SU1353477A1 - Method of desorption of solvents from activated carbon - Google Patents
Method of desorption of solvents from activated carbon Download PDFInfo
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- SU1353477A1 SU1353477A1 SU843827298A SU3827298A SU1353477A1 SU 1353477 A1 SU1353477 A1 SU 1353477A1 SU 843827298 A SU843827298 A SU 843827298A SU 3827298 A SU3827298 A SU 3827298A SU 1353477 A1 SU1353477 A1 SU 1353477A1
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- coal
- heating
- activated carbon
- desorption
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Abstract
Изобретение относитс к технологии десорбции растворителей из активированного угл , примен емой в химической , медицинской и пищевой промышленности и позвол ющей снизить энергоемкость процесса. Десорбцию дизтилового эфира или толуола из акти- вированного угл ведут нагревом электромагнитным полем сверхвысокой частоты, например, 2,45 ГГЦ в импульсном режиме при частотах повторени импульсов 20-100 Гц, интенсивности импульсов нагрева 1-10 Вт/г угл , температуру нагрев.а угл поддерживают не вьппе 120-150° С, при этом газообразный носитель, например азот, также подают в импульсном режиме с амплитудой давлений 1-5 атм синфаз- но с импульсами нагрева. Степень десорбции 90% достигаетс при удельных энергозатратах 1,4-3,75 кВт/кг продукта. 1 табл. (Л 00 ел 00 4 1The invention relates to a technology for the desorption of solvents from activated carbon used in the chemical, medical, and food industries and allowing the process to be energy intensively reduced. The desorption of dithyl ether or toluene from an activated carbon is carried out by heating with an electromagnetic field of ultrahigh frequency, for example, 2.45 GHz in a pulsed mode at pulse repetition frequencies of 20-100 Hz, heating intensity of pulses 1-10 W / g of coal, heating temperature. coal is not maintained at 120-150 & C, while a gaseous carrier, for example, nitrogen, is also supplied in a pulsed mode with an amplitude of pressures of 1–5 atm in phase with heating pulses. The degree of desorption of 90% is achieved with a specific energy consumption of 1.4-3.75 kW / kg of product. 1 tab. (L 00 el 00 4 1
Description
fOfO
1135347711353477
Изобретение относитс к адсорбционной технике, в частности к де- сорбции и рекуперации органических растворителей, и может быть использо- -вано в химической, медицинской и пищевой промышленност х, например, при производстве кормовых витаминных добавок дл животноводства.The invention relates to an adsorption technique, in particular to the desorption and recovery of organic solvents, and can be used in the chemical, medical and food industries, for example, in the production of feed vitamin supplements for animal husbandry.
Целью изобретени вл етс снижение энергоемкости процесса.The aim of the invention is to reduce the energy intensity of the process.
Пример. Пары растворител , в частности диэтилового эфира концентрацией 0,5-2,0 г/м, подают в нижнюю часть сорбционной колонны, заполненной гранулированным активированным углем марки АР-Б с диаметром гранул 3-4 ММ . Диаметр колонны 50 мм, высота сло сорбента не менее 250 мм. После насыщени активированного угл парами диэтилового эфира массой 50 г колонну отсоедин ют от реакционного аппарата и сорбент нагревают дли-. тельными импульсами энергии СВЧ частотой 2,45 Гц и удельной мощностью 10 Вт/г (амплитудное значение) в те- .0Example. Solvent vapors, in particular diethyl ether, with a concentration of 0.5-2.0 g / m, are fed to the bottom of the sorption column filled with granulated activated carbon of the AR-B brand with a granule diameter of 3-4 MM. The diameter of the column is 50 mm, the height of the sorbent layer is not less than 250 mm. After saturating the activated carbon with 50 g diethyl ether vapor, the column is disconnected from the reaction apparatus and the sorbent is heated for a long time. tal pulses of energy microwave frequency of 2.45 Hz and a specific power of 10 W / g (amplitude value) in those- .0
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охлаждают рассолом при температуре не менее минус 20 С. При данной температуре в виде насьщенных паров уноситс - 10% растворител . Таким образом из 50 г удаетс рекуперировать 40,5 г растворител .cooled with brine at a temperature of at least minus 20 ° C. At this temperature, 10% of the solvent is carried off in the form of saturated vapors. Thus, out of 50 g, 40.5 g of solvent can be recovered.
Примеры осуществлени способа десорбции толуола и диэтилового эфира электромагнитным полем СВЧ из активированного угл приведены в таблице.Examples of the method of desorption of toluene and diethyl ether by the electromagnetic field of the microwave from activated carbon are given in the table.
Из таблицы следует, что наименьшие энергозатраты 1,4 кВт/кг продукта , обеспечивакнцие степень десорбции, равную 90%, достигаютс при частоте повторени импулвсов 50 Гц. В то же врем при частоте повторени 20 и 100 Гц можно подобрать такие параметры импульсов, которые обеспечивают более низкие энергозатраты по срав-. нению с известным устройством, где энерго затраты составл ют 4,0 кВт/кг продукта.It follows from the table that the lowest energy consumption of 1.4 kW / kg of the product, ensuring a desorption rate equal to 90%, is achieved at a repetition rate of 50 Hz pulses. At the same time, with a repetition frequency of 20 and 100 Hz, it is possible to select such pulse parameters that provide lower power consumption in comparison. with a known device, where the energy consumption is 4.0 kW / kg product.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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SU843827298A SU1353477A1 (en) | 1984-12-19 | 1984-12-19 | Method of desorption of solvents from activated carbon |
Applications Claiming Priority (1)
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SU843827298A SU1353477A1 (en) | 1984-12-19 | 1984-12-19 | Method of desorption of solvents from activated carbon |
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SU1353477A1 true SU1353477A1 (en) | 1987-11-23 |
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SU843827298A SU1353477A1 (en) | 1984-12-19 | 1984-12-19 | Method of desorption of solvents from activated carbon |
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5925168A (en) * | 1997-01-31 | 1999-07-20 | Judkins; Roddie R. | Method and apparatus for separating gases based on electrically and magnetically enhanced monolithic carbon fiber composite sorbents |
WO2006099696A1 (en) * | 2005-03-24 | 2006-09-28 | Desclean Belgie, Naamloze Vennootschap | Method and device for fumigating products in an enclosed space |
CN100592869C (en) * | 2005-03-24 | 2010-03-03 | 德克勒恩比利时股份有限公司 | Method and device for fumigating products in an enclosed space |
RU2697688C1 (en) * | 2015-11-13 | 2019-08-16 | Чжуне Чантянь Интернэшнл Инджиниринг Ко., Лтд. | Flue gas cleaning device with activated carbon and flue gas cleaning method |
RU2753521C1 (en) * | 2018-05-10 | 2021-08-17 | Чжуне Чантянь Интернешнал Энджиниринг Ко., Лтд | Centralized and autonomous waste gas treatment system for multiple work processes and how to manage it |
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1984
- 1984-12-19 SU SU843827298A patent/SU1353477A1/en active
Non-Patent Citations (1)
Title |
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Авторское свидетельство СССР № 799792, кл. В 01 D 53/08, 1979. * |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5925168A (en) * | 1997-01-31 | 1999-07-20 | Judkins; Roddie R. | Method and apparatus for separating gases based on electrically and magnetically enhanced monolithic carbon fiber composite sorbents |
WO2006099696A1 (en) * | 2005-03-24 | 2006-09-28 | Desclean Belgie, Naamloze Vennootschap | Method and device for fumigating products in an enclosed space |
CN100592869C (en) * | 2005-03-24 | 2010-03-03 | 德克勒恩比利时股份有限公司 | Method and device for fumigating products in an enclosed space |
RU2697688C1 (en) * | 2015-11-13 | 2019-08-16 | Чжуне Чантянь Интернэшнл Инджиниринг Ко., Лтд. | Flue gas cleaning device with activated carbon and flue gas cleaning method |
RU2753521C1 (en) * | 2018-05-10 | 2021-08-17 | Чжуне Чантянь Интернешнал Энджиниринг Ко., Лтд | Centralized and autonomous waste gas treatment system for multiple work processes and how to manage it |
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