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

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APPENDIX 2 PAPER CONSUMPTION IN VARIOUS COUNTRIES Consumption per capita Consumption Country (kg) 1 Country-Based (1000 t) 1995 2007 1995 2007 Austria 192 268 1550 2196 Belgium 237 375 2 2663 2 4089 Cyprus NA 132 NA 105 Czechoslovakia NA 159 NA 1622 Denmark 214 229 1134 1256 Finland 175 369 896 1933 French 164 144 9631 8754 Germany 194 254 15821 20873 Greece 82 108 857 1157 Hungary NA 97 NA 967 Ireland 102 115 361 476 Italia 140 205 8076 11894 Latvia NA 87 NA 195 Lithuania NA 50 NA 180 Halaman 124 dari 131
APPENDIX 2 (continuation) Consumption per capita (kg) Consumption Country 1 Country-Based 1995 2007 (1000 t) Luxemburg 168 375 2 See Belgium See Belgium Nederland 201 210 3120 3502 Norway 176 188 756 874 Malta NA 84 NA 34 Poland NA 109 NA 4209 Portugal 82 120 802 1277 Slovakia NA 91 NA 496 Slovenia NA 210 NA 421 Spain 129 190 5147 7708 Sweden 210 256 1857 2314 UK Non Europe Countries 194 200 11288 12157 USA 332 288 87409 87496 China 22 55 26499 72900 Indonesia 14 25 NA 5985 Japan 239 246 30018 31255 Halaman 125 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
Page 90 and 91: merupakan sumber karbon yang berkon
Page 92 and 93: Gambar 5.1 Fase-Fase Pada Tahapan P
Page 94 and 95: 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 142 and 143: APPENDIX 2 (continuation) Country C
Page 144 and 145: Coated wood-free paper - integrated
Page 146 and 147: APPENDIX 4 ENERGY CONSUMPTION FOR U
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
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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
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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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