SU267500A1 - Method of waste water purification from mercury - Google Patents

Method of waste water purification from mercury Download PDF

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Publication number
SU267500A1
SU267500A1 SU681270344A SU1270344A SU267500A1 SU 267500 A1 SU267500 A1 SU 267500A1 SU 681270344 A SU681270344 A SU 681270344A SU 1270344 A SU1270344 A SU 1270344A SU 267500 A1 SU267500 A1 SU 267500A1
Authority
SU
USSR - Soviet Union
Prior art keywords
mercury
wastewater
waste water
ozone
water purification
Prior art date
Application number
SU681270344A
Other languages
Russian (ru)
Inventor
В.А. Скрипник
Е.В. Леонтович
В.В. Лизунов
Е.А. Соловьев
А.Е. Горенбейн
В.Т. Пустовит
В.П. Чвирук
Original Assignee
Skripnik V A
Leontovich E V
Lizunov V V
Solovev E A
Gorenbejn A E
Pustovit V T
Chviruk V P
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
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Publication date
Application filed by Skripnik V A, Leontovich E V, Lizunov V V, Solovev E A, Gorenbejn A E, Pustovit V T, Chviruk V P filed Critical Skripnik V A
Priority to SU681270344A priority Critical patent/SU267500A1/en
Application granted granted Critical
Publication of SU267500A1 publication Critical patent/SU267500A1/en

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  • Removal Of Specific Substances (AREA)
  • Treatment Of Water By Oxidation Or Reduction (AREA)

Description

Известны способы очистки сточных вод от ртути путем осаждени  ее в ви де сульфида или сорбции на ионообмен ных смолах. Однако содержание ртути в сточных водах после такой очистки превьшает санитарную норму. С целью повьпнени  степени очистки сточных вод от ртути и переведени  металлической ртути в ионную форму предлагаетс  сточные воды пред варительно подкисл ть до рН не более 4 и обрабатывать окислителем, например озоном или хлором. Далее ртуть осаждают в виде сульфида или улавливают на ионообменных смолах. Доза окислител  составл ет 30-50 мл/ Обработанна  таким образом вода содержит ртуть в количестве 0,0010 ,002 мл/г при санитарной норме 0,005 мг/л. Пример 1. Озон получают из кислорода воздуха при напр жении между электродами 16 кВт и скорости , подачи воздуха 1 л/мин. Концентраци  озона в озоно-воздушной смеси составл ет 20 мг/л. В производственной сточной воде, вз той дл  опытов, содержитс  0,105 мг/л общей ртути и 0,023 мг/л окисленной. Контакт воды с озоном осуществл ют в колонне при распылении озона в воде с помощью пластинки (размер отверстий 100 мк), вмонтированной в дно колонны, высота которой 1,5 м,100%-ное окисление металлической ртути достигаетс  при рН 4 и дозе озона около 40-50 мл/л. Окисленную ртуть улавливают на ионообменной смоле в колонне высотой 25 см при скорости прохождени  воды 100 мл/ч.Methods are known for purifying wastewater from mercury by precipitating it in the form of sulfide or sorption on ion exchange resins. However, the content of mercury in wastewater after such treatment exceeds the sanitary standard. In order to purify wastewater from mercury and convert metallic mercury to ionic form, it is proposed to acidify the wastewater to a pH of no more than 4 and treat it with an oxidizing agent, such as ozone or chlorine. Further, mercury is precipitated in the form of sulfide or captured on ion exchange resins. The dose of oxidant is 30-50 ml / The water treated in this way contains mercury in an amount of 0.0010, 002 ml / g at a sanitary rate of 0.005 mg / l. Example 1. Ozone is obtained from air oxygen at a voltage between the electrodes of 16 kW and speed, with an air supply of 1 l / min. The ozone concentration in the ozone-air mixture is 20 mg / l. In the industrial wastewater, taken for the experiments, 0.105 mg / l of total mercury and 0.023 mg / l of oxidized water are contained. The water is contacted with ozone in a column by spraying ozone in water using a plate (100 µm hole size) embedded in the bottom of the column, 1.5 m high, 100% oxidation of metallic mercury is achieved at a pH of 4 and the ozone dose is about 40-50 ml / l. The oxidized mercury is trapped on an ion exchange resin in a 25 cm high column at a water flow rate of 100 ml / h.

0,0023 0,0023

0,105 0,0022 0,1050.105 0.0022 0.105

АН-2Ф0,105 0,0011AN-2F0.105 0.0011

Пример 2. Сточные воды (рН 12-13) производства хлора и каустика ртутным способом содержат ртуть: в осадке 10-20 мг/л, в растворе 12 мг/л; количество общей ртути 0,023 мг/л.Example 2. Wastewater (pH 12-13) produced by chlorine and caustic by the mercury method contains mercury: in the sediment 10-20 mg / l, in solution 12 mg / l; the amount of total mercury is 0.023 mg / l.

Осаждение взвесей производ т при рН 8. После 10 мин отстаивани  подкислением устанавливают рН, равный 4The sedimentation of the suspension is carried out at a pH of 8. After 10 minutes of settling by acidification, the pH is set to 4

Хлорирование воды ведут при концентрации хлора 30 мг/л. Через 20 мин достигаетс  полное окисление металлической ртути. После осаждени  ионов ртути трехкратным избытком сульфида натри  и фильтровани  содержание ртути в сточной воде ниже 0,005 мг/л.Chlorination of water is carried out at a chlorine concentration of 30 mg / l. After 20 minutes, complete oxidation of metallic mercury is achieved. After the precipitation of mercury ions by a threefold excess of sodium sulfide and filtration, the mercury content in the wastewater is below 0.005 mg / l.

Claims (1)

Формула изобретени Invention Formula Способ очистки сточных вод от ртути осаждением ртути в виде сульфида или с применением улавливани  на ионообменных смолах, отличающийс  тем, что, с целью повыщени  степени очистки, сточные воды предварительно подкисл ют до рН не более 4 и обрабатывают окислителем , например озоном или хлором.The method of purifying wastewater from mercury by precipitating mercury as sulphide or using trapping on ion exchange resins, characterized in that, in order to increase the degree of purification, the wastewater is pre-acidified to a pH of not more than 4 and treated with an oxidizing agent, such as ozone or chlorine.
SU681270344A 1968-09-13 1968-09-13 Method of waste water purification from mercury SU267500A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU681270344A SU267500A1 (en) 1968-09-13 1968-09-13 Method of waste water purification from mercury

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU681270344A SU267500A1 (en) 1968-09-13 1968-09-13 Method of waste water purification from mercury

Publications (1)

Publication Number Publication Date
SU267500A1 true SU267500A1 (en) 1981-06-30

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SU681270344A SU267500A1 (en) 1968-09-13 1968-09-13 Method of waste water purification from mercury

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SU (1) SU267500A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2900074A1 (en) * 2006-04-24 2007-10-26 Tredi Sa Treatment of solid wastes e.g. fiber-cement polluted by mercury, useful to fix mercurial species e.g. elemental mercury as sulfur amalgam in solid wastes, comprises oxidization and sulfidation of mercurial species in alkaline medium

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2900074A1 (en) * 2006-04-24 2007-10-26 Tredi Sa Treatment of solid wastes e.g. fiber-cement polluted by mercury, useful to fix mercurial species e.g. elemental mercury as sulfur amalgam in solid wastes, comprises oxidization and sulfidation of mercurial species in alkaline medium

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