m0lzf 2026-06-05T18:03:13+02:00 Microsoft® Excel® 2016 2026-06-05T18:25:30+02:00 Microsoft® Excel® 2016 Microsoft® Excel® 2016 Microsoft® Excel® 2016 2026-06-05T18:03:13+02:00 2026-06-05T18:25:30+02:00 m0lzf tetml={filename={D:\drim\repository\projects\drim_26_0\metadata\6\1\61bd4eed044aceff3c1d35670d03f9af\61bd4eed044aceff3c1d35670d03f9af.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 ●●CONFIDENTIAL-RESTRICTED 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 1 AFI Approved for Inquiry All 2026-06-05 M. JACQUEMIN F. PÈRE L. GRANADOS 0 AFI Approved for Inquiry All 2025-08-04 M. JACQUEMIN L. GRANADOS L. GRANADOS Rev. Status Description Sheet Date Prepared by Checked by Approved by Project Name ACCSION Process Process Data Sheet Cover ●●CONFIDENTIAL-RESTRICTED Business Owner Process Department Team Leader Distribution List Check Project ACL (Access Control List) 624001C39 / 624001C39T01 / 624001C39T02 PROCESS DATA - TAIL GAS COMPANDER - NITROGEN WASTE EXPANDER Index of Revisions Project No. Document No. Page / of 53573 53573-62-01-PR-013739-KH 1 / 5 Case-Name: N/A Printed by / date / time: RNETW / Revision 1 05/06/26 / 18:02 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 ●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. furnished. This print is lent subject to return on demand. Process Process Data Sheet Compressor 01 Item Number 624001C39 / 624001C39T01 / 624001C39T02 02 03 Designation PROCESS DATA - TAIL GAS COMPANDER - NITROGEN WASTE EXPANDER 04 05 Number required 1 Supplier/Type 06 Driver Electrical Motor 07 08 MACHINE ARRANGEMENT 09 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 The compressor and expander are placed after a Pressure Swing Adsorber (PSA). The cyclic nature of the upstream process induces cyclic fluctuations (30 sec) of inlet streams of the compander : +0.5% / -1.2% on the molecular weight of the tail gas (see page 5) client-logo.bmp 29 30 31 32 33 Scheme is presented for illustrative purposes, vendor to advise on number of compression stages and coolers. 2 34 The turbine preheater is out of vendor scope, but turbine inlet temperature is linked to this exchanger which is heated using heat 2 35 recovery from the Flue Gas Compressor. Refer to document 53573-62-01-PR-013712 for details on the impact on Flue Gas 2 36 Compressor. 37 Process scheme is based on two turbines in series but supplier to recommend optimized number for best economic solution. 38 39 START-UP philosophy 40 41 Start-up is done with flue gas (see page 5 for start-up composition). Compressor running on its recycle line with discharge pressure ≥6 42 bar(a). Minimum flowrate and outlet pressure should be calculated by vendor based on machine and recycle valve sizing. 43 44 On expander side, gas is available by by-passing the PSA (available flowrate and pressure are given on page 4). Actual operating 45 conditions should be calculated by vendor (lower pressure if required and lower flowrate if required are possible). 46 PSA constraint AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR Line revised under Rev. No. 1Project NameProject No. Document No. Sheet / of Revision ACCSION 53573 53573-62-01-PR-013739-KH 2 / 5 1 Case-Name: N/A Printed by / date / time: RNETW / 20/07/23 / 16:15 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} SUCTION TAIL GAS COMPRESSOR Pressure Temperature Pipe diameter Design pressure min. / max. SIDE STREAM TAIL GAS COMPRESSOR Available Pressure (can be lowered for optimization) Temperature Pipe diameter Design pressure min. / max. DISCHARGE TAIL GAS COMPRESSOR (2) Molar Flowrate (3) Mass Flowrate Pressure Temperature Pipe diameter Design pressure Design temperature min. / max. INTERCOOLERS TAIL GAS COMPRESSOR (see page 5 for hot water conditions) Outlet Temperature (gas side) First Intercooler Outlet Temperature (gas side) Second Intercooler Outlet Temperature (gas side) Aftercooler SUCTION NITROGEN WASTE EXPANDER Molar Flowrate Mass Flowrate Pressure Temperature Pipe diameter Design pressure Design temperature min. / max. DISCHARGE NITROGEN WASTE EXPANDER (4) Molar Flowrate Mass Flowrate Pressure Temperature Pipe diameter Design pressure Design temperature min. / max. Line revised under Rev. No. °C N/A 1 1 1 1 1 18:02 / / 1 1 1 1 RNETW ACCSION AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR 36 41 3 / 39 44 48 53 51 1 52 38 v.t.a v.t.a v.t.a 43 1 1 36.4 24.0 v.t.a -20 / 65 1 1 29 28 35 31 41.7 25.6 Process Data Sheet 32 33.0 15 261 429 261 526 16 20 490 46.1 01 02 barg °C Compressor 1 1 Fluid 1 Mass Flowrate Designation Number required 624001C39 / 624001C39T01 / 624001C39T02 Item Number client-logo.bmp Process 24.5 v.t.a 0.0 12.3 1.013 1.013 v.t.a 10.45 413 074 RATED SUMMER see page 5 for detailed composition and properties Driver Supplier/Type Electrical Motor NOMINAL SUMMER CASE (1) NOMINAL WINTER 03 04 PROCESS DATA - TAIL GAS COMPANDER - NITROGEN WASTE EXPANDER 05 06 1 START-UP 10 09 08 07 Nm 3 /h 282 946 249 170 bar(a) (5) 1.013 kg/h 249 226 11 1 466 699 Molar Flowrate 412 977 Design temperature 12 356 104" 13 12 18 -0.2 / 6 -20 / 65 12.2 °C DN 12.4 1 1.013 Nm 3 /h °C 63 05/06/26 Printed by / date / time: 61 58 1 1 5 1Project No. 53573-62-01-PR-013739-KH 1 Document No. Project Name 53573 Revision Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 Case-Name: 62 60 Rev. 54 49 46 19 20 33 50 47 37 27 23 24 ●●CONFIDENTIAL-RESTRICTED 14 30 17 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. 21 22 42 40 34 Molar Flowrate 59 55 28" 56 45 v.t.a DN 104" bar(g) 57 2 2 1.087 Mass Flowrate kg/h 21 191 20 785 bar(a) (6) For start-up, expander available flowrate is 179 178 Nm3/h already preheated at the right temperature. Design temperature °C 433 564 v.t.a 4.9 295 643 433 763 10.5 25 26 Nm 3 /h DN v.t.a kg/h bar(a) °C barg 487 889 bar(a) °C 2 0.15 °C -20 / 180 1.080 1.080 1.080 v.t.a 9.0 12 203 - 10.57 12 698 9.99 Sheet / of 9.6 barg 10" 12.0 -20 / 65 - - DN bar(g) kg/h 572 258 524 805 524 888 DN 72" v.t.a 524 805 524 888 v.t.a Nm 3 /h 447 520 410 909 410 973 v.t.a bar(a) 6.83 6.83 v.t.a v.t.a °C -20 / 80 v.t.a °C v.t.a v.t.a v.t.a v.t.a °C °C kg/h 572 258 v.t.a v.t.a v.t.a °C v.t.a v.t.a v.t.a Nm 3 /h 447 520 410 909 410 973 (6) v.t.a v.t.a 6.83 6.87 1 1 1 1 1 (1) The RATED case should be used for the sizing of the machine, IGV can be set to 0. The NOMINAL SUMMER case should be used for the power consumption optimization. (2) After final aftercooler. Aftercooler should be sized with an approach of 20°C between water inlet and gas outlet. (3) No leaks on the compressor as it is accepted to contaminate process fluid with seal gas (4) Intermediate pressure between the two turbines should be optimized on the NOMINAL SUMMER case to reach 2°C at the outlet of the second wheel. (5) For start-up, compressor flowrate with recycle can be around 80% of Nominal flow. To be defined by vendor according to available gas at Expander inlet. 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 ●●CONFIDENTIAL-RESTRICTED 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. 1 01 Item Number 624001C39 / 624001C39T01 / 624001C39T02 02 03 Designation PROCESS DATA - TAIL GAS COMPANDER - NITROGEN WASTE EXPANDER 04 RATED NOMINAL NOMINAL 05 START-UP CASE SUMMER SUMMER WINTER 06 07 ENERGY 08 Isothermal efficiency compressor % 09 Thermodynamic power compressor kW 10 Mechanical losses (including main oil pump) kW 11 Power at motor coupling (including losses) kW 12 Power at motor terminals kW 13 Motor rating kW 14 Surge limit in % of nominal flow (p=constant) % 15 Driver rotating speed RPM 16 17 UTILITIES 18 Seal gas flowrate requirement (operation / standstill) Nm 3 /h / 19 Leakage flowrate of seal gas in the process gas Nm 3 /h 20 Seal gas vent flowrate Nm 3 /h 21 Instrument air flowrate Nm 3 /h 22 Electrical frequency Hz 50 23 24 HOT WATER CONDITIONS TO COMPRESSOR INTERCOOLERS 25 ME - Glycol content in hot water % vol 0% 1 26 Water fouling factor m2°C/W 0.0001 27 Water Inlet Pressure bar(a) 19.5 1 28 Design Pressure bar(g) 25.0 1 29 Design Temperature °C -20 / 230 1 30 Maximum Allowable Pressure Drop per Intercooler mbar 2 500 1 31 Hot Water (1) (see scheme) Flow m3/h 32 Hot Water (1) (see scheme) Intercooler Inlet Temperature °C 26.1 21.7 16.4 26.1 33 Hot Water (1) (see scheme) Intercooler Outlet Temperature °C T Gas in - 6°C T Gas in - 6°C 1 34 Hot Water (2) (see scheme) Flow m3/h 35 Hot Water (2) (see scheme) Intercooler Inlet Temperature °C 26.1 21.7 16.4 26.1 36 Hot Water (2) (see scheme) Intercooler Outlet Temperature °C T Gas in - 6°C T Gas in - 6°C 1 37 Hot Water (3) (see scheme) Flow m3/h 38 Hot Water (3) (see scheme) Intercooler Inlet Temperature °C 26.1 21.7 16.4 26.1 39 Hot Water (3) (see scheme) Intercooler Outlet Temperature °C T Gas in - 6°C T Gas in - 6°C 1 40 Overdesign on heat transfer area % 10 41 42 COOLING WATER (for auxiliary equipment) 43 Cooling water flowrate m 3 /h v.t.g 1 44 Water fouling factor m2h°C/kcal 0.0002 1 45 Water inlet temperature °C 23.1 18.7 13.4 23.1 46 Maximum allowable water temperature increase °C 15.0 47 Water inlet pressure bar(a) 4.0 48 Allowable water pressure drop (skid) mbar 1 000 49 50 OPTIMIZATION CRITERIA 51 Running time h/year 52 Power evaluation €/MWh AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR v.t.a : values to be advised by vendor. Process Item Specifications & Data Sheets Process Data Sheet Compressor : 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 %) Project Name ACCSION Line revised under Rev. No. Project No. Document No. Sheet / of 53573 53573-62-01-PR-013739-KH 4 / 5 Revision 1 granularity=word contentanalysis={punctuationbreaks=false dehyphenate=false} layoutanalysis={tabledetect=0 layoutdetect=0} SUCTION TAIL GAS COMPRESSOR Composition Carbon dioxide (CO 2 ) %mol Water (H 2 O) %mol Nitrogen (N 2 ) %mol Oxygen (O 2 ) %mol Argon (Ar) %mol Carbon monoxide (CO) ppm Nitric oxide (NO) ppm Nitric dioxide (NO2) ppm Sulfure dioxide (SO2) ppm Methane (CH4) ppm Density (1) kg/m3 Molecular Weight (1) g/mol Molar Heat Capacity (1) kcal/Nm3/°C Viscosity (1) kg/m/h SIDE STREAM TAIL GAS COMPRESSOR Composition Carbon dioxide (CO 2 ) %mol Water (H 2 O) %mol Nitrogen (N 2 ) %mol Oxygen (O 2 ) %mol Argon (Ar) %mol Carbon monoxide (CO) ppm Nitric oxide (NO) ppm Nitric dioxide (NO2) ppm Sulfure dioxide (SO2) ppm Methane (CH4) ppm Density (1) kg/m3 Molecular Weight (1) g/mol Molar Heat Capacity (1) kcal/Nm3/°C Viscosity (1) kg/m/h NITROGEN WASTE EXPANDER Composition Carbon dioxide (CO 2 ) %mol Water (H 2 O) %mol Nitrogen (N 2 ) %mol Oxygen (O 2 ) %mol Argon (Ar) %mol Carbon monoxide (CO) %mol Nitric oxide (NO) ppm Nitric dioxide (NO2) ppm Sulfure dioxide (SO2) ppm Methane (CH4) ppm Density (1) kg/m3 Molecular Weight (1) g/mol Molar Heat Capacity (1) kcal/Nm3/°C Viscosity (1) kg/m/h (1) Physical properties at suction Line revised under Rev. No. 50 47 28 32 37 33 - N/A Printed by / date / time: RNETW / 34 41 44 49 05/06/26 Sheet / of Revision Case-Name: 18:02 / 1 Rev. 53573 53573-62-01-PR-013739-KH 5 / 5 ACCSION 1 1 48 1Project No.Document No. 1 AL_CRYO_PROCESS_DS_TEMPLATE_COMPRESSOR 40 1 1 1 9.3 164.6 1 42 1 1 1 45 46 - Derived from G-TPL-13-0-1, Rev. 1, issued 26-Jun-18 38 1 39 1 1 1 43 Project Name 1 35 1 36 1 1 1 - - - 1 1 30 1 31 1 - - 27 1 1 1 25 0.36 ●●CONFIDENTIAL-RESTRICTED 21 1 22 26 1 1 29 1 1 40.86% 1 20 1 19 1 1 18 1 17 16 12 1 14 1 13 1 0.00% 07 08 11 10 09 Supplier/Type 06 Driver Electrical Motor Item Number 624001C39 / 624001C39T01 / 624001C39T02 PROCESS DATA - TAIL GAS COMPANDER - NITROGEN WASTE EXPANDER 02 04 03 client-logo.bmp Process Process Data Sheet Compressor 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. CASES 01 Designation 05 Number required 1 6.97% 70.38% 23 24 15 1 574 0.92% 0.50% 0.47% 164.6 39.8 55.72% 4.00% 0.47% 0.00% 0.00% 21.55% - 0.34 - - - - 54.60% 52.94% 0.00% 22.8 26.0 23.7 42.50% 39.71% 3.89% 4.00% 12.2 12.2 9.3 18.5 - - 31.85 10.03 0.06 1 016 0.06 0.06 0.06 36.97 36.70 37.15 0.36 0.36 11.9 0.32 0.32 0.06 1.06% 1.06% 905 905 31.85 0.34 18.5 10.03 1 574 39.8 6.97% 0.92% 0.00% 70.38% 21.55% - START-UP RATED NOMINAL SUMMER NOMINAL WINTER NMW LMW NMW 0.0 0.0 89.18% 8.81% 8.82% 8.82% 0.38 0.38 25.3 24.7 0.00% 500 500 92.3 67.0 0.00% 303.3 1.58 1.57 1.59 38.06% 35.37% 35.77% 66.7 424.6 304.7 55.78% 58.69% 58.22% 0.00% 5.13% 5.04% 5.10% 0.95% 0.86% 0.87% 748 352 355.5 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.38 0.06 24.9 17.37 17.41 16.89 37.25 37.70 37.63 89.18% 1.16% 0.19% 0.06 0.06 0.99% 0.85% 0.85% 0.0 5.54 5.44 0.00% 0.00% 0.00% 0.0 0.0 0.0 88.85% 0.09 5.45 28.66 28.63 28.63 6.4 4.5 4.5 0.0 0.0 1 1 1 0.32 22.2 22.0 22.0 0.09 0.06 0.00 0.00 0.00 1.00 0.00 0.69 0.31 1.00 0.00 0.00 0.20 0.20 0.60 0.00 0.50 0.00