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

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APPENDIX 4 ENERGY CONSUMPTION FOR UTILITY IN THE MILL GENERALLY Energy Process/Activities Consumption (kWh/t) Description Biological Effluent Treatment Using pump, agitator, and aeration. Mechanical + aerobic 4 – 8 Biogas product and utilization not Mechanical + aerobic/anaerobic (biogas not considered) Mechanical + aerobic/anaerobic (biogas considered) 5 – 10 Surplus 20 – 15 considered. Energy balance by using biogas (waste water treatment of recycled fiber industry produce around 25 kWh/t) Raw Water Treatment 2 – 5 Using raw water pump and preparation Pressurized Air 20 – 30 Using compressor and air-dryer Work Transportation 1 – 2 Using Forklift and Industrial Truck Finishing (Without packaging) 10 – 40 Using rewinder, broke pulping, including packaging line Administration NA ( 1 (1) NA : Not Available ) Not Considered (<strong>for</strong> office, canteen, etc.) Source : PTS, Examination studies: Energy optimization in European mills (not published), Munich 2004 to 2007 unpublished from [249, Blum et al. 2007] Halaman 130 dari 131
GHG EMISSION FROM VARIOUS COUNTRIES No. Country MtCO2 equivalent % from World GHG 1. USA 6928 20,6 2. China 4938 14,7 3. EU-25 4725 14 4. Russia 1915 5,7 5. India 1884 5,6 6. Japan 1317 3.9 7. Germany 1009 3 8. Brazil 851 2,5 9. Canada 680 2 10. UK 654 1,9 11. Italy 531 1,6 12. South Korea 521 1,5 13. French 513 1,5 14. Mexico 512 1,5 15. Indonesia 503 1,5 16. Australia 491 1,5 17. Ukraine 482 1,4 18. Iran 480 1,4 19. South Africa 417 1,2 20. Spain 381 1,1 21. Poland 381 1,1 22. Turk 355 1.1 23. Arab Saudi 341 1 24. Argentina 289 0,9 25. Pakistan 285 0,8 Top 25 27915 83 Rest of World 5751 17 Developed Countries 17355 52 Developing Countries 16310 48 Notes: Data year 2000. Total emission not included fuel and the changing of land and <strong>for</strong>est usage Halaman 131 dari 131
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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,
Page 96 and 97: 5.2.2.1.a. Rotary Kiln Incinerator
Page 98 and 99: Di Indonesia, penerapan insinerator
Page 100 and 101: mikroba termofilik. Pada suhu di at
Page 102 and 103: 5.2.3.1.b. Proses pengomposon siste
Page 104 and 105: zat organik telah dipertimbangkan s
Page 106 and 107: Gambar 5.8 Digestasi Anaerobik Satu
Page 108 and 109: meningkatkan produktivitas berbagai
Page 110 and 111: menyebabkan terjadinya pencemaran u
Page 112 and 113: Gambar 5.10. (A). Cyclone dan Multi
Page 114 and 115: Gambar 5.12. Electrostatic Precipit
Page 116 and 117: disemprotkan dan mengalir ke bawah
Page 118 and 119: Counter Current Packed Tower Bubble
Page 120 and 121: Metode FGD Metode Kering Absorben R
Page 122 and 123: NOx yang terbentuk sebagai hasil pe
Page 124 and 125: Metoda Non selective catalytic redu
Page 126 and 127: BAB VI PENUTUP Indonesia ikut berpe
Page 128 and 129: Teknologi pengelolaan lingkungan me
Page 130 and 131: Gavrilescu, D. 2008. “Energy from
Page 132 and 133: Stultz, S.C., and J.B. Kitto., 2000
Page 134 and 135: No Company Name APPENDIX 1 DISTRIBU
Page 136 and 137: LANJUTAN No Company Name Mill Site
Page 138 and 139: LANJUTAN No Company Name Mill Site
Page 140 and 141: APPENDIX 2 PAPER CONSUMPTION IN VAR
Page 142 and 143: APPENDIX 2 (continuation) Country C
Page 144 and 145: Coated wood-free paper - integrated
Page 149 and 150: MINISTRY OF INDUSTRY CENTER FOR PUL
Page 151 and 152: TECHNOLOGY MAPPING GUIDELINE FOR PU
Page 153 and 154: EXECUTIVE SUMMARY The development o
Page 155 and 156: pulp bleaching done by adding a hea
Page 157 and 158: device SOx and NOx and also control
Page 159 and 160: 3.3 Application Washing Technologie
Page 161 and 162: Figure 3.7 Black Liquor Impregnatio
Page 163 and 164: Table 3.5 Conservation Of Energy In
Page 165 and 166: 15% CH4, CFCs by 12% and 4% N2O, an
Page 167 and 168: governments and stakeholders as a b
Page 169 and 170: Figure 1.1 Forecast of GHG Emission
Page 171 and 172: paper industry in Indonesia are 81
Page 173 and 174: Table 1.5 Specific Energy Consumpti
Page 175 and 176: Table 1.8 Details of Carbon Emissio
Page 177 and 178: have a good opacity, and easy to ab
Page 179 and 180: Figure 2.1 Process Diagram of Kraft
Page 181 and 182: Kraft pulping process using alkalin
Page 183 and 184: urned, and Na2SO4 reduced to Na2S.
Page 185 and 186: Kondensat Recovery boiler Secondary
Page 187 and 188: Pulp mills in Indonesia fulfill the
Page 189 and 190: The main energy source used in the
Page 191 and 192: alkaline pH, high contamination COD
Page 193 and 194: will be generated carbon emission s
Page 195 and 196: 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
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Table 4.5 Overview of Investment Fo
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chemistry, and biology process or a
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ii. b. Anaerobic System Anaerobic p
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experience growth to form granular
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Table 5.1. Sources and Types of Sol
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There are several solid waste manag
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technology development is equipped
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esulting energy for steam productio
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With this system, the fluidization
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In the composting process temperatu
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closed system requires an investmen
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generally composed of CH 4 55-70%;
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Figure 5.8 Anaerobic Digestion One
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Figure 5.9 Flowchart of Two Phase A
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Table 5.4 Sources and Characteristi
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5.3.2.1 Separation of Particulate P
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). Filter Cloth (Fabric Filter) The
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time. Separation of pollutants carr
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Figure 5.14 Packed Tower Scrubber B
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C. SOx Gas Control SOx gases can be
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Type of FGD Method Dry Method Absor
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D. NOx Gas Control NOx emission can
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Method Selective non catalytic redu
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incoming gas fan. To avoid the risk
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Some processes that can save energy
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REFERENCES Adams, Terry N., 1997,.
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Industry”, Environmental Energy T
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_____EPA, 2010. “Available and Em
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CONTINUE No Company Name Mill Site
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APPENDIX 2 (continuation) Consumpti
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APPENDIX 3 SPECIFIC ENERGY CONSUMPT
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Source : all data taken from [249,
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APENDIX 4 GHG EMISSION FROM VARIOUS
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