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CN101798163A - Method for accelerating microwave pyrolytic process of oily sludge by pyrolyzing residue thereof - Google Patents

Method for accelerating microwave pyrolytic process of oily sludge by pyrolyzing residue thereof Download PDF

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Publication number
CN101798163A
CN101798163A CN201010151222A CN201010151222A CN101798163A CN 101798163 A CN101798163 A CN 101798163A CN 201010151222 A CN201010151222 A CN 201010151222A CN 201010151222 A CN201010151222 A CN 201010151222A CN 101798163 A CN101798163 A CN 101798163A
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sludge
microwave
pyrolysis
residue
oil sludge
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CN101798163B (en
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雍兴跃
张建
祝威
侯影飞
屈一新
王际东
陈远超
张丁
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Shengli Oilfield Shengli Engineering & Consulting Co Ltd
Beijing University of Chemical Technology
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Shengli Oilfield Shengli Engineering & Consulting Co Ltd
Beijing University of Chemical Technology
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation of by-products of wastewater, sewage or sludge processing

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Abstract

本发明公开了一种利用自身热解残渣加快油污泥微波热解过程的方法,即将油泥或者污泥在充氮条件下进行微波热解,然后控制在700℃-850℃进行微波焚烧5-15分钟,得到固体微波残渣;然后将该微波残渣按照油泥或污泥重量的0.5-5%与油泥或者污泥混合均匀,再对油泥或者污泥在充氮条件下进行微波热解。可以加快油泥或者污泥的热解过程,缩短热解时间,有效地节约了油泥或者污泥处理的能耗,提高了处理效率,微波热解后的残渣还可循环利用;而且本发明方法成本低,经济,可广泛推广使用。The invention discloses a method for accelerating the microwave pyrolysis process of oil sludge by using its own pyrolysis residue, that is, carrying out microwave pyrolysis of oil sludge or sludge under nitrogen-filled conditions, and then controlling microwave incineration at 700°C-850°C for 5- After 15 minutes, a solid microwave residue is obtained; then the microwave residue is uniformly mixed with the oil sludge or sludge according to 0.5-5% of the weight of the oil sludge or sludge, and then the oil sludge or sludge is subjected to microwave pyrolysis under nitrogen filling conditions. It can speed up the pyrolysis process of oil sludge or sludge, shorten the pyrolysis time, effectively save the energy consumption of oil sludge or sludge treatment, improve the treatment efficiency, and the residue after microwave pyrolysis can be recycled; and the method cost of the present invention is Low cost, economical, and can be widely used.

Description

一种利用自身热解残渣加快含油污泥微波热解过程的方法 A method for accelerating the microwave pyrolysis process of oily sludge by using its own pyrolysis residue

技术领域technical field

本发明涉及一种油污泥微波热解的方法,尤其涉及利用廉价的自身热解残渣加快油污泥微波热解过程的方法,实现了油泥,或者污泥微波热解的节能、提高微波热解效率。The invention relates to a method for microwave pyrolysis of oil sludge, in particular to a method for accelerating the microwave pyrolysis process of oil sludge by using cheap self-pyrolysis residues, which realizes the energy saving of oil sludge or sludge microwave pyrolysis, and improves the efficiency of microwave thermal decomposition. solution efficiency.

背景技术Background technique

油泥或者污泥的热解,一般采用传统方法进行间接加热热解。该方法存在能耗高、易结焦和回收液体油物质含有较高的芳香族化合物等缺点。由于微波热解存在热解和微波催化的双重效应。因此,采用微波技术对油泥、污泥热解成为一种新的热解技术。但是,由于油泥或者污泥中缺乏足够的有利于微波吸附的物质,造成微波热解油泥、或者污泥的过程很长,甚至在很长时间内都不能够达到对油泥、污泥热解的温度,处理效率低、能耗特别大,不能够实现油泥、污泥的减量化和资源化处理。通常,人们把活性炭作为微波吸收剂,采用添加活性炭的方法,促进微波热解过程,成本较高。基于此,急需采用一种新的廉价微波吸收剂,添加到油泥,或者污泥中,以加快其微波热解过程速度,实现油泥,或者污泥微波热解的节能、提高微波热解效率的方法。The pyrolysis of oil sludge or sludge generally uses traditional methods for indirect heating pyrolysis. This method has the disadvantages of high energy consumption, easy coking, and the recovered liquid oil contains relatively high aromatic compounds. Due to microwave pyrolysis, there are dual effects of pyrolysis and microwave catalysis. Therefore, using microwave technology to pyrolyze oil sludge and sludge has become a new pyrolysis technology. However, due to the lack of sufficient substances beneficial to microwave adsorption in oil sludge or sludge, the process of microwave pyrolysis of oil sludge or sludge is very long, and even the pyrolysis of oil sludge and sludge cannot be achieved within a long period of time. temperature, low treatment efficiency, and particularly high energy consumption, it is impossible to realize the reduction and recycling of oil sludge and sludge. Usually, activated carbon is used as a microwave absorber, and the method of adding activated carbon is used to promote the microwave pyrolysis process, and the cost is relatively high. Based on this, there is an urgent need to use a new cheap microwave absorber, which can be added to oil sludge or sludge to speed up the microwave pyrolysis process, realize energy saving of oil sludge or sludge microwave pyrolysis, and improve microwave pyrolysis efficiency. method.

发明内容Contents of the invention

本发明的目的是解决现有技术中的问题,提供一种廉价的利用自身热解残渣加快油污泥微波热解过程的方法。The purpose of the present invention is to solve the problems in the prior art and provide a cheap method for accelerating the microwave pyrolysis process of oil sludge by using its own pyrolysis residue.

为实现上述目的,本发明的技术方案为,将油泥或者污泥在充氮条件下进行微波热解,然后控制在700℃-850℃进行微波焚烧5-15分钟,得到固体微波残渣;然后将该微波残渣按照油泥或污泥重量的0.5-5%与油泥或者污泥混合均匀,再对油泥或者污泥在充氮条件下进行微波热解。这样,添加微波残渣的油泥或者污泥将会得到有效的微波热解。In order to achieve the above purpose, the technical solution of the present invention is to carry out microwave pyrolysis of oil sludge or sludge under nitrogen-filled conditions, and then control microwave incineration at 700°C-850°C for 5-15 minutes to obtain solid microwave residue; then The microwave residue is evenly mixed with the oil sludge or sludge according to 0.5-5% of the weight of the oil sludge or sludge, and then the oil sludge or sludge is subjected to microwave pyrolysis under a nitrogen filling condition. In this way, oil sludge or sludge with added microwave residue will be efficiently pyrolyzed by microwave.

本发明方法可以加快油泥或者污泥的热解过程,缩短热解时间,有效地节约了油泥或者污泥处理的能耗,提高了处理效率,微波热解后的残渣还可循环利用;而且本发明方法成本低,经济,可广泛推广使用。The method of the invention can accelerate the pyrolysis process of oil sludge or sludge, shorten the pyrolysis time, effectively save the energy consumption of oil sludge or sludge treatment, improve the treatment efficiency, and the residue after microwave pyrolysis can be recycled; and the present invention The inventive method is low in cost, economical and can be widely popularized and used.

具体实施方式Detailed ways

实施例1:Example 1:

首先油泥在充氮条件下进行微波热解,然后控制在700℃进行微波焚烧15分钟,得到微波残渣;其次,在含水率70%的油泥中添加油泥质量1.0%的油泥微波焚烧残渣,在充氮条件下可以使微波热解的时间缩短至2小时左右。如果增加残渣的添加量至5%,可以使含水率70%的油泥微波热解时间缩短在5秒以内,使油泥的微波热解过程基本消失,直接进入到微波焚烧过程,最后得到残渣。该残渣也可与油泥按照比例混合进行使用。Firstly, the oil sludge was subjected to microwave pyrolysis under the condition of nitrogen filling, and then microwave incineration was carried out at 700°C for 15 minutes to obtain microwave residues; secondly, microwave incineration residues of oil sludge mass of 1.0% were added to the oil sludge with a water content of 70%, and the microwave incineration residue was added to the oil sludge with a water content of 70%. Under nitrogen conditions, the microwave pyrolysis time can be shortened to about 2 hours. If the addition of residue is increased to 5%, the microwave pyrolysis time of oil sludge with a water content of 70% can be shortened to less than 5 seconds, the microwave pyrolysis process of oil sludge basically disappears, and the microwave incineration process is directly entered, and finally residue is obtained. The residue can also be mixed with oil sludge in proportion to use.

实施例2:Example 2:

污泥在充氮条件下进行微波热解,然后控制在850℃进行微波焚烧5分钟,得到微波残渣;在含水率70%的污泥中添加污泥质量1.0%的污泥微波焚烧残渣,在充氮条件下可以使微波热解的时间缩短至3小时左右。如果增加残渣的添加量至4.5%左右,可以使含水率70%的污泥微波热解时间缩短在30分钟以内;经过30分钟左右的微波热解后,油泥温度持续升高,进入到微波焚烧过程;经过焚烧,得到微波残渣。该微波残渣也可与油泥按照比例混合进行使用。Sludge was subjected to microwave pyrolysis under nitrogen-filled conditions, and then microwave incineration was carried out at 850°C for 5 minutes to obtain microwave residue; 1.0% of sludge mass was added to sludge with a moisture content of 70% to obtain microwave incineration residue. The time of microwave pyrolysis can be shortened to about 3 hours under the condition of nitrogen filling. If the amount of residue added is increased to about 4.5%, the microwave pyrolysis time of sludge with a moisture content of 70% can be shortened to within 30 minutes; after about 30 minutes of microwave pyrolysis, the temperature of the sludge continues to rise and enters microwave incineration Process; After incineration, microwave residues are obtained. The microwave residue can also be mixed with oil sludge in proportion for use.

实施例3:Example 3:

在含水率70%的油泥中添加1.0%实施例1得到的油泥微波焚烧残渣,在充氮条件下同样可以使其微波热解的时间缩短至2小时左右。如果增加残渣的添加量至5%,可以使含水率70%的油泥微波热解时间缩短在5秒以内,使油泥的微波热解过程基本消失,直接进入到微波焚烧过程,最后得到残渣。该残渣同样也可与油泥按照比例混合进行使用。Adding 1.0% of the sludge microwave incineration residue obtained in Example 1 to the sludge with a water content of 70% can also shorten the microwave pyrolysis time to about 2 hours under nitrogen filling conditions. If the addition of residue is increased to 5%, the microwave pyrolysis time of oil sludge with a water content of 70% can be shortened to less than 5 seconds, the microwave pyrolysis process of oil sludge basically disappears, and the microwave incineration process is directly entered, and finally residue is obtained. The residue can also be mixed with oil sludge in proportion to use.

实施例4:Example 4:

在含水率70%的污泥中添加1.0%实施例2得到的污泥微波焚烧残渣,在充氮条件下同样可以使其微波热解的时间缩短至3小时左右。如果增加残渣的添加量至4.5%左右,可以使含水率70%的污泥微波热解时间缩短在30分钟以内;经过30分钟左右的微波热解后,油泥温度持续升高,进入到微波焚烧过程;经过焚烧,得到微波残渣。该微波残渣同样也可与油泥按照比例混合进行使用。Adding 1.0% of the sludge microwave incineration residue obtained in Example 2 to the sludge with a water content of 70% can also shorten the microwave pyrolysis time to about 3 hours under the condition of nitrogen filling. If the amount of residue added is increased to about 4.5%, the microwave pyrolysis time of sludge with a moisture content of 70% can be shortened to within 30 minutes; after about 30 minutes of microwave pyrolysis, the temperature of the sludge continues to rise and enters microwave incineration Process; After incineration, microwave residues are obtained. The microwave residue can also be mixed with oil sludge in proportion for use.

Claims (1)

1.一种利用自身热解残渣加快油污泥微波热解过程的方法,其特征在于,其方法为:将油泥或者污泥在充氮条件下进行微波热解,然后控制在700℃-850℃进行微波焚烧5-15分钟,得到固体微波残渣;然后将该微波残渣按照油泥或污泥重量的0.5-5%与油泥或者污泥混合均匀,再对油泥或者污泥在充氮条件下进行微波热解。1. A method for accelerating the microwave pyrolysis process of oil sludge by using its own pyrolysis residue, characterized in that the method is: carry out microwave pyrolysis of oil sludge or sludge under nitrogen-filled conditions, and then control it at 700°C-850°C Perform microwave incineration at ℃ for 5-15 minutes to obtain solid microwave residue; then mix the microwave residue with oil sludge or sludge evenly according to 0.5-5% of the weight of the oil sludge or sludge, and then treat the oil sludge or sludge under nitrogen-filled conditions Microwave pyrolysis.
CN2010101512225A 2010-04-16 2010-04-16 Method for accelerating microwave pyrolytic process of oily sludge by pyrolyzing residue thereof Expired - Fee Related CN101798163B (en)

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Cited By (8)

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CN102199434A (en) * 2011-04-13 2011-09-28 西安建筑科技大学 Method for quick pyrolysis of coal direct liquefaction residues by utilizing microwaves
CN102350431A (en) * 2011-07-28 2012-02-15 中国石油大学(北京) Method for separating oil content of organic matters from crude oil-containing wastes
CN103361089A (en) * 2013-07-18 2013-10-23 华南理工大学 Method for promoting kitchen garbage microwave pyrolysis with its pyrolysis residue to produce tar
CN103739180A (en) * 2013-12-17 2014-04-23 辽宁石油化工大学 Method for microwave pyrolysis treatment of oil sludge
CN105668975A (en) * 2015-10-19 2016-06-15 蓝德环保科技集团股份有限公司 Sludge microwave-drying treatment method
CN110590087A (en) * 2019-07-24 2019-12-20 中国石油大学(华东) A kind of treatment method of oily sludge
CN111233301A (en) * 2020-03-06 2020-06-05 山东产研绿洲环境产业技术研究院有限公司 Oil sludge treatment method and oil sludge treatment system
CN116177834A (en) * 2023-04-20 2023-05-30 西南科技大学 Method for pyrolysis treatment of oily sludge solid waste by utilizing microwave absorbent

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CN101100344A (en) * 2007-05-23 2008-01-09 郭银飞 Treatment method for heating and drying sludge by microwave and low-temperature smoke gas
CN101456604A (en) * 2008-12-31 2009-06-17 广东上九生物降解塑料有限公司 Method for rapidly treating wastewater by using microwave energy

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CN101100344A (en) * 2007-05-23 2008-01-09 郭银飞 Treatment method for heating and drying sludge by microwave and low-temperature smoke gas
CN101456604A (en) * 2008-12-31 2009-06-17 广东上九生物降解塑料有限公司 Method for rapidly treating wastewater by using microwave energy

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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102199434A (en) * 2011-04-13 2011-09-28 西安建筑科技大学 Method for quick pyrolysis of coal direct liquefaction residues by utilizing microwaves
CN102199434B (en) * 2011-04-13 2013-06-05 西安建筑科技大学 Method for direct liquefaction residues of coal by utilizing microwaves quick pyrolysis
CN102350431A (en) * 2011-07-28 2012-02-15 中国石油大学(北京) Method for separating oil content of organic matters from crude oil-containing wastes
CN102350431B (en) * 2011-07-28 2013-07-17 中国石油大学(北京) Method for separating oil content of organic matters from crude oil-containing wastes
CN103361089A (en) * 2013-07-18 2013-10-23 华南理工大学 Method for promoting kitchen garbage microwave pyrolysis with its pyrolysis residue to produce tar
CN103739180A (en) * 2013-12-17 2014-04-23 辽宁石油化工大学 Method for microwave pyrolysis treatment of oil sludge
CN105668975A (en) * 2015-10-19 2016-06-15 蓝德环保科技集团股份有限公司 Sludge microwave-drying treatment method
CN105668975B (en) * 2015-10-19 2018-03-09 蓝德环保科技集团股份有限公司 Sludge microwave drying treatment method
CN110590087A (en) * 2019-07-24 2019-12-20 中国石油大学(华东) A kind of treatment method of oily sludge
CN111233301A (en) * 2020-03-06 2020-06-05 山东产研绿洲环境产业技术研究院有限公司 Oil sludge treatment method and oil sludge treatment system
CN116177834A (en) * 2023-04-20 2023-05-30 西南科技大学 Method for pyrolysis treatment of oily sludge solid waste by utilizing microwave absorbent

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