JP2006187750A - Sulfate pitch treatment method - Google Patents

Sulfate pitch treatment method Download PDF

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JP2006187750A
JP2006187750A JP2005025665A JP2005025665A JP2006187750A JP 2006187750 A JP2006187750 A JP 2006187750A JP 2005025665 A JP2005025665 A JP 2005025665A JP 2005025665 A JP2005025665 A JP 2005025665A JP 2006187750 A JP2006187750 A JP 2006187750A
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sulfuric acid
oil
treatment
acid pitch
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Akira Matsunaga
旭 松永
Yukio Hirose
幸雄 広瀬
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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
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a sulfate pitch physicochemical treatment method which aims to convert sulfate pitch, hazardous waste, generated at the manufacturing of illegal light oil, and the like, into a product with a low environmental load by efficient and low-cost detoxification treatment and aims to obtain valuable material. <P>SOLUTION: Electrolyzed reduced water 4 (alkaline water generated on a cathode when electrolysis is carried out after adding an electrolysis auxiliary agent, such as common salt, in a water-flow type electrolyzer) is supplied to the sulfate pitch 1, and the sulfate pitch 1 is solubilized by using an ultrasonic irradiation means 5 with a warming means 6. Subsequently water 8 is removed by an oil-water separation means 7, and then sludgy oil 11 of which the viscosity is decreased is treated in a main treatment device 12 comprising one of wet oxidation treatment, catalytic wet oxidation treatment, supercritical water oxidation treatment, supercritical water methanation treatment, and supercritical water gasification or hydrogenation treatment. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

発明の詳細な説明Detailed Description of the Invention

本発明は不正軽油の製造の際などに発生する有害廃棄物である硫酸ピッチを効率良く、低コストで無害化処理して環境負荷の低い生成物に変換するとともに有価物を得ることを目的とした硫酸ピッチの物理化学的処理方法に関するものである。  It is an object of the present invention to obtain a valuable product while converting sulfuric acid pitch, which is a hazardous waste generated in the production of illegal light oil, etc., to a product with low environmental impact by detoxifying efficiently and at low cost. The present invention relates to a method for physicochemical treatment of sulfuric acid pitch.

硫酸ピッチの処理処分の方法として固化埋立、回収法、焼却処理などの方法がある。  There are methods such as solidification landfill, recovery, and incineration as methods for disposal of sulfuric acid pitch.

固化埋立は硫酸ピッチに界面活性剤、生石灰粉、水などを添加混合して固化して埋め立てる方法であり、昔は行なわれていた。しかし、現在は土壌汚染や地下水汚染を引き起こすために禁じられている。  Solidification landfilling is a method of adding a surfactant, quick lime powder, water and the like to sulfuric acid pitch, solidifying and solidifying the landfill. However, it is currently forbidden to cause soil and groundwater contamination.

回収法は硫酸ピッチに水を加え、蒸気を吹き込んで攪拌しながら、80℃程度に加温すると、油、アルキルスルホン酸、希硫酸の3層に分離する。これを分別して油分は残存硫酸を中和し、アルキルスルホン酸は精製して回収する。希硫酸は中和して廃水として放流する。この方法は経済的に採算がとれず、実用化までには至らなかった。  In the recovery method, water is added to sulfuric acid pitch, and the mixture is separated into three layers of oil, alkylsulfonic acid, and dilute sulfuric acid by heating to about 80 ° C. while blowing steam and stirring. By separating this, the oil neutralizes the residual sulfuric acid, and the alkylsulfonic acid is purified and recovered. Dilute sulfuric acid is neutralized and discharged as waste water. This method is not economically profitable and has not been put to practical use.

焼却処理は前処理として消石灰あるいは苛性ソーダなどのアルカリを用いて中和処理を行ったうえで、焼却処理する方法である。現在はこの方式が行なわれているが、焼却時に発生する硫酸フュームを除去するために湿式電気集塵機を使用する必要があり、耐食材料を使用しなければならないため、設備が高価になる。また、前処理として消石灰を用いると苛性ソーダより薬品費は安価であるが、固形廃棄物の処理費が必要になる。一方、苛性ソーダを使用した場合は薬品費が高価であるが、水溶性の塩しか発生しないので処理費は安くなる。ただし、還元性のある亞硫酸ソーダが発生するので、COD規制のある地域では酸化処理しなければ放流できない。  The incineration treatment is a method of incineration treatment after performing neutralization treatment using alkali such as slaked lime or caustic soda as pretreatment. Although this method is currently used, it is necessary to use a wet electrostatic precipitator to remove sulfuric acid fumes generated during incineration, and the use of a corrosion-resistant material makes the equipment expensive. Further, when slaked lime is used as pretreatment, the chemical cost is lower than that of caustic soda, but the cost of processing solid waste is required. On the other hand, when caustic soda is used, the chemical cost is high, but since only water-soluble salts are generated, the processing cost is low. However, reducing sodium sulfate sulfate is generated, so it cannot be discharged unless it is oxidized in an area with COD regulations.

発明が解決しようとする課題Problems to be solved by the invention

硫酸ピッチは主として潤滑油の精製過程で、原料の鉱物性油などに含まれる不純物を濃硫酸で除去する際に廃棄物として生じるものであるが、その処理が困難であるために、現在はプロセス転換が行なわれており大手の石油精製施設における発生量は極めて少量になっている。その他、潤滑油を再生する際にも発生するが、現在、不法投棄で問題になっているのは不正軽油を生産する際に発生する物である。軽油を自動車燃料として購入すると、軽油引取税がその価格の中に含まれている。一方、灯油とA重油は税金がかからないので、灯油とA重油を混合して軽油を製造して脱税するケースが続出した。この脱税を防ぐため、灯油とA重油に対して、識別剤としてクマリンが添加されるようになった。ところが、このクマリンを除去するために濃硫酸で洗浄して原料がわからないように加工した軽油を販売し、脱税する不法行為が横行するようになった。この硫酸洗浄工程から発生するのが、現在、問題となっている硫酸ピッチである。  Sulfuric acid pitch is mainly generated in the process of refining lubricating oil, and it is generated as waste when removing impurities contained in mineral oil as raw material with concentrated sulfuric acid. Conversions are taking place, and the amount generated in major oil refineries is very small. In addition, it also occurs when reclaiming lubricating oil, but what is currently a problem with illegal dumping is the one that occurs when producing illegal light oil. When light oil is purchased as automobile fuel, the light oil tax is included in the price. On the other hand, kerosene and heavy fuel oil A are not taxed, and there are a number of cases where kerosene and heavy fuel oil A are mixed to produce light oil and tax is eliminated. In order to prevent this tax evasion, coumarin has been added as an identification agent to kerosene and A heavy oil. However, to remove this coumarin, illegal activities to sell tax oils that were washed with concentrated sulfuric acid and processed so that the raw materials were not known were rampant. What is generated from this sulfuric acid washing step is sulfuric acid pitch which is currently a problem.

硫酸ピッチを排出する業者はもともと不法行為を承知でやっているので、焼却などのコストがかかる処理を行なうはずがなく、ドラム缶に詰めて不法投棄を行なうのである。硫酸ピッチは腐食性が強いので、やがては土壌汚染や地下水汚染を引き起こす。しかし、不法投棄されたものは誰かが処理しなければならず、そのためには現行の焼却処理よりも安価な処理方法を開発する必要がある。そのためには既存の処理方法に改良を加えたり、あるいは適当な前処理と組み合わせることによって硫酸ピッチの処理方法として適応させることも考えられる。  Since the manufacturer that discharges sulfuric acid pitch is aware of illegal activities, it is impossible to carry out costly processes such as incineration, and it is illegally dumped in drums. Sulfuric acid pitch is highly corrosive and will eventually cause soil and groundwater contamination. However, someone who has been dumped illegally has to deal with it. To that end, it is necessary to develop a treatment method that is cheaper than the current incineration treatment. For this purpose, it is conceivable to improve the existing processing method or to adapt it as a sulfuric acid pitch processing method by combining with an appropriate pretreatment.

問題を解決するための手段Means to solve the problem

本発明は硫酸ピッチ、特に不正軽油製造に伴い排出される硫酸ピッチを安価に無害化する処理方法を提供することを目的とする。
この目的を達成するために、まず請求項1により可溶化前処理として硫酸ピッチに対して、電解還元水(流水型電解水生成器において食塩などを補充して電気分解を行い、陰極側に生成したアルカリ性の水)を供給する。電解還元水(強還元水)はpH11〜12.5(11以上)、ORP−0.5〜−1.2V(−0.6V以下)の物性を持ち、界面活性作用および油脂乳化作用があり、硫酸ピッチを可溶化する。
It is an object of the present invention to provide a treatment method for detoxifying sulfuric acid pitch, particularly sulfuric acid pitch discharged in connection with illegal light oil production, at low cost.
In order to achieve this object, first, as a solubilization pretreatment according to claim 1, electrolysis is carried out by replenishing electrolytic pitched water (sodium chloride etc. in a flowing water type electrolyzed water generator) with respect to sulfuric acid pitch. Supplied alkaline water). Electrolytically reduced water (strongly reduced water) has physical properties of pH 11 to 12.5 (11 or more), ORP-0.5 to -1.2 V (-0.6 V or less), and has a surface active action and an oil emulsifying action. Solubilize sulfuric acid pitch.

可溶化前処理において請求項2により加温や超音波照射を行なうことにより可溶化が促進される。硫酸ピッチは可溶化により粘性が低下して流動しやすくなる。また、放置すると油層と水層に分離する。硫酸を含む水層は苛性ソーダなどのアルカリを添加して中和して排出される。一方、炭化水素およびクマリンスルホン酸を主成分とするアルキルスルホン酸などを含む油層は水を含んだスラッジ状となり、次に請求項1、3,4,5による硫酸ピッチ本処理にかけられる。これらの処理方法は汚泥や糞尿などの処理方法として既存のものである。  In the solubilization pretreatment, the solubilization is promoted by performing heating or ultrasonic irradiation according to claim 2. Sulfuric acid pitch decreases in viscosity due to solubilization and becomes easy to flow. If left untreated, it separates into an oil layer and an aqueous layer. The aqueous layer containing sulfuric acid is neutralized by adding an alkali such as caustic soda and discharged. On the other hand, the oil layer containing hydrocarbon and alkyl sulfonic acid mainly composed of coumarin sulfonic acid becomes sludge containing water, and is then subjected to sulfuric acid pitch main treatment according to claims 1, 3, 4 and 5. These treatment methods are existing treatment methods for sludge, manure, and the like.

請求項1における本処理方式である湿式酸化および触媒湿式酸化は高温高圧の水に空気を吹き込んで有機物を酸化する方式である。湿式酸化は昔から行われていた方法である。触媒湿式酸化は大阪ガス(株)が開発した方法で既存の湿式酸化より効率が高く、一部実用プラントが運転されている。この処理により可溶化前処理された硫酸ピッチの油分は酸化される。その結果、油分に含まれる炭化水素とアルキルスルホン酸は二酸化炭素、水、硫酸および残留灰分になる。硫酸は排水中に溶解しているので、アルカリで中和する必要がある。また、残留灰分は排水処理において分離除去される。  The wet oxidation and catalytic wet oxidation, which are the main treatment methods in claim 1, are methods for oxidizing organic substances by blowing air into high-temperature and high-pressure water. Wet oxidation is a method that has been performed for a long time. Catalytic wet oxidation is a method developed by Osaka Gas Co., Ltd., which is more efficient than existing wet oxidation, and some practical plants are in operation. By this treatment, the oil component of sulfuric acid pitch that has been pre-solubilized is oxidized. As a result, hydrocarbons and alkyl sulfonic acids contained in the oil become carbon dioxide, water, sulfuric acid and residual ash. Since sulfuric acid is dissolved in the waste water, it must be neutralized with alkali. Residual ash is separated and removed in wastewater treatment.

請求項3における本処理方式である超臨界水酸化処理はオルガノ(株)が開発した方法であり、この方法により下水汚泥を処理した例が報告されている(用水と廃水;Vol.44No.10,39〜43(2002).)。超臨界水とは水の臨界点(温度374℃、圧力22Mpa)以上の温度、圧力状態にある高温・高圧の水である。常温・常圧の水にははとんど溶解しない炭化水素類や酸素などのガスも超臨界水には任意の割合で溶解する。したがって、超臨界水の存在下で酸素を通気すれば有機物と酸素が十分に溶解して混合されるため効率良く酸化が行われる。硫酸ピッチの本処理により発生するのは二酸化炭素、水、硫酸および残留灰分である。硫酸は排水中に溶解しているので、アルカリで中和する必要がある。また、残留灰分は排水処理において分離除去される。  The supercritical water oxidation treatment which is the main treatment method in claim 3 is a method developed by Organo Corp., and an example in which sewage sludge is treated by this method has been reported (water and wastewater; Vol. 44 No. 10). 39-43 (2002).). Supercritical water is high-temperature and high-pressure water in a pressure state at a temperature equal to or higher than the critical point of water (temperature 374 ° C., pressure 22 Mpa). Gases such as hydrocarbons and oxygen that are hardly soluble in water at normal temperature and pressure will also dissolve in supercritical water at an arbitrary ratio. Therefore, if oxygen is passed in the presence of supercritical water, the organic substance and oxygen are sufficiently dissolved and mixed, so that the oxidation is efficiently performed. Carbon dioxide, water, sulfuric acid and residual ash are generated by this treatment of sulfuric acid pitch. Since sulfuric acid is dissolved in the waste water, it must be neutralized with alkali. Residual ash is separated and removed in wastewater treatment.

請求項4における本処理方式である超臨界水メタン化処理は超臨界水により有機物を溶解、低分子化して、メタン化触媒によりメタンと二酸化炭素に分解する方法である。この方法を有機系廃棄物の処理に用いた例が報告されている(第13回廃棄物学会研究発表会講演論文集;286〜288(2002)。硫酸ピッチの本処理により発生するのはメタン、二酸化炭素、硫酸および残留灰分である。硫酸は排水中に溶解しているので中和処理してから放流される。また、残留灰分は排水処理において分離除去される。  The supercritical water methanation treatment, which is the main treatment method according to claim 4, is a method in which an organic substance is dissolved and reduced in molecular weight with supercritical water and decomposed into methane and carbon dioxide with a methanation catalyst. An example of using this method for the treatment of organic waste has been reported (Proceedings of the 13th Waste Society Research Presentation; 286-288 (2002). The main treatment of sulfuric acid pitch is methane. Carbon dioxide, sulfuric acid and residual ash, since sulfuric acid is dissolved in the waste water, it is discharged after neutralization, and the residual ash is separated and removed in the waste water treatment.

請求項5における本処理方式である超臨界水ガス化・水素化処理は有機系廃棄物を対象として超臨界水により不活性ガスを充填した状態で触媒を用いてガス化・水素化する方法である。触媒として水酸化カリウムのようなアルカリ触媒やニッケル触媒が有効である。この方法によりバイオマス系廃棄物から水素とメタンを主成分とする混合ガスを得た例が報告されている。(第14回廃棄物学会研究発表会講演論文集;593〜595(2003)。硫酸ピッチの本処理により発生するのは水素、メタン、硫酸および還元性硫黄などである。排水処理においては硫酸の中和と還元硫黄の酸化および残留灰分の除去などが行われる。  The supercritical water gasification / hydrogenation treatment as the present treatment method according to claim 5 is a method of gasifying and hydrogenating organic waste using a catalyst in a state in which an inert gas is filled with supercritical water. is there. As the catalyst, an alkali catalyst such as potassium hydroxide or a nickel catalyst is effective. An example of obtaining a mixed gas mainly composed of hydrogen and methane from biomass waste by this method has been reported. (Proceedings of the 14th Waste Society Research Presentation; 593-595 (2003). Hydrogen, methane, sulfuric acid, reducible sulfur, etc. are generated by the main treatment of sulfuric acid pitch. Neutralization and oxidation of reduced sulfur and removal of residual ash are performed.

発明実施の形態Embodiment of the Invention

以下本発明にかかる電解還元水を用い硫酸ピッチの可溶化前処理および本処理方法の具体的な実施例を図を用いて説明する。  Specific examples of sulfuric acid pitch solubilization pretreatment and this treatment method using electrolytically reduced water according to the present invention will be described below with reference to the drawings.

図1は硫酸ピッチの処理システムの構成であり電解還元水を用いた硫酸ピッチの可溶化前処理および既存の本処理を組み合わせたシステムから構成される。硫酸ピッチ1は可溶化タンク2に入り、電解水生成器3より生成した電解還元水4と攪拌混合される。可溶化を促進するために超音波発振器5から超音波が発振されるとともに、加温手段6により加温される。その後、油水分離手段7により油水分離された水8は中和手段9により中和されて処理水10として排水される。一方、油水分離されたスラッジ状油11は本処理装置12に入り、高温高圧の水13あるいは超臨界水14と攪拌混合される。さらに酸化や分解に必要な材料(空気や触媒)15が添加される。反応が終了後、排ガス16および排水17が排出され、排水17は中和、還元硫黄の酸化、残留灰分の除去などの排水処理手段18で処理されてから処理水19として放流される。  FIG. 1 shows the configuration of a sulfuric acid pitch treatment system, which is composed of a system combining sulfuric acid pitch solubilization pretreatment using electrolytically reduced water and the existing main treatment. The sulfuric acid pitch 1 enters the solubilization tank 2 and is agitated and mixed with the electrolytic reduced water 4 generated from the electrolytic water generator 3. In order to promote solubilization, ultrasonic waves are oscillated from the ultrasonic oscillator 5 and heated by the heating means 6. Thereafter, the water 8 separated by the oil / water separation means 7 is neutralized by the neutralization means 9 and discharged as treated water 10. On the other hand, the oily water-separated sludge-like oil 11 enters the treatment apparatus 12 and is stirred and mixed with high-temperature and high-pressure water 13 or supercritical water 14. Further, a material (air or catalyst) 15 necessary for oxidation or decomposition is added. After the reaction is completed, the exhaust gas 16 and the waste water 17 are discharged, and the waste water 17 is treated as waste water treatment means 18 such as neutralization, oxidation of reduced sulfur, and removal of residual ash, and then discharged as treated water 19.

発明の効果The invention's effect

本発明にかかる電解還元水を用いた硫酸ピッチの可溶化前処理により、硫酸ピッチは低粘性の流動しやすいスラッジ状の油と硫酸を含む水に分離する。スラッジ状の油は湿式酸化あるいは触媒湿式酸化あるいは超臨界水酸化などの処理を行うことにより無害な二酸化炭素(炭酸ガス)に変換できる。クマリンスルホン酸を主成分とするアルキルスルホン酸は焼却すると硫黄酸化物となり排ガスの処理が困難である。それに対して本処理では硫黄酸化物はほとんど水に溶解するので排ガス処理が容易であり高価な排ガス処理装置が不要である。排水はアルカリで中和すれば放流できる。本処理システムでは残留灰分の処理は必要であるが、焼却処理の場合と比較して処分が厄介な固形廃棄物がほとんど生じないのも利点である。一方、前記の可溶化処理により分離したスラッジ状の油を超臨界処理水と攪拌混合して溶解して、触媒を用いてメタン化あるいは水素化することにより付加価値の高い可燃性ガスとしてリサイクルすることができる。  By the pretreatment for solubilization of sulfuric acid pitch using the electrolytically reduced water according to the present invention, the sulfuric acid pitch is separated into sludge-like oil that is easy to flow and water containing sulfuric acid. Sludge-like oil can be converted to harmless carbon dioxide (carbon dioxide) by performing treatments such as wet oxidation, catalytic wet oxidation, or supercritical water oxidation. Alkyl sulfonic acid mainly composed of coumarin sulfonic acid becomes sulfur oxide when incinerated, and it is difficult to treat exhaust gas. On the other hand, in the present treatment, sulfur oxides are almost dissolved in water, so that the exhaust gas treatment is easy and an expensive exhaust gas treatment device is unnecessary. Wastewater can be discharged if neutralized with alkali. Although the present treatment system requires treatment of residual ash, it is also advantageous in that almost no solid waste that is difficult to dispose is produced compared to incineration. On the other hand, the sludge-like oil separated by the above-mentioned solubilization treatment is dissolved by stirring and mixing with supercritical water, and recycled as high-value combustible gas by methanation or hydrogenation using a catalyst. be able to.

硫酸ピッチの処理システムSulfuric acid pitch treatment system

符号の説明Explanation of symbols

1…硫酸ピッチ
2…可溶化タンク
3…電解水生成装置
4…電解還元水
5…超音波発振器
6…加温手段
7…油水分離手段
8…油水分離により分離した水
9…中和手段
10…処理水
11…スラッジ状油
12…本処理装置
13…高温高圧の水
14…超臨界水
15…酸化や分解に必要な材料(空気や触媒)
16…排ガス
17…排水
18…中和、還元硫黄の酸化、残留灰分の除去などの排水処理手段
19…処理水
DESCRIPTION OF SYMBOLS 1 ... Sulfuric acid pitch 2 ... Solubilization tank 3 ... Electrolyzed water production | generation apparatus 4 ... Electrolytic reduction water 5 ... Ultrasonic oscillator 6 ... Heating means 7 ... Oil-water separation means 8 ... Water separated by oil-water separation 9 ... Neutralization means 10 ... Treated water 11 ... Sludge oil 12 ... This treatment device 13 ... High-temperature and high-pressure water 14 ... Supercritical water 15 ... Materials necessary for oxidation and decomposition (air and catalyst)
16 ... exhaust gas 17 ... waste water 18 ... waste water treatment means 19 such as neutralization, oxidation of reduced sulfur, removal of residual ash, etc .... treated water

Claims (5)

不正軽油製造の際などに発生する有害廃棄物である硫酸ピッチを無害化処理することを目的として硫酸ピッチに対して電解還元水(流水型電気分解器で食塩のような電解補助剤を添加して電気分解した際に陰極で発生するアルカリ性の水、強還元水とも呼称する)を注入する可溶化前処理を行うことにより、強還元水の界面活性作用および油脂乳化作用により乳化して低粘性の流体とする。この流体から油水分離して得られた含水スラッジ状の油を湿式酸化処理あるいは触媒湿式酸化処理して炭酸ガスなどに変換して無害化することを特徴とする硫酸ピッチの処理方法。        For the purpose of detoxifying sulfuric acid pitch, which is a hazardous waste generated during the production of illegal diesel oil, electrolytically reduced water (electrolytic auxiliary agent such as salt is added to the sulfuric acid pitch with a flowing water type electrolyzer). By solubilizing pretreatment that injects alkaline water generated at the cathode when electrolyzed and also called strong reduced water) Fluid. A method for treating sulfuric acid pitch, characterized in that a hydrous sludge-like oil obtained by oil-water separation from this fluid is converted into carbon dioxide gas or the like by wet oxidation or catalytic wet oxidation to render it harmless. 請求項1において硫酸ピッチに対して電解還元水を注入する際に、電解還元水を加温または超音波照射または両者を併用することにより乳化を促進することを特徴とする硫酸ピッチの可溶化前処理方法。        The electrolytic pitch water is injected into the sulfuric acid pitch according to claim 1, and the emulsification is promoted by heating the electrolytic reduced water or irradiating with ultrasonic waves or using both in combination. Processing method. 請求項1および2における硫酸ピッチの可溶化前処理を行った後、油水分離した得られた含水スラッジ状の油を超臨界水酸化処理して炭酸ガスなどに変換して無害化することを特徴とする硫酸ピッチの処理方法。        After the solubilization pretreatment of sulfuric acid pitch in claim 1 and 2, the water-containing sludge-like oil obtained by oil-water separation is supercritically hydroxylated to convert it into carbon dioxide gas or the like to render it harmless. A method for treating sulfuric acid pitch. 請求項1および2における硫酸ピッチの可溶化前処理を行った後、油水分離して得られた含水スラッジ状の油を超臨界水メタン化処理によりメタンなどに変換して無害化することを特徴とする硫酸ピッチの処理方法。        The hydrous sludge-like oil obtained by oil-water separation after the pretreatment for the solubilization of sulfuric acid pitch in claims 1 and 2 is converted into methane and the like by decontamination by supercritical water methanation. A method for treating sulfuric acid pitch. 請求項1および2における硫酸ピッチの可溶化前処理を行った後、油水分離して得られた含水スラッジ状の油を超臨界水ガス化・水素化処理により水素およびメタンなどに変換して無害化することを特徴とする硫酸ピッチの処理方法。        After the pre-solubilization treatment of sulfuric acid pitch in claims 1 and 2, the water-containing sludge-like oil obtained by oil-water separation is converted to hydrogen, methane, etc. by supercritical water gasification and hydrogenation treatment, and is harmless A method for treating sulfuric acid pitch, characterized by comprising:
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Cited By (8)

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JP2006239631A (en) * 2005-03-04 2006-09-14 Kankyo System Kenkyusho:Kk Treatment process of sulfate pitch
JP2010075901A (en) * 2008-09-29 2010-04-08 Hitachi Plant Technologies Ltd Method for separating oil from sludge
WO2013159534A1 (en) * 2012-04-23 2013-10-31 西安交通大学 Method for treating wastewater resulting from wool-washing by coupling ultrasonic wave demulsification and supercritical water oxidation
CN103980967A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for preparing oily sludge blended coal water slurry by using fluorine-containing polycarboxylic acid dispersing agent through ultrasonic dispersion
CN103979768A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge blended with coal water slurry
CN103979756A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge by using supercritical fluid through rapid swelling
CN104492459A (en) * 2014-12-17 2015-04-08 河海大学 Composite catalyst for preparing hydrogen through supercritical water gasification of low-moisture-content dehydrated sludge and application of composite catalyst
CN112876036A (en) * 2021-02-23 2021-06-01 扬州阿鲁达环境科技有限公司 Ultrasonic-based oily sludge treatment system and process

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006239631A (en) * 2005-03-04 2006-09-14 Kankyo System Kenkyusho:Kk Treatment process of sulfate pitch
JP4630088B2 (en) * 2005-03-04 2011-02-09 株式会社環境システム研究所 Sulfuric acid pitch treatment method
JP2010075901A (en) * 2008-09-29 2010-04-08 Hitachi Plant Technologies Ltd Method for separating oil from sludge
WO2013159534A1 (en) * 2012-04-23 2013-10-31 西安交通大学 Method for treating wastewater resulting from wool-washing by coupling ultrasonic wave demulsification and supercritical water oxidation
CN103980967A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for preparing oily sludge blended coal water slurry by using fluorine-containing polycarboxylic acid dispersing agent through ultrasonic dispersion
CN103979768A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge blended with coal water slurry
CN103979756A (en) * 2014-05-27 2014-08-13 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge by using supercritical fluid through rapid swelling
CN103979768B (en) * 2014-05-27 2015-03-18 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge blended with coal water slurry
CN103979756B (en) * 2014-05-27 2015-05-20 陕西延长石油(集团)有限责任公司 Method for tempering oily sludge by using supercritical fluid through rapid swelling
CN104492459A (en) * 2014-12-17 2015-04-08 河海大学 Composite catalyst for preparing hydrogen through supercritical water gasification of low-moisture-content dehydrated sludge and application of composite catalyst
CN112876036A (en) * 2021-02-23 2021-06-01 扬州阿鲁达环境科技有限公司 Ultrasonic-based oily sludge treatment system and process

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