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1.
The low-temperature catalytic oxidation of
heavy crude oil (Xinjiang Oilfield, China) was studied
using three types of catalysts including oil-soluble, watersoluble,
and dispersed catalysts. According to primary
screening, oil-soluble catalysts, copper naphthenate and
manganese naphthenate, are more attractive, and were
selected to further investigate their catalytic performance in
in situ upgrading of heavy oil. The heavy oil compositions
and molecular structures were characterized by column
chromatography, elemental analysis, and Fourier transform
infrared spectrometry before and after reaction. An
Arrhenius kinetics model was introduced to calculate the
rheological activation energy of heavy oil from the viscosity–
temperature characteristics. Results show that the
two oil-soluble catalysts can crack part of heavy components
into light components, decrease the heteroatom
content, and achieve the transition of reaction mode from
oxygen addition to bond scission. The calculated rheological
activation energy of heavy oil from the fitted Arrhenius
model is consistent with physical properties of heavy oil
(oil viscosity and contents of heavy fractions). It is found
that the temperature, oil composition, and internal molecular
structures are the main factors affecting its flow
ability. Oil-soluble catalyst-assisted air injection or air
huff-n-puff injection is a promising in situ catalytic
upgrading method for improving heavy oil recovery. 相似文献
2.
MasahiroYOSHIDA NobuyukiOTA 《石油学报(石油加工)》2001,17(1):101-106
The direct upgrading process from heavy crude oil to sweet and light oil (IKC process) has been developed for about 10 years in Idemitsu Kosan. Compared with conventional refinery scheme consisting of YR-HDS, VGOHYC and so on, the new refinery scheme combined with IKC process and Topper was always economically feasible with lower cost and smaller energy consumption. In the existing refinery of no middle distillate HDS and residue HDS of HYC plants to supplement IKC process is expected to be one of the efficient methods to cope with the environmental regulations. 相似文献
3.
In heavy oil production,the loss of energy to ambient surroundings decreases the temperature of the heavy oil flowing upwards in a vertical wellbore,which increases the oil viscosity and the oil may not flow normally in the wellbore.Therefore,it is necessary to lower the heavy oil viscosity by heating methods to allow it to be lifted easily.Heating of heavy oil in an oil well is achieved by circulating hot water in annuli in the well(tubing-casing annulus,casing-casing annulus).In this paper,based on heat transfer principles and fluid flow theory,a model is developed for produced fluids and hot water flowing in a vertical wellbore.The temperature and pressure of produced fluids and hot water in the wellbore are calculated and the effect of hot water on heavy oil temperature is analyzed.Calculated results show that the hot water circulating in the annuli may effectively heat the heavy oil in the tubing,so as to significantly reduce both oil viscosity and resistance to oil flow. 相似文献
4.
Research on Optimized Utilization of Naphtha Resources Based on Adsorptive Separation with Zeolite 总被引:7,自引:0,他引:7
ShenBenxian LiuJichang WangZhenxian 《中国炼油与石油化工》2005,(1):49-55
By means of molecular scale management, the technology of separating normal paraffins from naphtha through adsorption using 5A molecular sieves was studied with the purpose of optimizing the utilization of naphtha. The raw materials used in steam cracking and catalytic reforming processes could be allocated properly. During the adsorption process, the separation efficiency of the normal paraffins was above 99.9% with the purity of normal paraffins in the desorption oil exceeding 98.2%. With the use of the desorption oil as the feedstock of steam cracking, the ethylene yield increased from 29.7%--35.0% to 41.4%-49.2% compared to that of the naphtha in the existing plant under similar operation conditions. The potential aromatic content of the raffinate oil rose from 30.6% to 43.5% compared to that in naphtha. The research octane number of the raffinate oil reached more than 85 with an increase of 20 units compared to that of naphtha, so the raffinate oil is more suitable for use as a blending component for high-octane clean gasoline. 相似文献
5.
《中国油气》2003,(2)
With China's entry into World Trade Organization,PetroChina is facing the unprecedented severe challenge fromits domestic counterparts in the chemicals sector, wherePetroChina is relatively weak in the production scale andfacilities. One of the key issues for PetroChina to solveurgently to reinforce its profit-makng capability rapidly isto boost the competitiveness of its ethylene facilities.Currently, PetroChina has seven sets of ethylene units witha total annual production capacity of 1.65 million tons. Theunits are usually small in the scale except for those at JilinPetrochemical Company and Daqing PetrochemicalCompany.Taking advantage of oil refining integration The enterprises with the ethylene units are usually ownedwith a certain scale of oil refining capacity. PetroChina hasa great potential to tap in the efforts to make use of the oilrefining and chemical integration for optimization of rawmaterials and reciprocation of their respective advantages.PetroChina should make comprehensive use of dry 相似文献
6.
Traditional fluid production profile logging is not usually suitable for heavy-viscous crude oil wells.Biodegradation of heavy oil can lead to the loss of n-alkanes,and the use of chromatogram fingerprint techniques in studying the production contributions of single layers in heavy oil commingled wells has limitations.However,aromatic compounds are relatively well preserved.We took the heavy oil commingled wells of small layers NG55 and NG61 in the ninth area of the Gudong oil field as examples.Based on the principle of chromatography,the whole-oil GC-MS was used,and the aromatic parameters which have a strongly linear relationship with the ratio of mixed two end member oils were verified and selected in laboratory.Studies showed that the ratio of (1,4,6-+ 2,3,6-trimethylnaphthalene) to 1,2,5-trimethylnaphthalene has a strongly linear relationship with the ratio of the mixed two end member oils (R2=0.992).The oil contributions from single layers NG55 and NG61 in six commingled heavy oil wells were calculated using established charts and this relationship.The calculated results are consistent with the results of long period dynamic monitoring and logging interpretation in the study area and can provide a scientific basis for monitoring production performance and hierarchical management of reservoirs.The study provides a new geochemical method for calculation of the contributions of single layers in heavy oil commingled wells when conventional fluid production profile logging is not suitable. 相似文献
7.
Wu Feiyue Weng Huixin Luo Shixian 《中国炼油与石油化工》2008,(3):33-38
On the basis of formulating the 9-lump kinetic model for gasoline catalytic upgrading and the 12- lump kinetic model for heavy oil FCC, this paper is aimed at development of a combined kinetic model for a typical FDFCC process after analyzing the coupled relationship and combination of these two models. The model is also verified by using commercial data, the results of which showed that the model can better predict the product yields and their quality, with the relative errors between the main products of the unit and commercial data being less than five percent. Furthermore, the combined model is used to predict and optimize the operating conditions for gasoline riser and heavy oil riser in FDFCC. So this paper can offer some guidance for the processing of FDFCC and is instructive to model research and development of such multi-reactor process and combined process. 相似文献
8.
Tatiana Montoy Blanca L. Argel Nashaat N. Nassar Camilo A. Franco Farid B. Corte′s 《石油科学(英文版)》2016,13(3):561-571
The production of heavy and extra-heavy oil is
challenging because of the rheological properties that crude
oil presents due to its high asphaltene content. The upgrading
and recovery processes of these unconventional oils are
typically water and energy intensive, which makes such
processes costly and environmentally unfriendly. Nanoparticle
catalysts could be used to enhance the upgrading and
recovery of heavy oil under both in situ and ex situ conditions.
In this study, the effect of the Ni-Pd nanocatalysts
supported on fumed silica nanoparticles on post-adsorption
catalytic thermal cracking of n-C7 asphaltenes was investigated
using a thermogravimetric analyzer coupled with
FTIR. The performance of catalytic thermal cracking of n-C7
asphaltenes in the presence of NiO and PdO supported on
fumed silica nanoparticles was better than on the fumed
silica support alone. For a fixed amount of adsorbed n-C7
asphaltenes (0.2 mg/m2), bimetallic nanoparticles showed
better catalytic behavior than monometallic nanoparticles,
confirming their synergistic effects. The corrected Ozawa–
Flynn–Wall equation (OFW) was used to estimate the
effective activation energies of the catalytic process. The
mechanism function, kinetic parameters, and transition state
thermodynamic functions for the thermal cracking process of
n-C7 asphaltenes in the presence and absence of nanoparticles
are investigated. 相似文献
9.
References: 《中国炼油与石油化工》2007,(4):1-6
Over the past decades SINOPEC has been uninterruptedly engaging in the development and upgrading of deep catalytic cracking (DCC) technology for manufacturing propylene from heavy oil. Recently SINOPEC after having made a lot of progress in the area of oil refining at the molecular level has developed a new generation DMMC-1 type catalyst designed for the DCC process. The laboratory evaluation tests have shown that compared to the existing MMC-2 type catalyst that features the best comprehensive performance, the DMMC-1 type catalyst has increased the propylene yield by 2.2% with the propylene selectivity increased by 10%. The said catalyst has improved its ability for heavy oil cracking and coke selectivity along with reduction of olefin content in gasoline to achieve a better product distribution and improve the product quality. The results of application of the said catalyst in a 650-kt/a commercial DCC unit at SINOPEC Anqing Branch Company have revealed that the DMMC- 1 catalyst demonstrated an enhanced capability for heavy oil cracking and could increase the total liquid yield to 84.56 m% from 83.92 m%, the LPG yield to 38.90 m % from 34.60 m %, the propylene yield to 17.80 m% from 15.37 m% and the propylene concentration to 45.91 m% from 44.91 m%, and reduce the coke yield from 7.61 m% to 7.05 m% and the olefin content in gasoline from 42.3 v% to 37.5 v%, resulting in an incremental profit amounting to 52.19 million RMB a year. This technology has further upgraded and developed the DCC technology which has been commanding a leading position among the industry peers. 相似文献
10.
The highly viscous crude oil from Shuguang No.1 zone of Liaohe oifield features high density,high viscosity and low wax content.It contains no gasoline fraction and its diesel oil fraction yiled is only 7.19%,which belongs to the low sulfur naphthenic stocks crude oil.Its heavy fraction is not suited for producing lubricating oil.Its heavy oil,whick contains more resins nd asphaltens and less wax,is not an ideal feedstock for catalytic cracking ,but is the ideal raw material for producing high-grade paving asphalt.Now this highy viscous crude oil is used as fuel oil after being emulsified in Liaohe oilfield,but its viscosity is so hight tha it cannot be atomized uniformly and burned completely,resuting not only in waste of oil resource but also in reduction of economical benefit.To make full use of this oil resource and alleviate the shortfall of high grade paving asphalt in China,various brands of asphal meeting Q/SHR003-1998 and ESSO specifications were developed by blending vaceuum residue of the said oil and a blending compo-net which are rich in aromatics and deficient in wax.The impct of blending component on proerties of blended ashalt has been investigated and road perfomances of these blended asphalts were studied.The labroatory test results show that the blended asphalts have good road performance and antiaging property. 相似文献
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12.
以辽河减压渣油为原料,采用C5为溶剂,在压力4.0~7.0 MPa、剂油质量比4:1及温度160/180 ℃的条件下进行深度溶剂脱沥青试验,残炭降低率50%左右,90%以上的沥青质得到脱除,并富集到脱油沥青中。采用溶剂脱沥青-脱沥青油催化裂化-沥青残渣焦化组合工艺加工辽河减压渣油的研究结果表明:随溶剂脱沥青压力的提高,脱沥青油的收率增加,压力为7.0 MPa时,总脱沥青油收率达到74.22%,沥青残渣收率明显降低;轻、重脱沥青油催化裂化的平均液化气+轻油收率分别为25.74%及12.72%,沥青残渣焦化的液化气+轻油收率均值为7.17%。采用组合工艺技术,辽河减压渣油的液化气+轻油收率较减压渣油直接焦化提高了4.06 百分点。 相似文献
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14.
Traditional processing technology is not suitable for Tahe crude oil due to its low light distillate yield and poor quality. A new process, atmospheric flash evaporation-solvent deasphalting combined process, was put forward. The appropriate operating conditions of solvent deasphalting process were as follows: iso-pentane solvent, temperature of 175°C, pressure of 3.7MPa, solvent volume ratio of 5.0. Compared with atmospheric distillation-delayed coking process, total liquid product yield by new process could reach 78.77%, increasing by 9.47%. The quality of deasphalting oil met the feed requirements for catalytic cracking and de-oiled asphalt could be used as asphalt mixture additives. 相似文献
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16.
应对高硫劣质原油的炼油总工艺流程设计 总被引:1,自引:0,他引:1
针对加工高硫劣质原油的发展模式,总结了延迟焦化+循环流化床(CFB)锅炉、渣油加氢+重油催化裂化以及溶剂脱沥青+IGCC等三种成熟的炼油总工艺流程,分析了各流程的局限性。在炼油总工艺流程设计中,对炼油厂大型化和原油来源多样性的矛盾、加工非常规超重质原油、炼油厂多产汽油和提供化工轻油的矛盾、生产低硫产品以及油煤一体化的发展等问题提出了可行的思路和建议。 相似文献
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目前,世界范围内增产的石油将主要是重质原油及重质合成油,炼油企业正面临着原料重质化和劣质化、产品轻质化和清洁化、炼制过程清洁化和低碳化的压力,需要尽快提升重油转化加工水平,提升重油轻质化的转化效率。以脱碳、加氢两种石油炼制技术路线为核心,分析了减黏裂化、溶剂脱沥青、延迟焦化、渣油催化裂化、渣油加氢等各种技术的现状及技术进展,并评价了影响渣油加工工艺选择的技术经济因素。延迟焦化技术将依然是渣油加工的主要技术手段之一,但是其经济性和环境表现略差;沸腾床、浆态床加氢技术将在渣油加工技术中承担越来越重要的角色,但在原料适应性和转化深度、催化剂寿命和消耗等方面还有待进一步提高;渣油加工组合工艺因能充分发挥各种渣油加工技术的组合优势,在实际生产中应优先加以考虑。 相似文献
19.
掺炼丙脱沥青对焦化装置安全运行及产品的影响 总被引:3,自引:0,他引:3
中国石油天然气股份有限公司独山子石化分公司延迟焦化装置丙脱沥青掺炼比例的上升,使焦化原料的粘度和残炭升高,轻质油收率下降,焦炭收率上升。而更为严重的是:生产出的焦炭产品是弹丸焦,焦化蜡油残炭大幅超标。以上问题的出现,严重影响了焦化装置的安全运行,如严重影响冷焦和除焦操作的安全;关键机泵封油的密封效果差或可能中断;关键部位结焦;原料泵可能抽空等。针对存在的问题,分析了原因并提出了相应措施和建议。 相似文献