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

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Type of FGD Method Type of FGD Non-Regeneration Wet Method FGD Method FGD Method Table 5.6 Wet FGD and Dry Type Absorbent Reaction By Product Limestone scrubbing CaCO3 - slurry CaCO3+ H2O+2SO2 2CaSO3 + CO2 + H2O CaSO3+1/2O2 CaSO4 CaSO4 Absorbent Reaction By Product Lime scrubbing CaO – slurry CaO+H2O Ca(OH)2 SO2+ H2O H2SO3 H2SO3+Ca(OH)2 CaSO3.2H2O CaSO3.2H2O+1/2O2 CaSO4. 2H2O CaSO3, CaSO4 Absorbent Reaction By Product Dual alkali NaOH solution or 2NaOH+SO2Na2SO3+H2O Na2SO3+H2O+SO22NaHSO3 Na2SO3 Mg(OH)2 – slurry Mg(OH)2+SO3MgSO3+H2O Mg(OH)2+2SO2Mg(HSO3)2 Reaction in Oxidized Tank: MgSO3+1/2O2MgSO4 Mg(HSO3)2+Mg(OH)22MgSO3+2H2 Na2SO3, Na2SO4 MgSO3, MgSO4 Page 103 of 132
Type of FGD Method Dry Method Absorbent Reaction By Product O NH3 and water 2NH4OH+SO2(NH4)2SO3+H2O (NH4)2SO3+SO3+SO2+H2O2NH4HS Lime Spray Drying CaO and CaCO3 powder Type of FGD Regeneration Wet Method Wellman-Lord (W- L) Process O3+H2 Na2SO3 + SO2 + H2O 2NaHSO3 Na2SO3 + 1/2O2 Na2SO4 2Na2SO3+ SO3+ H2O Na2SO4 + 2NaHSO3 2NaHSO3 + heat Na2SO3 + SO2 + H2O Na2CO3 + SO2 Na2SO3 + CO2 (NH4)2SO4 CaSO3, CaSO4 Page 104 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
Page 215 and 216: Figure 3.11 FBC and CFBC Page 52 of
Page 217 and 218: Other energy conservation can be do
Page 219 and 220: process of separating water from th
Page 221 and 222: facilities. For the hood that uses
Page 223 and 224: 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: C. SOx Gas Control SOx gases can be
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 and 278: REFERENCES Adams, Terry N., 1997,.
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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