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Journal of Non-Newtonian Fluid Mechanics — Template for authors

Publisher: Elsevier

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Guideline source

Categories	Rank	Trend in last 3 yrs
Applied Mathematics	#83 of 548	down by 32 ranks
Mechanical Engineering	#151 of 596	down by 49 ranks
Chemical Engineering (all)	#77 of 279	down by 15 ranks
Condensed Matter Physics	#133 of 411	down by 32 ranks
Materials Science (all)	#156 of 455	down by 40 ranks

Journal quality:

High

Last 4 years overview: 431 Published Papers | 1803 Citations

Indexed in: Scopus

Last updated: 13/07/2020

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Journal Performance & Insights

CiteRatio

SCImago Journal Rank (SJR)

Source Normalized Impact per Paper (SNIP)

A measure of average citations received per peer-reviewed paper published in the journal.

Measures weighted citations received by the journal. Citation weighting depends on the categories and prestige of the citing journal.

Measures actual citations received relative to citations expected for the journal's category.

4.2

2% from 2019

CiteRatio for Journal of Non-Newtonian Fluid Mechanics from 2016 - 2020
Year	Value
2020	4.2
2019	4.3
2018	4.4
2017	4.0
2016	3.9

Graph view

0.873

8% from 2019

SJR for Journal of Non-Newtonian Fluid Mechanics from 2016 - 2020
Year	Value
2020	0.873
2019	0.944
2018	1.038
2017	1.14
2016	1.145

Graph view

1.301

9% from 2019

SNIP for Journal of Non-Newtonian Fluid Mechanics from 2016 - 2020
Year	Value
2020	1.301
2019	1.436
2018	1.506
2017	1.535
2016	1.706

Graph view

Insights

CiteRatio of this journal has decreased by 2% in last years.
This journal’s CiteRatio is in the top 10 percentile category.

Insights

SJR of this journal has decreased by 8% in last years.
This journal’s SJR is in the top 10 percentile category.

Insights

SNIP of this journal has decreased by 9% in last years.
This journal’s SNIP is in the top 10 percentile category.

Journal of Non-Newtonian Fluid Mechanics

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Elsevier

Journal of Non-Newtonian Fluid Mechanics

The journal will appeal to people working on fundamental developments in the rheological sciences and applications on both the macroscopic and microscopic scale. Subjects considered suitable for the journal include the following (not necessarily in order of importance): •The development of rheological equations of state for non-Newtonian liquids from both a continuum and microstructure starting point, but the outlook will always be practical in the sense that abstract developments with no hope of application will not be welcomed. •The use of rheological equations of state in the solution of meaningful flow problems involving one or more fluid phases. Analytic and/or numerical solutions would be in order. These should be problems which involve the equations of continuity and motion and energy in a non-trivial way. •Experimental work associated with complex fluids, including - confirmation or otherwise of prediction from rheological equations of state developments and the confirmation of predictions from the solved flow problems - novel flow situations which would suggest the need for further analytical work - rheometry - practical situations of flow which are in need of systematic theoretical and experimental research. Such issues and developments commonly arise, for example, in the polymer processing, petroleum, pharmaceutical, biomedical and consumer product industries. However, this list is not meant to be representative, not exhaustive. •Problems involving heat and mass transfers and mixing in flowing non-Newtonian liquids. •Instabilities, unsteady and turbulent or chaotic flow characteristics in non-Newtonian fluids. Comments and Proposals: We are interested in receiving comments/feedback on this and our other journals and welcome publication proposals for books, electronic products, new journals and co-operation for existing journals. Read Less

Mathematics

Last updated on	13 Jul 2020
ISSN	0377-0257
Impact Factor	High - 1.628
Open Access	No
Sherpa RoMEO Archiving Policy	Green
Plagiarism Check	Available via Turnitin
Endnote Style	Download Available
Bibliography Name	elsarticle-num
Citation Type	Numbered [25]
Bibliography Example	G. E. Blonder, M. Tinkham, T. M. Klapwijk, Transition from metallic to tunneling regimes in superconducting microconstrictions: Excess current, charge imbalance, and supercurrent conversion, Phys. Rev. B 25 (7) (1982) 4515–4532. URL 10.1103/PhysRevB.25.4515

Top papers written in this journal

Journal Article • DOI: 10.1016/S0377-0257(97)00004-9 •

Thixotropy—a review

Howard A. Barnes

01 May 1997 - Journal of Non-newtonian Fluid Mechanics

Abstract:

The ensuing mechanical response to stressing or straining a structured liquid results in various viscoelastic phenomena, either in the linear region where the microstructure responds linearly with respect to the stress and strain but does not itself change, or in the nonlinear region where the microstructure does change in re... The ensuing mechanical response to stressing or straining a structured liquid results in various viscoelastic phenomena, either in the linear region where the microstructure responds linearly with respect to the stress and strain but does not itself change, or in the nonlinear region where the microstructure does change in response to the imposed stresses and strains, but does so reversibly. The complication of thixotropy arises because this reversible, microstructural change itself takes time to come about due to local spatial rearrangement of the components. This frequently found time-response of a microstructure that is itself changing with time makes thixotropic, viscoelastic behaviour one of the greatest challenges facing rheologists today, in terms of its accurate experimental characterisation and its adequate theoretical description. Here a history of thixotropy is given, together with a description of how it is understood today in various parts of the scientific community. Then a mechanistic description of thixotropy is presented, together with a series of applications where thixotropy is important. A list of different examples of thixotropic systems is then given. Finally the various kinds of theories that have been put forward to describe the phenomenon mathematically are listed. read more

Topics:

Thixotropy (56%)56% related to the paper

1,367 Citations

Journal Article • DOI: 10.1016/0377-0257(77)80021-9 •

A new constitutive equation derived from network theory

Nhan Phan Thien¹, Roger I. Tanner¹ •

01 Jul 1977 - Journal of Non-newtonian Fluid Mechanics

Abstract:

A constitutive equation is derived from a Lodge—Yamamoto type of network theory for polymeric fluids. The network junctions are not assumed to move strictly as points of the continuum but allowed a certain “effective slip”. The rates of creation and destruction of junctions are assumed to depend on the instantaneous elastic e... A constitutive equation is derived from a Lodge—Yamamoto type of network theory for polymeric fluids. The network junctions are not assumed to move strictly as points of the continuum but allowed a certain “effective slip”. The rates of creation and destruction of junctions are assumed to depend on the instantaneous elastic energy of the network, or equivalently, the average extension of the network strand, in a simple manner. Agreement between model predictions and the I.U.P.A.C. data on L.D.P.E. is good. read more

Topics:

Constitutive equation (54%)54% related to the paper, Elastic energy (51%)51% related to the paper, Network theory (50%)50% related to the paper

1,066 Citations

Journal Article • DOI: 10.1016/S0377-0257(98)00094-9 •

The yield stress—a review or ‘παντα ρει’—everything flows?

Howard A. Barnes

01 Feb 1999 - Journal of Non-newtonian Fluid Mechanics

Abstract:

An account is given of the development of the idea of a yield stress for solids, soft solids and structured liquids from the beginning of this century to the present time. Originally, it was accepted that the yield stress of a solid was essentially the point at which, when the applied stress was increased, the deforming solid... An account is given of the development of the idea of a yield stress for solids, soft solids and structured liquids from the beginning of this century to the present time. Originally, it was accepted that the yield stress of a solid was essentially the point at which, when the applied stress was increased, the deforming solid first began to show liquid-like behaviour, i.e. continual deformation. In the same way, the yield stress of a structured liquid was originally seen as the point at which, when decreasing the applied stress, solid-like behaviour was first noticed, i.e. no continual deformation. However as time went on, and experimental capabilities increased, it became clear, first for solids and lately for soft solids and structured liquids, that although there is usually a small range of stress over which the mechanical properties change dramatically (an apparent yield stress), these materials nevertheless show slow but continual steady deformation when stressed for a long time below this level, having shown an initial linear elastic response to the applied stress. At the lowest stresses, this creep behaviour for solids, soft solids and structured liquids can be described by a Newtonian-plateau viscosity. As the stress is increased the flow behaviour usually changes into a power-law dependence of steady-state shear rate on shear stress. For structured liquids and soft solids, this behaviour generally gives way to Newtonian behaviour at the highest stresses. For structured liquids this transition from very high (creep) viscosity (>106 Pa.s) to mobile liquid ( read more

Topics:

Yield surface (59%)59% related to the paper, Shear stress (57%)57% related to the paper, Yield (engineering) (56%)56% related to the paper,

950 Citations

Journal Article • DOI: 10.1016/0377-0257(82)85016-7 •

A simple constitutive equation for polymer fluids based on the concept of deformation-dependent tensorial mobility

H. Giesekus¹ •

01 Jan 1982 - Journal of Non-newtonian Fluid Mechanics

Abstract:

Some time ago a theory of elastic fluids such as concentrated polymer solutions and melts was presented based on the concept of a multitude of penetrating statistical continua. The configurations of these depend on the deformation history, and their relative motion is determined by the coordinated part-stress in connection wi... Some time ago a theory of elastic fluids such as concentrated polymer solutions and melts was presented based on the concept of a multitude of penetrating statistical continua. The configurations of these depend on the deformation history, and their relative motion is determined by the coordinated part-stress in connection with a tensorial mobility which is a function of all configuration tensors. The simples special case of thise theory is given by a model with only one configuration tensor which both the stress and mobility tensors depend on. In this paper a further specialization is introduced by assuming a linear dependency of stress as well as of mobility tensors on the configuration tensor. Some relationship to a modified retation model, recently presented by Curtiss and Bird, is hereby established. This model which is of the rate-type and is non-linear in the configuration and stress tensors, respectively, nevertheless permits analytic solutions of some of the most important types of flow. These are explicitly given for both steady and transient extensional and shear flows. Besides shear thinning and non-vanishing first and second normal-stress differences, an extensional viscosity with finite asymptotic values as well as non-exponential stress relaxation and start-up curves are predicted, with stress-overshoot at least in the case of shear flow. read more

Topics:

Tensor (56%)56% related to the paper, Extensional viscosity (56%)56% related to the paper, Deformation (mechanics) (56%)56% related to the paper,

894 Citations

Journal Article • DOI: 10.1016/0377-0257(94)01282-M •

A review of the slip (wall depletion) of polymer solutions, emulsions and particle suspensions in viscometers: its cause, character, and cure

Howard A. Barnes

01 Mar 1995 - Journal of Non-newtonian Fluid Mechanics

Abstract:

Slip occurs in the flow of two-phase systems because of the displacement of the disperse phase away from solid boundaries. This arises from steric, hydrodynamic, viscoelastic and chemical forces and constraints acting on the disperse phase immediately adjacent to the walls. The enrichment of the boundary near the wall with th... Slip occurs in the flow of two-phase systems because of the displacement of the disperse phase away from solid boundaries. This arises from steric, hydrodynamic, viscoelastic and chemical forces and constraints acting on the disperse phase immediately adjacent to the walls. The enrichment of the boundary near the wall with the continuous (and usually low-viscosity) phase means that any flow of the fluid over the boundary is easier because of the lubrication effect. Because this effect is usually confined to a very narrow layer — with typical thickness of 0.1–10 μm—it so resembles the slip of solids over surfaces that it has historically been given the same terminology. The restoring force for all the forces that cause an increase in concentration is usually osmotic, and this will always limit the effective slip. In dilute systems, concentration gradients can be present over relatively large distances out from walls, giving what might be interpreted on an overall basis as a thick solvent-only layer. However, as the concentration of the system increases, the layer gets thinner and thinner because it is more difficult to create with the large reverse osmotic force present. However, the enormous increase in the bulk viscosity with increase in concentration means that although thinner, the layer becomes, paradoxically, even more important. Slip manifests itself in such a way that viscosity measured in different size geometries gives different answers if calculated the normal way — in particular the apparent viscosity decreases with decrease in geometry size (e.g. tube radius). Also, in single flow curves unexpected lower Newtonian plateaus are sometimes seen, with an apparent yield stress at even lower stresses. Sudden breaks in the flow curve can also be seen. Large particles as the disperse phase (remember flocs are large particles), with a large dependence of viscosity on the concentration of the dispersed phase are the circumstances which can give slip, especially if coupled with smooth walls and small flow dimensions. The effect is usually greatest at low speeds/flow rates. When the viscometer walls and particles carry like electrostatic charges and the continuous phase is electrically conducted, slip can be assumed. In many cases we need to characterise the slip effects seen in viscometers because they will also be seen in flow in smooth pipes and condults in manufacturing plants. This is usually done by relating the wall shear stress to a slip velocity using a power-law relationship. When the bulk flow has also been characterized, the flow in real situations can be calculated. To characterise slip, it is necessary to change the size of the geometry, and the results extrapolated to very large size to extract unambigouos bulk-flow and slip data respectively. A number of mathematical manipulations are necessary to retrieve these data. We can make attempts to eliminate slip by altering the physical or chemical character of the walls. This is usually done physically by roughening or profiling, but in the extreme, a vane can be used. This latter geometry has the advantage of being easy to make and clean. In either case—by extrapolation or elimination—we end up with the bulk flow properties. This is important in situations where we are trying to understand the microstructure/flow interactions. read more

Topics:

Slip (materials science) (67%)67% related to the paper, Newtonian fluid (52%)52% related to the paper, Shear stress (52%)52% related to the paper,

818 Citations

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13. What is Sherpa RoMEO Archiving Policy for Journal of Non-Newtonian Fluid Mechanics?

We extracted this data from Sherpa Romeo to help researchers understand the access level of this journal in accordance with the Sherpa Romeo Archiving Policy for Journal of Non-Newtonian Fluid Mechanics. The table below indicates the level of access a journal has as per Sherpa Romeo's archiving policy.

RoMEO Colour	Archiving policy
Green	Can archive pre-print and post-print or publisher's version/PDF
Blue	Can archive post-print (ie final draft post-refereeing) or publisher's version/PDF
Yellow	Can archive pre-print (ie pre-refereeing)
White	Archiving not formally supported

FYI:

Pre-prints as being the version of the paper before peer review and
Post-prints as being the version of the paper after peer-review, with revisions having been made.

14. What are the most common citation types In Journal of Non-Newtonian Fluid Mechanics?

The 5 most common citation types in order of usage for Journal of Non-Newtonian Fluid Mechanics are:.

S. No.	Citation Style Type
1.	Author Year
2.	Numbered
3.	Numbered (Superscripted)
4.	Author Year (Cited Pages)
5.	Footnote

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Journal of Non-Newtonian Fluid Mechanics — Template for authors

Related Journals

Journal Performance & Insights

CiteRatio

SCImago Journal Rank (SJR)

Source Normalized Impact per Paper (SNIP)

4.2

0.873

1.301

Insights

Insights

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Journal of Non-Newtonian Fluid Mechanics

Journal of Non-Newtonian Fluid Mechanics

Top papers written in this journal

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Abstract:

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What to expect from SciSpace?

Speed and accuracy over MS Word

Plagiarism Reports via Turnitin

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Frequently asked questions

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No word template required

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Trusted by academicians

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