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

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MINISTRY OF INDUSTRY CENTER FOR PULP AND PAPER RESEARCH AND DEVELOPMENT Jl. Raya dayeuhkolot No 132, Kotak Pos 1005. Bandung 40258 Telp (022) 5202980 & 5202871; Fax (022) 5202871 TECHNOLOGY MAPPING GUIDELINE FOR PULP AND PAPER INDUSTRY IN IMPLEMENTATION OF ENERGY CONSERVATION AND CO2 EMISSION REDUCTION IN INDUSTRIAL SECTOR (PHASE 1) CENTER FOR ASSESSMENT ON GREEN INDUSTRY AND ENVIRONMENT AGENCY FOR ASSESSMENT ON POLICY, CLIMATE AND QUALITY OF INDUSTRY 2011 i
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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
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 146 and 147: APPENDIX 4 ENERGY CONSUMPTION FOR U
Page 150 and 151: TECHNOLOGY MAPPING GUIDELINE FOR PU
Page 152 and 153: FOREWORD Praise the Lord giving us
Page 154 and 155: - Paper making technology which is
Page 156 and 157: closed hood system and optimize the
Page 158 and 159: TABLE OF CONTENT FOREWORD ………
Page 160 and 161: 5.3.2.3. Emission of Non Condensabl
Page 162 and 163: LIST OF TABLES Table 1.1 Indonesian
Page 164 and 165: CHAPTER I INTRODUCTION 1.1 Environm
Page 166 and 167: a commitment to reduce CO2 emission
Page 168 and 169: Table 1.1 Indonesian National Green
Page 170 and 171: the policy, it will show the differ
Page 172 and 173: According to several industry surve
Page 174 and 175: Table 1.6 Energy Saving Opportuniti
Page 176 and 177: CHAPTER II OVERVIEW OF THE PULP AND
Page 178 and 179: Classification Process Mechanical C
Page 180 and 181: pulp (non-integrated mill only). Th
Page 182 and 183: d. Chemical Recovery For reasons of
Page 184 and 185: dried and calcined in a lime kiln t
Page 186 and 187: Pulp mills can produce the energy b
Page 188 and 189: Figure 2.3 Papermaking Process In t
Page 190 and 191: 2.3 Environmental Management Techno
Page 192 and 193: alternative. Another advantage is t
Page 194 and 195: disturbance to the surrounding envi
Page 196 and 197: technology toward the acquisition o
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8. Apply Chip screening bar-type ch
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3.2 Modification Of Continues Delig
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Figure 3.4 Summary Of The Various C
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Cooking starts with an initial dige
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3.2.3 Black Liquor Impregnation Fig
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4. Heat recovery bleaching unit 5.
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Table 3.3 Conservation Of Energy in
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Energy Conservation in Chemical Rec
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3.5 Optimization of Biomass and Coa
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Table 3.5. Conservation Of Energy I
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CHAPTER IV PAPERMAKING TECHNOLOGY F
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Typically, the sheet pressing proce
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A. Direct B. Indirect Figure 4.4 Ai
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Table 4.2 Energy Conservation Oppor
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Table 4.4 Source of Carbon Emission
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CHAPTER V ENVIRONMENTAL MANAGEMENT
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loads and are complex compounds tha
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To optimize and distribute the micr
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anaerobic digestion sludge (mud). I
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Table 5.2 Advantages and Weaknesses
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Figure 5.1 Phase on Anaerobic Proce
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for the potential impact of polluti
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etween a few seconds to several hou
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has already implemented in the pape
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Composting Process Technology and A
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Figure 5.6 Stages of Anaerobic Dige
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Figure 5.7 Anaerobic Digestion Wet
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a-2. Phase Two Digestion Two-phase
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Pulp and paper industries in some c
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Chemical pulping process and semi-c
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Figure 5.10 (A). Multiple Cyclone a
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gas flow will be attracted by the p
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Venturi Scrubber: The liquid that i
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Figure 5.15 Several Types of Absorb
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Type of FGD Method Type of FGD Non-
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First of all exhaust gas is passed
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gas stream in a catalytic coating c
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5.3.2.3 Emission of Non-Condensable
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CHAPTER VI CLOSING REMARKS Indonesi
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and the extent to which can potenti
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Journal, September/October 2008, Vo
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Thomas. 2003.. Anaerobic Digester M
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No Company Name Mill Site APPENDIX
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CONTINUE No Company Name Mill Site
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CONTINUE 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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Paper Grades APPENDIX 3 Energy Cons
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APPENDIX 4 ENERGY CONSUMPTION FOR U
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