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BIOREFINERY AND METHOD FOR REVAMPING A CONVENTIONAL REFINERY OF MINERAL OILS INTO SAID BIOREFINERY

机译:生物炼油厂和将矿物油的常规炼油厂改造为人造生物炼油厂的方法

摘要

The invention relates to a method for revamping a conventional refinery of mineral oils into a new biorefinery, wherein said biorefinery is characterized by a production scheme which enables the treatment of raw materials of a biological origin for the production of biofuels with a high productivity and reduced hydrogen consumption. Said method allows the re-use of existing plants, enabling, in particular, the revamping of a refinery containing a system comprising two hydrodesulfurization units, U1 and U2, into a biorefinery comprising a unit for the production of hydrocarbon fractions from mixtures of a biological origin, containing fatty acid esters, by hydrolysis of the same (ID), hydrodeoxygenation and isomerization. Each of said hydrodesulfurization units U1 and U2 comprises: a hydrodesulfurization reactor, (Al) for the unit U1, and (A2) for the unit U2, wherein said reactor contains a hydrodesulfurization catalyst, one or more heat exchangers between the feedstock and effluent of the reactor, a heating system of the feedstock upstream of the reactor, a treatment unit of acid gases downstream of the reactor, containing an absorber (B) for H2S, said unit called Tl in the unit U1 and T2 in the unit U2, and the method of the present invention comprises: installing a unit ID, comprising a hydrolysis reactor Rid, upstream of the unit U1, installing a connection line LD between the unit ID and the unit U1, installing a line L between the units U1 and U2 which connects them in series, possibly installing a product recycling line for the unit U1 and possibly installing a recycling line for the unit U2, substituting the hydrodesulfurization catalyst, in the reactor A1, with a hydrodeoxygenation catalyst, substituting, the hydrodesulfurization catalyst, in the reactor A2, with a hydroisomerization catalyst, installing a by-pass line X of the treatment unit of acid gases T2 of the unit U2, substituting the absorber (B), in the unit for the treatment of acid gases T1, with a specific absorber for CO2 and H2S. The new operational configuration, obtained with the method object of the present invention, allows materials of a biological origin to be converted to biofuels, controlling the corrosion phenomena, reducing the hydrogen consumption, increasing the productivity and recovering glycerine, as by-product, that can be commercially exploited.
机译:本发明涉及一种将常规的矿物油精炼厂改造成新的生物精炼厂的方法,其中所述生物精炼厂的特征在于一种生产方案,该方案能够处理生物来源的原料,从而以高生产率和降低的成本生产生物燃料。氢消耗。所述方法允许再利用现有的工厂,特别是使包含包含两个加氢脱硫单元U1和U2的系统的炼油厂改建为包括用于从生物混合物中生产烃馏分的装置的生物炼油厂。通过脂肪酸(ID)的水解,加氢脱氧和异构化反应而衍生的含有脂肪酸酯的脂肪酸。每个所述加氢脱硫单元U1和U2包括:加氢脱硫反应器,(U1)用于单元U1,和(A2)用于单元U2,其中所述反应器包含加氢脱硫催化剂,在原料和流出物之间的一个或多个热交换器。反应器,反应器上游原料的加热系统,反应器下游酸性气体的处理单元,其中包含H 2 S的吸收器(B),该单元在单元中称为T1在单元U2中的U1和T2,以及本发明的方法包括:在单元U1的上游安装包括水解反应器R id 的单元ID,在单元之间安装连接线LD在ID和单元U1中,在单元U1和U2之间串联连接的管线L上安装管线L,可能在单元U1中安装产品回收管线,并且单元U2中可能安装回收管线,以取代加氢脱硫催化剂。反应器A1,带有双氢在反应器A2中,用加氢异构化催化剂代替加氢脱硫催化剂,然后在反应器A2中安装脱氢催化剂,将单元U2的酸性气体T2的处理单元的旁路管线X安装在吸收器(B)中。用CO 2 和H 2 S的特定吸收剂处理酸性气体T1。利用本发明的方法目的获得的新的操作配置允许将生物来源的材料转化为生物燃料,控制腐蚀现象,减少氢消耗,提高生产率并回收甘油作为副产物。可以进行商业开发。

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