RU2683835C1 - Method of wastewater treatment from heavy metal ions - Google Patents
Method of wastewater treatment from heavy metal ions Download PDFInfo
- Publication number
- RU2683835C1 RU2683835C1 RU2018129052A RU2018129052A RU2683835C1 RU 2683835 C1 RU2683835 C1 RU 2683835C1 RU 2018129052 A RU2018129052 A RU 2018129052A RU 2018129052 A RU2018129052 A RU 2018129052A RU 2683835 C1 RU2683835 C1 RU 2683835C1
- Authority
- RU
- Russia
- Prior art keywords
- gypsum
- sorbent
- heavy metal
- metal ions
- wastewater treatment
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 15
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 7
- 150000002500 ions Chemical class 0.000 title claims abstract description 6
- 238000004065 wastewater treatment Methods 0.000 title description 5
- 229910052602 gypsum Inorganic materials 0.000 claims abstract description 15
- 239000010440 gypsum Substances 0.000 claims abstract description 15
- 239000002594 sorbent Substances 0.000 claims abstract description 14
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims abstract description 8
- 239000002351 wastewater Substances 0.000 claims abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000012153 distilled water Substances 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 4
- 229910000029 sodium carbonate Inorganic materials 0.000 claims abstract description 4
- 239000011734 sodium Substances 0.000 claims description 3
- -1 sorbent treatment Chemical class 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 claims 1
- 238000001179 sorption measurement Methods 0.000 abstract description 3
- 239000000843 powder Substances 0.000 abstract description 2
- 238000000746 purification Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 239000007787 solid Substances 0.000 abstract 1
- 238000001914 filtration Methods 0.000 description 6
- JPVYNHNXODAKFH-UHFFFAOYSA-N Cu2+ Chemical compound [Cu+2] JPVYNHNXODAKFH-UHFFFAOYSA-N 0.000 description 3
- 229910001431 copper ion Inorganic materials 0.000 description 3
- 239000008267 milk Substances 0.000 description 3
- 210000004080 milk Anatomy 0.000 description 3
- 235000013336 milk Nutrition 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- WLZRMCYVCSSEQC-UHFFFAOYSA-N cadmium(2+) Chemical compound [Cd+2] WLZRMCYVCSSEQC-UHFFFAOYSA-N 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000002699 waste material 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
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/58—Treatment of water, waste water, or sewage by removing specified dissolved compounds
- C02F1/62—Heavy metal compounds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
- B01J20/045—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium containing sulfur, e.g. sulfates, thiosulfates, gypsum
-
- 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
- C02F1/28—Treatment of water, waste water, or sewage by sorption
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Inorganic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Removal Of Specific Substances (AREA)
Abstract
Description
Изобретение относится к технологии очистки воды, в частности к очистке сточных вод от ионов меди сорбцией.The invention relates to water treatment technology, in particular to the treatment of wastewater from copper ions by sorption.
Известен способ очистки сточных вод от тяжелых металлов и органических веществ (SU 1560483, CO2F 1/28, Б.И. N 16, 1990 г.), включающий обработку золой и отделение осадка осаждением, в котором сточные воды последовательно обрабатывают сначала золой, содержащей оксид кальция 30-50%, до рН=8,75-9,25, а затем золой, содержащей оксид кальция 3-5%, до рН=6,5.A known method of treating wastewater from heavy metals and organic substances (SU 1560483, CO2F 1/28, B.I. N 16, 1990), comprising treating with ash and separating the precipitate by sedimentation, in which the wastewater is first treated with ash containing calcium oxide 30-50%, up to pH = 8.75-9.25, and then ash containing calcium oxide 3-5%, up to pH = 6.5.
Недостатками данного способа является большой расход сорбента в связи с малой сорбционной емкостью золы по отношению к меди, низкая скорость фильтрации и сложность технологического процесса.The disadvantages of this method is the high consumption of the sorbent in connection with the low sorption capacity of the ash in relation to copper, low filtration rate and the complexity of the process.
Известен способ очистки сточных вод от ионов меди (SU 1495308, C02F 1/62 Б.И. N 27, 1989), в котором воду обрабатывают щелочным раствором и активированным углем с последующим выдерживанием смеси при температуре 50-55 градусов в течение 30 минут и отделением осадка.A known method of wastewater treatment from copper ions (SU 1495308, C02F 1/62 B.I. N 27, 1989), in which the water is treated with an alkaline solution and activated carbon, followed by maintaining the mixture at a temperature of 50-55 degrees for 30 minutes and separation of sediment.
Недостатками данного способа являются большой расход сорбента, низкая скорость фильтрации и дополнительные затраты на технологические операции по подогреву и отстаиванию раствора.The disadvantages of this method are the high consumption of the sorbent, low filtration rate and additional costs for technological operations for heating and settling the solution.
Наиболее близким по технической сущности к заявляемому техническому решению является выбранный за прототип способ очистки сточных вод от ионов меди, который основан на фильтрации через слой сорбента толщиной слоя 0,075-0,09 м, а в качестве сорбента используется отходы измельченного пеногипса (RU №2360868, C02F 1/28, BO1J 20/28, 26.05.2008).The closest in technical essence to the claimed technical solution is the selected prototype method of wastewater treatment from copper ions, which is based on filtering through a sorbent layer with a layer thickness of 0.075-0.09 m, and as a sorbent the waste of ground foam gypsum is used (RU No. 2360868, C02F 1/28, BO1J 20/28, 05.26.2008).
Недостатком данного способа является большой расход сорбента и необходимость измельчения сорбента перед фильтрацией.The disadvantage of this method is the high consumption of the sorbent and the need for grinding the sorbent before filtration.
Задачей, на решение которой направлено заявляемое изобретение, является уменьшение расхода сорбента без фильтрации через измельченный сорбент.The problem to which the invention is directed, is to reduce the consumption of the sorbent without filtering through crushed sorbent.
Поставленная задача в предлагаемом решении достигается тем, что в способе очистки сточных вод от ионов тяжелых металлов, включающем обработку сорбентом, путем отстаивания в течение 3-х часов в присутствии готовых гипсовых изделий с размерами 20×20×20 мм, полученных при затворении порошкообразного гипса дистиллированной водой, с добавлением карбоната натрия Na2CO3 в соотношении 15% от массы гипса.The problem in the proposed solution is achieved by the fact that in the method of wastewater treatment from heavy metal ions, including sorbent treatment, by settling for 3 hours in the presence of finished gypsum products with dimensions 20 × 20 × 20 mm obtained by mixing gypsum powder distilled water, with the addition of sodium carbonate Na 2 CO 3 in the ratio of 15% by weight of gypsum.
ПРИМЕР КОНКРЕТНОГО ВЫПОЛНЕНИЯ.EXAMPLE OF SPECIFIC IMPLEMENTATION.
Предлагаемый способ осуществляется следующим образом. В качестве фильтрующего материала используют готовые изделия из гипса, которые получают следующим образом: в однородное гипсовое молочко, полученное при затворении порошкообразного гипса CaSO4⋅0,5H2O дистиллированной водой, замешиваются кристаллы карбоната натрия Na2CO3 в соотношении 15% от массы CaSO4⋅0,5H2O. Гипсовое молочко разливается в формы с кубическими ячейками размерами 20×20×20 мм. Результатом схватывания гипсового молочка являются гипсовые изделия.The proposed method is as follows. Ready-made gypsum products are used as the filtering material, which are prepared as follows: in a homogeneous gypsum milk obtained by mixing powdered gypsum CaSO 4 ⋅0.5H 2 O with distilled water, crystals of sodium carbonate Na 2 CO 3 are mixed in a ratio of 15% by weight CaSO 4 ⋅0.5H 2 O. Gypsum milk is poured into molds with cubic cells measuring 20 × 20 × 20 mm. The setting of gypsum milk results in gypsum products.
Очистке подвергались сточные воды, содержащие ионы тяжелых металлов. Отбор проб проводился после 3-х часов контакта сорбента со сточной водой. Определялась концентрация ионов меди, свинца и кадмия. Контроль за степенью очистки воды от ионов тяжелых металлов проводился на атомно-абсорбционном спектрометре.Wastewater containing heavy metal ions was treated. Sampling was carried out after 3 hours of contact of the sorbent with wastewater. The concentration of copper, lead and cadmium ions was determined. The degree of purification of water from heavy metal ions was monitored using an atomic absorption spectrometer.
В таблице приведены полученные результаты по качеству очистки сточных вод.The table shows the results obtained on the quality of wastewater treatment.
Claims (1)
Priority Applications (1)
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RU2018129052A RU2683835C1 (en) | 2018-08-07 | 2018-08-07 | Method of wastewater treatment from heavy metal ions |
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RU2018129052A RU2683835C1 (en) | 2018-08-07 | 2018-08-07 | Method of wastewater treatment from heavy metal ions |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2182130C2 (en) * | 1999-10-14 | 2002-05-10 | Институт химии и химической технологии СО РАН | Method of treatment of sewage containing copper ions |
US7144361B2 (en) * | 2003-04-28 | 2006-12-05 | Hitachi Koki Co., Ltd. | Continuous flow type centrifuge having rotor body and core body disposed therein |
RU2360868C1 (en) * | 2008-05-26 | 2009-07-10 | Государственное образовательное учреждение высшего профессионального образования "Петербургский государственный университет путей сообщения" | Method of sewage water purification from copper ions |
RU2477708C2 (en) * | 2011-07-01 | 2013-03-20 | Федеральное государственное образовательное учреждение высшего профессионального образования "Петербургский государственный университет путей сообщения" | Method of cleaning effluents of copper ions |
RU2550188C1 (en) * | 2013-12-30 | 2015-05-10 | Федеральное государственное бюджетное учреждение науки Институт химии Дальневосточного отделения Российской академии наук (ИХ ДВО РАН) | Method for producing silicate sorbent |
CN107175065A (en) * | 2017-05-05 | 2017-09-19 | 陕西科技大学 | A kind of processing of organo-mineral complexing Contaminated Loess leacheate and reuse method |
-
2018
- 2018-08-07 RU RU2018129052A patent/RU2683835C1/en not_active IP Right Cessation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
RU2182130C2 (en) * | 1999-10-14 | 2002-05-10 | Институт химии и химической технологии СО РАН | Method of treatment of sewage containing copper ions |
US7144361B2 (en) * | 2003-04-28 | 2006-12-05 | Hitachi Koki Co., Ltd. | Continuous flow type centrifuge having rotor body and core body disposed therein |
RU2360868C1 (en) * | 2008-05-26 | 2009-07-10 | Государственное образовательное учреждение высшего профессионального образования "Петербургский государственный университет путей сообщения" | Method of sewage water purification from copper ions |
RU2477708C2 (en) * | 2011-07-01 | 2013-03-20 | Федеральное государственное образовательное учреждение высшего профессионального образования "Петербургский государственный университет путей сообщения" | Method of cleaning effluents of copper ions |
RU2550188C1 (en) * | 2013-12-30 | 2015-05-10 | Федеральное государственное бюджетное учреждение науки Институт химии Дальневосточного отделения Российской академии наук (ИХ ДВО РАН) | Method for producing silicate sorbent |
CN107175065A (en) * | 2017-05-05 | 2017-09-19 | 陕西科技大学 | A kind of processing of organo-mineral complexing Contaminated Loess leacheate and reuse method |
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Effective date: 20200808 |