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CN1843945A - 利用射流技术的海水淡化处理系统 - Google Patents

利用射流技术的海水淡化处理系统 Download PDF

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CN1843945A
CN1843945A CNA2006100804427A CN200610080442A CN1843945A CN 1843945 A CN1843945 A CN 1843945A CN A2006100804427 A CNA2006100804427 A CN A2006100804427A CN 200610080442 A CN200610080442 A CN 200610080442A CN 1843945 A CN1843945 A CN 1843945A
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seawater
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徐小宁
嵇明
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Priority to EP07251990A priority patent/EP1857171A3/en
Priority to US11/803,721 priority patent/US20070284299A1/en
Priority to IL183223A priority patent/IL183223A0/en
Priority to JP2007130632A priority patent/JP2007307553A/ja
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
    • C02F1/441—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by reverse osmosis
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/025—Reverse osmosis; Hyperfiltration
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D61/00—Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/02—Reverse osmosis; Hyperfiltration ; Nanofiltration
    • B01D61/04—Feed pretreatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/02—Treatment of water, waste water, or sewage by heating
    • C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F9/00—Multistage treatment of water, waste water or sewage
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D2311/00—Details relating to membrane separation process operations and control
    • B01D2311/04—Specific process operations in the feed stream; Feed pretreatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/001—Processes for the treatment of water whereby the filtration technique is of importance
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/34—Treatment of water, waste water, or sewage with mechanical oscillations
    • C02F1/36—Treatment of water, waste water, or sewage with mechanical oscillations ultrasonic vibrations
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/02—Non-contaminated water, e.g. for industrial water supply
    • C02F2103/026—Treating water for medical or cosmetic purposes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/08—Seawater, e.g. for desalination
    • 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
    • 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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  • Water Supply & Treatment (AREA)
  • Engineering & Computer Science (AREA)
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  • Environmental & Geological Engineering (AREA)
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  • Chemical Kinetics & Catalysis (AREA)
  • Nanotechnology (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Water Treatments (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
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Abstract

本发明涉及一种利用射流技术的海水淡化处理系统，过滤装置，声能处理装置，淡化装置三部分组成。粗滤、精滤后的海水进入声能处理装置，经声能处理装置处理过的海水成为小分子团海水，储存在储水池中，经泵送至反渗透膜，渗透后的水，成为淡水，储存在淡水池中。上述过程中，可将反渗透膜改为蒸馏器。本发明的优点在于：海水淡化设备的结构简单，投资少，成本低，性能稳定。不仅将海水淡化，而且还将海水短链为小分子团水，易于人体的吸收利用。

Description

利用射流技术的海水淡化处理系统
技术领域
本发明涉及海水淡化处理装置，具体涉及一种利用射流技术的海水淡化处理系统，属于国际专利分类C02F1/00“水、废水、污水的处理”技术领域。
背景技术
目前，国内外采用的海水淡化的方法比较多，如变相法、蒸发法、蒸馏法、冷却法、膜分离法、反渗透法、电渗析法、化学平衡法、离子交换法、水合法、溶剂萃取法等。目前处于领先地位的是闪急蒸馏法，约占当今海水淡化总产量的70％。其缺点是：设备投资多，海水循环量大，制水量小，制水速度慢，浓缩率较低，操作费用高。
发明内容
本发明的目的，在于克服上述方法的不足，提供一种采用射流技术的新型海水淡化处理系统。
本发明的目的是由以下技术方案实现的。
利用射流技术的海水淡化处理系统，包括过滤装置，声能处理装置，淡化装置三部分组成。过滤装置包括海水采集口，连接海水泵，连接粗过滤装置，再连接精过滤装置。精滤后的海水进入声能处理装置，根据实际需要，该声能处理装置可以为二级至多级。经声能处理装置处理过的海水，已成为小分子团海水，储存在储水池中，经泵送至反渗透膜，渗透后的水，成为淡水，储存在淡水池中。
本发明的另一种方案是：将上述方案中的反渗透膜改为蒸馏器，经蒸馏器蒸馏出的淡水，储存在淡水池中。
所述的声能处理装置主要为一流体声能发生器，是一金属腔体，包括一中腔体及上、下轴腔所组成；上、下轴腔的上、下两端面的轴心设有同轴的两个出口，中腔体上均匀分布有入口。中腔体上分布的入口为4-40个。该入口为顺流体走向的斜孔，该入口轴线与外圆切线的夹角为30°-90°。该入口孔径与出口孔径的比值为100∶1-20。所述的流体声能发生器内腔上轴腔的根直径与中腔体的直径之比为1∶1-5。
本发明的优点在于：结构简单，设备投资少，成本低，性能稳定。不仅将海水淡化，而且还将海水短链为小分子团水，易于人体的吸收利用。
附图说明
图1为本发明海水淡化处理系统的装备组合示意图；
图2、3为声能处理装置中声能发生器的内腔结构示意图。
图中：1、海水采集口，2、海水泵，3、粗滤装置，4、精滤装置，5、空压机，6、声能处理装置，7、小分子海水储水池，8、泵，9、反渗透膜，10、淡水池，11、流体声能发生器.
具体实施方式
如图1所示，准备淡化的海水，通过海水采集口1，由海水泵2送至粗滤装置3，进行初步过滤，滤除多种杂质。粗滤后，进入精滤装置4，进行灭菌等处理。精滤后进入声能处理装置6，由空压机5送空气至流体声能发生器11，经二级(可多级)射流振动处理，成为精制的小分子海水，存入小分子海水储水池7中，再经泵8送至反渗透膜9，经反渗透处理后，去除盐分，成为淡水，存入淡水池10内，可供使用。(上述粗滤装置和精滤装置均为现有技术中应用的装置。)
如图2所示，流体声能发生器1为一金属腔体，包括一中腔体及上、下轴腔所组成；上、下轴腔的上、下两端面的轴心设有同轴的两个出口，中腔体上均匀分布有入口。中腔体上分布的入口为440个。该入口为顺流体走向的斜孔，该入口轴线与外圆切线的夹角为30°-90°。入口孔径与出口孔径的比值为100∶1-20。所述的流体声能发生器1内腔上轴腔的根直径与中腔体的直径之比为1∶1-5。发生器的频率为100HZ-30万HZ，发生器的声强大于100dB。液体压力泵的压力为0.2Mpa-80Mpa；液体压力泵的功率为2KW-500KW。
本发明所称的射流技术，即流体声能加工技术，其原理如下：流体声能加工的过程可以简述为：根据对固态、液态、气态等不同的被加工物质的不同特性和加工目的，选择特定的流体动力介质、特定的声频、特定的声强、特定的声场分布和其它工艺条件，在这些条件下对被加工物质进行声能加工处理，使被加工物质发生相应的力学效应、或热学效应、或化学效应、或生物效应、或以上多种效应所引起的变化，达到声能加工的目的。
“流体动力式声能发生器是以流体为动力源，利用调整液体或高速气体来产生可听声与超声的发生器。……的独特优点是结构简单、造价低、处理量大，操作方便，经久耐用，⑦”并且更重要的是它的“耗能小，动力源方便，因而很适合于工业应用。⑧”虽然理论上流体动力式声能发声器具有上述7种优点，但要研制出如本发明的流体动力式声能水煤浆制备系统必须跨越从理论的可能性达到技术现实性之间的距离。
“目前流体动力式声能发声器在工业应用方面已显示出它的独特优点，展示出它的巨大生命力。然而，由于…其中涉及到的数学处理非常困难，因而至今…发声机理还没有得到较为令人满意的解释，大部分的研究仅限于有关实验现象分析。在一系列的应用中，主要基于经验公式以及具体不同的状况的实验曲线给出的结果与特征趋势来考虑问题。对于实际要求来说，理论上的精确预示与计算有关的声波特征，如频率、强度、声场分布等等，无疑能更有利于它的应用以及控制。因而，对流体动力发声器声波的产生和特征的进一步研究是今后值得深入探讨的研究方向。⑨”
上述“关于声能”部份的注释内容引自应崇福所著《超声学》一书：⑦……引自第495页第七章第7.3节；⑧……引自第506页第七章第7.3.6节；⑨……引自第506页第七章第7.3.6节。《超声学》为中国科学出版社出版；【京】新登字092号；1990年12月第一版1993年12月第二次印刷。

Claims (7)

1、一种利用射流技术的海水淡化处理系统，其特征在于：它包括过滤装置，声能处理装置，淡化装置三部分，过滤装置的组成为：海水采集口(1)，连接海水泵(2)，海水泵(2)连接粗过滤装置(3)，粗过滤装置(3)的出口连接精过滤装置(4)的入口；精过滤装置(4)的出口连接声能处理装置(6)，最后一级声能处理装置连接小分子团海水储水池(7)，储水池(7)通过泵(8)连接反渗透膜(9)，由管路连接淡水池(10)。
2、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的反渗透膜(9)可以由蒸馏器来替代。
3、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的声能处理装置(6)为一级至多级流体声能发生器(11)的组合；流体声能发生器(11)是一金属腔体，包括一中腔体及上、下轴腔所组成；上、下轴腔的上、下两端面的轴心设有同轴的两个出口，中腔体上均匀分布有入口。
4、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的中腔体上分布的入口为4-40个。
5、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的入口为顺流体走向的斜孔，该入口轴线与外圆切线的夹角为30°-90°。
6、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的入口孔径与出口孔径的比值为100∶1-20。
7、根据权利要求1所述的利用射流技术的海水淡化处理系统，其特征在于：所述的流体声能发生器(11)内腔上轴腔的根直径与中腔体的直径之比为1∶1-5。
CNA2006100804427A 2006-05-16 2006-05-16 利用射流技术的海水淡化处理系统 Pending CN1843945A (zh)

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Application Number Priority Date Filing Date Title
CNA2006100804427A CN1843945A (zh) 2006-05-16 2006-05-16 利用射流技术的海水淡化处理系统
EP07251990A EP1857171A3 (en) 2006-05-16 2007-05-15 Seawater desalination system with sonic energy pretreatment.
US11/803,721 US20070284299A1 (en) 2006-05-16 2007-05-15 Seawater desalination system using jet technique
IL183223A IL183223A0 (en) 2006-05-16 2007-05-15 Seawater desalination system using jet technique
JP2007130632A JP2007307553A (ja) 2006-05-16 2007-05-16 噴射流技術を利用する海水淡水化システム

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WO2009062364A1 (fr) * 2007-11-13 2009-05-22 Xiaohua Xu Système de dessalement de l'eau de mer utilisant la technique de jet cavitant
WO2016161862A1 (zh) * 2015-04-08 2016-10-13 李岳桓 矿石组成物及其制成的水产生器、海水淡化设备和小分子水产生方法
CN108128940A (zh) * 2017-11-22 2018-06-08 南京悠谷新材料科技有限公司 海水淡化处理设备

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