m0lzf 2026-06-05T16:22:25+02:00 Microsoft® Excel® 2016 2026-06-09T17:31:37+02:00 Microsoft® Excel® 2016 Microsoft® Excel® 2016 Microsoft® Excel® 2016 2026-06-05T16:22:25+02:00 2026-06-09T17:31:37+02:00 m0lzf tetml={filename={D:\drim\repository\projects\drim_26_0\metadata\2\6\2639b33d7d69483443cdda36f954418e\2639b33d7d69483443cdda36f954418e.tet.xml} elements={annotations=false bookmarks=false destinations=false fields=false javascripts = false} } granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●INTERNAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly Rev. 0 furnished. This print is lent subject to return on demand. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR Business Owner Process Department Team Leader Distribution List Check Project ACL (Access Control List) 2 AFI Approved for Inquiry All 2026-06-05 M. JACQUEMIN F. PÈRE L. GRANADOS 1 AFI Approved for Inquiry All 2025-10-01 M. JACQUEMIN L.GRANADOS L.GRANADOS 0 AFI Approved for Inquiry All 2025-05-13 Z.BONDOUX M.HEINRCH L.GRANADOS Rev. Status Description Sheet Date Prepared by Checked by Approved by Project Name ACCSION Process Process Data Sheet Cover ●INTERNAL 621001C12 PROCESS DATA - WET FEED GAS COMPRESSOR Index of Revisions Project No. Document No. Page / of 53573 53573-62-01-PR-013712 1 / 7 Case-Name: N/A Printed by / date / time: RNETW / Revision 2 05/06/26 / 16:22 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential ●C information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●CONFIDENTIAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly Rev. 1 furnished. This print is lent subject to return on demand. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR Case-Name: N/A Project Name ACCSION Process Process Data Sheet Compressor client-logo.bmp 01 Item Number Unit No. N/A Unit Name 02 C12 03 Designation WET FLUE GAS COMPRESSOR 04 Number required 1 Supplier/Type 05 Driver Electrical Motor 06 07 TABLE OF CONTENTS 08 09 Page 10 Process description and vendor scope of supply 2 11 Process gas characteristics for the design of the machine 3 12 Hot water characteristics and utilities 4 13 Design Philosophy 5 14 Design Philosophy - continuation 6 15 Process gas composition and physical characteristics 7 16 17 PROCESS DESCRIPTION AND VENDOR SCOPE OF SUPPLY 18 19 20 PROCESS SCHEME 21 22 23 24 25 26 27 28 29 30 Ho 31 32 33 PROCESS DESCIPTION 34 35 The WET FLUE GAS COMPRESSOR (C12) compresses wet flue gas from low to medium pressure and is divided into two sections. 36 The WET FLUE GAS contains acidic components (e.g HNO3, H2SO4) that can condense in the intercooler of section 1 of the 37 compressor; vendor to advise on material selection. 38 Section 2 is adiabatic in order to recover heat at the compressor discharge with a heat recovery system (outside vendor scope of 39 supply). This heat will be used to preheat the gas going through the expander side of the compander of the plant, see below scheme. Compressor discharge temperature will then be calculated according to needed temperature at the inlet of the expander, 40 see design philosophy page 5 and 6. 41 This datasheet contains the process specifications for DESIGN, NOMINAL, TURNDOWN and START-UP cases. 42 Vendor to optimize the compressor operation and TCO considering all cases and power evaluation. 43 Heat integration is performed on the first stage intercooler, pressure ratio to be chosen to reach specified temperature at 44 the inlet of intercooler. 45 Vendor to advise the number of compression stages and intercoolers in both sections. 46 Vendor to advise the sealing gas configuration. 47 48 49 HOT WATER SYSTEM Cold water Hot water 50 51 52 53 54 GAS FEED FG Compressor PROCESS C39 Expander Line revised under Rev. No. Project No. Document No. Sheet / of 53573 53573-62-01-PR-013712 2 / 7 Printed by / date / time: N/A / 28/02/23 2 2 2 2 2 2 Revision 2 / 11:07 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●INTERNAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly Rev. furnished. This print is lent subject to return on demand. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR 01 Item Number 02 621001C12 03 Designation PROCESS DATA - WET FEED GAS COMPRESSOR 04 05 Number required 1 Supplier/Type 06 Driver Electrical Motor 07 RATED NOMINAL NOMINAL CASE START UP 08 DESIGN WINTER SUMMER 09 Fluid (see page 5 for detailed composition and properties) Flue gas Flue gas Flue gas Air 10 SUCTION 11 Molar Flowrate (wet basis) Nm 3 /h 601 413 552 936 545 230 2 12 Mass Flowrate (wet basis) kg/h 835 595 767 768 761 551 2 13 Volume Flowrate m 3 /h 693 721 637 797 615 487 2 14 Inlet Pressure (1) bar(a) 0.990 0.990 0.990 1.013 2 15 Temperature (1) °C 35.0 35.0 28.4 23.8 2 16 Duct diameter DN 146" 2 17 Design pressure min. / max. mbarg -0.09 / +0.09 2 18 Design temperature min. / max. °C -20 / +80 2 19 20 Section 1 DISCHARGE (before intercooler) (6) 21 Section 1 discharge pressure bar(a) v.t.a v.t.a v.t.a 22 Section 1 discharge temperature (2) °C v.t.a v.t.a v.t.a 2 23 Section 2 DISCHARGE 24 Molar Flowrate (wet basis) (3) Nm 3 /h v.t.g v.t.g v.t.g 25 Mass Flowrate (wet basis) kg/h v.t.a v.t.a v.t.a 26 Section 2 discharge pressure bar(a) 8.60 8.27 8.27 2 27 Temperature (4) °C v.t.g v.t.g v.t.a 2 28 Water content kg/h 29 Pipe diameter DN 84" 2 30 Design pressure bar(g) 9 2 31 Design temperature min. / max. °C -20 / 250 2 32 33 HOT WATER 34 Minimum available hot water temperature °C 26.1 26.1 26.1 26.1 2 35 36 ENERGY 37 Polytropic efficiency % 38 Thermodynamic power kW 39 Mechanical losses (including main oil pump) kW 40 Power at motor coupling (including losses) kW 41 Total power at motor terminals kW 42 Motor rating kW 43 Surge limit in % of flow (p=constant) % 44 Driver rotating speed RPM 45 Notes: Nm 3 = m 3 reduced to 0°C and 1.013 bar abs. 46 (1) Before inlet flange (inlet silencer if required), no inlet filter is required. 47 (2) Vendor to advise temperature, according to design philosophy page 5. 2 48 (3) Vendor to advise on the condensed fluid in the intercooler and %H2O content in compressed gas. 49 (4) Vendor to guarantee temperature, according to design philosophy page 5. 2 50 (5) Vendor to advise minimum load of the compressor. 2 (6) Possibility to have acid condensates in intercooler during transitory phases. 2 Case-Name: : values to be guaranteed by vendor with the following tolerances : Pressure (- 0 %) ; Power construction tolerances (+ 0 %) ; Power measurement tolerances (< 1.5 %, advise if different) ; Discharged flow (- 0 %) ; Temperature (+ 1°C) ; Water flow (+ 5 %) ; Leakage flowrate of process gas (+ 0 %) 0Project Name No.Document No. ACCSION 53573 53573-62-01-PR-013712 N/A : values to be advised by vendor. Process Process Data Sheet Compressor Printed by / date / time: client-logo.bmp Line revised under Rev. No. Sheet / of 3 / 7 Revision 2 RNETW / 05/06/26 / 16:22 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●INTERNAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly furnished. This print is lent subject to return on demand. Rev. 0 AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR 01 Item Number 02 621001C12 03 Designation PROCESS DATA - WET FEED GAS COMPRESSOR 04 05 06 CASE 07 08 09 HOT WATER 10 ME- Glycol content in hot water % vol 11 Hot water flowrate m 3 /h 12 Hot water intercooler outlet temperature °C Process Item Specifications & Data Sheets Process Data Sheet Compressor RATED DESIGN v.t.a v.t.a NOMINAL WINTER 0 v.t.a v.t.a Gas T in - 6°C (8) NOMINAL SUMMER START UP 13 Water fouling factor m 2 h°C/kcal 0.0001 2 14 Water inlet pressure bar(a) 19.5 2 15 Allowable water pressure drop (skid) mbar 2 500 2 16 Design pressure barg 25.0 17 Design temperature min. / max. °C -20 / 230 18 19 20 COOLING WATER (for auxiliary equipment) 21 ME- Glycol content in cooling water % vol 0 22 Cooling water temperature - process design °C 23.1 13.4 18.7 23.1 2 23 Cooling water supply pressure bar (a) 4.0 24 Temperature elevation in equipment (skid) °C 15.0 25 Allowable water pressure drop (skid) mbar 1 000 26 27 28 UTILITIES 29 Seal gas nature (9) 30 Seal gas flowrate (standstill / normal operation) Nm 3 /h 31 Seal gas leakage into process section (overall) Nm 3 /h 32 Seal gas leakage to atmosphere (overall) Nm 3 /h 33 Minimum seal gas pressure bara 34 Instrument air flowrate Nm 3 /h 35 Frequency Hz 50.0 36 37 38 Notes: Nm 3 = m 3 reduced to 0°C and 1.013 bar abs. 39 40 41 (8) See page 5 for design philosophy. Minimum hot water temperature is 118°C. 2 42 (9) Please refer to Technical Requisition Summary. 43 44 : values to be advised by vendor. 45 46 : values to be guaranteed by vendor with the following tolerances : Pressure (- 0 %) ; Power construction tolerances (+ 0 %) ; 47 Power measurement tolerances (< 1.5 %, advise if different) ; Discharged flow (- 0 %) ; Temperature (+ 1°C) ; 48 Water flow (+ 5 %) ; Leakage flowrate of process gas (+ 0 %) 49 v.t.a Line revised under Rev. No. Project Name Project No. Document No. Sheet / of Revision ACCSION 53573 53573-62-01-PR-013712 4 / 7 2 Case-Name: N/A Printed by / date / time: RNETW / 05/06/26 / 16:22 2 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●INTERNAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly Rev. furnished. This print is lent subject to return on demand. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR Step 3 � Flue Gas Compressor - Nominal Winter Case Step 4 � Flue Gas Compressor - Rated Case Process Process Data Sheet Compressor client-logo.bmp 01 Item Number 02 621001C12 03 Designation PROCESS DATA - WET FEED GAS COMPRESSOR 04 05 Number required 1 Supplier/Type 06 Driver Electrical Motor 07 DESIGN PHILOSOPHY 08 09 Step 1 � Compander - Expander side 10 Determine the temperature needed at the inlet of the expander (= a1) to reach 2°C after the expansion. Use a1 in the following formula to determine 11 the temperature needed at the outlet of the Flue Gas Compressor (= z1) : 12 z1 = a1 + 45°C and minimum z1 value should be 181°C 13 14 STEP 1 15 Variables Fixed values Calculated values 16 a1 2°C after expansion z1 17 18 Step 2 � Flue Gas Compressor - Nominal Winter Case 19 On this case, determine the optimum pressure at the outlet of the first stage. Make sure that the gas temperature is high enough so that the hot 20 water temperature is not lower than 118°C. Use formula Tw_out = Tg_in - 6°C : 21 STEP 2 22 Variables Fixed values Calculated values 23 Intermediate P Tg_in Tw_out 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 Qin= 552 936 Nm3/h or 767 768 kg/h Tsuction = 35°C Still on the Nominal Winter case, work on the second section of the compressor to determine which intercooler gas outlet temperature (=y2) allows to reach calculated specification on discharge temperature (=z1) : Qin= 552 936 Nm3/h or 767 768 kg/h Tsuction = 35°C STEP 3 Variables Fixed values Calculated values y2 z1 - On the rated case, reinject the temperature y2 determined in step 2 as the gas outlet temperature and design the intercooler on the Rated case conditions. Use an approach of 6°C between gas inlet temperature and water outlet temperature : Qin= 601 413 Nm3/h or 835 595 kg/h Tsuction = 35°C Stage 1 Stage 1 Stages 2 &3 Tdischarge = z1°C STEP 4 Variables Fixed values Calculated values Hot water flow y2 ; Tw_in x1 ; intercooler UA ; Tw_out ; Tdischarge Stage 1 Tg_in = x2 Tg_out = y2 Tw_out = x2-6°C Tg_in = x2 Tg_out = y2 Tw_out = x2-6°C Tw_in = 26.1°C Tw_in = 26.1°C UA installed = Rated Design Tg_in = x1 Tg_out = y2 Tw_out = xl-6°C Tw_in = 26.1°C Stages 2 &3 Stages 2 &3 Tdischarge = z1°C Tdischarge = ?°C Line revised under Rev. No. 0Project NameProject No. Document No. Sheet / of Revision ACCSION 53573 53573-62-01-PR-013712 5 / 7 2 Case-Name: N/A Printed by / date / time: RNETW / 05/06/26 / 16:22 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third ●INTERNAL Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly Rev. furnished. This print is lent subject to return on demand. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR Process Process Data Sheet Compressor STEP 5 Fixed values Calculated values y2 ; x2 ; Tw_in ; intercooler surface Tw_out client-logo.bmp 01 Item Number 02 621001C12 03 Designation PROCESS DATA - WET FEED GAS COMPRESSOR 04 05 Number required 1 Supplier/Type 06 Driver Electrical Motor 07 DESIGN PHILOSOPHY - CONTINUATION 08 09 Step 5 � Flue Gas Compressor – Nominal Winter and Summer cases check 10 The purpose of this step is not to design anything but only to predict and estimate performances based on the design that was calculated in the 11 previous steps. Inject the intercooler surface calculated in step 4 in the Nominal Winter and Summer cases. Update corresponding water flow to still 12 reach the correct outlet temperature y2 : 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 Case-Name: N/A Qin= 552 936 Nm3/h or 767 768 kg/h Tsuction = 35°C Variables Hot water flow Stage 1 UA installed = Rated Design Tg_in = x2 Tg_out = y2 Tw_out = x2-6°C Tw_in = 26.1°C Stages 2 &3 Tdischarge = z1 Line revised under Rev. No. 0Project NameProject No. Document No. Sheet / of Revision ACCSION 53573 53573-62-01-PR-013712 6 / 7 2 Printed by / date / time: RNETW / 05/06/26 / 16:22 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} Ammonia (NH3) Formaldehyde Acetaldehyde Others Total Mercury (Hg) PCDD / PCDF HAP - EPA BTEX Molar Heat Capacity (10) kcal/Nm3/°C Viscosity (10) kg/m/h Notes : (10) Physical properties at suction Dust content µg/Nm 3 Acid Process Condensates Line revised under Rev. No. 2 Nm 3 = m 3 reduced to 0°C and 1.013 bar abs. μg/Nm3 mg/Nm3 31.12 NOMINAL WINTER NOMINAL SUMMER START UP ppmm Composition (wet basis) Oxygen (O 2 ) %mol Argon (Ar) μg/Nm3 23 24 17.2 ppmm 17.3 - ppmm 32 0.1 0.1 0.332 0.313 - 0.333 17.1 ppmm Methane (CH 4 ) 46 49 50 47 48 43 0.065 0.065 37 38 Dust content 10 35 / N/A Printed by / date / time: RNETW / 05/06/26 2 Sheet / of Revision Please note that acidic process condensates (pH around 2-3) are generated during condensation of wet flue gas at intercooler, vendor to advise on material selection. Case-Name: 16:22 Rev. 53573 53573-62-01-PR-013712 7 / 7 ACCSION 0Project No.Document No. AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR 42 44 2 Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 40 41 45 Project Name 31.31 1.237 1.014 0.065 0.071 2 2 33 28.76 2 34 2 36 0.333 31 29 31.14 1.204 ng/Nm3 30 2 Molecular Weight (10) g/mol 10.0 - 1.205 ●INTERNAL 21 2 22 28 2 Mass density (10) kg/m3 10.0 10.0 2 20 2 19 0.071 - 29.8 8.9 - 2 18 2 17 16 0.89 0.82 0.83 0.91 10 2 15 2 14 13 2 FLUID 07 08 6.75 11 12 09 06 Driver Electrical Motor 03 Designation 68.31 68.41 69.37 76.60 05 Number required 1 Supplier/Type 01 Item Number 621001C12 PROCESS DATA - WET FEED GAS COMPRESSOR 02 04 Air Liquide Confidential Information This print is the property of L’Air Liquide S.A. or its (direct and indirect) affiliates or subsidiaries and contains valuable confidential information. Copyright and all other rights in this print are expressly reserved. No part of this print may be disclosed by the intended recipient to a third party, reproduced, copied, lent, or disposed of, directly or indirectly, nor used for any purpose other than that for which it is expressly furnished. This print is lent subject to return on demand. client-logo.bmp Process Process Data Sheet Compressor %mol 4.18 2.83 1.90 %mol Carbon dioxide (CO 2 ) %mol %mol Nitrogen (N 2 ) 4.10 6.75 39 ppmm 25 26 27 8.6 Carbon monoxide (CO) %mol ppmm Sulfur trioxide (SO 3 ) ppmm Nitric dioxide (NO 2 ) ppmm Sulfur dioxide (SO2) 0.1 20.55 191.6 - 6.85 20.03 0.040 19.77 Flue gas Flue gas Flue gas 0.147 0.070 260.3 188.9 - - - - CASES RATED DESIGN Water (H 2 O) Nitric oxide (NO) Air 19.76 - < 2 < 1 < 1 < 10 dry @10%O2 0.05 dry @10%O2 5.0 dry @10%O2 1.0 dry @10%O2 - - 0.00 0.00 1.00 0.00 0.20 0.20 1.00 0.00 0.69 0.31 0.00 0.50 0.00 1.00 0.00 0.00 0.20 0.20 0.60