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Table of Content

    12 August 2024, Volume 55 Issue 8
    RESEARCH AND CONCEPTUAL DESIGN OF FLUID CATALYTIC CRACKING REACTION SYSTEM AT ULTRA-HIGH REACTION TEMPERATURE
    2024, 55(8):  1-6. 
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    The fluid catalytic cracking process has been developed from gasoline production scheme to light olefin production scheme, and the reaction temperature has increased significantly, which has led to more serious thermal cracking reaction, and the methane and ethane yield increases significantly. Therefore, the reaction taking place in the reactor with outlet temperature higher than 530 ℃ is defined as the ultra-high temperature fluid catalytic cracking reaction system, and how to inhibit thermal cracking reaction in this system is studied, and the technical idea of inhibiting the thermal cracking reaction is proposed. The conceptual design of the ultra-high temperature fluid catalytic cracking reaction system can provide a design basis for the development of the fluid catalytic cracking reaction system at ultra-high reaction temperature to reduce the yield of methane and ethane.
    RESEARCH AND DEVELOPMENT OF RIGHT TECHNOLOGY FOR HIGH-VALUE UTILIZATION OF HEAVY OIL UNDER CARBON PEAKING AND CARBON NEUTRALITY GOALS
    2024, 55(8):  7-17. 
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    The key to the low-carbon transformation development of oil refining is the efficient and high-value utilization of heavy component (vacuum residue) with high carbon contents. The conventional coking feedstock with poor quality was divided into deoiled asphalt (DOA) and deasphalted oil (DAO) by solvent deasphalting technology, and then based on the "like dissolves like" rule, two types of low-value DOA and catalytic cracking light cycle oil (LCO) were mixed for hydrogenation (component refining), while DAO was used for hydrogenation alone, and the RIGHT (RIPP InteGrated Hydrotreating Technology) technology of SINOPEC Petrochemical Research Institute Co., Ltd. was formed. Hydrogenated DOA can be coked to produce petroleum coke with low metal (V mass fraction<150 μg/g, Ni mass fraction<150 μg/g) or low metal and low sulfur (sulfur mass fraction<3.0%), which can provide high-quality precursors for high-end carbon materials. Compared with conventional coking technology, RIGHT technology can reduce the yield of low-grade petroleum coke with high metal and high sulfur content by about 70%. The hydrogenated LCO can meet the LTAG feed requirements, thus producing light aromatics(BTX) and gasoline components with high octane number. DAO was hydrogenated at LHSV (liquid hourly space velocity) twice as high as that of conventional residual oil. After hydrogenation, hydrogen mass fraction in DAO was 12.25%-12.32%, micro-carbon residue was less than 2.0%, and the mass fraction of metal (Ni+V) was less than 0.1 μg/g. Hydrotreated DAO can be applied as a high-quality FCC/DCC feedstock, it can produce more components of light olefins and gasoline components with high octane number and greatly reduce catalyst consumption. Based on the characteristics of high metal content in DOA and LCO blended oil, a series of resource recycling catalysts RRC with high demetallization and metal capacity were developed. After operation, a large amount of metal V and Ni were deposited on the catalyst, which is a valuable resource for obtaining high-value V and Ni, especially V metal. The turnaround cycle of the DAO hydrotreating unit can be increased to 4 years, which can solve the problem of the short operation cycle of residue hydrotreating unit. At the same time, the rear catalyst can be regenerated, which can improve the utilization rate of catalyst resources. RIGHT technology can produce high-value, low-sulfur and low-metal petroleum coke and chemical materials from vacuum residue through component refining technology, thus realizing the low-carbon and high-value utilization of high-carbon components in the refining field.
    DEVELOPMENT AND APPLICATION OF CONTINUOUS LIQUID PHASE DIESEL HYDROTREATING TECHNOLOGY BY DUAL REACTOR ZONE
    Zhang Rui Ding Shi Xi Yuanbing Kai Xu Wen-Bin CHEN
    2024, 55(8):  18-25. 
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    Through analysis, it was found that the main factor affecting the ultra-deep desulfurization of liquid phase diesel hydrogenation technology was the hydrogen sulfide,a by-product dissolved in the oil. The dissolution law and distribution of hydrogen sulfide in diesel oil were simulated by real oil products, it was found that adding a small amount of hydrogen was effective for ultra-deep desulfurization in liquid phase technology. A continuous liquid phase diesel hydrotreating technology by dual reactor zone (SLHTDr) was developed. The results of the medium scale test showed that the inhibition of hydrogen sulfide on the deep desulfurization could be overcome by adding hydrogen in the second reaction zone according to the volume ratio of hydrogen and oil of 30-50. The diesel oil with sulfur mass fraction less than 10 μg/g could be obtained under mild process conditions (a reaction temperature of 305℃, a volume space velocity of 6.0h-1). The industrial application results of SLHTDr showed that the energy consumption of the unit was 11.9% lower than that of the same kind technologies,thelow energy consumption production was realized,and the carbon emissions of the production process was reduced. It provides technical support for further upgrading of diesel quality and reducing carbon emissions in the future.
    STUDY ON CATALYTIC CRACKING PROCESS OF HYDROGENATED STRAIGHT-RUN DIESEL
    2024, 55(8):  26-31. 
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    The effects of reaction severity and catalyst type on catalytic cracking of hydrogenated straight-run diesel were investigated in a small fixed fluidized bed unit. Two processing schemes were designed to produce more liquefied petroleum gas (LPG) and gasoline from catalytic cracking of hydrogenated straight-run diesel. The experimental results showed that conversion rates exceeded 75% on the different catalysts rich in Y-type zeolite and ZSM-5 zeolite under different reaction conditions, such as reaction temperature of 520-600 ℃ and catalyst/oil mass ratio of 6.0-10.0. With the increase of conversion rate, the yield of LPG increased, the yield of gasoline decreased and the research octane number (RON) increased. To produce more LPG, it’s suitable for using ZSM-5 zeolite catalyst at the temperature of 600 ℃ and catalyst/oil mass ratio of 9.96, the yields of LPG and propylene were 36.48% and 16.33%, respectively. Besides, the total yield of ethylene, propylene and butylene was 34.49%. To produce more gasoline, it’s suitable for using Y-type zeolite catalyst at the temperature of 520 ℃ and catalyst/oil mass ratio of 6.05, the yield of gasoline was 60.22% and the RON was 94.1. Under the crude oil price system of 80 $/bbl(1bbl=159L), the per ton oil profits of the two processing schemes were 329.5 Yuan and 296.9 Yuan, respectively.
    STUDY ON PREPARATION OF SBS MODIFIED ASPHALT FROM CHUNFENG AND TAHE VACUUM RESIDUE
    2024, 55(8):  32-37. 
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    In order to solve the problem of poor compatibility difficulty in modification of Chunfeng vacuum residue with SBS,the composition of Chunfeng vacuum residueand Tahe vacuum residue was complementary,and the method of compounding first and modifying later was adopted. The compatibility between Chunfeng vacuum residue and SBS was improved, and the modification difficulty of Chunfeng vacuum residue was reduced. The compatibility difference between the two kinds of residue was analyzed in detail fromthe aspects of element composition, structural parameters and group composition. Finally, using Chunfeng and preferred Tahe vacuum residue as raw materials, the process conditions were optimized by uniform design test method. SBS modified asphalt with storage stability and performance meeting theI-B and I-Cspecifications of “Technical Requirements of Polymer Modified Asphalt” was preparedby selecting appropriate process conditions.
    INDUSTRIAL PRACTICE OF ALKYLATION UNIT FOR ADDING C5 FRACTION FROM GAS-FRACTIONATED UNIT
    2024, 55(8):  38-44. 
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    In order to widen the range of SINOALKY sulfuric acid alkylation unit feedstock, improve the yield of alkylated oil and solve the problem of high vapor pressure of gasoline in summer, a petrochemical company has carried out the industrial practice of adding a small amount of gas-fractionated C5 fraction into the alkylation unit. In August 2021, it was found that the pressure difference in the reaction feed pipeline of the alkylation unit was abnormally increased by 0.6 MPa. The site pressure measurement showed that the blockage was in the reaction feed pipeline of the alkylation unit and the related equipment. Through the detection and analysis of various analysis methods, it was determined that the main reason for the increase of pressure difference in the feed pipelines and equipment of the alkylation reactor was that there were trace impurities of N-methyldiethanolamine in the C5 fraction. Those trace impurities reacted with the sulfur dioxide in the circulating isobutane to form a brownish-yellow amine sulfite salt, resulting in the clogging of the feed pipeline and equipment. Through the innovation of process facilities, the addition of gas-fractionated C5 water washing and agglomeration dewatering process, the production practice has proved that this gas-fractionated C5 processing method had a good effect on removing impurities. The mass concentration of nitrogen in the washing water and the total outlet of the neutralization tank was controlled at 126.2 mg/L and 47.5 mg/L, respectively. The pH of water samples from the total discharge of the neutralization tanks was stable at 6-7. At the same time, the quality of the alkylated oil product was also up to the standard, and the continuous blending of gas-fractionated C5 has been successfully realized. It provides a strong theoretical support for the research and application of this method.
    REACTION TYPES OF FIXED-BED RESIDUE HYDROTREATING AND INFLUENCE OF RESIDUE CHARACTERISTICS ON TEMPERATURE RISE OF REACTOR
    Shao Zhicai Deng Zhonghuo Liu Tao Dai Lishun
    2024, 55(8):  45-51. 
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    The pilot-scale experiment of residue hydrogenation was carried out on a fixed-bed reactor with four reactors in series, and the reactions on different type catalysts were analyzed. The results showed that on the hydrodemetallization catalyst, the main reaction was hydrodesulfurization and hydrodemetallization. The removal amount of sulfur and (Ni+V) was for 67.12% and 83.67% of the total amount of removal, respectively. On the catalysts for hydrodesulfurization and carbon reduction, hydrodenitrogenation, hydrodesulphurization and aromatics hydrogenation saturation were the main reactions; the removal amounts of nitrogen and sulfur accounted for 78.57% and 32.88% of the total amount removed, respectively; the increase of hydrogen mass fraction accounted for 66.96% of the total increase. The increasing range of reactor temperature rise of fixed bed residue hydrogenation industrial unit during processing different characteristic feedstock was investigated. The results showed that compared with processing low sulfur and high nitrogen residue, the reduction of sulfur content and density of hydrogenation products of high sulfur and low nitrogen residue was greater, more hydrodesulfurization and aromatics hydrogenation saturation reactions occurred on the catalysts, and the temperature rise of hydrodemetallization reactor and the total temperature rise of all stages of the reactor were higher.
    DEVELOPMENT AND APPLICATION OF ADSORBENT FOR DESULFURIZATION AND DEALCOHOLIZATION IN PROPANE DEHYDROGENATION UNIT
    2024, 55(8):  52-57. 
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    A renewable adsorbent for the removal of sulfides and oxygen-containing compounds from propane feedstock in propane dehydrogenation(PDH)unit was studied. The influence of regeneration times on the adsorption performance and mechanical strength of the adsorbent was investigated by a fixed-bed simulation experiment. The results showed that the retention rates of desulfurization, dealcoholization and mechanical strength were 89.4%, 88.5% and 83.2%,respectively,after 150 times regeneration. Under actual operating conditions in industrial unit, the effect of propane desulfurization and dealcoholization was significant. After nearly six years of continuous operation, when the inlet impurity content was far above the average level, the mass fraction of methanol and sulfur in the raw propane could be reduced to less than 1.0 μg/g, which could meet the technical requirements of the PDH unit. The successful application of adsorbent for desulfurization and dealcoholization in PDH unit has solved the problem that propane raw materials in China could not match the technical requirements of imported process package, and provided a feasible path for the diversification of raw materials for PDH units in China.
    PROBLEM ANALYSIS DURING THE OPERATION OF 4.0 Mt/a HYDROCRACKING UNIT
    2024, 55(8):  58-64. 
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    Taking a 4 Mt/a diesel and gas oil hydrocracking unit as an example, through analyzing the hot and difficult problems such as the pressure drop of the wound tube heat exchanger and vibration of the feed pipeline, the corresponding solving methods and measures were put forward. At the same time, the energy-saving optimization of large-scale hydrocracking unit was carried out. The results indicated that in order to realize the accurate control of the wound tube heat exchanger temperature, the "X" type control mode should be adopted in the design stage of the new unit. After the unit was scaled up, optimization scheme should be adopted to meet the requirements of the pipeline based on the operating characteristics and site layout issues of the unit. For the process flow with naphtha stabilization column and naphtha fractionation column, it was important to consider the medium characteristics to reduce the impact of pipeline liquid hammer and pipeline vibration. In addition, the optimized operation mode of the new hydrogen compressor and ordinary centrifugal pump could provide a certain reference for the smooth operation of large-scale hydrocracking unit.
    PREPARATION OF ZIRCONIUM-DOPED ALUMINA AND ITS CATALYTIC REFORMING PERFORMANCE
    2024, 55(8):  65-73. 
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    High-purity alumina doped with zirconium was prepared by the hydrolysis method of aluminum alkoxide, and the effects of zirconium doping amount on its physical and chemical properties, such as specific surface area and pore structure, were investigated. Using the zirconium-doped alumina as raw material, a zirconium-doped alumina carrier was prepared by extrusion, further loaded with Pt to prepare reforming catalyst. Naphtha was used as raw material, the effects of zirconium content variation on the catalyst’s reactivity were investigated, and the influencing mechanism was also discussed. The results showed that the introduction of Zr could change the L acid strength of the γ-Al2O3 carrier, thus changing the ratio of the metal center to acid center on the catalyst. When the mass fraction of Zr was 0.20%-0.33%, the acid center and metal center of the catalyst exhibited good synergy, displaying higher catalytic activity and aromatic selectivity for naphtha reforming.
    Pd-LOADED CATALYST FOR CATALYTIC DECARBONYLATION OF DIMETHYL OXALATE TO PRODUCE DIMETHYL CARBONATE
    2024, 55(8):  74-83. 
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    In order to develop a high efficient and low cost synthetic process for dimethyl carbonate (DMC), supported Pd catalysts were prepared by impregnation method on Naβ(25), NaZSM-5(25), NaY(6), NaY(8),NaY(10) zeolites, and it was first used in the decarbonylation reaction of dimethyl oxalate (DMO). The composition, valence, pore structure, morphology and crystal of the catalysts were characterized by X-ray diffraction, X-ray photoelectron spectroscopy, transmission electron microscopy and Fourier transform infrared spectroscopy. The results showed that DMC was synthesized by the decarbonylation of DMO over Pd/NaY (6) catalyst. Under the optimum conditions such as a reaction temperature of 220 ℃,a reaction time of 90 min,a catalyst dosage of 1.0 g, a mass ratio of 1,4-dioxane to DMO of 4:1, and Pd loading 0.2%, the conversion of DMO and the selectivity of DMC were 82.59% and 62.33%, respectively. After five cycles of regeneration, the catalyst showed good catalytic activity for DMO decarboxylation. Finally, the reaction mechanism of DMC synthesis by DMO decarbonylation over Pd/NaY (6) catalyst was reasonably deduced.
    STUDY ON CHARACTERISTICS OF SILICA GEL MODIFIED BY SILANE REAGENT AND ITS ADSORPTION PERFORMANCE OF DIESEL
    2024, 55(8):  84-91. 
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    Six kinds of silane reagents were selected for grafting modification of B-type silicone, the physical and chemical characteristics of adsorption materials were investigated by means of nitrogen adsorption-desorption test, solid-state infrared spectroscopy analysis, thermogravimetric and mass spectrometry analysis, elemental analysis, and toluene adsorption test, and the adsorption performance of diesel was studied bystatic adsorption equilibrium test. The results showed that amino group, sulfhydryl group and epoxy group could be successfully grafted onto silica gel;the specific surface area, total pore volume, most probable pore size, and average pore size of the modified silica gel all decreased;the adsorption amount of toluene was positively correlated with the specific surface area of modified silica gel. According to the different content of nitrogen in modified silicone, the degree of modification reaction was related to the selection of silane reagent.The static test results showed that among the six silane reagents, the amino and epoxy group modified silica gel could improve the selectivity of the adsorbent for bicyclic aromatic hydrocarbons, and could significantly improve the selectivity of the adsorbent for sulfur compounds in diesel fraction. Sulfhydryl modified silica gel could reduce the selectivity of the adsorbent forsulfur compounds, while amino, thiol and epoxy modified silica gel all reduced the selectivity of the adsorbent for monocyclic aromatic hydrocarbons.
    SYNTHESIS OF NOVEL ANIONIC-NONIONIC SURFACTANTS AND THEIR INTERACTION WITH HIGHLY INTERFACIAL ACTIVE SURFACTANT18-AC
    2024, 55(8):  92-98. 
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    anionic-nonionic surfactants with alkyl chains of different number of carbon atoms were synthesized, and the interaction between sodium nonylphenol polyoxyethylene ether sulfate (9-EOS), sodium dodecylphenol polyoxyethylene ether sulfate (12-EOS) and high performance surfactant (18-AC) was studied by surface tension technique. The results showed that there was an antagonistic effect between 9-EOS and 18-AC, while there was a synergistic effect between 12-EOS and 18-AC. In addition, the effects of the compound system on the wettability and oil-water interface properties of the mixtures were systematically studied. The compound system effectively reduced the contact angle on the crude oil surface. When the 12-EOS molar fraction is 0-0.6, the 12-EOS/18-AC system has a synergistic effect on the wettability, the contact angle is lower than that of individual surfactants, and the oil-water interface performance is improved.
    MOLECULAR SIMULATION ON STRUCTURE AND PERFORMANCE RELATIONSHIPS OF PHOSPHATE ESTER EXTREME PRESSURE ANTIWEAR AGENT
    2024, 55(8):  99-106. 
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    To investigate the relationship between molecular structure parameters of phosphate ester extreme pressure antiwear agents and their extreme pressure antiwear performance at the molecular level, triethyl phosphate was selected as model compound, and the interaction mechanism between phosphate ester molecules and the Fe(110) surface was studied by molecular simulation method. It was revealed that phosphate ester molecules mainly adsorbed onto the Fe surface by providing electrons through O atom in the P=O group. Then the molecular simulation method was used to calculate various structural parameters of different phosphate ester extreme pressure antiwear agents. A genetic function approximation was used to establish the relationship equation between the molecular structure parameters of phosphate ester extreme pressure antiwear agents and extreme pressure antiwear performance. The results of the internal and external tests show that the equation has good predictive effect. According to the equation, the key structural parameters that affect the extreme pressure antiwear performance of phosphate ester molecules include the charge of the O or S atom in the P=O or P=S group, the chemical bond energy of the C—O or C—S bond, and the content of S atom.
    EXPERIMENTAL STUDY ON FLOW CHARACTERISTICS OF CATALYST PARTICLES IN INCLINED PIPE WITH NEGATIVE PRESSURE GRADIENT
    2024, 55(8):  107-112. 
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    On the Φ150mm×3600mm negative pressure gradient tube-valve experimental device,the characteristicparameters of the axial dynamic pressure in the inclined tube with different catalyst particle mass flow rates (Gs) were measured and analyzed,and the flow characteristics of catalyst particles in inclined tube of FCC unit were studied. The results showed that the pressure storage capacity of the inclined pipe increased with the increase of particle mass flow rate Gs and the lean phase stratified flow and dense phase stratified flow appeared successively in the pipe.The pressure distribution, dominant frequency, amplitude and pressure variance in the inclined tube correspond to the flow pattern, which could be used for quantitative identification of the flow pattern. When Gs=65.96 kg/(m2.s), there were multiple flow patterns in the inclined pipe, including transition packed-bed flow, packed-bed flow and dense phase flow. The aeration gas was injected into the middle of the inclined pipe to effectively improve the particle conveying capacity and the pressure storage capacity of the inclined pipe.
    INVESTIGATION ON SYNTHESIS OF LANTHANUM DIALKYLDITHIOPHOSPHATE AND ITS PERFORMANCE IN LUBRICATING GREASES
    2024, 55(8):  113-119. 
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    Lanthanum dialkyldithiophosphate (LaDDP) was synthesized by using n-octanol, phosphorus pentasulfide and lanthanum nitrate as the primary raw materials. The structure of LaDDP was characterized by infrared spectroscopy(IR) and nuclear magnetic resonance spectroscopy (NMR). LaDDP was addedinto the base greaseprepared with 500N base oil and lithium stearate as thickener, and the performances of grease such as dropping point, penetration, oil separation (steel mesh method), extreme pressure, anti-wear properties and oxidation stability were tested. Moreover, the performance of LaDDP was compared with that of zinc dialkyldithiophosphate (ZDDP) when added to the same base grease.The results indicated that LaDDP significantly improved the oxidation stability of the base grease, and it is superior to ZDDP in terms of extreme pressure and colloid stability. These results demonstrated the potential of LaDDP as an effective additive for enhancing the performance of lubricating grease.The bond energy of the active site in the model compound LaDDP was calculated by molecular simulation, and the mechanism of extreme pressure and anti-wear properties of LaDDP in the friction process was speculated.
    STUDY ON PERFORMANCE OF A NOVEL 5 mm2/s GRADE PENTAERYTHRITOL ESTER LUBRICANT BASE OIL FOR AERO-ENGINE
    2024, 55(8):  120-128. 
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    MIL-PRF-23699G Enhanced Ester (EE) lubricating oil has become the highest standard to measure the extreme load-carrying properties, and high-temperature oxidation stability. The oxidation stability of dipentaerythritol ester was weaker than that of pentaerythritol ester at high temperature, and long-chain fatty acid could not simultaneously improve the oxidation stability and the extreme load-carrying properties of pentaerythritol ester. A novel structure of 5 mm2/s grade pentaerythritol ester base oil was synthesized by direct esterification of pentaerythritol, adipic acid and C5-C9 monounsaturated fatty acids. Compared with current mixed esters of pentaerythritol esters and dipentaerythritol esters, the new pentaerythritol ester base oil had better viscosity-temperature performance, low temperature fluidity and rubber compatibility, and its oxidation induction period and Falex failure load were improved by more than 20%. The existing problems of using dipentaerythritol ester and long chain fatty acid in the existing synthesis technology of 5 mm2/s grade polyol ester base oil were solved. It is expected to provide a reference for the research and development of the next generation of EE-enhanced ester-based aero-engine lubricant oil products.
    INFLUENCE MECHANISM OF TCP AND T706 ON CORROSION WEAR PERFORMANCE OF AERO-TURBINE ENGINE LUBRICATING OIL
    2024, 55(8):  129-135. 
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    Aiming at the problem of corrosion wear caused by aviation turbine engine lubricating oil on the friction surface of the transmission system of the turbine engine, based on the evaluation method of corrosion wear of aviation turbine engine lubricating oil, the influence of impurities such as chlorine and sulfur content in the additives of trimethylphenol phosphate (TCP) and benzotriazole (T706) in aviation turbine engine lubricating oil on the corrosion wear of the friction pair was studied by using a four ball tester, and the mechanism of its impact on corrosion was revealed. The results showed that impurities such as chlorine in both TCP and T706 could cause corrosion wearof metal, the influence of chlorine in T706 on corrosion wear was greater than that of chlorinein TCP.The corrosion caused by chlorine in T706 is mainly electrochemical corrosion,but not chemical corrosion. However, the influence of sulfur in T706 on surface corrosion of metal is more complicated,when the sulfur content is low, shallow corrosion is prone to occur; when the sulfur content is high, deep corrosion occurs, forming dense corrosion pits.Organic acidis not the main factor causing metal corrosion, so the introduction of acid scavengers does not significantly improve metal corrosion.Urea as a corrosion inhibitorcan greatly improve the metal corrosion caused by chlorine in T706.
    RESEARCH AND ANALYSIS ON DIRECT PREPARATION PROCESS OF POLYUREA LUBRICATING GREASE
    2024, 55(8):  136-144. 
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    The effects of direct preparation conditions (feeding sequence, refining temperature, and refining time) on the properties of polyurea grease were investigated, and the influence of feeding method on the chemical composition and average molecular structure of polyurea thickeners and its relationship with the properties of polyurea grease were analyzed. The prepared polyurea lubricating grease by direct method was characterized by infrared spectroscopy, thermogravimetric analysis and scanning electron microscopy, the structure-activity relationship of the grease was thoroughly explored, and the products were compared with those obtained by the prefabricated method. The basic optimized experimental scheme was to dissolve organic diamine in the base oil, raise the temperature to 80-90 ℃, add isocyanate and organic monoamine at the same time, react for 60 min, then react for 1.5 h at temperature of 170-180 ℃. The results of structural and performance characterization indicated that the number and proportion of urea group in polyurea thickener prepared by the direct and prefabrication methods were different under the same types and ratios of base oil and thickener, as well as the same preparation conditions. There were differences in the number and proportion of urea groups in the polyurea thickeners obtained by the direct method and prefabricated method, which led to differences in the performance of polyurea lubricating grease products. When the mass fraction of thickening agent was 20%, the dropping point tetrapolyurea grease prepared by the prefabrication method was 20 ℃ higher than that by the direct method, the oil content of a steel mesh was only 21.8% of that by the direct method, the leaching loss was only 41.3% of that of direct method, the corrosion rate of copper strip was one grade higher than that of the direct method, and the last non-seizure load for the prefabricated method was 24.5% higher than that of the direct method. In a word, the colloidal stability, oxidation stability, and extreme pressure plus anti-wear performance of polyurea lubricating grease prepared by the direct method were slightly inferior to those of the prefabricated method, but its mechanical stability was superior to that by the prefabricated method.
    EFFECT OF TREATING MALODOROUS GASES BY NON-THERMAL PLASMA COUPLING CATALYST
    2024, 55(8):  145-150. 
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    To improve the limitation of non-thermal plasma (NTP) technology andbroaden its application in the treatment of odorous gas, Cu doped catalyst was combined with NTP technology. The H2S degradation efficiency, influence of coupling methods, internal structure and external structure were researched comprehensively. In addition, the role of catalyst and synergetic mechanism were approached. The results showed that the contact points between the catalyst particles and the reactor wall enhanced the discharge process,while the output of high-energy electrons was lower in external structure system.Compared with the single NTP system, the built-in coupling system could cut off the H2S and make itcontact with the active substance sufficiently, which improved the discharge efficiency, and the output efficiency could reach 64.79% at 35 V.
    ADVANCED TREATMENT OF CONCENTRATED WASTEWATER FROM REVERSE OSMOSIS IN REFINERY AND PETROCHEMICAL ENTERPRISES BASED ON BIOLOGICAL FILTER
    2024, 55(8):  151-156. 
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    A side-linebiologicaldenitrification filter combined carbon-based biological aerated filter (CBAF) was used to investigate the removal efficiency of organic matter and total nitrogen in reverse osmosis (RO) concentrated wastewater produced in the process of refinery wastewater reuse,and the change of organic matter in the treatment process was analyzed. The results showed that the combined process could effectively remove the total nitrogen in the RO concentrated water (the average removal rate 51.25%) and reduce chemical oxygen demand (COD) by 59.44%. The main pollutants in the ROconcentrated wastewater are humic acids and dissolved microbial metabolites, and the fluorescence intensity of the main pollutants in the wastewater was significantly decreasedafter the treatment with CBAF. The concentrations of hydrophilic organic carbons such as low molecular weight acids substances, building block,low molecular weight neutralsubstances, humic and biopolymer were reduced by 81.65%, 68.58%, 63.85%, 60.83% and 49.3%, respectively. At the same time, due to the adsorption of the carrier, the CBAF reactor has a high removal rate of both hydrophilic and hydrophobic organic carbon (64.2% and 74.58%, respectively).
    DELTA-BASE DATA GENERATION METHOD FOR CATALYTIC REFORMING UNDER SIGNIFICANT CHANGES IN FEED PROPERTIES
    2024, 55(8):  157-163. 
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    In view of the large variation of catalytic reforming feed properties, a new method of Delta-Base data generation by variable step size calculation and molecular level mechanism model was proposed. The method calculates the change rate of the absolute value of product mass fraction with the change of the absolute value of feed property when the feed property is disturbed, and divides the range of the rate of change into several equal parts. According to the different range of the change rate value obtained from each calculation, the variable disturbance step was selected for the next step of calculation, and then the midpoint value of each variable disturbance in the calculation process was taken to verify the product quality score, thus, the accuracy of the calculation results was ensured while the calculation efficiency was improved. The results showed that the relative error of each product quality fraction calculated by this method was less than 2.5%, the fitting equations of different product quality fractions could be obtained by fitting the calculated data, and the three-stage Delta-Base data of aromatic potential content variation could be generated by fitting the equations. Compared with the product prediction results, when the aromatic potential content of the feed was 42%, it was found that the average deviation between the predicted value of the Delta-Base data and the calculated value of the fitting equation was 0.16%, which showed that the method had excellent accuracy, and the Delta-Base data generated by the molecular level mechanism model can better reflect the real molecular reaction process.
    SIMPLE MODELING OF REFINING PROCESSAND ON-LINE SIMULATION OF ATMOSPHERIC AND VACUUM DISTILLATION PROCESS BASED ON CAPE-OPEN STANDARD
    2024, 55(8):  164-177. 
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    Simple refining process model is widely used in operation monitoring, on-line calculation, real-time optimization and other fields. However, most of the models only correlate the input and output variables, so they can not calculate the composition of each group of diverting quantities and can not be integrated into the simulation software to simulate the whole process. In this study,the separation process was simplified,and a simple refinery column model based on CAPE-OPEN standardwas developed. Firstly, the refining process was simplified as a continuous separation unit, and the model parameters could be corrected according to the actual product datato simulate a real process. Secondly, the model parameters were combined with the actual operating variable data, and radial basis interpolation was used to establish the influence of operating variables on the model parameters, so as to realize the simulation of various operating conditions. Finally, three working conditions of commercial atmospheric and vacuum distillation unit were verified. The results showed that compared with Aspen's calculation results, the deviation of the preflash column was mostly within 2%, and the average deviation of the side lines of the atmospheric and vacuum column was less than 3%;compared with the actual results, the average error is less than 5%, in line with the allowable engineering error range. The calculation speed of the model is fast, andthe calculation of each columnis completed in about 0.2 s, which is suitable for on-line production and scheduling.
    RESEARCH PROGRESS AND DEVELOPMENT PROSPECT OF NATURAL ESTER INSULATING OIL
    2024, 55(8):  178-186. 
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    With the increasing demand for energy and the increasing emphasis on environmental protection, natural ester insulating oil has gradually become a green substitute for mineral oil due to its outstanding fire safety performance, excellent natural degradation ability and good insulation properties. The development status of natural ester insulating oil at domestic and abroad was reviewed, and the current quality standards of natural ester transformer oil were compared and analyzed. The disadvantages of natural ester insulating oil in heat dissipation performance, low-temperature performance, oxidation stability and electrical performance were summarized.The latest research trends and improvement methods were summarized. In addition, typical products of natural ester insulating oil in the market were summarized and its future development was prospected, which provided guidance for power equipment oil.