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  <front>
    <journal-meta />
    <article-meta>
      <title-group>
        <article-title>APMP: an alternative for Packaging Industry</article-title>
      </title-group>
      <contrib-group>
        <contrib contrib-type="author">
          <string-name>Omid Ramezani</string-name>
          <email>O_Ramezani@sbu.ac.ir</email>
          <xref ref-type="aff" rid="aff0">0</xref>
        </contrib>
        <contrib contrib-type="author">
          <string-name>Hossein Kermanian</string-name>
          <xref ref-type="aff" rid="aff0">0</xref>
        </contrib>
        <contrib contrib-type="author">
          <string-name>Mohammad Angoraj Taghavi</string-name>
          <xref ref-type="aff" rid="aff1">1</xref>
        </contrib>
        <aff id="aff0">
          <label>0</label>
          <institution>Department of Cellulose and Paper Technology, Faculty of New Technologies and Energy, Zirab Science and Technology Park, Shahid Beheshti University</institution>
          ,
          <addr-line>Zirab, Savadkoh, Mazandaran</addr-line>
          ,
          <country country="IR">Iran</country>
        </aff>
        <aff id="aff1">
          <label>1</label>
          <institution>Pulping Division, Atrak Paper Manufacturing Company</institution>
          ,
          <addr-line>Isfahan, Iran</addr-line>
          ,
          <institution>Former Address: APMP Pulping Division, Maragheh Paper Industries Company</institution>
          ,
          <addr-line>Maragheh, East Azarbayejan</addr-line>
          ,
          <country country="IR">Iran</country>
        </aff>
      </contrib-group>
      <fpage>499</fpage>
      <lpage>506</lpage>
      <abstract>
        <p>APMP process has been conventionally used to produce writing and printing papers. Maragheh Paper Industries Company (MPIC) was first company in Iran which started producing alkaline peroxide mechanical pulp (APMP) on a new Andritz 50000 tones/year at its mill in Maragheh city followed by establishment of another 50000 tones/year in Kermanshah city, Iran. Due to lack of required chemicals for the process including H2O2, Sodium Silicates, DTPA and Magnesium Sulfate and the subsequent high production costs mill trials were performed to examine the suitability of APMP process for producing packaging paperboards for which only alkaline addition is adequate. Different ranges of Alkali dosage were experimented and the resulted pulps were both evaluated online using FiberScan System supplied by Andritz and the laboratory tests. The results from this investigation demonstrated that APMP can be utilized as an alternative to produce standard quality packaging pulp and paper other than the printing purposes using less production costs.</p>
      </abstract>
      <kwd-group>
        <kwd>Pulp and Paper Industry</kwd>
        <kwd>APMP</kwd>
        <kwd>Packaging Papers</kwd>
        <kwd>Bleaching</kwd>
        <kwd>Strength Properties</kwd>
      </kwd-group>
    </article-meta>
  </front>
  <body>
    <sec id="sec-1">
      <title>1 Introduction</title>
      <p>
        Pulp and Paper industry is changing rapidly; environmental concerns will be the big
issue of the new developing industrial generation focusing on paper recycling and
new pulping and bleaching technologies. NSSC pulp produced from a wide selection
of raw material has been traditionally used to supply the fluting paperboard used in
the packaging industry thanks to special strength properties in the end product RCT
and CMT supported by extensive literatures published (
        <xref ref-type="bibr" rid="ref1 ref2 ref3 ref4 ref5 ref6 ref7 ref8 ref9">1-9</xref>
        ). Environmental issues
towards sulfur-free processes (
        <xref ref-type="bibr" rid="ref10 ref11">10- 11</xref>
        ) have been the driving force for replacement of
neutral sulfite semi-chemical pulps with recycled (
        <xref ref-type="bibr" rid="ref12 ref13 ref14">12-14</xref>
        ) and mechanical pulps
(15Copyright ©by the paper’s authors. Copying permitted only for private and academic purposes.
19) in the packaging industry and the recent fiber analysis have confirmed this
altering trend (
        <xref ref-type="bibr" rid="ref20 ref21">20-21</xref>
        ). In Iran, the recycling fibers, however, do not meet the quality
specifications required for the packaging industry and particularly the corrugating
medium especially in the small papermaking mills because of the lack of certain wet
end chemistry strategy and not economically compromising the use of different
chemicals.
      </p>
      <p>
        The APMP process was first introduced at the 1989 International Mechanical
Pulping Conference (
        <xref ref-type="bibr" rid="ref22">22</xref>
        ). Since then, a number of studies have been reported from
the Andritz Pilot Plant in Springfield, Ohio on the characteristics of the APMP
process, on how it compares to CTMP and pre-bleached CTMP, and on its
application to various wood species (
        <xref ref-type="bibr" rid="ref23 ref24 ref25 ref26">23-26</xref>
        ).
      </p>
      <p>Generally, APMP is used most favorably for two special areas in high-yield
pulping. One area involves high-brightness pulp grades when peroxide bleaching is
necessary. The other involves a specific hardwood species for which caustic
pretreatment is needed to reduce energy consumption and, more importantly, to
obtain acceptable pulp strength. Alkaline Peroxide Pulping is conventionally used to
produce writing and printing grades, but because of high Lignin content and the
physical properties, the end product might have some applications in the packaging
papers.</p>
      <p>In the area of achieving high brightness with peroxide bleaching, a certain amount
of sodium hydroxide has to be applied. In the APMP process, both sodium hydroxide
(NaOH) and hydrogen peroxide (H2O2) are applied prior to refining. Not only does
the sodium hydroxide function as a necessary component of bleaching reagents, but it
also softens the fibers. As a result, the refining energy is reduced, and the pulp is
improved by having greater strength and lower shive content. In this way, the
chemical potential of sodium hydroxide is realized more fully, and the long fiber
content is better preserved.</p>
      <p>The APMP process, like conventional CMP or CTMP, consists of two primary
components—impregnation and refining. During the impregnation stage, chips are
steamed, pressed, chemically impregnated, and retained in the reaction bin to allow
the chemical reactions to run to completion. Fiberization and fibrillation are
completed with conventional atmospheric refining. The key to the success of any
APMP process lies in chip impregnation. The goal at the impregnation stage is to
achieve the best efficiency with the chemicals used. These chemicals include not
only caustic and peroxide chemicals but stabilizers including DTPA, Sodium Silicate
and Magnesium Sulfate (Epsom salt). The optimization of the conditions depends on
the wood species and the requirements for pulp quality. Careful selection of species
ensures the high brightness product unless reaching to the target brightness is not
feasible.</p>
      <p>Two APMP pulp mills were delivered to Iran by Andritz AG, Vienna, Austria to
Gharb Paper Industries (GPIC), Bakhtaran Province and Maragheh Paper Industries
(MPIC), Azarbayejan Province with the production capacity of 50000 ton/year from
which the latter was successfully started up in 2006. The mill has been designed to
produce writing and printing grades. The mill process variables have been
customized for two local selected species i.e. Populus alba and Populus nigra. Soon
after the start-up and commissioning of the factory, use of other various Populus
species and hardwoods other than the above mentioned ones became indispensible
due to the lack of industrial plantation which high variation in the brightness level
affected the market demand for the final product. Moreover, lack of an industrial
production plant for any of the chemicals used (except Sodium Hydroxide) escalated
the shipping and handling problems increasing the production costs. This paper
reports the mill trials carried out in MPIC to modify the process for the production of
corrugating medium.
2</p>
    </sec>
    <sec id="sec-2">
      <title>Materials and Methods</title>
      <p>A mixture of Populus species including P. alba, P. nigra, P. euroamerican and P.
deltoids chips was selected to supply the pulp mill. No certain selection for the
Populus alba and Populus nigra applied as the pulp mill was designed for. PulpExpert
PEX131 supplied by Andritz, recorded the results of the process modification on the
strength properties excluding RCT and CMT which were determined separately
according to Tappi standards. The target was to reach to minimum requirements for
the corrugating medium as specified by the institute of standards and industrial
research of Iran, ISRI number 3488 (table 1).
The standard consumption of chemicals in MPIC formulated by Andritz AG is
presented in table 2.</p>
      <p>The main objective was the production of a modified refiner mechanical pulp with
solely NaOH usage. According to the standard consumption of chemicals, two pulp
mill trials with the presence of bleaching-enhancing chemicals and without the
bleaching-enhancing chemicals keeping constant the other production variables were
studied. The results determined by PulpExpert PEX131 and laboratory measurements
are demonstrated in table 3.</p>
      <sec id="sec-2-1">
        <title>Analysis</title>
        <sec id="sec-2-1-1">
          <title>Freeness</title>
        </sec>
      </sec>
      <sec id="sec-2-2">
        <title>Treatmen t</title>
        <p>ml, cs</p>
        <sec id="sec-2-2-1">
          <title>Air Resistance</title>
        </sec>
        <sec id="sec-2-2-2">
          <title>Gurley, s</title>
        </sec>
        <sec id="sec-2-2-3">
          <title>Burst Index Kpa.m2/g</title>
        </sec>
        <sec id="sec-2-2-4">
          <title>Tear Index mN.m2/g</title>
        </sec>
        <sec id="sec-2-2-5">
          <title>Tensile Index stretch TEA</title>
        </sec>
        <sec id="sec-2-2-6">
          <title>Ring Crush</title>
        </sec>
        <sec id="sec-2-2-7">
          <title>Test</title>
        </sec>
        <sec id="sec-2-2-8">
          <title>Concora</title>
        </sec>
        <sec id="sec-2-2-9">
          <title>Medium Test</title>
        </sec>
        <sec id="sec-2-2-10">
          <title>Scattering</title>
        </sec>
        <sec id="sec-2-2-11">
          <title>Coefficient</title>
        </sec>
        <sec id="sec-2-2-12">
          <title>Brightness</title>
        </sec>
        <sec id="sec-2-2-13">
          <title>Specific</title>
        </sec>
        <sec id="sec-2-2-14">
          <title>Energy</title>
          <p>N.m/g</p>
          <p>%
J/m2
(N)
(N)
Cm2/g
T 525, %
(KWh/AD</p>
          <p>MT)</p>
          <p>56
(Kg/AD
MT)</p>
          <p>75
(Standa
rd)</p>
          <p>86
(Kg/AD</p>
          <p>MT)
236
50
1.08
3.22
28.2
1.13
13
116
170
613
39
1200
236
38
2.06
4.49
48.5
1.45
27
119
180
533
37.8
1100
202
35
2.87
5.06
64.3
2.12
53
145
210
407
35
950</p>
          <p>As indicated in table 3, presence of bleaching-enhancing chemicals affected slight
improvement in the physical and mechanical properties of the pulp. The authors
failed to find evidence explaining this effect, however, coagulation effect of chelating
agents for extractives, metal ions and other contaminants should increase the
effectiveness of sodium hydroxide functionality to soften the fibers and subsequently
preserve the long fiber content. Also, table 3 suggests that removing the
bleachingenhancing chemicals diminishes some physical and mechanical properties below the
required range outlined in the Iranian corrugating standard (table 1). In order to
compensate the inferior physical properties and to clarify the alkali charge effect, two
alkaline dosage ranges, 56 and 86 Kg/ADMT were corresponded to standard alkaline
dosage of 75 Kg/ADMT (table 4).</p>
          <p>Reduction of alkaline charge in no-bleaching-enhancing chemical treatment to 56
Kg/ADMT deteriorated the pulp properties far below the standard specifications with
the increase in specific energy consumption corresponding to 1200 KWh/ADMT.
Charge of 86 Kg/ADMT alkaline improved the physical properties and reduced
specific energy consumption to 950 (KWh/ADMT).</p>
          <p>A comparison of paper properties between the two packaging papers produced in
MPIC and Mazandaran Wood and Paper Company is shown in fig 1. As evident from
the figure, the properties of paperboard produced in MPIC are almost identical or
superior to the properties of the corrugating medium produced in Mazandaran Wood
and Paper Company.</p>
        </sec>
      </sec>
    </sec>
    <sec id="sec-3">
      <title>Conclusion</title>
      <p>The results from this investigation demonstrated that APMP can be utilized as an
alternative to produce standard quality packaging pulp and paper other than the
printing purposes using less production costs and with properties comparable to the
packaging paperboard of Mazandaran Wood and Paper Company.
Acknowledgments. The authors would like to thank Maragheh Paper Industries
Company for the kind support in the production trials.</p>
    </sec>
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