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SU1168510A1 - Method of extracting germanium from weak solutions - Google Patents

Method of extracting germanium from weak solutions Download PDF

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Publication number
SU1168510A1
SU1168510A1 SU843694156A SU3694156A SU1168510A1 SU 1168510 A1 SU1168510 A1 SU 1168510A1 SU 843694156 A SU843694156 A SU 843694156A SU 3694156 A SU3694156 A SU 3694156A SU 1168510 A1 SU1168510 A1 SU 1168510A1
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USSR - Soviet Union
Prior art keywords
germanium
anode
solution
carried out
extraction
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Application number
SU843694156A
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Russian (ru)
Inventor
Анатолий Александрович Ермаков
Хачик Погосович Погосян
Анатолий Михайлович Андрианов
Игорь Георгиевич Васильев
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Физико-химический институт АН УССР
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Priority to SU843694156A priority Critical patent/SU1168510A1/en
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Publication of SU1168510A1 publication Critical patent/SU1168510A1/en

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Abstract

1. СПОСОБ ИЗВЛЕЧЕНИЯ ГЕРМАНИЯ ИЗ БЕДНЫХ РАСТВОРОВ осаждением с получением концентрата германи , отличающийс  тем, что, с целью ускорени  процесса, извлечение ведут путем электрохимической обработки исходного германий со держащего раствора с растворимым анодом при рН 5-8,5 и скорости подачи раствора 1-5 л/ч на 1 дм анода. 2. Способ по п. 1, о т л и ч а ющ и и с   тем, что процесс ведут с железным или алюминиевым анодом.1. METHOD OF GERMANY EXTRACTION FROM POOR SOLUTIONS by precipitation to obtain germanium concentrate, characterized in that, in order to accelerate the process, extraction is carried out by electrochemical treatment of the initial germanium containing solution with a soluble anode at pH 5-8.5 and the feed rate of solution 1- 5 l / h per 1 dm anode. 2. The method according to claim 1, of which is carried out with the fact that the process is conducted with an iron or aluminum anode.

Description

ОдOd

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ел i Изобретение относитс  к химиче кой технологии рассе нных элементов , а именно к технологии герман и предназначено дл  извлечени  гер мани  из бедных растворов с получ нием концентратов. Целью изобретени   вл етс  уск ние процесса. Пример 1. К 1000 мл раст вора прибавл ют 1 г сульфата натри и довод т NaOH до рН 7. Полученньй раствор пропускают через элект химическую  чейку объемом в 50 см содержащую два плоскопараллельных электрода из алюмини . Рассто ние между электродами 10 мм. Скорость пропускани  раствора 15 мл/мин (3,5 л/ч на 1 дм анода). Площадь анода 0,25 дм. Плотность тока 0,75 А/дм. Напр жение 3,1 В. Полу ченную суспензию отфильтровьшают. Осадок сушат при до посто нного веса. В фильтрате и осадке определ ют концентрацию германи . Остаточна  концентраци  германи  в растворе 0,11 мг/л (допустима  концентраци  германи  в сливных во дах 2 мг/л-см). Степень осаждени  германи  99,5%, масса концентрата 152 мг. Содержание германи  в концентрате 39,1%. 02 Пример 2. Пример выполн ют аналогично примеру 1. Объем раствора 3000 мл. Германий осаждают из раствора. Дополнительно электролит не ввод т, рН не регулируют. Электроды из железа (сталь ст. 3). Скорость пропускани  раствора 4 мл/мин (1 л/ч на 1 дм анода). Плотность тока 0,75 А/дм, напр жение 1 Б. Остаточна  концентраци  германи  в фильтрате 0,1 мг/л. Степень осаждени  германи  98,2%. Масса концентрата 76 мг. Содержание герман11  в концентрате 21,2%., Пример 3 . Пример выполн ют аналогично примеру 1. Объем раствора 200 мл. Германий осаждают из раствора. Электроды из железа (сталь ст. 3). Скорость пропускани  раствора 4 мл/мин (1 л/ч на 1 дм анода), рН-8,5. Плотность тока 0,5 А/дм, напр жение 3,7 В. Остаточна  концентраци  германи  в фильтрате 2,0 мг/л. Степень осаждени  германи  99,9%. Масса концентрата 520 мг. Содержание германи  в концентрате 41,7%. Технико-экономический эффект предлагаемого способа состоит в ускорении процесса при одновремен-, ном увеличении концентрации германи  в целевом продукте в 4-200 разThe invention relates to chemical technology of scattered elements, namely, German technology, and is intended to extract germanium from poor solutions to produce concentrates. The aim of the invention is to accelerate the process. Example 1. To 1000 ml of a solution, 1 g of sodium sulfate is added and the NaOH is adjusted to pH 7. The resulting solution is passed through a 50 cm electronic cell containing two plane-parallel aluminum electrodes. The distance between the electrodes is 10 mm. The solution flow rate is 15 ml / min (3.5 L / h per 1 dm of anode). Anode area 0.25 dm. Current density 0.75 A / dm. The voltage is 3.1 V. The resulting suspension is filtered. The precipitate is dried at constant weight. The concentration of germanium is determined in the filtrate and the precipitate. The residual concentration of germanium in the solution is 0.11 mg / l (permissible concentration of germanium in the discharge water is 2 mg / l-cm). Germanium deposition degree is 99.5%, concentrate weight is 152 mg. The concentration of germanium in the concentrate is 39.1%. 02 Example 2. An example is carried out analogously to example 1. A solution volume of 3000 ml. Germanium precipitated from solution. Additionally, the electrolyte is not introduced, the pH is not adjusted. Electrodes from iron (steel Art. 3). The flow rate of the solution is 4 ml / min (1 l / h per 1 dm of the anode). The current density is 0.75 A / dm, the voltage is 1 B. The residual concentration of germanium in the filtrate is 0.1 mg / l. Germanium deposition degree is 98.2%. Concentrate weight 76 mg. The content of german11 in the concentrate is 21.2%., Example 3. The example is carried out analogously to example 1. A solution volume of 200 ml. Germanium precipitated from solution. Electrodes from iron (steel Art. 3). The flow rate of the solution is 4 ml / min (1 l / h per 1 dm of the anode), pH-8.5. The current density is 0.5 A / dm, the voltage is 3.7 V. The residual concentration of germanium in the filtrate is 2.0 mg / l. Germanium deposition rate is 99.9%. Concentrate weight 520 mg. The concentration of germanium in the concentrate is 41.7%. Technical and economic effect of the proposed method is to accelerate the process while simultaneously increasing the concentration of germanium in the target product by 4-200 times

Claims (2)

1. СПОСОБ ИЗВЛЕЧЕНИЯ ГЕРМАНИЯ ИЗ БЕДНЫХ РАСТВОРОВ осаждением с получением концентрата германия, отличающийся тем, что, с целью ускорения процесса, извлечение ведут путем электрохимической обработки исходного германийсодержащего раствора с растворимым анодом при pH = 5-8,5 и скорости подачи раствора 1-5 л/ч на 1 дм2 анода.1. METHOD FOR REMOVING GERMANY FROM POOR SOLUTIONS by precipitation to obtain a germanium concentrate, characterized in that, in order to accelerate the process, the extraction is carried out by electrochemical treatment of the initial germanium-containing solution with a soluble anode at pH = 5-8.5 and a solution feed rate of 1-5 l / h at 1 dm 2 of the anode. 2. Способ поп. ^отличающийся тем, что процесс ведут с железным или алюминиевым анодом.2. The method of pop. ^ characterized in that the process is conducted with an iron or aluminum anode. >>
SU843694156A 1984-01-13 1984-01-13 Method of extracting germanium from weak solutions SU1168510A1 (en)

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SU843694156A SU1168510A1 (en) 1984-01-13 1984-01-13 Method of extracting germanium from weak solutions

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5277882A (en) * 1989-04-28 1994-01-11 Union Miniere S.A. Process for recovering germanium

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Отходы германи . Технические услови . ТТ0.046. 055.ТУ. М., 1979, с. 14-18. Тананаев И.В. и Шпирт М.Я. Хими германи . М., Хими , 1967, с. 369. *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5277882A (en) * 1989-04-28 1994-01-11 Union Miniere S.A. Process for recovering germanium

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