Solids Deposition during "Cold Flow" of Wax-Solvent Mixtures in a Flow-loop Apparatus with Heat Transfer

被引:66
作者
Bidmus, Hamid O. [1 ]
Mehrotra, Anil K. [1 ]
机构
[1] Univ Calgary, Dept Chem & Petr Engn, Calgary, AB T2N 1N4, Canada
基金
加拿大自然科学与工程研究理事会;
关键词
INTERFACE TEMPERATURE; TURBULENT-FLOW; LAMINAR-FLOW; CRUDE-OIL; PIPELINES; SYSTEMS; SHEAR; BEHAVIOR;
D O I
10.1021/ef900224r
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
"Cold flow" refers to the pipeline flow of a "waxy" crude oil at a temperature, which is below its wax appearance temperature (WAT) and above its pour point temperature (PPT), whereby precipitated wax crystals remain suspended in the flowing crude oil. It has been suggested as an alternative technology for decreasing solids deposition (Merino-Garcia, D.; Correra, S. Pet. Sci. Technol. 2008, 26, 446). An experimental investigation was undertaken to study solids deposition under cold flow in a flow-loop apparatus, incorporating a small double-pipe heat exchanger. The experiments were performed using 3 and 6 mass % mixtures of a petroleum wax dissolved in Norpar13 (a paraffinic solvent comprising C-9-C-16) at different wax-solvent mixture temperatures, T-h, and two flow rates over a deposition time of I h. Two sets of deposition experiments were performed: cold flow with {WAT >= T-h > PPT} and "hot flow" with {T-h > WAT}. The deposit mass decreased with a decrease in wax concentration and with an increase in the coolant temperature. However, the deposit mass decreased with a decrease in the mixture temperature, under cold flow, but it increased with a decrease in the mixture temperature, under hot flow. Also, the deposit mass, under cold flow, was not affected by flow rate. Predictions from a pseudosteady-state heat-transfer model were in good agreement with experimental results, indicating the deposition process to be thermally driven. The liquid-deposit interface temperature in all cases was equal to the WAT of the liquid phase. Variations in both the wax content and the carbon number distribution in deposit samples are discussed.
引用
收藏
页码:3184 / 3194
页数:11
相关论文
共 38 条
[1]  
[Anonymous], OIL GAS J
[2]   A critical review of the Modeling of wax deposition mechanisms [J].
Azevedo, LFA ;
Teixeira, AM .
PETROLEUM SCIENCE AND TECHNOLOGY, 2003, 21 (3-4) :393-408
[3]  
Becker J.R., 2000, P 2000 SPE ANN TECH
[4]   Modeling of deposit formation from "waxy" mixtures via moving boundary formulation: Radial heat transfer under static and laminar flow conditions [J].
Bhat, NV ;
Mehrotra, AK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (17) :6948-6962
[5]   Measurement and prediction of the phase behavior of wax-solvent mixtures:: Significance of the wax disappearance temperature [J].
Bhat, NV ;
Mehrotra, AK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (13) :3451-3461
[6]   Measurement of the liquid-deposit interface temperature during solids deposition from wax-solvent mixtures under static cooling conditions [J].
Bidmus, Hamid ;
Mehrotra, Anil K. .
ENERGY & FUELS, 2008, 22 (02) :1174-1182
[7]   Measurement of the Liquid-Deposit Interface Temperature during Solids Deposition from Wax-Solvent Mixtures under Sheared Cooling [J].
Bidmus, Hamid ;
Mehrotra, Anil K. .
ENERGY & FUELS, 2008, 22 (06) :4039-4048
[8]   Heat-transfer analogy for wax deposition from paraffinic mixtures [J].
Bidmus, HO ;
Mehrotra, AK .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2004, 43 (03) :791-803
[9]  
BIDMUS HO, 2009, THESIS U CALGARY CAL
[10]   EVALUATION OF DOWNHOLE ELECTRIC IMPEDANCE HEATING-SYSTEMS FOR PARAFFIN CONTROL IN OIL-WELLS [J].
BOSCH, FG ;
SCHMITT, KJ ;
EASTLUND, BJ .
IEEE TRANSACTIONS ON INDUSTRY APPLICATIONS, 1992, 28 (01) :190-195