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Transesterification of Jatropha curcas oil was carried out in the presence of solid acid, the effects of types of catalysts and reaction conditions on the bio-diesel yields and the components in the process of the preparation of methyl esters were examined.

采用固体酸催化酯交换方法,研究了由麻疯树油制备脂肪酸甲酯过程中催化剂类型及工艺条件对生物柴油产率和产品组成的影响。

Three high volatile bituminous coals were used pyrolysis with solid heat carrier to investigate the product distribution and characteristic of gas, tar and char.

以三种高挥发分烟煤为原料,对固体热载体煤热解获得的气、油、焦产物产率、组成和性质进行了考察。

Duration: long-term storage is not changed as a result of prolonged pressure reactor and agglomeration effects do not affect the use of powerful bacteria producing enzymes able to focus on solving the pipe plug, grease trap maintenance and odor problem.

有效 期:长期贮存不变质,如因长时间堆压而结块不影响使用效果强大的产酶杆菌能集中解决管道堵塞、隔油器维护和异味问题。

As to multi-layer reservoirs,each layer can be divided into three areas:area of gravel-packing,area of perforation and area of radial flow.Each area has its own governing equaiton and the solution is expressed by Green function.The well bore pressure and layer-rate is given through Green function in Laplace space.The pressure drop and skin factor isobtained also in each area.

根据多层砾石充填完井的渗流特点,将每个产层在径向上分成3个区域,即砾石充填区、射孔区、地层径向流区,每个区域有各自的渗流方程,对n层油藏有3n个渗流方程,将每个区域的方程用Green函数来表示,由各层的Green函数得到井筒混合压力、分层压力及分层产量在Laplace空间上的解,最后得到每层各区域的压力损失、表皮系数以及井底压力和分层产量与时间的变化关系。

Thus,the potential production estimate,qualitative and half quantitative evaluation can be done by a boundary line equation.

目前我们应用该项资料在确定含油产状、预测原油密度等方面做了一定的工作,并取得了较好的效果。

In the condition of solvent and catalyzer by Autoclave, the Hydro-liquefaction experimentation indicates that the hydrogen consumption is 5%, conversion rate is about 90%, the rate of liquid of coal is about 55%, showing that low rank coal of the west China is important liquefaction resources.

通过高压釜在溶剂和催化剂条件下的加氢液化试验可知,在氢耗量5%左右时,煤的液化转化率达90%以上,油产率达55%以上,这表明我国西部低煤级煤可作为重要的液化用煤资源。

The invention has the advantages that: 1 the preparation method is simple, the obtained pine needle essential oil has good quality and higher yield, the yield is increased by 30 to 49 percent or so compared with that of directly adopting the steam distillation; 2 the hydrophilic ionic liquid can be reclaimed and recycled by adopting the ion exchange method, which can not cause the environmental pollution.

本发明的优点:1制备方法简单,得到松针精油质量好,得率较高,比直接采用水蒸气蒸馏法的产率高30~49%左右;2亲水的离子液体可以采用离子交换法回收循环使用,不会造成环境污染。

Chemical detection is mainly production rate and the ratio of three to analysis and judge, through the transformer oil content of gas.

化学检测主要是通过变压器油中特征气体的含量、产气速率和三比值法进行分析判断,它对变压器的潜伏性故障及故障发展程度的早期发现具有有效性。

The results indicate the mutual effect exists between the single coals, which could increase the maximum of thermal weight loss obviously and has a small effect on the temperature extent of the weight loss. The main pyrolysis production of coal is coke, but the main production of waste plastics is tar; the yield of water became decrease and the gas became increase by adding the waste plastics. And the CRI and CSR decreased with the ratio of waste plastics in coal. The main ingredients of tar from blend coal are aromatic hydrocarbon and alkane, while those of waste plastics are alkane and alkene. The result of co-coking with coal and waste plastics make the light tar and the aromatic hydrocarbon increase obviously. The combustible ingredient(CO、H2、CH4) of gas from co-coking with coal increase at different ratio; Co-coking with coal and waste plastics could increase the combustible ingredient and thermal value of gas.

结果表明,废塑料与煤混合物在煤的塑性温度区间内存在明显的相互作用,使最大热解失重峰迁移,热解速率变大,且随着废塑料配比的增加呈现规律性的变化;煤热解产物固体焦炭为主,而废塑料的热解产物以焦油为主,废塑料的添加使得总体焦炭和水产率下降,焦炉煤气和焦油的产率增加,即共焦化呈现出明显的&增油减水&效应;随着塑料添加量的增加,焦炭热强度呈现劣化趋势;废塑料代替瘦煤配煤炼焦可使其比例提高到3%而不影响焦炭的质量;纯煤焦化所得焦油以芳香烃类和烷烃类为主,而废塑料热解焦油以烷烃和烯烃为主;废塑料配煤炼焦,可使得的焦油呈现&环构化&和&轻质化&趋势;废塑料的添加可使煤气中的可燃组分(CO、H2、CH4)的含量均有不同程度的增加;废塑料配煤炼焦可以优化焦炉煤气的组成,增加煤气中的可燃组分,提高焦炉煤气的热值。

This reaction system can catalyze soybean oil and sunflower oil too,and the conversion rate was 83.51%and 88.57%respectively.

该反应体系可用于催化大豆油和葵花子油生产生物柴油,产率分别为88.57%和83.51%。

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