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

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Journal, September/October 2008, Vol.7.No.5, 537- 546. Gielen,D; Tam,C. 2006. “ Energy Use, Technologies and CO2 Emission in the Pulp and Paper Industry” WBCSD, IEA, Paris, 9 October 2006. Green, R.P., and G. Hough, 1992,. “Chemical Recovery in The Alkaline Pulping Processes”, Third edition, Tappi Press, Atlanta, Hayashi, D., Krey, M., CO2 .2005. Emission Reduction Potential of Large Scale Efficiency Energy Measures in Heavy Industry in China, India, Brazil, Indonesia, and South Africa, HWWI Research Paper No. 6, Hamburg. Johan Gullichsen, Hannu Paulapuro., 1998., “Papermaking Science and Technology”, Published in cooperation with the Finnish Paper Engineers' Association and TAPPI, Helsinki Kilponen, L., P. Ahtila., J. Parpala., Matti Pihko., 2000,. “Improvement of Pulp Mill Energy Efficiency in An Integrated Pulp and Paper Mill”, Publication of the Laboratory of Energy Economics and Power Plant Engineering, Helsinki University of Technology. Kocurek, M.J., 1989., “Pulp and Paper Manufacture, Vol. 5: Alkaline Pulping”, Joint Textbook Committee of The Paper Industry. Kramer K.J., et al, 2009. Energy Efficiency Improvement and Cost Saving Opportunities for the Pulp and Paper Industry, Berkeley Lab University of California, Berkeley. Kraristya. 2004. Teknologi digester. kharistya.wordpress.com Lawrence, E.O., 2009., “Energy efficiency Improvement and Cost Saving opportunities for the Pulp and Paper Page 115 of 132
Industry”, Environmental Energy Technologies Division, US Environmental Protection Agency. Miner, R., Garcia, J.P. 2007. The Greenhouse Gas and Carbon Profile of the Global Forest Products Industry, NCASI Special Report No. 07-02. NCASI-IFC, 2009. A Calculation Tool for Characterizing the Emission from the Forest Products Value Chain, Including Forest Carbon. NCASI, 2005. Calculation Tools for Estimating Greenhouse Gas Emission from Pulp and paper Mills. Research Triangle Park.NC.USA. Noel de Nevers. 2000. Air Pollution Control Engineering, 2 nd Ed., McGraw-Hill International Edition. Ohman, F., H. Theliander., 2007., Filtration Preperties of Lignin Precipitated from Black Liquor, Tappi Journal, Vol. 6 No. 7. Paramsothy, 2004. Optimizing Hydrolysis/Acidogenesis Anaerobic Reactor With TheApplication of Microbial Reaction Kinetic. University of Peradeniya. Tropical Agricultural Research Vol 16: 327-338. Ray, B.K., Reddy, B.S., 2008. Understanding Industrial Energy Use, Indira Gandhi Institute, Mumbai. Smith. A., et al. 2001. Waste Management Options and Climate Change. AEA Technology. Abingdon. Smook, G.A., “Handbook for Pulp dan Paper Technologists”, Joint Textbook Committee of the Paper Industry. Springer, Allan. 1993., Pollution Control for Pulp and Paper Industry, McGraw-Hill International Edition. Stultz, S.C., and J.B. Kitto., 2000., “Steam / Its Generation and Use”, The Babcock & Wilcox Company. Page 116 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
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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
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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 and 276: Some processes that can save energy
Page 277: REFERENCES Adams, Terry N., 1997,.
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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