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Performance of thermochemical conversion of fat, oils, and grease into kerosene-like hydrocarbons in different production scales

机译:脂肪,油和油脂在不同生产规模下热化学转化为类煤油烃的性能

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摘要

This work aims to investigate the effect of catalytic cracking of residual fat, oils, and grease (FOG) from grease traps in different production scales (bench, laboratory, and pilot) on the reaction products yields and OLP properties and the feasibility to produce kerosene-like hydrocarbons. The cracking experiments were carried out in batch mode at 450 degrees C and 1.0 atmosphere, with 10% (wt.) Na2CO3 using a laboratory scale cylindrical borosilicate-glass reactor of 143 mL, a bench scale stirred tank slurry reactor of 1.5 L, and a pilot scale stirred tank slurry reactor of 143 L (1:10:1000). The reaction liquid products were physical and chemical analyzed for acid and saponification values, density, kinematic viscosity, refractive index, and copper strip corrosion. FT-IR analysis provided the qualitative chemical composition of OLP obtained in bench, laboratory, and pilot scales, as well as kerosene, light and heavy diesel-like hydrocarbons fractions obtained by distillation of OLP produced in pilot scale with 10% (wt.) Na2CO3. The chemical compositions of OLP and kerosene-like hydrocarbons fraction obtained in pilot scale determined by NMR and GC-MS. The results showed an OLP yield ranging from 62.90 to 66.57% (wt.), a coke yield ranging between 7.02 and 9.79% (wt.), and a gas yield ranging from 16.32 to 22.40% (wt.), showing a mean absolute percentage deviation of 2.12%, 11.88%, and 14.91% for OLP, gas, and coke yields respectively, obtained in different production scales (10:1000). The OLP acid values varied from 19.08 to 10.45 mg KOH/g, the density between 0.820 and 0.835 g/cm(3), and the kinematic viscosity from 3.28 to 4.21 mm(2) s(-1). The yield of kerosene-like hydrocarbons fraction average 14.90% (wt.) with an acid value of 5.43 mg KOH/g, density of 0.740 g/cm(3), and kinematic viscosity of 0.66 mm(2) s(-1), while those of light and heavy diesel-like hydrocarbons fractions average 32.01% (wt.) and 19.35% (wt.) respectively. FT-IR and NMR analysis of OLP and kerosene-like hydrocarbons fraction confirms the presence of functional groups characteristic of hydrocarbons (alkenes, alkanes, ring-containing alkenes, and ring-containing alkanes, and cycloalkanes) and oxygenates (carboxylic acids, ketones, fatty alcohols, and dienes). The GC-MS analysis of OLP and kerosene-like hydrocarbons fraction obtained in pilot scale with 10% (wt.) Na2CO3 identified in OLP 76.97% hydrocarbons (39.44% alkenes, 31.91% alkanes, 4.12% ring-containing alkenes, and 1.50% ring containing alkenes) and 23.03% oxygenates (12.14% carboxylic acids, 6.98% ketones, 1.90% fatty alcohols, and 2.01% dienes).
机译:这项工作旨在研究来自不同生产规模(工作台,实验室和中试)的隔油池中残留油脂,油脂的催化裂化对反应产物收率和OLP性质的影响以及生产煤油的可行性。类碳氢化合物。使用143 mL实验室规模的圆柱形硼硅酸盐玻璃反应器,1.5 L的台式搅拌釜淤浆反应器,在450摄氏度和1.0个大气压,含10%(wt。)Na2CO3的间歇模式下进行裂解实验。 143 L(1:10:1000)的中试搅拌釜淤浆反应器。对反应液体产物进行物理和化学分析,以测定其酸和皂化值,密度,运动粘度,折射率和铜带腐蚀。 FT-IR分析提供了在实验室,实验室和中试规模获得的OLP的定性化学组成,以及通过以10%(wt。)的中试规模蒸馏得到的OLP蒸馏得到的煤油,轻质和重柴油样烃馏分。碳酸氢钠通过NMR和GC-MS以中试规模获得的OLP和类煤油烃馏分的化学组成。结果显示,OLP产率为62.90%至66.57%(wt。),焦炭产率为7.02至9.79%(wt。),气体产率为16.32至22.40%(wt。),显示出绝对绝对值在不同的生产规模下(10:1000)获得的OLP,天然气和焦炭产率的百分比偏差分别为2.12%,11.88%和14.91%。 OLP酸值从19.08到10.45 mg KOH / g,密度在0.820到0.835 g / cm(3)之间,运动粘度从3.28到4.21 mm(2)s(-1)不等。煤油状烃馏分的平均产率为14.90%(wt。),酸值为5.43 mg KOH / g,密度为0.740 g / cm(3),运动粘度为0.66 mm(2)s(-1) ,而轻质和重质柴油状烃的平均含量分别为32.01%(wt。)和19.35%(wt。)。 OLP和类煤油烃馏分的FT-IR和NMR分析证实了存在烃类(烯烃,烷烃,含环烯烃,含环烷烃和环烷烃)和含氧化合物(羧酸,酮,脂肪醇和二烯)。在中试规模中获得的OLP和类煤油烃馏分的GC-MS分析,其中OLP中鉴定有76.97%的烃(39.44%的烯烃,31.91%的烷烃,4.12%的含环烯烃和1.50%的Na2CO3)含烯烃的环)和23.03%的含氧化合物(12.14%的羧酸,6.98%的酮,1.90%的脂肪醇和2.01%的二烯)。

著录项

  • 来源
    《Journal of Analytical & Applied Pyrolysis》 |2016年第7期|126-143|共18页
  • 作者单位

    Fac Environm & Sanit Engn UFPA, Lab Multiuser Water & Sludge Anal & Treatment LAM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Sect Chem Engn IME, Lab Catalyst Preparat & Catalyt Cracking, Praca Gen Tiburcio 80, BR-22290270 Rio De Janeiro, RJ, Brazil;

    Fac Environm & Sanit Engn UFPA, Lab Multiuser Water & Sludge Anal & Treatment LAM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Mat Engn UNIFESSPA, Quadra 17,Bloco 4, BR-68505080 Maraba, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Grad Program Nat Resource Engn UFPA, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Sect Chem Engn IME, Lab Catalyst Preparat & Catalyt Cracking, Praca Gen Tiburcio 80, BR-22290270 Rio De Janeiro, RJ, Brazil;

    Fac Environm & Sanit Engn UFPA, Lab Multiuser Water & Sludge Anal & Treatment LAM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil;

    Fac Chem Engn UFPA, Lab Separat Proc & Appl Thermodynam TERM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Fac Environm & Sanit Engn UFPA, Lab Multiuser Water & Sludge Anal & Treatment LAM, Rua Augusto Correia 1,Cx P 8619, BR-66075900 Belem, Para, Brazil|Leibniz Inst Agrartechn Potsdam Bornin eV, Dept Postharvest Technol, Max Eyth Allee 100, D-14469 Potsdam, Germany;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);美国《生物学医学文摘》(MEDLINE);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Catalytic cracking; Grease traps; Distillation; Green kerosene; Performance; Production scales;

    机译:催化裂化;油脂捕集;蒸馏;绿色煤油;性能;生产规模;

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