WO2012128671A1 - Method for producing a sorbent for removing oil and petroleum products from an aqueous surface and from soil - Google Patents
Method for producing a sorbent for removing oil and petroleum products from an aqueous surface and from soil Download PDFInfo
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- WO2012128671A1 WO2012128671A1 PCT/RU2012/000216 RU2012000216W WO2012128671A1 WO 2012128671 A1 WO2012128671 A1 WO 2012128671A1 RU 2012000216 W RU2012000216 W RU 2012000216W WO 2012128671 A1 WO2012128671 A1 WO 2012128671A1
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- sorbent
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Classifications
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- 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
- C02F1/288—Treatment of water, waste water, or sewage by sorption using composite sorbents, e.g. coated, impregnated, multi-layered
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- 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
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/265—Synthetic macromolecular compounds modified or post-treated polymers
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- 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
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3202—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the carrier, support or substrate used for impregnation or coating
- B01J20/3206—Organic carriers, supports or substrates
- B01J20/3208—Polymeric carriers, supports or substrates
- B01J20/3212—Polymeric carriers, supports or substrates consisting of a polymer obtained by reactions otherwise than involving only carbon to carbon unsaturated bonds
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- 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
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/32—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating
- B01J20/3231—Impregnating or coating ; Solid sorbent compositions obtained from processes involving impregnating or coating characterised by the coating or impregnating layer
- B01J20/3242—Layers with a functional group, e.g. an affinity material, a ligand, a reactant or a complexing group
- B01J20/3268—Macromolecular compounds
- B01J20/327—Polymers obtained by reactions involving only carbon to carbon unsaturated bonds
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
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- 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
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
Definitions
- the invention relates to a technology for the production of sorbents for cleaning water surface and soil from oil and oil products during their accidental or emergency spills, as well as for the treatment of oily wastewater.
- a known method of producing a sorbent of oil products including processing the carrier with a solution of active organic substances.
- Fibrous natural or synthetic material is used as a carrier, and solutions of alkyl carboxylic acids, higher aliphatic alcohols, their esters, polyolefins or paraffins in an organic low-boiling solvent selected from the class of hydrocarbons, halogenated hydrocarbons, ethers, sulfoxides are used as a solution of organic matter.
- the treatment is carried out at room temperature for 10-60 minutes at a concentration of active organic matter in solution from 0.1 to 1.0% in May, and after processing the sorbent is dried to constant weight at room temperature.
- This method does not provide repeated use of the sorbent in the collection of petroleum products, since the active substance applied to the carrier is easily washed off with oil and petroleum products.
- a known method of producing a sorbent for water purification from oil products and heavy metals including processing the fibrous carrier with titanium tetrachloride, followed by hydrolysis with water and drying.
- the fibrous carrier use cellulose-containing material. Titanium tetrachloride is used in the form of its 2 - 7% solution in hydrocarbons With 5 - With 7 . The process is carried out to the content of titanium dioxide in the sorbent from 5 to 15 May. % In this method, a combustible solvent is used.
- the process of obtaining the sorbent is complicated, since it is multi-stage. The resulting sorbent does not have buoyancy and, therefore, is not suitable for collecting oil from water surfaces.
- oxidized atactic polypropylene allows one to create a strong bond with cellulose due to the formation of a hydrogen bond between the carbonyl groups of the cellulose and the carboxyl groups of the polymer, which ensures high polymer resistance to washing out by oil products and high hydrophobicity of the sorbent.
- oxidized atactic polypropylene forms cluster-type compounds with the cellulose surface, which significantly increases the sorption properties of natural fibers. These properties make it possible to ensure multiple use of the sorbent.
- the conditions for the production of oxidized atactic polypropylene are not determined, which affect the modifying properties of the oxidized atactic polypropylene and the sorption properties of the sorbent with respect to oil and oil products.
- C 5 - C 7 aliphatic hydrocarbons which are classified as fire and explosive organic solvents, are used as a solvent to dissolve atactic polypropylene.
- the objective of the invention is to increase production safety, to develop a non-waste technology for producing a hydrophobic fibrous sorbent with a high capacity in relation to oil and oil products, suitable for repeated regeneration while maintaining a high capacity for oil and oil products.
- the problem is solved due to the fact that in the method of producing a sorbent for cleaning water surface and soil from oil and oil products, as in the prototype, hydrophobization of fibrous cellulosic material with a solution of oxidized atactic polypropylene is carried out, followed by drying to constant weight.
- atactic polypropylene is oxidized at a temperature of from 180 ° C to 240 ° C for 4 to 6 hours, dissolved in tetrachlorethylene; a fibrous cellulosic material is impregnated with a 0.4 to 0.5% solution of oxidized atactic polypropylene, excess the solution is drained and returned to recycling. The impregnated fibrous cellulosic material is dried by passing heated air through it. Vapor tetrachlorethylene is condensed and returned to the beginning of the process.
- fibrous cellulosic material batting, cotton wool or cotton waste can be used.
- the oxidation of atactic polypropylene is carried out at a temperature of 180 - 240 ° C and non-combustible tetrachlorethylene is used as a solvent for the oxidized atactic polypropylene, which is completely regenerated after drying the sorbent.
- This method of producing a sorbent for cleaning water surface and soil from oil and oil products allows to obtain a sorbent with high sorption of oil and oil products in the presence of water, a sufficiently high ability to retain absorbed oil and oil products.
- a sorbent has high buoyancy, is capable of multiple mechanical regeneration (spin up to 20 times) while maintaining high sorption ability, and can also be disposed of by known methods in road construction, burning in furnaces, and biodegradation.
- This set of sorption-protective products provides nature users with the practical opportunity to quickly and timely respond to both standard and possible emergency situations, arising in the process of extraction, transportation, refining and use of oil and oil products.
- the solution is cooled to room temperature, the resulting solution is poured into 40 g of cotton-based batting, soaked in batting at room temperature for 10-15 minutes, after which the excess solution is drained and returned to recycling, and hot air, heated to 80-100, is passed through the batting. ° C, until complete removal of the solvent. Air with solvent vapor enters the refrigerator, where tetrachlorethylene is condensed, which is reused to prepare a solution of oxidized atactic polypropylene.
- the resulting sorbent after cooling to room temperature is examined for the sorption of oil.
- a container of 200 cm 3 pour 80 cm 3 of water and 80 cm 3 of oil.
- 1 g of sorbent is placed on the surface and incubated for 1-3 minutes, the sorbent is taken out, the excess oil is allowed to drain for 1 min.
- Sorbent with oil is weighed. The weight difference of the sorbent before and after oil sorption determines the weight of the sorbed oil.
- the sorbent After the pressed oil, the sorbent is reused to collect oil.
- the proposed method for producing the sorbent is implemented on standard equipment for chemical production.
- a stainless steel reactor equipped with a mechanical stirrer and heating to 300 ° C was used.
- a solution of oxidized atactic polypropylene in tetrachlorethylene was prepared in the same reactor with mechanical stirring after cooling the oxidation product.
- the impregnation and drying of the fibrous cellulosic material is carried out in separate steel containers.
- standard tube coolers are used, cooled with cold tap water.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Analytical Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The method for producing a sorbent for removing oil and petroleum products from an aqueous surface and from soil is carried out by hydrophobization of a fibrous cellulose material with a solution of oxidized ataxic polypropylene. The ataxic polypropylene is oxidized at a temperature of 180°С to 240°С for 4 to 6 hours and dissolved in tetrachloroethylene. The fibrous cellulose material is impregnated with the resultant solution containing 0.4 to 0.5% of oxidized ataxic polypropylene, and excess solution is drained and recycled. The impregnated fibrous cellulose material is dried to a constant weight, with heated air being passed therethrough. The tetrachloroethylene vapours are condensed and returned to the beginning of the process.
Description
Способ получения сорбента для очистки водной поверхности и почвы от нефти и нефтепродуктов A method of producing a sorbent for cleaning water surface and soil from oil and oil products
Область техники Technical field
Изобретение относится к технологии производства сорбентов для очистки водной поверхности и почвы от нефти и нефтепродуктов при их случайных или аварийных разливах, а также для очистки нефтесодержащих сточных вод. The invention relates to a technology for the production of sorbents for cleaning water surface and soil from oil and oil products during their accidental or emergency spills, as well as for the treatment of oily wastewater.
Предшествующий уровень техники State of the art
Известен способ получения сорбента нефтепродуктов (RU 2071828 С 1 , МПК 6 B01J20/22, опубл. 20.01.1997г.), включающий обработку носителя раствором активных органических веществ. В качестве носителя используют волокнистый натуральный или синтетический материал, а в качестве раствора органического вещества используют растворы алкилкарбоновых кислот, высших алифатических спиртов, их эфиров, полиолефинов или парафинов в среде органического низкокипящего растворителя, выбранного из класса углеводородов, галогенуглеводородов, эфиров, сульфоксидов. При этом обработку ведут при комнатной температуре в течение 10 - 60 мин при концентрации активного органического вещества в растворе от 0,1 до 1 ,0 % мае, а после обработки сорбент высушивают до постоянного веса при комнатной температуре. A known method of producing a sorbent of oil products (RU 2071828 C 1, IPC 6 B01J20 / 22, publ. 01/20/1997), including processing the carrier with a solution of active organic substances. Fibrous natural or synthetic material is used as a carrier, and solutions of alkyl carboxylic acids, higher aliphatic alcohols, their esters, polyolefins or paraffins in an organic low-boiling solvent selected from the class of hydrocarbons, halogenated hydrocarbons, ethers, sulfoxides are used as a solution of organic matter. The treatment is carried out at room temperature for 10-60 minutes at a concentration of active organic matter in solution from 0.1 to 1.0% in May, and after processing the sorbent is dried to constant weight at room temperature.
Этот способ не обеспечивает многократного использования сорбента при сборе нефтепродуктов, так как активное вещество, наносимое на носитель, легко смывается нефтью и нефтепродуктами. This method does not provide repeated use of the sorbent in the collection of petroleum products, since the active substance applied to the carrier is easily washed off with oil and petroleum products.
Известен способ получения сорбента для очистки воды от нефтепродуктов и тяжелых металлов (RU 2132226 С1 , МПК 6 B01J20/06, B01J20/22, опубл. 27.06.1999г.), включающий обработку волокнистого носителя четыреххлористым титаном с последующим гидролизом водой и сушкой. В качестве волокнистого носителя используют целлюлозосодержащий материал. Четыреххлористый титан используют в виде его 2 - 7 %-ного раствора в углеводородах С5 - С7. Процесс ведут до содержания диоксида титана в сорбенте от 5 до 15 мае. %.
В этом способе используют горючий растворитель. Процесс получения сорбента сложен, так как многостадиен. Полученный сорбент не обладает плавучестью и, поэтому не пригоден для сбора нефти с водных поверхностей. A known method of producing a sorbent for water purification from oil products and heavy metals (RU 2132226 C1, IPC 6 B01J20 / 06, B01J20 / 22, publ. 06/27/1999), including processing the fibrous carrier with titanium tetrachloride, followed by hydrolysis with water and drying. As the fibrous carrier use cellulose-containing material. Titanium tetrachloride is used in the form of its 2 - 7% solution in hydrocarbons With 5 - With 7 . The process is carried out to the content of titanium dioxide in the sorbent from 5 to 15 May. % In this method, a combustible solvent is used. The process of obtaining the sorbent is complicated, since it is multi-stage. The resulting sorbent does not have buoyancy and, therefore, is not suitable for collecting oil from water surfaces.
Наиболее близким к предлагаемому техническому решению является способ получения сорбента для сбора нефти и нефтепродуктов с поверхности воды (RU 2061541 С1 , МПК 6 B01J20/22, опубл. 10.06.1996 г.), заключающийся в гидрофобизации волокнистого целлюлозного материала раствором окисленного атактического полипропилена в алифатических углеводородах и последующей сушке до постоянного веса. Closest to the proposed technical solution is a method of producing a sorbent for collecting oil and oil products from the water surface (RU 2061541 C1, IPC 6 B01J20 / 22, publ. 06/10/1996), which consists in the hydrophobization of fibrous cellulosic material with a solution of oxidized atactic polypropylene in aliphatic hydrocarbons and subsequent drying to constant weight.
Наличие карбоксильных групп в окисленном атактическом полипропилене позволяет создавать прочную связь с целлюлозой за счёт образования водородной связи между карбонильными группами целлюлозы и карбоксильными группами полимера, что обеспечивает высокую устойчивость полимера к вымыванию нефтепродуктами и высокую гидрофобность сорбента. Кроме того, окисленный атактический полипропилен образует с поверхностью целлюлозы соединения типа кластеров, что существенно увеличивает сорбционные свойства природных волокон. Указанные свойства позволяют обеспечить многократность использования сорбента. The presence of carboxyl groups in oxidized atactic polypropylene allows one to create a strong bond with cellulose due to the formation of a hydrogen bond between the carbonyl groups of the cellulose and the carboxyl groups of the polymer, which ensures high polymer resistance to washing out by oil products and high hydrophobicity of the sorbent. In addition, oxidized atactic polypropylene forms cluster-type compounds with the cellulose surface, which significantly increases the sorption properties of natural fibers. These properties make it possible to ensure multiple use of the sorbent.
В этом способе получения сорбента не определены условия получения окисленного атактического полипропилена, которые влияют на модифицирующие свойства окисленного атактического полипропилена и сорбционные свойства сорбента по отношению к нефти и нефтепродуктам. Кроме того, для растворения атактического полипропилена в качестве растворителя используют алифатические углеводороды С5 - С7, которые относятся к пожаро- и взрывоопасным органическим растворителям. In this method of producing the sorbent, the conditions for the production of oxidized atactic polypropylene are not determined, which affect the modifying properties of the oxidized atactic polypropylene and the sorption properties of the sorbent with respect to oil and oil products. In addition, C 5 - C 7 aliphatic hydrocarbons, which are classified as fire and explosive organic solvents, are used as a solvent to dissolve atactic polypropylene.
Раскрытие изобретения Disclosure of invention
Задачей предлагаемого изобретения является повышение безопасности производства, разработка безотходной технологии получения гидрофобного волокнистого сорбента, обладающего высокой емкостью по отношению к нефти и нефтепродуктам, пригодного для многократной регенерации с сохранением высокой емкости к нефти и нефтепродуктам.
Поставленная задача решена за счет того, что в способе получения сорбента для очистки водной поверхности и почвы от нефти и нефтепродуктов, также как в прототипе, проводят гидрофобизацию волокнистого целлюлозного материала раствором окисленного атактического полипропилена с последующей сушкой до постоянного веса. The objective of the invention is to increase production safety, to develop a non-waste technology for producing a hydrophobic fibrous sorbent with a high capacity in relation to oil and oil products, suitable for repeated regeneration while maintaining a high capacity for oil and oil products. The problem is solved due to the fact that in the method of producing a sorbent for cleaning water surface and soil from oil and oil products, as in the prototype, hydrophobization of fibrous cellulosic material with a solution of oxidized atactic polypropylene is carried out, followed by drying to constant weight.
Согласно изобретению атактический полипропилен окисляют при температуре от 180° С до 240° С в течение от 4 до 6 часов, растворяют его в тетрахлорэтилене, полученным от 0,4 до 0,5 %-ным раствором окисленного атактического полипропилена пропитывают волокнистый целлюлозный материал, избыток раствора сливают и возвращают в рецикл. Пропитанный волокнистый целлюлозный материал сушат, пропуская через него нагретый воздух. Пары тетрахлорэтилена конденсируют и возвращают в начало процесса. According to the invention, atactic polypropylene is oxidized at a temperature of from 180 ° C to 240 ° C for 4 to 6 hours, dissolved in tetrachlorethylene; a fibrous cellulosic material is impregnated with a 0.4 to 0.5% solution of oxidized atactic polypropylene, excess the solution is drained and returned to recycling. The impregnated fibrous cellulosic material is dried by passing heated air through it. Vapor tetrachlorethylene is condensed and returned to the beginning of the process.
В качестве волокнистого целлюлозного материала могут быть использованы ватин, вата или отходы хлопчатобумажного производства. As the fibrous cellulosic material, batting, cotton wool or cotton waste can be used.
В предложенном способе окисление атактического полипропилена ведут при температуре 180 - 240°С и в качестве растворителя окисленного атактического полипропилена используют негорючий тетрахлорэтилен, который после сушки сорбента полностью регенерируется. In the proposed method, the oxidation of atactic polypropylene is carried out at a temperature of 180 - 240 ° C and non-combustible tetrachlorethylene is used as a solvent for the oxidized atactic polypropylene, which is completely regenerated after drying the sorbent.
Этот способ получения сорбента для очистки водной поверхности и почвы от нефти и нефтепродуктов позволяет получить сорбент, обладающий высокой сорбцией нефти и нефтепродуктов в присутствии воды, достаточно высокой способностью удерживать поглощенные нефть и нефтепродукты. Такой сорбент обладает высокой плавучестью, способен к многократной механической регенерации (отжим до 20 раз) с сохранением высокой сорбционной способности, а также может быть утилизирован известными способами в строительстве дорог, сжиганием в топках, биоразложением. This method of producing a sorbent for cleaning water surface and soil from oil and oil products allows to obtain a sorbent with high sorption of oil and oil products in the presence of water, a sufficiently high ability to retain absorbed oil and oil products. Such a sorbent has high buoyancy, is capable of multiple mechanical regeneration (spin up to 20 times) while maintaining high sorption ability, and can also be disposed of by known methods in road construction, burning in furnaces, and biodegradation.
На основе сорбента могут быть изготовлены специальные нефтепоглощающие изделия - маты, салфетки, боновые заграждения. Основным технологическим элементом получения этих изделий является предлагаемый нами способ получения сорбента. Based on the sorbent, special oil-absorbing products can be made - mats, napkins, booms. The main technological element in the production of these products is our proposed method for producing the sorbent.
Этот набор сорбционно-защитных изделий обеспечивает природопользователям практическую возможность быстро и вовремя отреагировать как на стандартные, так и на возможные аварийные ситуации,
возникающие в процессе добычи, транспортировки, переработки и использования нефти и нефтепродуктов. This set of sorption-protective products provides nature users with the practical opportunity to quickly and timely respond to both standard and possible emergency situations, arising in the process of extraction, transportation, refining and use of oil and oil products.
Лучший вариант осуществления изобретения The best embodiment of the invention
10 г атактического полипропилена нагревают в реакторе до 240° С и через расплав полимера при перемешивании пропускают воздух в течение 4-6 часов. Затем подачу воздуха прекращают и реакционную массу охлаждают до 80° С и при перемешивании растворяют в 1900 г тетрахлорэтилена. 10 g of atactic polypropylene are heated in a reactor to 240 ° C and air is passed through the polymer melt with stirring for 4-6 hours. Then the air supply is stopped and the reaction mass is cooled to 80 ° C and dissolved in 1900 g of tetrachlorethylene with stirring.
Раствор охлаждают до комнатной температуры, полученным раствором заливают 40 г ватина на основе хлопка, пропитывают ватин при комнатной температуре в течение 10-15 минут, после чего избыток раствора сливают и возвращают в рецикл, а через ватин пропускают горячий воздух, нагретый до 80 - 100° С, до полного удаления растворителя. Воздух с парами растворителя поступает в холодильник, где конденсируется тетрахлорэтилен, который используют повторно для приготовления раствора окисленного атактического полипропилена. The solution is cooled to room temperature, the resulting solution is poured into 40 g of cotton-based batting, soaked in batting at room temperature for 10-15 minutes, after which the excess solution is drained and returned to recycling, and hot air, heated to 80-100, is passed through the batting. ° C, until complete removal of the solvent. Air with solvent vapor enters the refrigerator, where tetrachlorethylene is condensed, which is reused to prepare a solution of oxidized atactic polypropylene.
Полученный сорбент после охлаждения до комнатной температуры исследуют на сорбцию нефти. В ёмкость на 200 см 3 наливают 80 см 3 воды и 80 см 3 нефти. На поверхность помещают 1 г сорбента и выдерживают в течение 1 - 3 мин., сорбент вынимают, дают стечь излишней нефти в течение 1 мин. Сорбент с нефтью взвешивают. По разности веса сорбента до и после сорбции нефти определяют вес сорбированной нефти. The resulting sorbent after cooling to room temperature is examined for the sorption of oil. In a container of 200 cm 3 pour 80 cm 3 of water and 80 cm 3 of oil. 1 g of sorbent is placed on the surface and incubated for 1-3 minutes, the sorbent is taken out, the excess oil is allowed to drain for 1 min. Sorbent with oil is weighed. The weight difference of the sorbent before and after oil sorption determines the weight of the sorbed oil.
После отжатая нефти сорбент повторно используют для сбора нефти. After the pressed oil, the sorbent is reused to collect oil.
Результаты влияния условий окисления атактического полипропилена и его содержания в растворе тетрахлорэтилена на сорбцию сорбентом нефти приведены в таблице 1. The results of the influence of the oxidation conditions of atactic polypropylene and its content in a tetrachlorethylene solution on sorption by an oil sorbent are shown in Table 1.
Результаты влияния многократного использования сорбента (ватин пропитан 0,4 %-ным раствором окисленного атактического полипропилена при 240° С в течение 4 час.) для сбора нефти на его сорбционную способность показаны в таблице 2.
Таблица 1 The results of the effect of repeated use of the sorbent (batting is impregnated with a 0.4% solution of oxidized atactic polypropylene at 240 ° C for 4 hours) for collecting oil on its sorption ability are shown in table 2. Table 1
Концентра-Concentra-
Температу- Продолжитель- Содержание Молеку- ция окис- Ём- ра ность кислорода в лярная лен-ного кость окисления окисления, окисленном масса атактиче- сор- атактиче- час атактиче- окисленно- ского поли- бента, ского поли- ском поли- го атакти- пропилена г/г пропилена, пропилене, ческого в терахлор-Temperature- Duration- Content Molecule Oxidation Oxygen capacity in the flax flax bone of oxidation, oxidized mass of atactic-atactic- atactic-oxidized polybent, polic poly - propylene g / g propylene, propylene in terachlor
°С % полипропи этилене, ° C% polypropy ethylene,
лена % Lena%
Исходный - 1,04 26000 - Original - 1.04 26000 -
180 3 1,52 19900 0,4 20,5180 3 1.52 19900 0.4 20.5
180 4 3,34 16000 0,4 22,1180 4 3.34 16000 0.4 22.1
180 5 4,12 12400 0,4 23,0180 5 4.12 12400 0.4 23.0
180 5 4,12 12400 0,3 18,6180 5 4.12 12400 0.3 18.6
180 5 4,12 12400 0,45 23,6180 5 4.12 12400 0.45 23.6
180 5 4,12 12400 0,5 23, 4180 5 4.12 12400 0.5 23.4
180 5 4,12 12400 0,6 19,2180 5 4.12 12400 0.6 19.2
180 6 4,32 10600 0,4 22,3180 6 4.32 10600 0.4 22.3
180 8 4,8 6700 0,4 18,9180 8 4.8 6700 0.4 18.9
190 4 3,45 13800 0,4 22,7190 4 3.45 13800 0.4 22.7
190 5 4,2 12400 0,4 23,6190 5 4.2 12400 0.4 23.6
190 6 4,43 9800 0,4 23,8190 6 4.43 9800 0.4 23.8
200 4 3,56 13200 0,4 21 ,9200 4 3.56 13200 0.4 21, 9
200 5 4,6 1 1200 0,4 24,0200 5 4.6 1 1200 0.4 24.0
200 6 4,8 9600 0,4 23,8200 6 4.8 9600 0.4 23.8
240 2 2,03 20000 0,4 19,4240 2 2.03 20,000 0.4 19.4
240 4 1,92 10600 0,4 27,5240 4 1.92 10,600 0.4 27.5
240 5 1,81 8300 0,4 28,8240 5 1.81 8300 0.4 28.8
240 5 1 ,81 8300 0,3 18,2240 5 1, 81 8300 0.3 18.2
240 5 1,81 8300 0,45 28,7240 5 1.81 8300 0.45 28.7
240 5 1 ,81 8300 0,5 28,2240 5 1, 81 8300 0.5 28.2
240 5 1,81 8300 0,6 20,8240 5 1.81 8300 0.6 20.8
240 6 1 ,70 6400 0,4 27,0240 6 1, 70 6400 0.4 27.0
240 8 1,73 5400 0,4 18,7
Таблица 2 240 8 1.73 5400 0.4 18.7 table 2
Количество циклов регенерации The number of regeneration cycles
отжатием нефти от сорбента Ёмкость сорбента, на центрифуге, г/г количество раз squeezing oil from the sorbent Sorbent capacity, in a centrifuge, g / g number of times
1 27,5 1 27.5
2 26,72 26.7
3 26,93 26.9
4 26,44 26.4
5 26,55 26.5
6 26,86 26.8
7 26,37 26.3
8 26,28 26.2
9 25,79 25.7
10 25,810 25.8
1 1 24,91 1 24.9
12 24,612 24.6
13 24,213 24.2
14 23,614 23.6
15 23,415 23.4
16 23,416 23.4
17 23,217 23.2
18 22,818 22.8
19 22,619 22.6
20 22,520 22.5
21 21 ,821 21, 8
22 21,422 21.4
23 20,823 20.8
24 20,324 20.3
25 19,9
Промышленная применимость 25 19.9 Industrial applicability
Предлагаемый способ получения сорбента реализован на стандартном оборудовании для химического производства. Для стадии окисления использован реактор из нержавеющей стали, оборудованный механической мешалкой и нагревом до 300° С. Получение раствора окисленного атактического полипропилена в тетрахлорэтилене осуществляют в этом же реакторе при механическом перемешивании после охлаждения продукта окисления. Пропитку и сушку волокнистого целлюлозного материала проводят в отдельных стальных ёмкостях. Для регенерации паров тетрахлорэтилена из горячего воздуха используют стандартные трубчатые холодильники, охлаждаемые холодной водопроводной водой.
The proposed method for producing the sorbent is implemented on standard equipment for chemical production. For the oxidation stage, a stainless steel reactor equipped with a mechanical stirrer and heating to 300 ° C was used. A solution of oxidized atactic polypropylene in tetrachlorethylene was prepared in the same reactor with mechanical stirring after cooling the oxidation product. The impregnation and drying of the fibrous cellulosic material is carried out in separate steel containers. For the recovery of tetrachlorethylene vapors from hot air, standard tube coolers are used, cooled with cold tap water.
Claims
Формула изобретения Claim
Способ получения сорбента для очистки водной поверхности и почвы от нефти и нефтепродуктов путем гидрофобизации волокнистого целлюлозного материала раствором окисленного атактического полипропилена с последующей сушкой до постоянного веса, отличающийся тем, что атактический полипропилен окисляют при температуре от 180 °С до 240 °С в течение от 4 до 6 часов, растворяют его в тетрахлорэтилене, полученным от 0,4 до 0,5 %-ным раствором окисленного атактического полипропилена пропитывают волокнистый целлюлозный материал, избыток раствора сливают и возвращают в рецикл, пропитанный волокнистый целлюлозный материал сушат, пропуская через него нагретый воздух, пары тетрахлорэтилена конденсируют и возвращают в начало процесса.
A method of producing a sorbent for cleaning water surface and soil from oil and oil products by hydrophobization of fibrous cellulosic material with a solution of oxidized atactic polypropylene followed by drying to constant weight, characterized in that atactic polypropylene is oxidized at a temperature of from 180 ° C to 240 ° C for 4 up to 6 hours, dissolve it in tetrachlorethylene, obtained from 0.4 to 0.5% solution of oxidized atactic polypropylene impregnate fibrous cellulosic material, drain the excess solution t and returned to recycling, the impregnated fibrous cellulosic material is dried, passing heated air through it, the tetrachlorethylene vapor is condensed and returned to the beginning of the process.
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RU2011111226/05A RU2463106C1 (en) | 2011-03-24 | 2011-03-24 | Method of producing sorbent for cleaning water and soil of oil and oil products |
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RU2638855C1 (en) * | 2017-03-13 | 2017-12-18 | Михаил Николаевич Уразаев | Method of producing sorbent for water surface purifying from oil and oil products |
RU2687913C1 (en) * | 2018-07-20 | 2019-05-16 | Федеральное государственное бюджетное учреждение науки Институт химии Дальневосточного отделения Российской академии наук (ИХ ДВО РАН) | Method of producing sorption material for collecting oil and oil products |
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US5186831A (en) * | 1992-01-21 | 1993-02-16 | Leucadia, Inc. | Oil sorbent products and method of making same |
RU2036719C1 (en) * | 1991-03-19 | 1995-06-09 | Институт химии нефти СО РАН | Adsorbent for cleaning surface of water and soil from oil and oil products |
RU2061541C1 (en) * | 1993-08-17 | 1996-06-10 | Институт химии нефти СО РАН | Sorbent for oil and petroleum product collection from the water surface |
RU2071828C1 (en) * | 1993-04-21 | 1997-01-20 | Институт химии нефти СО РАН | Method of producing sorbent for oil products |
US6881493B2 (en) * | 1998-01-21 | 2005-04-19 | Atofina Research S.A. | Polyolefins and uses thereof |
RU2301812C1 (en) * | 2005-11-24 | 2007-06-27 | Государственное образовательное учреждение Высшего профессионального образования "Томский государственный университет" | Oxidized atactic polypropylene with the polar functional groups, the method of its production and the installation for the method realization |
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DE2358808A1 (en) * | 1973-11-26 | 1975-06-05 | Hoechst Ag | METHOD OF OBTAINING OIL |
CA2110559A1 (en) * | 1993-03-17 | 1994-09-18 | Toru Inaoka | Oil-absorbed composition, particulate oil absorber, oil-absorbent material and oil-absorbent pack |
RU2152250C1 (en) * | 1999-09-28 | 2000-07-10 | Быков Игорь Николаевич | Sorbent |
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RU2036719C1 (en) * | 1991-03-19 | 1995-06-09 | Институт химии нефти СО РАН | Adsorbent for cleaning surface of water and soil from oil and oil products |
US5186831A (en) * | 1992-01-21 | 1993-02-16 | Leucadia, Inc. | Oil sorbent products and method of making same |
RU2071828C1 (en) * | 1993-04-21 | 1997-01-20 | Институт химии нефти СО РАН | Method of producing sorbent for oil products |
RU2061541C1 (en) * | 1993-08-17 | 1996-06-10 | Институт химии нефти СО РАН | Sorbent for oil and petroleum product collection from the water surface |
US6881493B2 (en) * | 1998-01-21 | 2005-04-19 | Atofina Research S.A. | Polyolefins and uses thereof |
RU2301812C1 (en) * | 2005-11-24 | 2007-06-27 | Государственное образовательное учреждение Высшего профессионального образования "Томский государственный университет" | Oxidized atactic polypropylene with the polar functional groups, the method of its production and the installation for the method realization |
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