Loading...

Table of Content

    12 May 2016, Volume 47 Issue 5
    INTRINSIC REACTION KINETICS OF PARTIAL OXIDATION OF COKE TO CO ON SPENT CATALYST
    2016, 47(5):  1-5. 
    Asbtract ( 647 )   PDF  
    Related Articles | Metrics

    Spent catalyst with 1.7% of carbon content was prepared as the material for kinetic study. The intrinsic reaction kinetics of partial oxidation of coke was investigated at the reaction temperatures ranging from 510℃ to 780℃. The kinetic parameters of carbon conversion were obtained for various reaction conditions. For the carbon-water system, when the gasification of carbon took place below 780℃ with present of excessive carbon, the gasification of coke followed zero-order reaction, with the activation energy and the frequency factor of 161.23 kJ/mol and 116.2 s-1, respectively. For the carbon-oxygen-water system, when oxygen and water were excessive, the coke gasification in the temperature range of 510-665 ℃ followed first-order reaction with the activation energy and the frequency factor of 38.22 kJ/mol and 1.37 s-1; when the carbon and water were excessive, the oxygen consumption followed first-order reaction, with the activation energy and frequency factor to be 79.74 kJ/mol and 311 712 s-1, respectively. Experimental results indicated that the formation of CO was mainly from the reaction of carbon and oxygen at the reaction temperatures below 800 ℃. The relationship between the value of λ and T is λ=8.31e-16 736/(RT)], where λ is the molar ratio of CO to CO2 from the primary reaction of carbon and oxygen.

    INFLUENCE OF OILS ON OIL-COAL CO-PROCESSING
    2016, 47(5):  6-11. 
    Asbtract ( 718 )   PDF  
    Related Articles | Metrics

    The Influence of different feed oils(Tahe vacuum residue, FCC slurry oil and hydrogenated FCC slurry oil) on oil-coal co-processing was investigated in a pilot plant. The results show that it is difficult to conduct the coprocessing reaction under severe conditions for mixture of Tahe vacuum residue and coal. The coke yield is up to 5.49% when the conversion of >524 ℃ fraction reaches 62.24%, and that additon of FCC slurry could promote the conversion of >524 ℃ in the mixture at higher reaction temperature. Under even higher reaction temperature, the cracking rate of >524 ℃ fraction in the oil-coal slurry can reach to 83.58% and the coke formation be effectively controlled to 2.31% when the pre-hydrogenated FCC slurry is added. The pilot plant results showed that coal powder and residue can convert into liquids simultaneously using the mixture of vacuum residue, FCC slurry oil and coal powder as feed.

    MONTE CARLO SIMULATION OF EFFECT OF OLEFINS ON ADSORPTION OF THIOPHENE ON Cu(I)Y ZEOLITE
    2016, 47(5):  12-17. 
    Asbtract ( 579 )   PDF  
    Related Articles | Metrics

    The adsorption behavior of the thiophene and its mixture with olefins in Cu(I)Y zeolite was simulated by Grand Canonical Monte Carlo method. The n-nonane solution with S content of 300 μg/g was used to investigate the adsorption isotherm, adsorption distribution, and partial adsorption configurations. The results show that the thiophene follows the Langmuir-type adsorption on Cu(I)Yzeolite, and high temperature is not conducive to thiophene absorption. The effects of four types of olefins on desulfurization over Cu(I)Y zeolite were tested. The adsorption configuration proves that large molecular clusters of thiophene are formed by intermolecular forces, resulting in the Cu(I)Y supercagesare filled and that competitive adsorption exists between thiophene and cyclohexene. The adsorption results show that the Cu(I)Y zeoliteh has a better adsorption selectivity to thiophene. The order of effect of olefin on the adsorption of thiophene is as follows: cyclohexene > 1,5-hexadiene > 1-hexene > 1-octene.

    SARA ANALYSIS FOR 380# FUEL OIL AND THEIR OIL-WATER INTERFACIAL TENSION
    2016, 47(5):  18-23. 
    Asbtract ( 864 )   PDF  
    Related Articles | Metrics

    In this paper, saturates, aromatics, resins and asphaltenes were separated from 380# residual fuel oil,and the content and structure of the fractions were investigated by EA, GPC, FT-IR and 1H NMR. The interfacial tension (IFT) of 380# residual fuel and its fractions was measured, and the effects of pH value and salt content of aqueous phase on interfacial tension were studied. The results indicate that the aromatic is the most component in 380# residual fuel oil. The total content of asphaltene and resin is approximately 30%. Asphaltene contains more heteroatoms than resin. The molecular weight and aromatic carbon ratio (fA) of asphaltene is the largest, and its hydrogen carbon atom ratio [n(H)/n(C)] is minimum. It is found that the polar groups (hydroxyl, amino, carboxyl, etc) content of asphaltene is more than that of resin by the FT-IR analysis, so the asphaltene has higher interfacial activity. The interfacial tension sequence of the components in 380# residual fuel oil is: saturate>aromatic>resin>asphaltene. Because the acidic groups are more than the basic groups in residual fuel oil and in its components, the oil-water interfacial tension is declining sharply at the strong alkaline condition. The influence of salt content in aqueous phase on the interfacial tension is very small.

    DEVELOPMENT OF NEW EVAPORATION TECHNOLOGY FOR VACUUM DISTILLATION
    2016, 47(5):  24-28. 
    Asbtract ( 768 )   PDF  
    Related Articles | Metrics

    To improve the feed evaporation rate of vacuum distillation, on the basis of studying the process of the vacuum distillation unit, a pressurized atomizing feed for deep-cut technology was developed. The pressurized atomizing feed system was investigated by a vacuum distillation experimental unit. The changes of vaporization rate of feed in different feeding modes were investigated, and the results show that, under the same system pressure and feed temperature, the vaporization rate of the nozzle feed is higher than the rate of non-nozzle feed and the vapor and liquid mixture feed. Simulated industrial vacuum distillation operation, with the a pressurized atomizing feed model the oil yield can be increased by 2-5% and the separation efficiency of the vacuum distillation tower is increased, The experimental results show that the pressurized atomizing feed is an effective method to improve the vaporization rate of oil.

    CYCLONE-AIR FLOTATION TECHNOLOGY AND ITS APPLICATION IN OIL REMOVAL PRE-TREATMENT FOR ELECTRIC DESALTING WASTEWATER
    2016, 47(5):  29-34. 
    Asbtract ( 511 )   PDF  
    Related Articles | Metrics

    Oil pre-treatment of electric desalting wastewater is a difficult technical problem for crude oil refining industry. This paper introduces the field test by using independent R&D BIPTCFU-III-4 type centrifugal flotation prototype in SINOPEC Cangzhou Company, which is the first time to use centrifugal flotation technology to deal with electric desalting wastewater under harsh conditions. The field test has demonstrated that, when the inlet electric desalting wastewater oil content fluctuates between 7632.8-10 658.0 mg/L, the oil removal efficiency can be reached 95.0% with single-stage CFU and 95.6%-98.6% with two-stage CFUs in series. The outlet oil content can be controlled between 131.8-263.5 mg/L, and can totally meet the quality requirements of the influent of subsequent wastewater treatment processes. The centrifugal flotation technology also has some advantages such as enclosed operation, short hydraulic retention time. It can provide a feasible scheme for dealing with electric desalting wastewater, and deserve further exploration in engineering amplification applications.

    INFLUENCE OF HEAT EFFECT OF COKING REACTION ON COKE YIELD
    2016, 47(5):  35-40. 
    Asbtract ( 612 )   PDF  
    Related Articles | Metrics

    The overall reaction heat effect of residual oil not only reflects coking raw material structure, but also directly affects heavy oil products distribution, so it plays an important role for coking practical production process optimization. In this paper, based on the residual oil thermal reaction evaluation instrument, by static micro-testing, quantitatively measuring the reaction heat effect of residual oil under the condition of different temperature, studying the influence of residual oil thermal effect on coke yield, according to coking industry unit test data to verify theoretical feasibility. The results show that the endothermic effect of residual thermal process is negatively related with coke yield, inferior residual oil cracking endothermic phenomenon at 460 ℃ is stronger than 500 ℃, so it is better for furnace tube to adopt long-range and low intensity heating way. Prolonging the retention time of furnace tube sample in low temperature area and improving the heating load of residual oil, can moderately enhance residual conversion degree before entering reaction zone, can increase the cracking depth of oil sample in coke tower, reducing coke yield and increasing liquid efficiency.

    COMMERCIAL APPLICATION OF DN-3636 CATALYST IN DIESEL HYDROTREATING UNIT
    2016, 47(5):  41-45. 
    Asbtract ( 644 )   PDF  
    Related Articles | Metrics

    To meet the requirements of road-diesel national IV/V specifications in China, SINOPEC Zhenhai Refining and Chemical Company DHT-4 changed out catalyst with Criterion’s latest ULSD CENTERA DN-3636 in 2014. Catalyst performance test run was done with total feed rate of 344 tons/hr, in which SRGO, LCO and CLGO account for 68.9%, 12.9% and 18.2% separately. Product diesel S can be reduced to averaged 27 μg/g at conditions of CHPS pressure 5.3MPa, LHSV 1.74 h-1, H/O ratio 300 and R inlet T 331-332 ℃, WABT 358-359 ℃. When temperature was raised to R inlet 340.4 ℃, WABT 367.1 ℃, product diesel sulfur was less than 10 μg/g, which can meet diesel national V specifications. Performance test run showed that DN-3636 has high activities in HDS, HDN and HDAr for ULSD production. Compared to last cycle’s catalyst, SOR WABT needed for DN-3636 can be lowered down dramatically even with processing worse feed. Due to process more cracked diesel, reactor total delta T went up greatly by using DN-3636, which led to obvious energy consumption reduction.

    COMMERCIAL APPLICATION OF NJBMDA-Ⅱ CATALYS TIN WHITE OIL DEAROMATIZATION UNIT
    2016, 47(5):  46-50. 
    Asbtract ( 656 )   PDF  
    Related Articles | Metrics
    This article introduces the production engineering of and the application of high efficiency benzene hydrogenation catalyst NJBMDA-Ⅱ in this unit. The result shows that NJBMDA-Ⅱ has good activity at low temperature, with strong activity at initial temperature around 125 ℃. It also has high liquid phase space velocity, strong dearomatizing performance, high production efficiency. At conditions of 135 ℃,hydrogen partial pressure of 2.2 MPa, LHSV of 1.0 h-1 and H2/oil volume ratio of 400, aromatic content is less than 1% in the product oil. The production and control process is simple and reliable, which is able to meet the scale production demand of environment-friendly refined white oil with low aromatic content. The unit has fine economic benefit.
    HYDROGENATION ACTIVITY AND COKE RESTRAINING ABILITY OF OIL-SOLUBLE CATALYSTS FOR RESIDUE SLURRY-BED HYDROCRACKING
    2016, 47(5):  51-56. 
    Asbtract ( 646 )   PDF  
    References | Related Articles | Metrics

    Oil-soluble Mo and Ni catalysts applied in residue slurry-bed hydrocracking have been successfully synthesized and Mo/Ni catalyst has been obtained from the mixtures of these two kinds of monometallic catalysts. FT-IR and ASS analysis were used to characterize the properties of synthesized catalysts. Compared with thermal cracking in presence of hydrogen, KLAR slurry-bed hydrocracking was carried out, after the solubility study of Mo, Ni and Mo/Ni catalysts, to evaluate the hydrogenation activity of all catalysts. The results indicated Mo content was 5.60% in Mo catalyst and Ni content was 5.86% in Ni catalyst, respectively. The order of I (light oil yield per coke) was Mo>Mo/Ni>Ni, which meant the order of hydrogenation activity and coke restraining ability was Mo>Mo/Ni>Ni. Furthermore, Mo/Ni catalysts not only played a synergistic effect in hydrogenation activity but also could act as coke carrier and prevented the coke from gathering and growing.

    EFFECT OF NTA ON HDS AND HDN ACTIVITY OF Ni-Mo/Al2O3 FOR FCC DIESEL
    2016, 47(5):  57-61. 
    Asbtract ( 484 )   PDF  
    Related Articles | Metrics
    Ni-Mo/Al2O3 catalyst for catalytic diesel oil hydrotreating was prepared by incipient wetness impregnation method. The modified Ni-Mo/Al2O3 catalyst by nitrilotriacetic acid (NTA) during impregnation to research the effect of complex agent NTA on hydrodesulfurization (HDS) and hydrodenitrogenation (HDN) activity. The reaction activity was evaluated on a 100mL high-pressure hydrogenation fixed-bed reactor, and the physical and chemical properties were investigated by NH3-TPD, H2-TPR, BET and HRTEM. The results indicated that, catalyst Ni-Mo-NTA/Al2O3 has higher HDS and HDN activity than Ni-Mo/Al2O3. This result was due to that, modifying by NTA improved the surface acidity of the catalyst, reduced the interaction force between metal and supports, improved the reducibility of metal, and the pore structure was optimized, the MoS2 stack layer number distributed at 2~3, and the length of MoS2 lamella distributed at 2-4 nm, the dispersion of activity phase was promoted.
    STUDY OF ALKYLATION OF BENZENE AND SYNGAS OVER Pt/ZSM-5 CATALYST AND PROCESS CONDITIONS
    2016, 47(5):  62-66. 
    Asbtract ( 577 )   PDF  
    Related Articles | Metrics

    The one-step process to produce toluene and para-xylene through the alkylation reaction of benzene with syngas has been developed for the first time. Using 2wt% Pt/ZSM-5 zeolite as catalyst, the conversion of the benzene has reached 9.04% and the total selectivity of toluene and para-xylene is 82.85%, especially the selectivity of para-xylene is 9.18%. The optimized reaction condition is as follows: 500 ℃, 3.0 MPa, WHSV=3 h-1 and GHSV=12 000 cm3/(g?h). The catalyst catalysts were characterized by XRD,BET,TEM,NH3-TPD,H2-TPR and XPS to indicate the properties of catalyst, which will provide the foundation for the further study of this one-step process.

    SYNTHESIS OF Mo-Ni BULK CATALYST BY SOL-GEL METHOD AND HYDRODESULFURIZATION PERFORMANCE
    2016, 47(5):  67-73. 
    Asbtract ( 710 )   PDF  
    Related Articles | Metrics

    The bulk Mo-Ni composite oxide catalysts were prepared by sol-gel method and were characterized by XRD、BET、NH3-TPD. Using 2 wt% DBT- n-octane solution as the feed, the HDS performance of the catalysts were tested in a continuous flow fixed-bed reactor. According to the results of characterization and evaluation, the effects of calcination temperature, the solution pH of sol-gel process and the addition of starch on the properties and catalytic performance of the catalysts were investigated. The characterization results showed that oxided catalysts under more than 500℃ calcination were mainly composed of crystalline phase α-NiMoO4 and β-NiMoO4, while the sulfided catalysts were mainly composed of MoS2 and Ni2S3. The increasing of calcination temperature is beneficial for the formation of α-NiMoO4, while the enhancement of the alkaline solution is favorable to the formation of β-NiMoO4, the both significantly reduce the total acidity of catalysts. The addition of starch has little fact on the crystalline phase of oxided catalyst, but it can improve the dispersion of active component. The introduction of appropriate amount of starch can increase the specific surface area and pore volume of the catalysts. The results of hydrodesulfurization reaction indicated that the catalyst prepared under the conditions of calcination temperature 600 ℃, the pH solution 2, the starch amount 15g/(Mo+Ni)mol, exhibited a higher hydrodesulfurization activity. Under the conditions of 260 ℃, 2 h-1, 2.5 MPa and H2/oil volume ratio 300, the desulfurization rate of the feed containing 3 480 μg/g S over the catalyst reached to 98.3%, hydrogenation desulfurization (HYD) pathway was the prior way during the HDS reaction of DBT, and the HYD/DDS( direct desulfurization) ratio was 1.23.

    STUDY ON DENITRIFICATION BY COMPOSITE NANOPARTICLES CATALYST V-Fe/AC AT LOW TEMPERATURE
    2016, 47(5):  74-78. 
    Asbtract ( 385 )   PDF  
    Related Articles | Metrics

    V2O5-Fe2O3 composite nanoparticles were prepared through the high-pressure hydrothermal method.By changing the hydrothermal solvent,the morphology of nanoparticles was controlled.XRD and SEM results showed the B-V2O5-Fe2O3 nanoparticle was a rod like structure with H2O2 as solvent,and there were some small spherical particles adhered.The Q-V2O5-Fe2O3 of globular structure was prepared using NH3?H2O as solvent.And two morphologies of composite nanoparticles were of great crystallinity.The commercial columnar activated-coke were prepared with H2O2-HNO3 joint oxidation modification method to obtain HAC,different morphologies of the composite nanoparticles were loaded on which to prepare the B-V-Fe/AC and Q-V-Fe/AC catalysts.Under the conditions of Simulated flue temperature 200 ℃,space velocity 6 000 L/(Kg?h),AC's amount of 10 g and the total flow rate of the mixed gas was 1 L/min,of which φ(O2)=5%,φ(NO)=0.05%,φ(NH3)=0.05%,the denitrification performance of different catalysts were evaluated.The results showed,when the loading amount of B-V2O5-Fe2O3 is 1%,the denitrification performance of B-V-Fe/AC is the best with a rate of 69.42%,which were increased by 17.75% and 1.69%,compared to HAC and Q-V-Fe/AC.

    Effect of Ashless Combustion Supporting Additive on Diesel Engine Performance Under Simulated Plateau Environment
    2016, 47(5):  79-84. 
    Asbtract ( 418 )   PDF  
    Related Articles | Metrics

    Using an atmosphere simulation test device, the engine bench test under simulated plateau environment was carried out when the diesel engine was fueled with fuel(NO.0) and adding ashless combustion supporting additive fuel(NO.1). By testing the power, the fuel consumption rate, the emissions of soot and other harmful substances, to evaluate the effect of energy-saving and emissions reduction of diesel additive. The results indicated that in comparison to fuelled with NO.0, when the engine fuelled with NO.1 at simulated altitude of 3 000 m (70 kPa), the engine output power increased, the fuel consumption rate and CO,HC,soot emission decreased obviously, while NOx emission increased slightly. Add ashless combustion supporting additive can effectively improve the power of the diesel engine, save fuel and reduce emissions, improve the plateau adaptability of the engine.

    STUDY ON PREPARATION AND PROPERTIES OF LaF3 NANOPARTICLES LIQUID LUBRICATING ADDITIVE
    2016, 47(5):  85-88. 
    Asbtract ( 621 )   PDF  
    Related Articles | Metrics

    With lanthanum chloride,ammonium fluoride as raw material,silane coupling agent as the surface modification agent prepare colloid LaF3 By phase transfer method to transfer the prepared LaF3 colloid to methyl oleate,getting the diameter of 40 nm nano LaF3 addictives..Centrifugal sedimentation method and speed temperature control was used to study the additive of nano LaF3 dispersion stability and high-temperature stability. Tribological properties of nano LaF3 liquid additives were studied with a four-ball wear test machine, and steel ball surface were investigated by scanning electron microscopy (SEM) and (EDS). The results show that nano LaF3 liquid additives in the 100N base oil has good dispersion stability, with excellent extreme pressure, anti-wear and friction-reducing properties. Surface wear of steel balls significantly reduce and wear surface protecting film containing elements such as La,F.

    INHIBITION PROPERTY OF OLEIC IMIDAZOLINE AMIDE FOR A3 MILD STEEL CORROSION
    2016, 47(5):  89-94. 
    Asbtract ( 694 )   PDF  
    Related Articles | Metrics

    In this paper, the corrosion inhibition performance of a newly synthesized oleic acid imidazoline amide (EYP) which was intended to be used in the overhead circulating reflux system of fractionating tower was investigated by weight loss, potentiodynamic polarization and electrochemical impedance spectroscopy (EIS) tests. The surface morphologies of mild steel specimens were observed by scanning electron microscope (SEM) and the kinetic parameters were calculated from experimental weight loss results. Weight loss and SEM results demonstrated that EYP can effectively protect A3 mild steel from corrosion in simulative top cycle oil. The inhibition efficiency of EYP increased firstly and then decreased mildly with the increase of EYP concentration and the inhibition efficiency decreased mildly as the experimental temperature increased. Electrochemistry results showed that EYP was a mixed-type inhibitor retarding mild steel corrosion without changing the mechanism of anodic or cathodic reaction. The calculated kinetic parameters revealed that EYP was absorbed onto mild steel by both chemisorption and physisorption.

    OPTIMIZING PRODUCT DISTRIBUTION OF MIP PROCESS USING BP NEURAL NETWORK
    2016, 47(5):  95-100. 
    Asbtract ( 665 )   PDF  
    Related Articles | Metrics

    Fluid catalytic cracking (FCC) is a highly non-linear and strong coupled operation system and is too hard to be described by traditional mechanism model. The artificial neural network provides a promising way to solve the problem because of its strong nonlinear prediction and self-learning ability. In a practical application of this method for a 1Mt/a MIP unit, a 19-24-4 type of BP neural network to predict the yields of liquid petroleum gas (LPG), gasoline, diesel and coke was established using nineteen input variables including properties of feedstock, regenerated catalyst and operating variables and so on. Based on the BP neural network, the influences of the feedstock preheating temperature, outlet temperatures of two reaction zones and reaction pressure on product distribution were investigated and the operating variables are optimized using genetic algorithm(GA) with a view to maximize gasoline yield. The industrial data agree well with the predicted results and a significant improvement in the gasoline yield was gained under the optimized conditions.

    RESEARCH ON FAST EVALUATION FOR DIESEL CETANE NUMBER BY NEAR-INFRARED SPECTROSCOPY
    2016, 47(5):  101-107. 
    Asbtract ( 754 )   PDF  
    Related Articles | Metrics

    More than one thousand diesel samples were collected to establish near infrared spectroscopic database for determination of Cetane Number. On the research, disposable headspace bottle was used to satisfy the spectral fast acquisition. By adding a small amount of samples to the database could get suitability model in Maoming petrochemical. Robust and uniform calibration models were developed based on different types of diesel by partial least squares method,SVM and LSSVM algorithm. The standard error of prediction on diesel oil samples using PLS, SVM and LSSVM calibration model were 1.6, 1.4 and 1.3, respectively. The work is provided with advantages such as high-speed, saving modeling cost and low workload.

    DETERMINATION OF SULFUR COMPOUNDS IN LOW SULFUR GASOLINE
    2016, 47(5):  108-112. 
    Asbtract ( 625 )   PDF  
    References | Related Articles | Metrics
    The method was established for separation and determination of sulfur compounds in low-sulfurgasoline by gas chromatography-sulfur chemiluminescene detector (GC-SCD). The chromatographic condition for the determination of low-sulfur gasoline was optimized and the sensitivity was increased. The detection limit and reproducibility were investigated. The qualitative and quantitative assays for sulfur compounds in low-sulfur gasoline from selective hydrodesulfurization (RSDS) process and S Zorb gasoline adsorption desulfurization process were conducted by GC-SCD to demonstrate the feasibility. The methods can be applied to all kinds of catalytic gasoline fractions.