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1

Akhiar, Afifi, Felipe Guilayn, Michel Torrijos, Audrey Battimelli, Abd Halim Shamsuddin, and Hélène Carrère. "Correlations between the Composition of Liquid Fraction of Full-Scale Digestates and Process Conditions." Energies 14, no. 4 (2021): 971. http://dx.doi.org/10.3390/en14040971.

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Fast development of centralized agricultural biogas plants leads to high amounts of digestate production. The treatment and disposal of liquid fractions after on-site digestate solid–liquid separation remains problematic due to their high organic, nutrient and aromatic contents. This work aims to study the variability of the remaining compounds in the digestate liquid fractions in relation to substrate origin, process parameters and solid–liquid separation techniques. Twenty-nine digestates from full-scale codigestion biogas plants and one waste activated sludge (WAS) digestate were collected
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2

Schmitt, Vivien, Matthieu Dufresne, Jose Vazquez, Martin Fischer, and Antoine Morin. "Separation efficiency of a hydrodynamic separator using a 3D computational fluid dynamics multiscale approach." Water Science and Technology 69, no. 5 (2014): 1067–73. http://dx.doi.org/10.2166/wst.2014.014.

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The aim of this study is to investigate the use of computational fluid dynamics (CFD) to predict the solid separation efficiency of a hydrodynamic separator. The numerical difficulty concerns the discretization of the geometry to simulate both the global behavior and the local phenomena that occur near the screen. In this context, a CFD multiscale approach was used: a global model (at the scale of the device) is used to observe the hydrodynamic behavior within the device; a local model (portion of the screen) is used to determine the local phenomena that occur near the screen. The Eulerian–Lag
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3

KANJO, Yoshinori, Atsuhiro HONDA, and Michinobu NISHITANI. "Study on the Solid-liquid Separation of Wastewater with a Rotating Drum Screen." Japan journal of water pollution research 13, no. 1 (1990): 39–47. http://dx.doi.org/10.2965/jswe1978.13.39.

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4

Trotman, A. A., C. E. Mortley, D. G. Mortley, P. P. David, and P. A. Loretan. "A COMPARATIVE STUDY OF HYDROPONIC SYSTEMS FOR GROWING PEANUT." HortScience 28, no. 4 (1993): 267C—267. http://dx.doi.org/10.21273/hortsci.28.4.267c.

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Hydroponic growing systems have the potential to maximize phytomass production of peanut (Arachis hypogea) for Controlled Ecological Life Support Systems (CELSS). Two greenhouse experiments were conducted with plant nutrients supplied in a modified Evan's solutionusing a nutrient film technique. The objective of this research was to determine the effect of hydroponic growing systems on pod and foliage yield of `New Improved Spanish' and `Georgia Red' peanut. Sub-objectives were to evaluate (i) the impact of channel size and (ii) the impact of gradation in pore size on the separation of the roo
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5

Fedoliak, N. V., М. М. Liakh, and V. V. Mykhayliv. "The analysis of factors influencing the trajectory of the vibrating screen." Prospecting and Development of Oil and Gas Fields, no. 3(76) (September 27, 2020): 61–70. http://dx.doi.org/10.31471/1993-9973-2020-3(76)-61-70.

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Due to the fact that the shape of the trajectory of the sieve vibrating screen significantly affects the efficiency of cleaning the drilling mud from the drilled rock, this article identifies and analyzes the factors influencing the formation of the trajectory of the sieve. The study of the nature of the motion of the particles of the drilled rock is carried out. The motion-equation of the point of the jigging frame, respectively, and a certain section of the screen can be described by an non-homogeneous second-order differential equation (Newton equation). The equation of the trajectory of th
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6

McCallum, Jason L., Jennifer N. D. Vacon, and Christopher W. Kirby. "Ultra-Micro-Scale-Fractionation (UMSF) as a Powerful Tool for Bioactive Molecules Discovery." Molecules 25, no. 16 (2020): 3677. http://dx.doi.org/10.3390/molecules25163677.

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Herein is detailed the development and validation of an ultra-micro-scale-fractionation (UMSF) technique for the discovery of plant-based, bioactive molecules, coupling the advantages of ultra-performance liquid chromatography mass spectrometry (UPLC-MS) separations with microtiter plate-based bioassay screens. This novel one-step approach simultaneously uses UPLC to collect chemical profile information, while performing high-resolution fractionation, greatly improving workflow compared to methods relying on high-performance liquid chromatography (HPLC), solid phase extraction or flash systems
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7

Furuhashi, Kenichi, Fumio Hasegawa, Manabu Yamauchi, Yutaka Kaizu, and Kenji Imou. "Improving the Energy Balance of Hydrocarbon Production Using an Inclined Solid–Liquid Separator with a Wedge-Wire Screen and Easy Hydrocarbon Recovery from Botryococcus braunii." Energies 13, no. 16 (2020): 4139. http://dx.doi.org/10.3390/en13164139.

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The green colonial microalga Botryococcus braunii produces large amounts of hydrocarbons and has attracted attention as a potential source of biofuel. When this freshwater microalga is cultured in a brackish medium, the hydrocarbon recovery rate increases; furthermore, the colony size becomes large. In this study, the effects of such changes on the energy balance of harvesting and hydrocarbon recovery were studied via filtrate experiments on an inclined separator and extraction from a concentrated slurry. The inclined separator was effective for harvesting large-colony-forming algae. The water
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8

Pelevin, Aleksei, and Nikolai Sytykh. "The features of classification in hydrocyclones in the course of titanium magnetite ore grinding." Izvestiya vysshikh uchebnykh zavedenii. Gornyi zhurnal, no. 1 (February 17, 2021): 74–84. http://dx.doi.org/10.21440/0536-1028-2021-1-74-84.

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Research aim is to assess the use of hydrocyclones in the closed circuit of the second stage of grinding for the conditions of EVRAZ KGOK dressing mill. Methodology. Industrial tests were carried out under various solid phase capacities of two hydrocyclones GTs-710. Industrial testing results and their discussion. Increase in the content of solid and –71 µm class in the feed of the hydrocyclone results in discharge output increase. Decrease in the content of solid and increase in the content of –71 µm class result in the increased content of –71 µm class in the discharge. When increasing the c
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9

Sutter, Daniel, Matteo Gazzani, and Marco Mazzotti. "A low-energy chilled ammonia process exploiting controlled solid formation for post-combustion CO2capture." Faraday Discussions 192 (2016): 59–83. http://dx.doi.org/10.1039/c6fd00044d.

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A new ammonia-based process for CO<sub>2</sub>capture from flue gas has been developed, which utilizes the formation of solid ammonium bicarbonate to increase the CO<sub>2</sub>concentration in the regeneration section of the process. Precipitation, separation, and dissolution of the solid phase are realized in a dedicated process section, while the packed absorption and desorption columns remain free of solids. Additionally, the CO<sub>2</sub>wash section applies solid formation to enable a reduction of the wash water consumption. A rigorous performance assessment employing the SPECCA index (
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10

Grickus, Armands, and Sharif Guseynov. "ON A MATHEMATICAL MODEL DESCRIBING OPTIMAL PROCESSING MECHANISM OF DISPERSED GRANULAR MATERIALS IN GRAVITATIONAL FLOW WITH HORIZONTAL OR INCLINED VIBRATING SIEVE CLASSIFYING SCREENS." Environment. Technology. Resources. Proceedings of the International Scientific and Practical Conference 3 (June 15, 2017): 69. http://dx.doi.org/10.17770/etr2017vol3.2547.

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The investigation of motion and gravitational processing of disperse granular materials is very important for solution of a wide spectrum of technological processes, including the chemical technology of treatment (with or without the decoration-compression procedure) of granular mineral fertilizers and their drying and sorting/separation by means of vibrating sieve classifying screens, in particular. In this work, we have used the apparatus of the theory of continuous media for the mathematical modelling of dynamics of disperse granular materials, and by this we assume that a property of these
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11

Wang, Hui, Xiaodi Ma, Qibin Cheng, Xiaoli Xi, and Liwei Zhang. "Deep Eutectic Solvent-Based Microwave-Assisted Extraction of Baicalin from Scutellaria baicalensis Georgi." Journal of Chemistry 2018 (2018): 1–10. http://dx.doi.org/10.1155/2018/9579872.

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Deep eutectic solvents (DESs) have attracted significant attention as green media for the extraction and separation of natural compounds from Chinese medicine. In this study, a hydrophobic DESs-based microwave-assisted extraction (MAE) was successfully used to efficiently extract baicalin from Scutellaria baicalensis Georgi. Firstly, DecA: N4444-Cl (DES-1 , molar ratio 1 : 2) was screened and selected as the most appropriate DES by comparing the extraction yield in different hydrophobic DESs. Based on the extraction yield of baicalin, response surface methodology (RSM) was employed to model an
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12

Cilliers, J. "Solid—liquid separation." Powder Technology 68, no. 1 (1991): 98. http://dx.doi.org/10.1016/0032-5910(91)80071-p.

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13

Onofrio, Michelle D., Claude R. Mallet, Allen R. Place, and Juliette L. Smith. "A Screening Tool for the Direct Analysis of Marine and Freshwater Phycotoxins in Organic SPATT Extracts from the Chesapeake Bay." Toxins 12, no. 5 (2020): 322. http://dx.doi.org/10.3390/toxins12050322.

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Many detection methods for phycotoxins, bioactive compounds produced by harmful algae, focus on one compound or a class of related compounds. Multiple harmful algal species often co-occur in the environment, however, emphasizing the need to analyze for the presence of multiple groups of marine and freshwater phycotoxins in environmental samples, e.g., extracts from solid phase adsorption toxin tracking (SPATT). Two methods were developed to screen for 13 phycotoxins (microcystin-RR, -LR, -YR, azaspiracid-1, -2, karlotoxin 3, goniodomin A, brevetoxin-2, yessotoxin, pectenotoxin-2, dinophysistox
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14

Liu, Yucheng, Maoren Wang, Mingyan Chen, Meng Zhu, and Maoqi Liao. "Facilitating the natural semi-drying of oily sludge by changing the form of water." PLOS ONE 16, no. 1 (2021): e0245430. http://dx.doi.org/10.1371/journal.pone.0245430.

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Reducing the water content of oily sludge is essential for the disposal of it. Despite conditioning and solid-liquid separation, the water content of oily sludge generally exceeds 65%. A large amount of this water exists in the form of emulsified and bound water, reducing the efficiency of water removal during the natural semi-drying process of oily sludge. To shorten the time required for natural semi-drying, this study applied an orthogonal test to screen an oily sludge modified material (OSM). The effect and mechanism of OSM on the natural semi-drying of oily sludge were studied using a the
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15

Strobl, Laura, Thomas Diefenhardt, Martin Schlummer, Tanja Leege, and Swetlana Wagner. "Recycling Potential for Non-Valorized Plastic Fractions from Electrical and Electronic Waste." Recycling 6, no. 2 (2021): 33. http://dx.doi.org/10.3390/recycling6020033.

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This paper describes a study for waste of electrical and electronic equipment (WEEE) to characterise the plastic composition of different mixed plastic fractions. Most of the samples studied are currently excluded from material recycling and arise as side streams in state-of-the-art plastics recycling plants. These samples contain brominated flame retardants (BFR) or other substances of concern listed as persistent organic pollutants or in the RoHS directive. Seventeen samples, including cathode ray tube (CRT) monitors, CRT televisions, flat screens such as liquid crystal displays, small domes
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16

Hayward, Douglas G., Jon W. Wong, Kai Zhang, et al. "Multiresidue Pesticide Analysis in Ginseng and Spinach by Nontargeted and Targeted Screening Procedures." Journal of AOAC INTERNATIONAL 94, no. 6 (2011): 1741–51. http://dx.doi.org/10.5740/jaoacint.sgehayward.

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Abstract Five different mass spectrometers interfaced to GC or LC were evaluated for their application to targeted and nontargeted screening of pesticides in two foods, spinach and ginseng. The five MS systems were capillary GC/MS/MS, GC-high resolution time-of-flight (GC/HR-TOF)-MS, TOF-MS interfaced with a comprehensive multidimensional GC (GCxGC/TOF-MS), an MS/MS ion trap hybrid mass (qTrap) system interfaced with an ultra-performance liquid chromatograph (UPLC-qTrap), and UPLC interfaced to an orbital trap high resolution mass spectrometer (UPLC/Orbitrap HR-MS). Each MS system was tested w
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17

Anlauf, Harald. "Mechanical Solid Liquid Separation." Chemical Engineering & Technology 33, no. 8 (2010): 1231. http://dx.doi.org/10.1002/ceat.201090037.

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18

Huang, Rongrong, Sara Cathey, Laura Pollard, and Tim Wood. "UPLC-MS/MS Analysis of Urinary Free Oligosaccharides for Lysosomal Storage Diseases: Diagnosis and Potential Treatment Monitoring." Clinical Chemistry 64, no. 12 (2018): 1772–79. http://dx.doi.org/10.1373/clinchem.2018.289645.

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Abstract BACKGROUND The glycoproteinoses are a subgroup of lysosomal storage diseases (LSDs) resulting from impaired degradation of N-linked oligosaccharide side chains of glycoproteins, which are commonly screened by detecting the accumulated free oligosaccharides (FOSs) in urine via thin layer chromatography (TLC). The traditional TLC method suffers from limited analytical sensitivity and specificity and lacks quantification capability. Therefore, we developed an analytically sensitive and relatively specific assay using ultraperformance liquid chromatography–tandem mass spectrometry (UPLC-M
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19

Holdich, R. G., and G. Butt. "Solid/liquid separation by sedimentation." Proceedings of the Institution of Mechanical Engineers, Part E: Journal of Process Mechanical Engineering 211, no. 1 (1997): 43–52. http://dx.doi.org/10.1243/0954408971529539.

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The analysis of batch sedimentation tests performed for the purpose of continuous sedimentation vessel design is described. Conventional design techniques employ the concept of settling flux with, under certain conditions, a constitutive equation linking solid concentration and pressure in a unique and time-independent manner. Experimental studies employing measurement of local concentration and the liquid pressure gradient during sedimentation were used to determine the limits of the conventional design techniques. A 'maximum fluidized concentration' is defined which is the value above which
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20

Mujumdar, Arun S. "ADVANCES IN SOLID-LIQUID SEPARATION." Drying Technology 5, no. 3 (1987): 487–88. http://dx.doi.org/10.1080/07373938708916557.

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21

Alt, C. "Solid—liquid separation practice 3." Chemical Engineering and Processing: Process Intensification 29, no. 1 (1991): 62. http://dx.doi.org/10.1016/0255-2701(91)87009-r.

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22

Zaki, M. M., I. Nirdosh, and G. H. Sedahmed. "Liquid-solid mass transfer at vertical screens in bubble columns." Canadian Journal of Chemical Engineering 75, no. 2 (1997): 333–38. http://dx.doi.org/10.1002/cjce.5450750208.

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23

Mulhem, Basel, Günther Schulte, and Udo Fritsching. "Solid–liquid separation in suspension atomization." Chemical Engineering Science 61, no. 8 (2006): 2582–89. http://dx.doi.org/10.1016/j.ces.2005.11.035.

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24

Smith, M. R. "Solid-liquid separation process and technology." Chemical Engineering Science 42, no. 11 (1987): 2802–3. http://dx.doi.org/10.1016/0009-2509(87)87041-0.

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25

Landman, K. A., and L. R. White. "Solid/liquid separation of flocculated suspensions." Advances in Colloid and Interface Science 51 (August 1994): 175–246. http://dx.doi.org/10.1016/0001-8686(94)80036-7.

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26

Bisht, Kamal S., and Michael E. Dreyer. "Phase Separation in Porous Media Integrated Capillary Channels." Microgravity Science and Technology 32, no. 6 (2020): 1001–18. http://dx.doi.org/10.1007/s12217-020-09828-6.

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Abstract Phase separation in space is critical for gas-free propellant supply, life support systems, refueling of spacecraft in low earth orbit (LEO), and for deep space exploration missions. In the absence of gravity, the stability of the liquid-gas interface depends on capillary forces. High liquid flow rates, sudden accelerations, and vibrational disturbances can cause the free surface of the liquid to collapse, which results in the ingestion of gas. Propellant tanks may have screen channel liquid acquisition devices (SCLADs) to position and maintain a gas-free propellant supply to the outl
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27

Fujita, M., M. Ike, K. Kusunoki, T. Ueno, K. Serizawa, and T. Hirao. "Removal of color and estrogenic substances by fungal reactor equipped with ultrafiltration unit." Water Supply 2, no. 5-6 (2002): 353–58. http://dx.doi.org/10.2166/ws.2002.0190.

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Removal/degradation of color components and endocrine disruptors (EDs) by a bioreactor employing a white rot fungus Trametes hirsuta IFO4917 equipped with ultramembrane filtration (UF) unit was proposed and experimentally investigated. Among 20 white-rot fungal strains, T. hirsuta IFO4917 was screened as a most effective white-rot fungus for removal/degradation of color and EDs. This strain could effectively decolorize humic acid and degrade a wide range of Eds: bisphenol A (BPA), nonylphenol (NP), 17 beta-estradiol, estrone and estriol, although di-(2-ethylhexyl) phthalate (DEHP) could not be
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28

ZAKI, M. M., I. NIRDOSH, and G. H. SEDAHMED. "LIQUID-SOLID MASS TRANSFER AT HORIZONTAL WOVEN SCREENS WITH UPWARD COCURRENT GAS-LIQUID FLOW." Chemical Engineering Communications 186, no. 1 (2001): 43–56. http://dx.doi.org/10.1080/00986440108912869.

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29

Comert, Fatih, and Paul L. Dubin. "Liquid-liquid and liquid-solid phase separation in protein-polyelectrolyte systems." Advances in Colloid and Interface Science 239 (January 2017): 213–17. http://dx.doi.org/10.1016/j.cis.2016.08.005.

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30

Dahlstrom, Donald A. "Research needs in liquid-solid separation. How will separation happen?" Industrial & Engineering Chemistry Research 29, no. 6 (1990): 1020–25. http://dx.doi.org/10.1021/ie00102a011.

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31

Holdich, R. G. "Solid–liquid separation equipment selection and modelling." Minerals Engineering 16, no. 2 (2003): 75–83. http://dx.doi.org/10.1016/s0892-6875(02)00178-4.

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32

Anlauf, H. "Buchbesprechung: Solid-Liquid Separation. Von L. Svarovsky." Chemie Ingenieur Technik 74, no. 1-2 (2002): 140–41. http://dx.doi.org/10.1002/1522-2640(200202)74:1/2<140::aid-cite140>3.0.co;2-c.

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33

Seo, Young-Soo, Vladimir A. Samuilov, Jonathan Sokolov, et al. "DNA separation at a liquid-solid interface." ELECTROPHORESIS 23, no. 16 (2002): 2618–25. http://dx.doi.org/10.1002/1522-2683(200208)23:16<2618::aid-elps2618>3.0.co;2-w.

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34

Biggs, Simon. "Aggregate Structures and Solid-Liquid Separation Processes." KONA Powder and Particle Journal 24 (2006): 41–53. http://dx.doi.org/10.14356/kona.2006008.

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35

Wang, Steven, Guy Metcalfe, Robert L. Stewart, et al. "Solid–liquid separation by particle-flow-instability." Energy Environ. Sci. 7, no. 12 (2014): 3982–88. http://dx.doi.org/10.1039/c4ee02841d.

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A robust separation strategy using novel particle-flow-instability physics is successfully developed for adifficult-to-separate suspensionin which there is some combination of a small density difference between solid and liquid, high viscosity, and small-sized particles.
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36

KAWAI, Hideki, and Hiroshi TAKAHASHI. "Solid-liquid separation by Taylor vortex flow." Proceedings of Conference of Hokkaido Branch 2002.42 (2002): 40–41. http://dx.doi.org/10.1299/jsmehokkaido.2002.42.40.

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37

Dentel, Steven K. "Chemical Conditioning for Solid–Liquid Separation Processes." Drying Technology 28, no. 7 (2010): 843–49. http://dx.doi.org/10.1080/07373937.2010.490490.

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38

Fernandes, Fabiano A. N., and Sueli Rodrigues. "Educational software for gas-solid and liquid-solid separation equipment." Computer Applications in Engineering Education 11, no. 4 (2003): 226–32. http://dx.doi.org/10.1002/cae.10051.

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39

Conrath, Michael, Yulia Smiyukha, Eckart Fuhrmann, and Michael Dreyer. "Double porous screen element for gas–liquid phase separation." International Journal of Multiphase Flow 50 (April 2013): 1–15. http://dx.doi.org/10.1016/j.ijmultiphaseflow.2012.10.003.

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40

Kates, Patrick A., John J. Tomashek, David A. Miles, and L. Andrew Lee. "Parallel sample processing using dispersive INtip micro-purification on programmable multichannel pipettes." BioTechniques 68, no. 3 (2020): 148–54. http://dx.doi.org/10.2144/btn-2019-0140.

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Automation gives researchers the ability to process and screen orders of magnitude higher numbers of samples than manual experimentation. Current biomacromolecule separation methodologies suffer from necessary manual intervention, making their translation to high-throughput automation difficult. Herein, we present the first characterization of biomacromolecule affinity purification via dispersive solid-phase extraction in a pipette tip (INtip). We use commercially available resin and compare efficiency with batch and spin column methodologies. Moreover, we measure the kinetics of binding and e
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41

Lopes, B. Oliveira, V. A. Machado de Miranda, J. M. Freitas de Oliveira, A. G. Barbosa de Lima, S. José dos Santos Filho, and F. P. Macedo Farias. "Solid - Liquid Separation Process in Hydrocyclone by CFD." Diffusion Foundations 24 (September 2019): 76–103. http://dx.doi.org/10.4028/www.scientific.net/df.24.76.

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Mining is a relevant economic activity in many countries. In the treatment of ores, water is an indispensable input. For classification of minerals, the mineral industry uses the hydrocyclone process, where water is used as the medium for transporting dispersed ore particles, that are separated from the liquid by centrifugal force inside anequipmentnamed hydrocyclone.The constant advance of computers processing power, the evolution in the techniques and numerical methods, allow to simulate with great precision complex physical problems of fluid dynamics such as flow in hydrocyclones.In this se
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42

Iritani, Eiji. "Fundamentals of Membrane Utilization in Solid–Liquid Separation." MEMBRANE 39, no. 1 (2014): 2–7. http://dx.doi.org/10.5360/membrane.39.2.

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43

Miyata, Atsushi, Yasuhiro Matsui, Masao Shimada, and Hiromasa Yamashita. "Energy Management System Utilizing Intensive Solid Liquid Separation." Proceedings of the Water Environment Federation 2015, no. 2 (2015): 1–20. http://dx.doi.org/10.2175/193864715819558424.

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44

Paschke, N., and D. Taylor. "Solid/Liquid Separation: Waste Management and Productivity Enhancement." Journal of Environmental Quality 20, no. 2 (1991): 497–98. http://dx.doi.org/10.2134/jeq1991.00472425002000020029x.

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45

KAWAI, Hideki, Shingo KISHIKAWA, Hiroshige KIKURA, Masanori ARITOMO, and Hiroshi TAKAHASHI. "Experimental analysis of Taylor vortex solid-liquid separation." Proceedings of the JSME annual meeting 2004.2 (2004): 219–20. http://dx.doi.org/10.1299/jsmemecjo.2004.2.0_219.

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46

WANG, Li-yang, Zhi-chu ZHENG, Jun GUO, Jun ZHANG, and Chi TANG. "Investigation on separation efficiency of liquid/solid hydrocyclone." Journal of Hydrodynamics, Ser. B 18, no. 3 (2006): 400–404. http://dx.doi.org/10.1016/s1001-6058(06)60085-1.

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47

Liu, Xiao Xing, Qi Ying Pan, and Hao Su. "Study on Cross-Flow Solid-Liquid Separation Technology." Advanced Materials Research 712-715 (June 2013): 748–54. http://dx.doi.org/10.4028/www.scientific.net/amr.712-715.748.

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The technology, device current situation , theory ,applied prospect of cross-flow solid-liquid separation have been summarized. It has been studied to making several cuneiform slots on the rotator of traditional crossflow filter, allowing the rotator forms convergence space with canister's inside wall. When suspending liquid fill into the cuneiform convergence space, it will cause kinetic press and improve the efficiency of filtrating. .
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Yokoyama, K., T. Oka, H. Okada, Y. Fujine, A. Chiba, and K. Noto. "Solid-liquid magnetic separation using bulk superconducting magnets." IEEE Transactions on Appiled Superconductivity 13, no. 2 (2003): 1592–95. http://dx.doi.org/10.1109/tasc.2003.812799.

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Wang, Li-yang, Zhi-chu Zheng, Jun Guo, Jun Zhang, and Chi Tang. "Investigation on separation efficiency of liquid/solid hydrocyclone." Journal of Hydrodynamics 18, S1 (2006): 391–95. http://dx.doi.org/10.1007/bf03400478.

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Wakeman, R. J. "Selection of equipment for solid/liquid separation processes." Filtration & Separation 32, no. 4 (1995): 328. http://dx.doi.org/10.1016/0015-1882(95)90165-5.

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