CN201380045Y - Mine water desalination pretreatment device and reverse osmosis desalination equipment - Google Patents
Mine water desalination pretreatment device and reverse osmosis desalination equipment Download PDFInfo
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- CN201380045Y CN201380045Y CN200920105875U CN200920105875U CN201380045Y CN 201380045 Y CN201380045 Y CN 201380045Y CN 200920105875 U CN200920105875 U CN 200920105875U CN 200920105875 U CN200920105875 U CN 200920105875U CN 201380045 Y CN201380045 Y CN 201380045Y
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 79
- 238000010612 desalination reaction Methods 0.000 title claims abstract description 54
- 238000001223 reverse osmosis Methods 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 9
- 230000000694 effects Effects 0.000 abstract description 7
- 239000012528 membrane Substances 0.000 description 7
- 238000011001 backwashing Methods 0.000 description 5
- 239000003245 coal Substances 0.000 description 3
- 239000005416 organic matter Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
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- 241000894006 Bacteria Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000005065 mining Methods 0.000 description 1
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
- Y02A20/131—Reverse-osmosis
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- Separation Using Semi-Permeable Membranes (AREA)
Abstract
本实用新型提供了一种矿井水脱盐的预处理装置及反渗透脱盐设备,包括:水泵、叠片过滤器和超滤器,所述水泵、叠片过滤器和超滤器通过管道依次连接。本实用新型使得反渗透脱盐的预处理工艺更简单、处理效果更好、缩小了装置的体积。
The utility model provides a mine water desalination pretreatment device and reverse osmosis desalination equipment, comprising: a water pump, a laminated filter and an ultrafilter, and the water pump, the laminated filter and the ultrafilter are sequentially connected through pipelines. The utility model makes the pretreatment process of the reverse osmosis desalination simpler, the treatment effect is better, and the volume of the device is reduced.
Description
技术领域 technical field
本实用新型涉及一种水处理设备,特别是一种矿井水脱盐的预处理装置及反渗透脱盐设备。The utility model relates to water treatment equipment, in particular to a pretreatment device for mine water desalination and reverse osmosis desalination equipment.
背景技术 Background technique
我国煤矿大部分处在缺水的地区,矿井水资源化利用已成为解决矿区水资源短缺的主要途径。目前,国内矿井水脱盐处理主要采用反渗透脱盐处理工艺。为保证反渗透系统长期稳定、可靠运行,反渗透系统的预处理是非常重要的。反渗透系统的预处理必须满足反渗透进水的水质要求,即浊度<0.3NTU,污染指数FI值<4。预处理的主要目的是去除悬浮物、浊度、色度、有机物等。如果不除去这些物质,会聚集在膜表面使膜受到污染,并以固体形式析出,使膜性能变坏。最终导致膜的透水率和脱盐率下降,影响产水量和水质。Most of my country's coal mines are located in water-scarce areas, and the utilization of mine water resources has become the main way to solve the shortage of water resources in mining areas. At present, domestic mine water desalination treatment mainly adopts reverse osmosis desalination treatment process. In order to ensure the long-term stable and reliable operation of the reverse osmosis system, the pretreatment of the reverse osmosis system is very important. The pretreatment of the reverse osmosis system must meet the water quality requirements of the reverse osmosis influent, that is, the turbidity <0.3NTU, and the pollution index FI value <4. The main purpose of pretreatment is to remove suspended solids, turbidity, color, organic matter, etc. If these substances are not removed, they will accumulate on the surface of the membrane to contaminate the membrane and precipitate in solid form, deteriorating the performance of the membrane. Eventually, the water permeability and desalination rate of the membrane will decrease, which will affect the water production and water quality.
目前国内煤矿矿井水反渗透脱盐的预处理工艺采用传统的多介质过滤器、活性炭过滤器、精密过滤器和保安过滤器四级过滤。该处理工艺复杂、处理效果差,并且体积庞大、操作复杂,劳动强度大,难以适应目前我国煤矿的发展水平。At present, the domestic coal mine water reverse osmosis desalination pretreatment process adopts traditional four-stage filtration of multi-media filter, activated carbon filter, precision filter and security filter. The treatment process is complicated, the treatment effect is poor, and the volume is large, the operation is complicated, and the labor intensity is high, so it is difficult to adapt to the current development level of coal mines in my country.
实用新型内容Utility model content
本实用新型的目的一是提供一种矿井水脱盐的预处理装置,使得反渗透脱盐的预处理工艺更简单、处理效果更好、缩小装置的体积。The first purpose of the utility model is to provide a pretreatment device for mine water desalination, which makes the pretreatment process of reverse osmosis desalination simpler, has better treatment effect, and reduces the volume of the device.
本实用新型的目的二是提供一种反渗透脱盐设备,使得脱盐预处理工艺更简化,脱盐效果更好。The second purpose of the utility model is to provide a reverse osmosis desalination device, which simplifies the desalination pretreatment process and improves the desalination effect.
为了实现目的一,本实用新型提供一种矿井水脱盐的预处理装置,包括:水泵、叠片过滤器和超滤器,所述水泵、叠片过滤器和超滤器通过管道依次连接。In order to achieve the first objective, the utility model provides a pretreatment device for mine water desalination, including: a water pump, a laminated filter and an ultrafilter, and the water pump, the laminated filter and the ultrafilter are connected in sequence through pipelines.
由以上技术方案可知:本实用新型矿井水脱盐的预处理装置,将水泵、叠片过滤器和超滤器形成一个整体装置,具有以下优点:简化了预处理工艺,通过两种过滤器完成工作;处理效果好;缩小了装置的总体积,减小了对安装空间的要求;操作简单,降低了劳动者的劳动强度。It can be seen from the above technical scheme that the utility model mine water desalination pretreatment device forms a whole device with water pump, laminated filter and ultrafilter, which has the following advantages: the pretreatment process is simplified, and the work is completed through two kinds of filters ; The treatment effect is good; the total volume of the device is reduced, and the requirement for installation space is reduced; the operation is simple, and the labor intensity of the laborers is reduced.
为了实现目的二,本实用新型还提供一种反渗透脱盐设备,包括矿井水脱盐的预处理装置、高压泵和反渗透脱盐装置,所述矿井水脱盐的预处理装置的出水口、高压泵和反渗透脱盐装置通过管道依次连接,所述矿井水脱盐的预处理装置,包括:水泵、叠片过滤器和超滤器,所述水泵、叠片过滤器和超滤器通过管道依次连接。In order to achieve the second purpose, the utility model also provides a reverse osmosis desalination equipment, including a mine water desalination pretreatment device, a high pressure pump and a reverse osmosis desalination device, the water outlet of the mine water desalination pretreatment device, a high pressure pump and The reverse osmosis desalination device is connected sequentially through pipelines, and the pretreatment device for mine water desalination includes: a water pump, a laminated filter and an ultrafilter, and the water pump, laminated filter and ultrafilter are connected in sequence through pipelines.
由以上技术方案可知:本实用新型反渗透脱盐设备,通过增设矿井水脱盐的预处理装置,可以降低反渗透膜受污染的程度,防止膜因受到污染导致膜的透水率和脱盐率下降。From the above technical solutions, it can be known that the reverse osmosis desalination equipment of the utility model can reduce the degree of contamination of the reverse osmosis membrane by adding a pretreatment device for mine water desalination, and prevent the water permeability and desalination rate of the membrane from decreasing due to contamination of the membrane.
下面通过具体实施例并结合附图对本实用新型做进一步的详细描述。The utility model will be described in further detail below through specific embodiments in conjunction with the accompanying drawings.
附图说明 Description of drawings
图1为实用新型矿井水脱盐的预处理装置的结构示意图;Fig. 1 is the structural representation of the pretreatment device of utility model mine water desalination;
图2为实用新型反渗透脱盐设备的结构示意图。Fig. 2 is a structural schematic diagram of the utility model reverse osmosis desalination equipment.
具体实施方式 Detailed ways
实施例一Embodiment one
如图1所示,本实用新型的实施例一种矿井水脱盐的预处理装置,包括:水泵1、叠片过滤器2和超滤器3,所述水泵1、叠片过滤器2和超滤器3通过管道5依次连接。As shown in Figure 1, the embodiment of the utility model is a pretreatment device for mine water desalination, including: a
在具体应用中,将水泵1、叠片过滤器2和超滤器3固定在同一机架4内,通过水泵1将矿井水抽进管道5中。矿井水通过管道5首先流入叠片过滤器2,通过叠片过滤器2去除矿井水中沙粒、铁锈等悬浮物,并降低矿井水中有机物的含量;经过叠片过滤器2处理过的水通过管道5流入超滤器3,通过超滤器3,彻底滤除水中细菌、铁锈、胶体、大分子有机物等物质,保留对人体健康有益的微量元素,净化水的微生物、色度和浊度等主要指标,满足《GB5749-2006生活饮用水卫生标准》要求。In a specific application, the
通过矿井水脱盐的预处理装置处理过的矿井水,出水能力为5~30t/h,出水的水质可以达到浊度<0.3NTU,污染指数FI值<4,从而达到反渗透脱盐系统的预处理要求。The mine water treated by the mine water desalination pretreatment device has a water output capacity of 5-30t/h, the water quality of the effluent can reach turbidity<0.3NTU, and the pollution index FI value<4, so as to achieve the pretreatment of the reverse osmosis desalination system Require.
从上述技术方案可以看出,本实用新型一种矿井水脱盐的预处理装置有如下特点:As can be seen from the above technical scheme, a pretreatment device for mine water desalination of the utility model has the following characteristics:
1、简化了预处理工艺,处理效果好,提高了浊度去除率、污染指数FI值去除率和水回收率;1. The pretreatment process is simplified, the treatment effect is good, and the turbidity removal rate, pollution index FI value removal rate and water recovery rate are improved;
2、操作简单,降低了劳动者的劳动强度;2. The operation is simple, which reduces the labor intensity of workers;
3、装置的总体积小,降低了对安装空间的要求,使整套设备的制造成本下降。3. The total volume of the device is small, which reduces the requirement for installation space and reduces the manufacturing cost of the whole set of equipment.
实施例二Embodiment two
在所述叠片过滤器2中设有全自动反冲洗控制器。全自动反冲洗控制器不中断工作的情况下,在数秒内完成整个自动反冲洗过程。由设定的时间或压差信号自动启动反洗,反洗阀门改变过滤单元中水流方向,将截留在叠片过滤器2中盘片上的杂质冲洗出去。降低了工作人员清理过滤器的工作量,达到可以用很少的自用水量即可达到很好的清洗效果。A fully automatic backwashing controller is provided in the laminated
实施例三Embodiment three
在水泵1进水口处增设过滤器6。通过增设过滤器6可以防止大颗粒的杂质进入整套装置中,避免造成水泵1、叠片过滤器2工作效率下降。A
实施例四Embodiment four
如图2所示,本实施例一种反渗透脱盐设备,包括矿井水脱盐的预处理装置、高压泵8和反渗透脱盐装置7,所述矿井水脱盐的预处理装置的出水口、高压泵和反渗透脱盐装置通过管道5依次连接,所述矿井水脱盐的预处理装置包括:水泵1、叠片过滤器2和超滤器3,所述水泵1、叠片过滤器2和超滤器3通过管道5依次连接。As shown in Figure 2, a reverse osmosis desalination device in this embodiment includes a pretreatment device for mine water desalination, a high-
经过矿井水脱盐的预处理装置处理过的矿井水经出水口流入高压泵8的进水口。矿井水经过高压泵8加压后流入反渗透脱盐装置7,经反渗透脱盐装置7的反渗透脱盐处理可以去除水中的盐分,整个处理过程不消耗酸碱等化学物质,具有长期连续工作、操作简便、水质稳定、运行费用低、无化学污染物等突出优点。The mine water treated by the mine water desalination pretreatment device flows into the water inlet of the
最后应说明的是:以上实施例仅用以说明本实用新型的技术方案,而非对其限制;尽管参照前述实施例对本实用新型进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本实用新型各实施例技术方案的精神和范围。Finally, it should be noted that: the above embodiments are only used to illustrate the technical solutions of the present utility model, and are not intended to limit it; although the utility model has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: It is still possible to modify the technical solutions recorded in the foregoing embodiments, or perform equivalent replacements for some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit of the technical solutions of the various embodiments of the present invention. and range.
Claims (6)
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| Application Number | Priority Date | Filing Date | Title |
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| CN200920105875U CN201380045Y (en) | 2009-02-24 | 2009-02-24 | Mine water desalination pretreatment device and reverse osmosis desalination equipment |
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| CN200920105875U CN201380045Y (en) | 2009-02-24 | 2009-02-24 | Mine water desalination pretreatment device and reverse osmosis desalination equipment |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815813A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Pretreatment process for mine drainage water |
| CN102815814A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Mine drainage water deep treatment technology |
| CN115259460A (en) * | 2022-08-02 | 2022-11-01 | 淮南矿业(集团)有限责任公司 | Method for treating brackish mine water of coal mine |
-
2009
- 2009-02-24 CN CN200920105875U patent/CN201380045Y/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102815813A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Pretreatment process for mine drainage water |
| CN102815814A (en) * | 2011-06-10 | 2012-12-12 | 天源环保有限公司 | Mine drainage water deep treatment technology |
| CN115259460A (en) * | 2022-08-02 | 2022-11-01 | 淮南矿业(集团)有限责任公司 | Method for treating brackish mine water of coal mine |
| CN115259460B (en) * | 2022-08-02 | 2024-05-14 | 淮南矿业(集团)有限责任公司 | Treatment method of brackish mine water of coal mine |
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Assignee: ViewSonic energy (Fukang) Coal Industry Co Ltd Assignor: National Engineering Research Center for Gas Controlling of Pingan Mine Contract record no.: 2013990000576 Denomination of utility model: Pretreatment device and reverse osmosis desalination apparatus for desalination of mine water Granted publication date: 20100113 License type: Common License Record date: 20130911 |
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