Shie J L, Chang C Y, Lin J P, Le D J, Wu C H
Graduate Institute of Environmental Engineering, National Taiwan University, Taipei.
Water Sci Technol. 2001;44(10):349-63.
Oxidative thermal treatment of oil sludge with different oxygen concentrations of air by using a dynamic thermogravimetric (TG) reaction system is investigated. The experimental conditions employed are: gas flow rate of 50 cm3/min (value at 298 K) for 300 mg dry waste, a constant heating rate of 5.2 K/min, the oxygen concentrations in air of 1.09, 8.62 and 20.95 vol. % O2, and the temperature (T) range of 378-873 K. From the experimental results, the residual mass fractions (M) are about 78.95, 28.49, 8.77 and 4.13 wt. % at the oxidative T of 563, 713, 763 and 873 K for the case with 20.95 vol. % O2, respectively. The values of M with 8.62 and 1.09 vol. % O2 at T of 873 K are 4.87 and 9.44 wt. %, respectively. The distillation characteristics of the oil portion of liquid products (condensates of gas at 298 K) from the oxidative thermal treatment of oil sludge with 20.95 vol. % O2 at T of 378-873 K is close to those of commercial gasoline. Nevertheless, the liquid product contains a large amount of water. The distillation characteristics of the oil portions of liquid products with 8.62 and 1.09 vol. % O2 at T of 378-873 K are close to those of diesel and fuel oils, respectively. The oil quality with 8.62 vol. % O2 is better than that with 1.09 vol. % O2. However, the liquid product with 8.62 vol. % O2 still contains a large amount of water; nonetheless, that with 1.09 vol. % O2 is with negligible water. Compared with the oil product of nitrogen pyrolysis, the oil quality with 1.09 vol. % O2 is better. Certainly, low oxygen conditions (i.e. 1.09 vol. % O2) not only accelerate the thermal reaction of oil sludge, but also at the same time avoid or reduce the production of water. Further, from the analysis of benzene (B), ethylbenzene (E), toluene (T) and iso-xylene (X) concentrations of the oil portion of liquid products, the BETX concentrations of oil with 20.95 vol. % O2 are higher than those with 8.62 and 1.09 vol. % O2. The yields of liquid products with 20.95, 8.62 and 1.09 vol. % O2 at T of 378-873 K are 31.96, 34.42 and 37.3 wt. %, respectively. From the experimental results, the improvement effects of oxygen on the qualities of the oil portion of liquid products are obvious. The above technique not only formats good quality gasoline and diesel oils but also reduces large amount of oil sludge. If the oil exists with water, it may be obtained by further separation or collected by fractional condensation.
利用动态热重(TG)反应系统,研究了在不同空气氧浓度下对油泥进行氧化热处理的情况。采用的实验条件为:对于300mg干废料,气体流速为50cm³/min(298K时的值),恒定加热速率为5.2K/min,空气中的氧浓度分别为1.09、8.62和20.95体积%O₂,温度(T)范围为378 - 873K。从实验结果来看,对于氧含量为20.95体积%O₂的情况,在563、713、763和873K的氧化温度下,残余质量分数(M)分别约为78.95、28.49、8.77和4.13wt.%。在873K时,氧含量为8.62和1.09体积%O₂时的M值分别为4.87和9.44wt.%。在378 - 873K温度下,对氧含量为20.95体积%O₂的油泥进行氧化热处理得到的液体产物(298K时气体的冷凝物)中油部分的蒸馏特性与商业汽油接近。然而,该液体产物含有大量水分。在378 - 873K温度下,氧含量为8.62和1.09体积%O₂时液体产物中油部分的蒸馏特性分别与柴油和燃料油接近。氧含量为8.62体积%O₂时的油品质量优于氧含量为1.09体积%O₂时的。然而,氧含量为8.62体积%O₂的液体产物仍含有大量水分;而氧含量为1.09体积%O₂的液体产物中水分可忽略不计。与氮热解的油品相比,氧含量为1.09体积%O₂时的油品质量更好。当然,低氧条件(即1.09体积%O₂)不仅加速了油泥的热反应,同时还避免或减少了水的产生。此外,通过对液体产物中油部分的苯(B)、乙苯(E)、甲苯(T)和异辛烷(X)浓度分析可知,氧含量为20.95体积%O₂时油中的BETX浓度高于氧含量为8.62和1.09体积%O₂时的。在378 - 873K温度下,氧含量为20.95、8.62和1.09体积%O₂时液体产物的产率分别为31.96、34.42和37.3wt.%。从实验结果可知,氧对液体产物中油部分质量的改善效果明显。上述技术不仅能形成优质的汽油和柴油,还能减少大量油泥。如果油与水共存,可以通过进一步分离或分馏冷凝来获取。