Bilingual Tech Mapping for Pulp Paper Guideline - Asosiasi Pulp ...

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and the extent to which can potentially generate carbon emission and opportunities can be utilized as an energy source. Wastewater management in the pulp and paper industry using an anaerobic process technology that features a gas container for energy-efficient technology and environmentally friendly. Management of solid waste by landfill, incineration, composting and anaerobic digestion in general all of these alternatives can be applied in accordance with the characteristics of the waste to be treated with the terms fitted gas emission control to be used. Thus, to reduce gas emission into atmosphere. Page 113 of 132
REFERENCES Adams, Terry N., 1997,. “Kraft Recovery Boilers”, Tappi Press, Atlanta. APPI, 2008. Executive Summary of APP‟s Carbon Footprint Assessment. Environmental resources management. Bernstein, L., Roy, J., 2007. Fourth Assesment Report of IPCC of Working Group 3, Cambridge University Press. Borman, G.L., Ragland K.W., 1998,. “Combustion Engineering”, McGraw-Hill, Singapore,Brunner. Calvin R. 1994. Hazardous Waste Incineration. 2 nd Ed.. McGraw-Hill International Edition. Buku Pegangan Manajer Pengendalian Pencemaran Udara. Badan Pengendalian Lingkungan hidup Daerah Provinsi Jawa Barat CEPI. 2009. Transport Carbon Footprint – Assesment Guidelines. Brussels CEPI. 2007. Europian Paper Industry Develops Carbon Footprint Framework for Paper and Board. Bussels. Cici. Mehmet . 1968. Energy Consumption and Air Pollution in the manufacture of Pulp and Paper. Erc.Univ. Fen Bil. Derg.. 4. 1-2. 646 – 656. DoE. 2005. Energy and Environmental Profile of the US Pulp and Paper Industry. US Department of Energy. Elizabeth C.P.. paul N. C. 1981. Biogas production and utilization. Ann Arbor Science publishers Inc. Eriksson. E. Striple, H., Karlsson, P.E., 2009. Executive Summary for Billerud Carbon Footprint, Svenska Miljoinstitutet, Stockholm. Gavrilescu, D. 2008. “Energy from Biomass in Pulp and Paper” Environmental Engineering and Management Page 114 of 132
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KEMENTERIAN PERINDUSTRIAN BALAI BES
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PEDOMAN PEMETAAN TEKNOLOGI DI INDUS
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RINGKASAN EKSEKUTIF Perkembangan pe
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delignifikasi berlanjut (extended d
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potensi untuk dimanfaatkan. Atas da
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3.4. Optimasi kinerja Chemical Reco
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DAFTAR GAMBAR Gambar 1.1. Prediksi
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Tabel 3.1 Konservasi energi pada pe
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umi naik 0,5 o C, angka ini akan na
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kertas, industri tekstil, indusri k
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Gambar 1.1 Prediksi Emisi GRK di In
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tahun 2009, perusahaan industri pul
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pulp dan kertas dibandingkan dengan
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Tabel 1.8 Rincian Besaran Emisi Kar
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Pada pembuatan pulp mekanis lignin
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Gambar 2.1 Diagram Proses Pabrik Pu
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(misalnya, dissolving, non-kayu). P
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meningkatkan kandungan padatannya m
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Kondensat Recovery boiler Panas sek
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dari proses pemulihan kembali bahan
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Gambar 2.5 Distribusi Konsumsi Ener
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2.3.1 Pengelolaan Limbah cair Ditin
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Teknologi pengelolaan melalui peman
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BAB III TEKNOLOGI PROSES PULPING HE
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Tabel 3.1 Konservasi energi pada pe
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Gambar 3.2 Dimensi tumpukan serpih
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Gambar 3.4 Ringkasan berbagai siklu
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yang selanjutnya disimpan dalam hot
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Gambar 3.6 Digester kontinyu dengan
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Ringkasan konservasi energi pada pa
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wash master. Dilution factor sekita
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Tabel 3.4 Konservasi energi pada si
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3.5 Optimasi kinerja Power Boiler b
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Tabel 3.5.Konservasi energi pada si
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Konservasi energi lain yang dapat d
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4.1.2 Mesin Kertas : Bagian Pembent
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ditingkatkan dari 15 % menjadi 60 -
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Tabel 4.1 Perbandingan Kinerja Tekn
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Tabel 4.2 Peluang Penghematan Energ
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Tabel 4.4 Sumber Emisi Karbon pada
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BAB V PENGELOLAAN LINGKUNGAN PADA I
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diutamakan untuk mengolah air limba
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Untuk mengoptimalkan dan mendistrib
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5.1.2 Pengembangan Teknologi Anaero
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merupakan sumber karbon yang berkon
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Gambar 5.1 Fase-Fase Pada Tahapan P
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memasang peralatan seperti turbin,
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5.2.2.1.a. Rotary Kiln Incinerator
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Di Indonesia, penerapan insinerator
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mikroba termofilik. Pada suhu di at
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5.2.3.1.b. Proses pengomposon siste
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zat organik telah dipertimbangkan s
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Gambar 5.8 Digestasi Anaerobik Satu
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meningkatkan produktivitas berbagai
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menyebabkan terjadinya pencemaran u
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Gambar 5.10. (A). Cyclone dan Multi
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Gambar 5.12. Electrostatic Precipit
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disemprotkan dan mengalir ke bawah
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Counter Current Packed Tower Bubble
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Metode FGD Metode Kering Absorben R
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NOx yang terbentuk sebagai hasil pe
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Metoda Non selective catalytic redu
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BAB VI PENUTUP Indonesia ikut berpe
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Teknologi pengelolaan lingkungan me
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Gavrilescu, D. 2008. “Energy from
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Stultz, S.C., and J.B. Kitto., 2000
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No Company Name APPENDIX 1 DISTRIBU
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LANJUTAN No Company Name Mill Site
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LANJUTAN No Company Name Mill Site
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APPENDIX 2 PAPER CONSUMPTION IN VAR
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APPENDIX 2 (continuation) Country C
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Coated wood-free paper - integrated
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APPENDIX 4 ENERGY CONSUMPTION FOR U
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MINISTRY OF INDUSTRY CENTER FOR PUL
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TECHNOLOGY MAPPING GUIDELINE FOR PU
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EXECUTIVE SUMMARY The development o
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pulp bleaching done by adding a hea
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device SOx and NOx and also control
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3.3 Application Washing Technologie
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Figure 3.7 Black Liquor Impregnatio
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Table 3.5 Conservation Of Energy In
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15% CH4, CFCs by 12% and 4% N2O, an
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governments and stakeholders as a b
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Figure 1.1 Forecast of GHG Emission
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paper industry in Indonesia are 81
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Table 1.5 Specific Energy Consumpti
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Table 1.8 Details of Carbon Emissio
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have a good opacity, and easy to ab
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Figure 2.1 Process Diagram of Kraft
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Kraft pulping process using alkalin
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urned, and Na2SO4 reduced to Na2S.
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Kondensat Recovery boiler Secondary
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Pulp mills in Indonesia fulfill the
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The main energy source used in the
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alkaline pH, high contamination COD
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will be generated carbon emission s
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CHAPTER III PULPING TECHNOLOGY FOR
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Table 3.1 Conservation Of Energy In
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Figure 3.1 Mechanism of chip damage
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Figure 3.3 Cycle Of Displacement Ba
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Figure 3.5 System RDH equipment / S
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With a uniform temperature througho
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Table 3.2 Conservation Of Energy in
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3.3 Application Washing Technologie
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Udara kuaterner Udara sekunder ting
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sootblowing intelligent sootblowing
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Figure 3.11 FBC and CFBC Page 52 of
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Other energy conservation can be do
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process of separating water from th
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facilities. For the hood that uses
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4.2 Saving Energy and Carbon Emissi
Page 225 and 226: Table 4.3 Best 2009 World Energy In
Page 227 and 228: Table 4.5 Overview of Investment Fo
Page 229 and 230: chemistry, and biology process or a
Page 231 and 232: ii. b. Anaerobic System Anaerobic p
Page 233 and 234: experience growth to form granular
Page 235 and 236: Table 5.1. Sources and Types of Sol
Page 237 and 238: There are several solid waste manag
Page 239 and 240: technology development is equipped
Page 241 and 242: esulting energy for steam productio
Page 243 and 244: With this system, the fluidization
Page 245 and 246: In the composting process temperatu
Page 247 and 248: closed system requires an investmen
Page 249 and 250: generally composed of CH 4 55-70%;
Page 251 and 252: Figure 5.8 Anaerobic Digestion One
Page 253 and 254: Figure 5.9 Flowchart of Two Phase A
Page 255 and 256: Table 5.4 Sources and Characteristi
Page 257 and 258: 5.3.2.1 Separation of Particulate P
Page 259 and 260: ). Filter Cloth (Fabric Filter) The
Page 261 and 262: time. Separation of pollutants carr
Page 263 and 264: Figure 5.14 Packed Tower Scrubber B
Page 265 and 266: C. SOx Gas Control SOx gases can be
Page 267 and 268: Type of FGD Method Dry Method Absor
Page 269 and 270: D. NOx Gas Control NOx emission can
Page 271 and 272: Method Selective non catalytic redu
Page 273 and 274: incoming gas fan. To avoid the risk
Page 275: Some processes that can save energy
Page 279 and 280: Industry”, Environmental Energy T
Page 281 and 282: _____EPA, 2010. “Available and Em
Page 283 and 284: CONTINUE No Company Name Mill Site
Page 289 and 290: APPENDIX 2 (continuation) Consumpti
Page 291 and 292: APPENDIX 3 SPECIFIC ENERGY CONSUMPT
Page 293 and 294: Source : all data taken from [249,
Page 295: APENDIX 4 GHG EMISSION FROM VARIOUS
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