CN205387520U - 煤化工高盐废水的处理回收系统 - Google Patents
煤化工高盐废水的处理回收系统 Download PDFInfo
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- CN205387520U CN205387520U CN201620080504.3U CN201620080504U CN205387520U CN 205387520 U CN205387520 U CN 205387520U CN 201620080504 U CN201620080504 U CN 201620080504U CN 205387520 U CN205387520 U CN 205387520U
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- unit
- filtration unit
- water
- salt
- chemical industry
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- 239000011780 sodium chloride Substances 0.000 title claims abstract description 45
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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[C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 title claims abstract description 22
- 239000003245 coal Substances 0.000 title claims abstract description 22
- 239000011901 water Substances 0.000 title claims abstract description 22
- 150000003839 salts Chemical class 0.000 title abstract description 12
- 239000002351 wastewater Substances 0.000 claims abstract description 31
- 238000000108 ultra-filtration Methods 0.000 claims abstract description 20
- 238000005039 chemical industry Methods 0.000 claims abstract description 19
- 239000008234 soft water Substances 0.000 claims abstract description 10
- 239000007788 liquids Substances 0.000 claims abstract description 6
- 239000000706 filtrates Substances 0.000 claims abstract description 4
- 238000000034 methods Methods 0.000 claims description 22
- 238000001223 reverse osmosis Methods 0.000 claims description 18
- 238000001728 nano-filtration Methods 0.000 claims description 17
- 238000001704 evaporation Methods 0.000 claims description 14
- PMZURENOXWZQFD-UHFFFAOYSA-L na2so4 Chemical compound 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[Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 abstract description 12
- FAPWRFPIFSIZLT-UHFFFAOYSA-M sodium chloride Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 abstract description 12
- 229910001390 sodium chloride Inorganic materials 0.000 abstract description 12
- 229910052938 sodium sulfate Inorganic materials 0.000 abstract description 12
- 235000011152 sodium sulphate Nutrition 0.000 abstract description 12
- 241000276438 Gadus morhua Species 0.000 abstract description 5
- 235000019516 cod Nutrition 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 5
- 239000002699 waste materials Substances 0.000 abstract description 3
- 239000001123 sodium sulphates Substances 0.000 abstract 3
- 239000012141 concentrates Substances 0.000 abstract 1
- 239000007787 solids Substances 0.000 abstract 1
- 239000000126 substances Substances 0.000 description 8
- 238000000926 separation method Methods 0.000 description 4
- 239000002910 solid wastes Substances 0.000 description 4
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O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910001885 silicon dioxide Inorganic materials 0.000 description 2
- 239000000377 silicon dioxide Substances 0.000 description 2
- 238000001311 chemical methods and processes Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
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- 239000008233 hard water Substances 0.000 description 1
- 239000003921 oils Substances 0.000 description 1
- 239000000047 products Substances 0.000 description 1
- 239000002994 raw materials Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 230000000717 retained Effects 0.000 description 1
- KEAYESYHFKHZAL-UHFFFAOYSA-N sodium Chemical compound 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[Na] KEAYESYHFKHZAL-UHFFFAOYSA-N 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- FKNQFGJONOIPTF-UHFFFAOYSA-N sodium cation Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [Na+] FKNQFGJONOIPTF-UHFFFAOYSA-N 0.000 description 1
- 235000002639 sodium chloride Nutrition 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000004449 solid propellant Substances 0.000 description 1
- 239000011269 tars Substances 0.000 description 1
Classifications
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D3/00—Halides of sodium, potassium or alkali metals in general
- C01D3/04—Chlorides
- C01D3/06—Preparation by working up brines; seawater or spent lyes
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D5/00—Sulfates or sulfites of sodium, potassium or alkali metals in general
-
- 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/44—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis
- C02F1/442—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by nanofiltration
-
- 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
- C02F1/444—Treatment of water, waste water, or sewage by dialysis, osmosis or reverse osmosis by ultrafiltration or microfiltration
-
- 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
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/08—Multistage treatments, e.g. repetition of the same process step under different conditions
Abstract
Description
技术领域
[0001] 本实用新型涉及化工技术领域,具体涉及一种煤化工高盐废水的处理回收系统。
背景技术
[0002] 中国能源状况属于多煤少油类型,因此煤化工技术在能源的再生与消费中占有着 重要地位。煤化工是以煤炭为原料,经化学加工使煤转化为气体、液体、固体燃料及化学品 的过程,其主要包括煤的气化、液化、干馏,以及焦油的加工等。煤化工的应用发展不可避免 地会产生大量的废水,这是煤化工产业的一大特点,这些废水中主要含有大量的有机物及 无机盐,水质复杂。
[0003] 现有技术中,煤化工产业产生的废水的处理步骤主要是:微生物好氧厌氧-化学 氧化-反渗透膜分离,经过反渗透膜分离后产生的清水直接达到排放标准,而反渗透浓缩 水则含有6%左右的无机盐及少量C0D,目前针对这些高盐反渗透浓缩废水,企业采用的处 理办法是将其直接蒸干,以使外排的废水量大大降低,但是对于蒸干后产生的无机盐固废 则是煤化工企业处理的一大难题。以每小时产生60t反渗透浓缩水为计,采用上述方法处理 后每年产生的无机盐固废高达30000t,这些无机盐固废只能按危化品处理,给企业带来沉 重的经济负担。因此如何解决固废的排放问题,已成为煤化工企业的一大技术瓶颈。
发明内容
[0004] 本实用新型的目的是提供一种使用效果好、可以有效保证资源合理化利用的煤化 工高盐废水的处理回收系统。
[0005] 为实现上述目的,本实用新型采用的技术方案是:一种煤化工高盐废水的处理回 收系统,其特征在于:包括依次布置的软水器、超滤单元和纳滤单元,超滤单元的进液口和 滤液出口分别与软水器的软水出口、纳滤单元的进口端相连,纳滤单元的的透过液出口和 浓缩液出口分别通向第一、第二蒸发浓缩单元。
[0006] 采用上述技术方案产生的有益效果在于:使用时,将现有技术中经过微生物好氧 厌氧、化学氧化及反渗透膜分离处理后得到的高盐废水通入软化器内,通过软化器的软化 吸附作用,使得高盐废水的硬度下降,经软化后得到的废水经过超滤单元的超滤处理,可将 软水中的一部分悬浮物和C0D去除,这样得到的超滤滤液通过纳滤膜的道南效应即可将其 中的氯化钠和硫酸钠分离,最后经第一、第二蒸发浓缩单元蒸发浓缩从而得到氯化钠和硫 酸钠晶体。与现有技术相比,采用本实用新型公开的处理系统可以有效地从煤化工产业产 生的高盐废水中回收得到合格的氯化钠和硫酸钠产品,实现资源的合理化利用,达到了变 废为宝的目的。
附图说明
[0007]图1是本实用新型的结构不意图。
具体实施方式
[0008] 一种煤化工高盐废水的处理回收系统,其包括依次布置的软水器10、超滤单元30 和纳滤单元40,超滤单元30的进液口 31和滤液出口 32分别与软水器10的软水出口 12、纳滤 单元40的进口端41相连,纳滤单元40的透过液出口 42和浓缩液出口 43分别通向第一、第二 蒸发浓缩单元50、60。使用时,将现有技术中经过微生物好氧厌氧、化学氧化及反渗透膜分 离处理后得到的高盐废水从软化器10的硬水进口 11通入软化器10内,通过软化器10的软化 吸附作用,使得高盐废水的硬度下降,具体的,所述软化器10可以采用石灰-纯碱法、强酸型 阳树脂交换法以及弱酸性阳树脂交换法等任意一种方法对高盐废水加以软化,由于煤化工 用水产生的高盐废水中钙离子和镁离子的浓度较高,通过软化器10的软化作用可将高盐废 水中的钙离子和镁离子置换为钠离子,同时将高盐废水中的游离硅吸附去除,这样既可以 避免钙离子、镁离子以及游离硅在后序的过滤等设备中结垢影响设备的使用寿命,同时又 可以通过后序的纳滤单元40的过滤作用分离得到高浓度的氯化钠和硫酸钠。具体来说,一 方面经过超滤单元30的超滤处理,可将软水中的一部分悬浮物去除,提高色度要求,另外软 水中的C0D可以去除40%,超滤得到的浓缩液含量极少,因此从超滤单元30的浓液出口端33 排出后直接焚烧处理即可;另一方面针对超滤滤液,通过纳滤膜的道南效应,其对一价盐和 二价盐的截留率不同,因此可将超滤滤液中的氯化钠和硫酸钠分离,而纳滤膜对氯化钠的 截留率低,因此通过纳滤单元40后氯化钠是透过纳滤膜从其透过液出口42排出,然后经第 一蒸发浓缩单元50蒸发浓缩进而得到氯化钠晶体,而硫酸钠则被纳滤膜截留并从浓缩液出 口 43排出,然后经第二蒸发浓缩单元60蒸发浓缩进而得到硫酸钠晶体。与现有技术相比,采 用本实用新型公开的处理系统可以有效地对高盐废水加以处理,实现变废为宝。
[0009] 作为进一步的优选方案:所述软水器10和超滤单元30之间设置有高压反渗透单元 20(即高压R0 20),高压反渗透单元20的液体进口 21、浓液出口 22分别与软水器10的软水出 口 12、纳滤单元40的进口端41相连。高压反渗透单元20的进膜压力为3.0-8. OMPa,使用时, 高压反渗透单元20的清液出口 12通向外排水管道或水资源回收管道。通过高压反渗透单元 20的反渗透得到的清水是进料的三分之二,这些清水达标可以直接外排或者回收再利用, 如此可以大大降低后序超滤、纳滤单元30、40工段的处理压力,经检测,经高压反渗透单元 20反渗透得到的浓液中氯化钠、硫酸钠以及C0D的总含量约6%。
[0010] 进一步的,纳滤单元40中膜元件的截留分子量为100-600D;超滤单元30中膜元件 的截留分子量为1000-5000D;所述第一、第二蒸发浓缩单元50、60为多效蒸发浓缩设备或 MVR浓缩设备。采用上述结构的超滤、纳滤单元30、40以及第一、第二蒸发浓缩单元50、60可 以有效地对高盐废水加以处理,经检测,采用本实用新型公开的处理系统得到的氯化钠晶 体、硫酸钠晶体的纯度分别达95%以上和97%以上。
[0011] 为了进一步说明本实用新型的使用效果,以处理3t高盐废水为计,申请人对采用 本实用新型的各单元处理后得到的水质进行记录检测,结果如下表1所示。
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WO2018022825A1 (en) * | 2016-07-28 | 2018-02-01 | Veolia Water Technologies, Inc. | Enhanced process for selective salt recovery from wastewater and brines |
CN107902677A (zh) * | 2016-12-12 | 2018-04-13 | 威立雅水处理技术公司 | 从废水中生产硫酸钾和氯化钠的方法 |
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CN107777815A (zh) * | 2016-08-25 | 2018-03-09 | 中煤鄂尔多斯能源化工有限公司 | 一种煤化工浓盐水的处理系统和处理工艺 |
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CN102807296A (zh) * | 2012-08-30 | 2012-12-05 | 北京鑫佰利科技发展有限公司 | 一种高盐度工业废水深度处理回用工艺 |
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CN105585195A (zh) * | 2015-11-20 | 2016-05-18 | 安徽普朗膜技术有限公司 | 煤化工高盐废水的处理回收系统 |
WO2018022825A1 (en) * | 2016-07-28 | 2018-02-01 | Veolia Water Technologies, Inc. | Enhanced process for selective salt recovery from wastewater and brines |
CN108367211A (zh) * | 2016-07-28 | 2018-08-03 | 威立雅水处理技术公司 | 用于从废水、废盐和盐水中选择性回收盐的增强方法 |
US10427964B2 (en) | 2016-07-28 | 2019-10-01 | Veolia Water Technologies, Inc. | Enhanced process for selective salt recovery from wastewater, waste salts, and brines |
AU2017301936B2 (en) * | 2016-07-28 | 2019-11-14 | Veolia Water Technologies, Inc. | Enhanced process for selective salt recovery from wastewater and brines |
CN107902677A (zh) * | 2016-12-12 | 2018-04-13 | 威立雅水处理技术公司 | 从废水中生产硫酸钾和氯化钠的方法 |
WO2018111517A1 (en) * | 2016-12-12 | 2018-06-21 | Veolia Water Technologies, Inc. | Methods for producing potassium sulfate and sodium chloride from wastewater |
US10773969B1 (en) | 2016-12-12 | 2020-09-15 | Veolia Water Technologies, Inc. | Method for producing potassium sulfate and sodium chloride from wastewater |
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