X A CN 201210359981XA CN 201210359981 A CN201210359981 A CN 201210359981A CN 102826620 B CN102826620 B CN 102826620B
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 473
- 239000002994 raw material Substances 0.000 claims abstract description 130
- 239000012153 distilled water Substances 0.000 claims abstract description 87
- 238000010438 heat treatment Methods 0.000 claims description 11
- 239000002912 waste gas Substances 0.000 claims description 5
- 238000004891 communication Methods 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 20
- 239000000498 cooling water Substances 0.000 abstract description 6
- 238000000034 method Methods 0.000 description 14
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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Abstract
Description
技术领域 technical field
本发明涉及蒸馏水生产设备技术领域,具体涉及一种节能型蒸馏水机。 The invention relates to the technical field of distilled water production equipment, in particular to an energy-saving distilled water machine.
背景技术 Background technique
蒸馏水是指用蒸馏方法制备的纯水,广泛应用于医疗、科学研究、生产生活中,近年来,随着工业的发展对地表水以及地下水的污染原来越严重,以及人们生活水平、健康意识的提高,对食用纯净水的需求也越来越大。在蒸馏水的生产过程中,首先需要加热装置将水加热蒸发成为水蒸气,然后对水蒸气进行冷却,使其冷凝为蒸馏水。现有的蒸馏水生产设备不仅结构复杂,而且在冷凝的过程中需要消耗大量的冷却水,热交换效率低,蒸馏水的产水量小,能源消耗量大,生产成本高。 Distilled water refers to pure water prepared by distillation, which is widely used in medical treatment, scientific research, production and life. The demand for pure drinking water is also increasing. In the production process of distilled water, a heating device is first required to heat and evaporate water into water vapor, and then cool the water vapor to condense it into distilled water. The existing distilled water production equipment not only has a complex structure, but also consumes a large amount of cooling water during the condensation process, resulting in low heat exchange efficiency, small distilled water production, large energy consumption, and high production costs.
发明内容 Contents of the invention
本发明的目的是提供一种结构简单且热交换效率高、产水量大、热能利用率高的节能型蒸馏水机。 The purpose of the present invention is to provide an energy-saving distilled water machine with simple structure, high heat exchange efficiency, large water production volume and high heat energy utilization rate.
为了实现上述目的,本发明采用以下技术方案。 In order to achieve the above object, the present invention adopts the following technical solutions.
一种节能型蒸馏水机,包括预热装置以及与预热装置连接的热交换装置,所述预热装置包括壳体以及位于壳体内部的加热管,所述壳体还设有水蒸气收集加压装置,所述水蒸气收集加压装置设有水蒸气排出口、水蒸气吸入口, 所述热交换装置内部设有原料水进水通道、原料水回流通道、第一水蒸气通道、第二水蒸气通道、蒸馏水排出通道,所述热交换装置由若干A型热交换板与B型热交换板依次间隔设置组成,所述A型热交换板分别与相邻的B型热交换板构成供原料水通过的原料水间隙通道与供水蒸气通过的水蒸气间隙通道;所述水蒸气排出口与所述第一水蒸气通道连通,所述第一水蒸气通道与所述水蒸气间隙通道连通,所述水蒸气间隙通道与所述蒸馏水排出通道连通;所述原料水进水通道与所述原料水间隙通道连通,所述原料水间隙通道分别与所述原料水回流通道、所述第二水蒸气通道连通,所述原料水回流通道与所述预热装置的内腔连通,所述第二水蒸气通道与所述水蒸气吸入口连通。 An energy-saving distilled water machine, comprising a preheating device and a heat exchange device connected to the preheating device, the preheating device includes a shell and a heating tube inside the shell, the shell is also provided with a water vapor collection The water vapor collecting and pressurizing device is provided with a water vapor outlet and a water vapor suction port, and the inside of the heat exchange device is provided with a raw material water inlet channel, a raw material water return channel, a first water vapor channel, a second The water vapor channel and the distilled water discharge channel, the heat exchange device is composed of a number of A-type heat exchange plates and B-type heat exchange plates arranged at intervals in sequence, and the A-type heat exchange plates are respectively formed with adjacent B-type heat exchange plates for supply The raw material water gap channel through which raw material water passes and the water vapor gap channel through which water vapor passes; the water vapor outlet communicates with the first water vapor channel, and the first water vapor channel communicates with the water vapor gap channel, The water vapor gap channel communicates with the distilled water discharge channel; the raw material water inlet channel communicates with the raw material water gap channel, and the raw material water gap channel is respectively connected to the raw material water return channel, the second water The steam passage is connected, the raw material water return passage is connected with the inner chamber of the preheating device, and the second water vapor passage is connected with the water vapor suction port.
其中,所述A型热交换板与B型热交换板的四周紧密贴合;所述A型热交换板的底部右侧设有A板原料水进水通孔,底部左侧设有A板原料水回流通孔,底部中间设有A板蒸馏水排出通孔,上部两端设有A板第一水蒸气通孔,上部中间设有A板第二水蒸气通孔;所述B型热交换板的底部右侧设有B板原料水进水通孔,底部左侧设有B板原料水回流通孔,底部中间设有B板蒸馏水排出通孔,上部两端设有B板第一水蒸气通孔,上部中间设有B板第二水蒸气通孔。 Wherein, the A-type heat exchange plate and the B-type heat exchange plate are closely attached; the bottom right side of the A-type heat exchange plate is provided with an A-plate raw material water inlet hole, and the bottom left side is provided with an A-plate Raw material water return flow hole, there is a distilled water discharge through hole in the middle of the bottom of the A plate, the first water vapor through hole of the A plate is set at both ends of the upper part, and the second water vapor through hole of the A plate is set in the middle of the upper part; the B-type heat exchange On the right side of the bottom of the plate, there is a water inlet hole for the raw material water of the B plate, on the left side of the bottom, there is a return flow hole for the raw material water of the B plate, in the middle of the bottom, there is a through hole for the distilled water discharge of the B plate, and at both ends of the upper part, there are the first water holes of the B plate. The steam hole is provided with the second water vapor hole of the B plate in the middle of the upper part.
其中,所述壳体的侧边设置有原料水进口、原料水回流口、蒸馏水出口、水蒸气出口、水蒸气进口,所述水蒸气出口与所述水蒸气收集加压装置的水蒸气排出口连通,所述水蒸气进口与所述水蒸气收集加压装置的水蒸气吸入口连通;所述原料水进口、原料水回流口分别与原料水进水通道、原料水回流通道连通;所述蒸馏水出口与蒸馏水排出通道连通。 Wherein, the side of the housing is provided with a raw water inlet, a raw water return port, a distilled water outlet, a water vapor outlet, and a water vapor inlet, and the water vapor outlet is connected to the water vapor outlet of the water vapor collection and pressurization device. The water vapor inlet is connected with the water vapor suction port of the water vapor collection and pressurization device; the raw water inlet and the raw water return port are respectively connected with the raw water inlet channel and the raw water return channel; the distilled water The outlet communicates with the distilled water discharge channel.
其中,所述A板原料水进水通孔、B板原料水进水通孔与原料水进口连通并构成原料水进水通道,所述A板原料水回流通孔、B板原料水回流通孔与原料水回流口连通并构成原料水回流通道,所述A板蒸馏水排出通孔、B板蒸馏水排出通孔与蒸馏水出口连通并构成蒸馏水排出通道,所述A板第一水蒸气通孔、B板第一水蒸气通孔与水蒸气出口连通并构成第一水蒸气通道,所述A板第二水蒸气通孔、B板第二水蒸气通孔与水蒸气进口连通并构成第二水蒸气通道。 Wherein, the raw material water inlet hole of plate A and the raw material water inlet hole of plate B are connected with the raw material water inlet to form a raw material water inlet channel, and the raw material water return flow hole of plate A and the raw material water return flow hole of plate B are connected to the raw material water inlet. The hole communicates with the raw material water return port and forms a raw material water return channel. The distilled water discharge through hole of plate A and the distilled water discharge through hole of plate B communicate with the distilled water outlet to form a distilled water discharge channel. The first water vapor through hole of plate A, The first water vapor through hole of plate B communicates with the water vapor outlet and forms the first water vapor channel, and the second water vapor through hole of plate A and the second water vapor through hole of plate B communicate with the water vapor inlet and form the second water vapor channel. steam channel.
其中,所述A板原料水进水通孔处设有原料水侧流进口,A板原料水回流通孔处设有原料水侧流出口,A板第二水蒸气通孔处设有二次水蒸气逸出口;所述B板第一水蒸气通孔处设有一次水蒸气输入口,B板蒸馏水排出通孔处设有蒸馏水排出口;所述原料水间隙通道的底部分别与原料水侧流进口、原料水侧流出口连通;所述原料水间隙通道的顶部通过二次水蒸气逸出口与第二水蒸气通道连通;所述水蒸气间隙通道分别与一次水蒸气输入口、蒸馏水排出口连通。 Wherein, the raw material water inlet of plate A is provided with a side flow inlet of raw material water, the raw material water return hole of plate A is provided with a side flow outlet of raw material water, and the second water vapor through hole of plate A is provided with a secondary Water vapor escape port; the first water vapor through hole of the B plate is provided with a water vapor input port, and the distilled water discharge through hole of the B plate is provided with a distilled water discharge port; the bottom of the raw material water gap channel is respectively connected to the raw material water side The flow inlet and the raw material water side outlet are connected; the top of the raw material water gap channel is communicated with the second water vapor channel through the secondary water vapor escape port; the water vapor gap channel is connected with the primary water vapor input port and the distilled water discharge port respectively. connected.
其中,所述A型热交换板与B型热交换板依次间隔的设置,通过设置在两侧的固定筋条以及设置在端部的固定板与所述预热装置连接。 Wherein, the A-type heat exchange plate and the B-type heat exchange plate are sequentially arranged at intervals, and are connected to the preheating device through the fixing ribs arranged on both sides and the fixing plates arranged at the end.
其中,所述固定筋条与固定板连接的一端设有弹簧。 Wherein, a spring is provided at one end of the fixed rib connected to the fixed plate.
其中,所述热交换装置包括第一热交换装置、第二热交换装置,所述第一热交换装置、第二热交换装置分别连接在预热装置的两端。 Wherein, the heat exchange device includes a first heat exchange device and a second heat exchange device, and the first heat exchange device and the second heat exchange device are respectively connected to two ends of the preheating device.
其中,所述A型热交换板上设有A板凹槽,所述B型热交换板上设有B板凹槽。 Wherein, the A-type heat exchange plate is provided with an A-plate groove, and the B-type heat exchange plate is provided with a B-plate groove.
其中,所述壳体内部设有水位计。 Wherein, a water level gauge is provided inside the housing.
其中,所述壳体内部设有废气排出管。 Wherein, a waste gas discharge pipe is arranged inside the housing.
本发明的有益效果为: The beneficial effects of the present invention are:
(一)本发明的节能型蒸馏水机利用温度较低原料水作为冷却水对水蒸气进行冷凝,温度较低的原料水吸收热量后温度升高,再经加热管加热较短的时间即可产生大量一次水蒸气。在生产过程中,只需保证加热管每小时对原料水加热25分钟,即可保证原料水不断地产生大量水蒸气,减少了加热的时间,使得蒸馏水机的单位耗电量减少15KW/h,降低了能源消耗。 (1) The energy-saving water distiller of the present invention uses lower-temperature raw material water as cooling water to condense water vapor, and the lower-temperature raw material water absorbs heat and then rises in temperature, and then heated by a heating tube for a short period of time to produce A large amount of primary water vapor. In the production process, it is only necessary to ensure that the heating tube heats the raw water for 25 minutes per hour to ensure that the raw water continuously generates a large amount of water vapor, reducing the heating time and reducing the unit power consumption of the distilled water machine by 15KW/h. Reduced energy consumption.
(二)本发明的节能型蒸馏水机利用温度较低的原料水作为冷却水,经过热交换过程吸收热量后在热交换装置内部产生大量二次水蒸气,提高了单位时间内蒸馏水的产出量,提高了产水效率。 (2) The energy-saving distilled water machine of the present invention uses raw water with a lower temperature as cooling water, and after absorbing heat in the heat exchange process, a large amount of secondary water vapor is generated inside the heat exchange device, which increases the output of distilled water per unit time , improved water production efficiency.
(三)本发明结构简单、操作方便、热交换效率高,在生产过程中原料水的进水温度在25℃时,能够保证蒸馏水的出水温度28℃,具有很高热能利用率。 (3) The present invention has simple structure, convenient operation, and high heat exchange efficiency. During the production process, when the feed water temperature of the raw material water is 25°C, the outlet temperature of the distilled water can be guaranteed to be 28°C, and has a high heat energy utilization rate.
附图说明 Description of drawings
图1为本发明的节能型蒸馏水机的结构示意图。 Fig. 1 is a structural schematic diagram of an energy-saving water distiller of the present invention.
图2为本发明的节能型蒸馏水机的壳体的剖面结构示意图。 Fig. 2 is a schematic cross-sectional structural view of the housing of the energy-saving water distiller of the present invention.
图3为本发明的实施例1的A型热交换板的结构示意图。
Fig. 3 is a schematic structural view of the A-type heat exchange plate of
图4为本发明的实施例1的B型热交换板的结构示意图。 Fig. 4 is a schematic structural view of a B-type heat exchange plate in Example 1 of the present invention.
图5为本发明的实施例2的A型热交换板的结构示意图。 Fig. 5 is a schematic structural view of a type A heat exchange plate in Example 2 of the present invention.
图6为本发明的实施例2的B型热交换板的结构示意图。 Fig. 6 is a schematic structural view of a B-type heat exchange plate in Example 2 of the present invention.
附图标记包括: Reference signs include:
1—预热装置;11—原料水进口;12—原料水回流口;13—蒸馏水出口;14—水蒸气出口;15—水蒸气进口;16—壳体;2—热交换装置;21—A型热交换板;211—A板原料水进水通孔;212—A板原料水回流通孔;213—A板蒸馏水排出通孔;214—A板第一水蒸气通孔; 215—A板第二水蒸气通孔;216—原料水侧流进口;217—原料水侧流出口;218—二次水蒸气逸出口;219—A板凹槽;22—B型热交换板;221—B板原料水进水通孔;222—B板原料水回流通孔;223—B板蒸馏水排出通孔;224—B板第一水蒸气通孔;225—B板第二水蒸气通孔;226—一次水蒸气输入口;227—蒸馏水排出口;228—B板凹槽;3—水蒸气收集加压装置;4—固定筋条;5—固定板;6—弹簧。
1—preheating device; 11—raw water inlet; 12—raw water return port; 13—distilled water outlet; 14—water vapor outlet; 15—water vapor inlet; 16—shell; 2—heat exchange device; 21—A Type heat exchange plate; 211—A plate raw material water inlet through hole; 212—A plate raw material water return flow hole; 213—A plate distilled water discharge through hole; 214—A plate first water vapor through hole; 215—A plate Second water vapor through hole; 216—raw material water side flow inlet; 217—raw material water side flow outlet; 218—secondary steam escape outlet; 219—A plate groove; 22—B type heat exchange plate; 221—
具体实施方式 Detailed ways
以下结合附图对本发明进行详细的描述。 The present invention will be described in detail below in conjunction with the accompanying drawings.
实施例1。Example 1.
如图1至图4所示,一种节能型蒸馏水机,包括预热装置1以及与预热装置1连接的热交换装置2,所述预热装置1包括壳体16以及位于壳体1内部的加热管,所述壳体16内部还设有水蒸气收集加压装置3,所述水蒸气收集加压装置3设有水蒸气排出口、水蒸气吸入口,所述热交换装置2由若干开设有通孔的A型热交换板21与B型热交换板22依次间隔设置组成,所述A型热交换板21分别与相邻的B型热交换板22之间构成供原料水通过的原料水间隙通道与供水蒸气通过的水蒸气间隙通道,具体地为,A型热交换板21与前一块B型热交换板22构成原料水间隙通道,A型热交换板21与后一块B型热交换板22构成水蒸气间隙通道。所述热交换装置2内部设有原料水进水通道、原料水回流通道、第一水蒸气通道、第二水蒸气通道、蒸馏水排出通道;所述水蒸气排出口与所述第一水蒸气通道连通,所述第一水蒸气通道与所述水蒸气间隙通道连通,所述水蒸气间隙通道与所述蒸馏水排出通道连通;所述原料水进水通道与所述原料水间隙通道连通,所述原料水间隙通道分别与所述原料水回流通道、所述第二水蒸气通道连通,所述原料水回流通道与所述预热装置的内腔连通,所述第二水蒸气通道与所述水蒸气吸入口连通。
As shown in Figures 1 to 4, an energy-saving distilled water machine includes a
本实施例中,所述A型热交换板21与B型热交换板22的四周紧密贴合,中间设有间隙通道,所述A型热交换板21的底部右侧设有A板原料水进水通孔211,底部左侧设有A板原料水回流通孔212,底部中间设有A板蒸馏水排出通孔213,上部两端设有A板第一水蒸气通孔214,上部中间设有A板第二水蒸气通孔215;所述B型热交换板的底部右侧设有B板原料水进水通孔221,底部左侧设有B板原料水回流通孔222,底部中间设有B板蒸馏水排出通孔223,上部两端设有B板第一水蒸气通孔224,上部中间设有B板第二水蒸气通孔225,所述壳体16的侧边设置有原料水进口11、原料水回流口12、蒸馏水出口13、水蒸气出口14、水蒸气进口15,所述水蒸气出口14、水蒸气进口15分别与水蒸气收集加压装置3的水蒸气排出口、水蒸气吸入口连通;所述原料水进口11、原料水回流口12分别与原料水进水通道、原料水回流通道连接;所述蒸馏水出口13与蒸馏水排出通道连接。
In this embodiment, the sides of the A-type
本实施例中,所述A板原料水进水通孔211、B板原料水进水通孔221与原料水进口11连通并构成原料水进水通道;所述A板原料水回流通孔212、B板原料水回流通孔222与原料水回流口12连通并构成原料水回流通道;所述A板蒸馏水排出通孔213、B板蒸馏水排出通孔223与蒸馏水出口13连通并构成蒸馏水排出通道;所述A板第一水蒸气通孔214、B板第一水蒸气通孔224与水蒸气出口14连通并构成第一水蒸气通道;所述A板第二水蒸气通孔215、B板第二水蒸气通孔225与水蒸气进口15连通并构成第二水蒸气通道。
In this embodiment, the raw material
本实施例中,所述A板原料水进水通孔211处设有原料水侧流进口216,A板原料水回流通孔212处设有原料水侧流出口217,A板第二水蒸气通孔215处设有二次水蒸气逸出口218;所述B板第一水蒸气通孔224处设有一次水蒸气输入口226,B板蒸馏水排出通孔223处设有蒸馏水排出口227;所述原料水间隙通道的底部分别连通所述原料水侧流进口216、原料水侧流出口217与原料水进水通道、原料水回流通道;所述原料水间隙通道的顶部通过二次水蒸气逸出口218与第二水蒸气通道连通;所述水蒸气间隙通道分别连通一次水蒸气输入口224、蒸馏水排出口227与第一水蒸气通道、蒸馏水排出通道。
In this embodiment, the raw material
本实施例中,所述A型热交换板21与B型热交换板22依次间隔设置,任意两个相邻的A型热交换板21与B型热交换板22之间均设有间隙通道,由于A型热交换板21上面设有原料水侧流进口216、原料水侧流出口217、二次水蒸气逸出口218, B型热交换板22上面设有一次水蒸气输入口226、蒸馏水排出口227;温度较低的原料水通过A型热交换板21的原料水侧流进口216进入A型热交换板21与B型热交换板22之间的原料水间隙通道,完成热交换过程之后通过原料水侧流出口217流出A型热交换板21与B型热交换板22之间的原料水间隙通道;所述水蒸气收集加压装置3经过第一水蒸气通道排出的水蒸气通过B型热交换板22的一次水蒸气输入口226进入A型热交换板21与B型热交换板22之间的水蒸气间隙通道,并在水蒸气间隙通道内部完成冷凝过程,成为蒸馏水之后通过蒸馏水排出口227排出;因此,任意两个间隔的热交换板间隙通道中分别通过水蒸气与原料水,所述水蒸气与原料水通过热交换板隔开,不会相互接触。
In this embodiment, the A-type
本发明的节能型蒸馏水机的预热装置1与热交换装置2内部相互连通成一整体,分别构成原料水进水通道、原料水回流通道、蒸馏水排出通道、第一水蒸气通道、第二水蒸气通道。在生产过程中,所述节能型蒸馏水机内部将同时进行以下三个工作过程:
The
(一)、预热装置1的壳体16内部的加热管对壳体16内部的原料水进行加热,使得原料水的温度升高产生水蒸气,在此称为一次水蒸气,所述水蒸气收集加压装置3对上述一次水蒸气进行收集并施加压力后通过水蒸气出口14将一次水蒸气排出,排出的水蒸气进入第一水蒸气通道之后通过B型热交换板22的一次水蒸气输入口226进入A型热交换板21与B型热交换板22之间的供水蒸气通过的水蒸气间隙通道,经过与温度较低的原料水热交换之后成为蒸馏水,并通过蒸馏水排出通道排出。
(1) The heating tube inside the
(二)、温度较低的原料水通过外部的原料水输送管道输送到原料水进口11,然后进入到原料水进水通道,再通过A型热交换板21的原料水侧流进口216进入所述A型热交换板21与B型热交换板22之间的供原料水通过的原料水间隙通道,并在流动的过程中与热交换板另一侧的水蒸气进行热量交换,温度较低的原料水经过热交换的过程之后吸收热量成为温度较高的原料水,再通过A型热交换板21的原料水侧流出口217进入原料水回流通道,最后流回到预热装置1的壳体内部,经过加热管的加热之后成为水蒸气,重复上述工作过程(一)。
(2) Raw material water with low temperature is transported to the raw
(三)、温度较低的原料水经过热交换的过程之后吸收热量温度升高,产生大量二次水蒸汽,该部分二次水蒸气通过A型热交换板21的二次水蒸气逸出口218排出A型热交换板21与B型热交换板22之间的原料水间隙通道,然后进入第二水蒸气通道,通过水蒸气进口15进入所述水蒸气收集加压装置3,经过水蒸气收集加压装置3施加压力后通过水蒸气出口14排出并进入第一水蒸气通道,进入热交换板之间的水蒸气间隙通道,经过与温度较低的原料水热交换之后成为蒸馏水并通过蒸馏水排出通道排出。
(3) After the heat exchange process, the lower temperature raw water absorbs heat and the temperature rises to generate a large amount of secondary water vapor. This part of the secondary water vapor passes through the secondary
本发明的节能型蒸馏水机在生产过程中,同时进行上述三个工作过程,利用原料水作为冷却水对水蒸气进行冷却,在热交换的过程中,水蒸气冷凝为蒸馏水时释放的热能被温度较低的原料水吸收,原料水的温度升高至90~95℃,然后回流至预热装置1中经过加热管较短时间的加热之后即可产生大量的水蒸气,减少了原料水转化为水蒸气的过程中的加热时间,节约能源;同时在原料水与水蒸气进行热交换的过程中,温度升高之后的原料水也会产生大量的水蒸气,本部分称其为二次水蒸气,该部分二次水蒸气经过上述工作过程(三)成为蒸馏水,由于该部分水蒸气的产生,使得本发明的节能型蒸馏水机生产蒸馏水的单位时间内产水量增大,产水效率大大提高,生产成本降低。
In the production process of the energy-saving distilled water machine of the present invention, the above-mentioned three working processes are carried out simultaneously, and the water vapor is cooled by using raw water as cooling water. Lower raw material water absorption, the temperature of the raw material water rises to 90-95°C, and then returns to the
本实施例中,所述水蒸气收集加压装置3内部设有涡轮机,在生产过程中,所述涡轮机工作,将所述壳体16内产生的一次水蒸气与热交换装置2的原料水间隙通道内产生的二次水蒸气通过水蒸气进口15吸入所述水蒸气收集加压装置3,对吸入的水蒸气施加压力后通过水蒸气出口14排出,然后进入第一水蒸气通道,再进入热交换板之间的水蒸气间隙通道冷凝成为蒸馏水。
In this embodiment, the steam collecting and pressurizing
本实施例中,所述A型热交换板21与B型热交换板22依次间隔排列,通过分设在两侧的固定筋条4以及端部的固定板5与所述预热装置1连接。所述固定板5的作用有两个,一是与固定筋条4配合将多个A型热交换板21与B型热交换板22紧密叠加连接在一起,同时与预热装置1紧密连接;二是对所述节能型蒸馏水机内部的原料水进水通道、原料水回流通道、蒸馏水排出通道、第一水蒸气通道、第二水蒸气通道的末端进行密封。
In this embodiment, the A-type
优选的,所述固定筋条4与固定板5连接的一端设有弹簧6。所述弹簧6能够对所述A型热交换板21与B型热交换板之间的叠加压力进行调节,当所述A型热交换板21与B型热交换板的水蒸气间隙通道内的水蒸气压力降低时,所述弹簧6能够使得所述A型热交换板21与B型热交换板之间的间隙通道的宽度降低,保证A型热交换板21与B型热交换板22之间的密封性;当所述A型热交换板21与B型热交换板的水蒸气间隙通道内的水蒸气压力升高时,所述弹簧6能够使得所述A型热交换板21与B型热交换板之间的间隙通道的宽度增大,防止因压力过大而出现水蒸气泄露或者对热交换装置2造成损坏的情况发生。
Preferably, a
优选的,所述热交换装置2包括第一热交换装置、第二热交换装置,所述第一热交换装置、第二热交换装置分别连接在所述预热装置1的两端。生产过程中,第一热交换装置、第二热交换装置可以同时对一次水蒸气进行冷凝,同时能够产生更多的二次水蒸气,增加单位时间内蒸馏水的产出量,提高生产效率,减低成本。
Preferably, the
本实施例中,所述壳体16内部设有水位计。通过水位计测量所述壳体16内部的原料水的容量,所述壳体16还设置有观察窗口,用于观察壳体内部的情况。
In this embodiment, a water level gauge is provided inside the
本实施例中,所述壳体16内部设有废气排出管。所述废气排除管的开口位于壳体16内部空间的上部,在生产过程中,每一个小时将废气排出管打开2~3分钟,以排除壳体内部积累的氧气等气体,提高热交换的效率。
In this embodiment, the
实施例2。Example 2.
如图5至图6所示,本实施例与实施例1的区别在于,所述A型热交换板21设置有若干A板凹槽219,所述B型热交换板22上设置有若干B板凹槽228,所述A板凹槽219、B板凹槽228能够增加A型热交换板21、B型热交换板22的换热面积,提高换热效率。
As shown in Figures 5 to 6, the difference between this embodiment and
本实施例中未解释的技术特征,采用实施例1中的解释,在此不再进行赘述。
For the technical features not explained in this embodiment, the explanations in
以上实施例仅用于说明本发明的技术方案而非对本发明保护范围的限制,尽管参照较佳实施例对本发明作了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的实质和范围。 The above embodiments are only used to illustrate the technical solution of the present invention rather than limiting the protection scope of the present invention. Although the present invention has been described in detail with reference to the preferred embodiments, those of ordinary skill in the art should understand that the technical solution of the present invention can be carried out Modification or equivalent replacement without departing from the spirit and scope of the technical solution of the present invention.
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