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Process for producing refined diesel fuel and refined fuel for the engine

机译:生产精制柴油和用于发动机的精制燃料的方法

摘要

The process of producing refined fuel for high-pressure engines in the catalytic depolymerisation process consists of the drying of the municipal and/or organic waste constituting the feedstock and the subsequent treatment in the separation and evaporation block combined with the mixing turbine,where catalytic depolymerisation occurs. The distilled raw material is distilled in a distiller to obtain fuel for high-voltage engines and part of the fuel obtained is used to power the gas-electric generator. Catalytic Depolymerisation is carried out in the presence of catalyst-acting sodium aluminium silicate,the detection of sensors associated with the individual blocks of the catalytic depolymerisation process shall be automatically monitored by a technology process control block and, if deviations from the insufficient catalyst quantity are detected, an automatic catalyst dosing device shall be activated by means of which: is fed to the turbine mixing the catalyst dose in quantities from 5kg to 35kg per 1000 l fuel in the process,Then it goes back to monitoring the work of individual blocks. To this fuel is added a colloidal solution of nanoparticles of wax oxide (CeO2) of particle size from 10 nm to 50 nm in light petroleum distillates in order to provide the final concentration of nanoparticles of CeO2 wax oxide in the fuel from 20 ppm to 100 ppm and a colloidal solution of copper nanoparticles (Cu) with a particle size of 10 nm to 50 nm in paraffinic, naphthenic and aromatic hydrocarbons at boiling temperatures from 180oC to 350oC in order to provide the final concentration of the nanoparticles in the fuel from 20 ppm to 50 ppm.
机译:在催化解聚过程中生产用于高压发动机的精制燃料的过程包括干燥构成原料的市政废物和/或有机废物,以及随后在与混合涡轮机结合的分离和蒸发模块中进行的处理,其中催化解聚发生。蒸馏后的原料在蒸馏器中进行蒸馏以获得高压发动机的燃料,并且所获得的燃料的一部分用于为燃气发电机提供动力。催化解聚反应是在具有催化剂作用的硅铝酸钠存在下进行的,与催化解聚过程各个模块相关的传感器的检测应由工艺过程控制模块自动监控,如果与不足催化剂量的偏差为如果检测到这种情况,则应激活自动催化剂定量给料装置,该装置应通过以下方式启动:送入涡轮机,在此过程中将催化剂剂量按每1000升燃料5kg至35kg的量混合,然后返回到监视各个模块的工作。向该燃料中添加轻质石油馏出物中粒径为10 nm至50 nm的氧化蜡(CeO2)纳米粒子的胶体溶液,以使燃料中CeO2氧化蜡的纳米粒子的最终浓度为20 ppm至100沸腾温度为180oC至350oC时,在10纳米至50纳米的链烷烃,环烷烃和芳族烃中形成10 ppm至50 nm的铜纳米颗粒(Cu)的胶体溶液,以使燃料中的纳米颗粒最终浓度达到20 ppm至50 ppm。

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