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    <title>NOPR Collection:</title>
    <link>http://nopr.niscpr.res.in/handle/123456789/22589</link>
    <description />
    <pubDate>Sun, 11 Oct 2026 12:10:59 GMT</pubDate>
    <dc:date>2026-10-11T12:10:59Z</dc:date>
    <item>
      <title>Entroenthalpics: New model for solving solubility problem of high molecular weight biocompatible PVP macromolecules</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/22638</link>
      <description>Title: Entroenthalpics: New model for solving solubility problem of high molecular weight biocompatible PVP macromolecules
Authors: Goela, Kamna; Singh, Man
Abstract: PVP&#xD;
of 10,000; 29,000; 40,000 and 55,000 g/mol of their 0.001, 0.003, 0.005, 0.007&#xD;
and 0.009 mass fractions separately were solubilized in water at &lt;i&gt;T &lt;/i&gt;=&#xD;
(293.15, 298.15, 303.15 and 308.15) K at an interval of 50 C temperature. The&#xD;
solubility has been a primary parameter for preparing their mixtures with water&#xD;
for industrial applications. Since, solubility and physicochemical properties&#xD;
(PCP) are closely associated for useful formulations. Thus, in the present work&#xD;
their densities, viscosities, surface tension, sound velocity, refractive index&#xD;
and UV absorption study are reported. The density increases by 0.04 % with an&#xD;
increase in mass fraction by 0.002, irrespective of the molecular weights of&#xD;
PVP. In general, on increasing the concentration of PVP; the&#xD;
&#xD;
increase&#xD;
in viscosity is 1.44; 2.67; 3.69 and 3.81 % at &lt;i&gt;T &lt;/i&gt;= (293.15 to 308.15) K,&#xD;
respectively. Analysis of UV absorption reveals the stabilization at 220 nm for&#xD;
PVP 10,000 and the absorption maxima is less than PVP 10,000 by 0.468. At an&#xD;
arbitrary point 1.5 on absorbance scale the wavelength is being narrowed down&#xD;
by 21, 11, 9, and 9 nm with an increase in molecular weights, reveals that UV&#xD;
light is unable to influence interacting behaviour of PVP higher molecular&#xD;
weights.
Page(s): 648-654</description>
      <pubDate>Fri, 01 Nov 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/22638</guid>
      <dc:date>2013-11-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Dynamic Mergers Drive Industrial Competition Evolution: A Network Analysis Perspective</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/22637</link>
      <description>Title: Dynamic Mergers Drive Industrial Competition Evolution: A Network Analysis Perspective
Authors: Hou, Rui; Yang, Jianmei; Yao, Canzhong
Abstract: This&#xD;
paper presents a novel method to explore the relationship between dynamic&#xD;
mergers and evolution of industrial competition by introducing complex network&#xD;
tool. Taking the beer industry of China as an example, we establish&#xD;
Markets-Firms bipartite time series networks, weighted Markets-Firms time&#xD;
series networks and industrial competition time series networks by using the&#xD;
data from 1992 to 2009 respectively. Through analyzing the changes of topology&#xD;
index on these networks, we find that dynamic mergers play a key important role&#xD;
in the evolution process of industrial competition. The results show that&#xD;
dynamic mergers promote the local fragmented submarkets to be consolidated into&#xD;
a global market for this industry, and they also show the evolution process&#xD;
that competitive relationship among rivals turns from local segmented markets&#xD;
to a global cross-market gradually. In this paper, we provide a new view to&#xD;
observe the changes of industrial competition relationship driven by dynamic mergers.
Page(s): 635-647</description>
      <pubDate>Fri, 01 Nov 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/22637</guid>
      <dc:date>2013-11-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Bioprocess for semi-industrial production of immunomodulator polysaccharide Pleuran by &lt;i&gt;Pleurotus ostreatus &lt;/i&gt;in submerged culture</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/22636</link>
      <description>Title: Bioprocess for semi-industrial production of immunomodulator polysaccharide Pleuran by &lt;i&gt;Pleurotus ostreatus &lt;/i&gt;in submerged culture
Authors: Maftoun, Parisa; Malek, Roslinda; Abdel-Sadek, Mahmoud; Aziz, Ramlan; Enshasy, Hesham El
Abstract: Pleuran,&#xD;
is a polysaccharide belongs to glucan group which made of D-glucose moieties&#xD;
linked with (1→3)-&lt;img src='/image/spc_char/beta.gif' border=0&gt;&#xD;
and (1→6)-&lt;img src='/image/spc_char/beta.gif' border=0&gt;&#xD;
glycosidic linkages. The importance of this compound is based on its wide&#xD;
biotherapeutic application as immunomodulator and anticancer polysaccharide.&#xD;
This compound is produced only naturally using specific type of mushroom named &lt;i&gt;Pleurotus&#xD;
ostreatus. &lt;/i&gt;Traditionally, this type of mushroom was cultivated using solid&#xD;
state cultivation system in green houses. Nowadays, submerged cultivation is&#xD;
considered as alternative cultivation strategy for mushroom based on its many&#xD;
advantages such as: short cultivation time, high yield, fully controlled&#xD;
cultivation condition, and fewer steps in polysaccharide extraction and purification&#xD;
compared to solid state fermentation. Thus, the present work was focused on the&#xD;
development of pleuran production process in semi-industrial scale using&#xD;
submerged cultivation system. At first, high yield production medium was&#xD;
&#xD;
selected&#xD;
followed by study on the kinetics of cell growth and EPS production in shake&#xD;
flasks. Second, cultivations were conducted in semi-industrial scale using &lt;i&gt;in&#xD;
situ &lt;/i&gt;sterilizable 16-L stirred tank bioreactor under controlled and&#xD;
uncontrolled pH conditions. The results showed that bioreactor cultivation&#xD;
under controlled pH condition improved EPS production process and the maximal&#xD;
volumetric and specific pleuran produced in this study were 1.98 g/L and 0.445&#xD;
g/g, respectively.&#xD;
&#xD;
&lt;/span&gt;&lt;/span&gt;
Page(s): 655-662</description>
      <pubDate>Fri, 01 Nov 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/22636</guid>
      <dc:date>2013-11-01T00:00:00Z</dc:date>
    </item>
    <item>
      <title>Textiles industrial water footprint: methodology and study</title>
      <link>http://nopr.niscpr.res.in/handle/123456789/22635</link>
      <description>Title: Textiles industrial water footprint: methodology and study
Authors: Wang, Laili; Ding, Xuemei; Wu, Xiongying; Yu, Jianming
Abstract: The&#xD;
concept of water footprint (WF) is an important breakthrough in the evolving of&#xD;
methodologies, approaches and indicators for measuring freshwater appropriation&#xD;
and assessing the wastewater discharge. Industrial water footprint (IWF)&#xD;
methodology, which concentrates on the industrial production stages, can&#xD;
present a clear graphic of freshwater consumption and impacts caused by&#xD;
wastewater discharge at both product and technology level. In this paper, IWFs&#xD;
of seven kinds of knitted fabrics were calculated through field survey and&#xD;
referred to published literatures. These case studies revealed that the&#xD;
majority of the IWFs were caused by grey industrial water footprints, the&#xD;
volume of water required to dilute pollutants. Dyeing, bleaching and washing&#xD;
were freshwater intensive technologies. Generally this may be one of the&#xD;
typical features of dyed and finished fabrics. It is meaningful to reduce the&#xD;
freshwater consumption of the hot-spots through the improvement of freshwater&#xD;
management pattern and production techniques. Specific recommendations for&#xD;
further research in this field were also proposed in this study accordingly.
Page(s): 710-715</description>
      <pubDate>Fri, 01 Nov 2013 00:00:00 GMT</pubDate>
      <guid isPermaLink="false">http://nopr.niscpr.res.in/handle/123456789/22635</guid>
      <dc:date>2013-11-01T00:00:00Z</dc:date>
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