NIRANI SUGARS LIMITED • MRN GROUP
Daily Manufacturing Report (DMR) — Unit No-2 (Mudhol)
Unit: Unit 2•Crop Date: 2025-12-01•Season: 2025-26•Crop Day: 19•Source: Daily DMR SY 2025-26. (5).xlsx
DMR MODULECrop Day: 19
NIRANI SUGARS LIMITED — UNIT NO-2
Daily Performance Report for Season 2025-26 vs Previous Season 2024-25
Selected Unit
Unit 2 (Mudhol)
Crop Date
2025-12-01
Total Parameters
49 Items
Workbook Source
Daily DMR SY 2025-26. (5).xlsx
Official Daily Manufacturing Report Table
Full season metrics with targets, today vs to-date values, and previous season comparisons
Sl | Particulars | UOM | Target Fixed | Today (25-26) | To Date | Prev Today (24-25) | Prev To Date | State | Audit |
|---|---|---|---|---|---|---|---|---|---|
| 1 | Cane Crushed (MT) | MT | 15200 | 14,165.603 | 266,277.328 | 14,494.561 | 243,690.111 | INPUT | — |
| 2 | Crushing for Distillery | MT | 15001 | 3,957.587 | 86,775.448 | 6,428.43 | 72,671.073 | INPUT | — |
| 3 | Crushing for sugar | MT | — | 10,208.016 | 179,501.88 | 8,066.131 | 164,574.249 | INPUT | — |
| 4 | Total Bagging Qtls | Qtls | — | 11,540 | 171,870 | 8,780 | 137,145.5 | INPUT | — |
| 5 | Exp.Recovery in Boiling House % Cane | % | — | 8.06 | 6.493 | 4.919 | 6.008 | INPUT | — |
| 6 | Net Mix. Juice % Cane | % | 105 | 108.578 | 109.381 | 105.5 | 106.23 | INPUT | — |
| 7 | Juice Qty in MT | MT | — | 15,380.71 | 291,256.881 | 15,523.675 | 259,077.822 | INPUT | — |
| 8 | Imbibition % Cane | % | 38 | 38.085 | 38.894 | 37.069 | 35.964 | INPUT | — |
| 9 | Imbibition % Fibre | % | — | 285.657 | 281.733 | 267 | 258 | INPUT | — |
| 10 | Imbibition Qty in MT | MT | — | 5,395 | 103,565.783 | 5,373 | 87,640 | INPUT | — |
| 11 | Fibre % Cane | % | — | 13.332 | 13.806 | 13.873 | 13.916 | INPUT | — |
| 12 | Pol % Cane | % | — | 13.785 | 12.517 | 12.029 | 11.931 | INPUT | — |
| 13 | Bagasse Production in MT | MT | — | 4,102.603 | 77,013.933 | 4,343.886 | 72,252.289 | INPUT | — |
| 14 | Pol % Bagasse | % | 1.8 | 1.99 | 1.915 | 2.35 | 2.129 | INPUT | — |
| 15 | LMJ Brix % | % | 2.35 | 2.15 | 2.069 | 2.35 | 2.35 | INPUT | — |
| 16 | Moisture % Bagasse | % | 49 | 51.24 | 49.617 | 50.48 | 50.106 | INPUT | — |
| 17 | Filter Cake in MT | MT | — | 265.6 | 4,845.62 | 250.5 | 3,741.473 | INPUT | — |
| 18 | Pol % Filter cake | % | 1.8 | 2.2 | 2.128 | 2.28 | 2.253 | INPUT | — |
| 19 | Concentrated cane juice Sent to distillery in MT | MT | — | 1,071.796 | 21,965.546 | 1,555.442 | 18,354.606 | INPUT | — |
| 20 | B/C Heavy % on Canefx | % | — | 4.408 | 5.122 | — | — | CALCULATED | |
| 21 | B-Heavy Molasses Production in MT | MT | — | 450 | 9,194.649 | 419.619 | 8,641.594 | INPUT | — |
| 22 | Total Losses (Without diversion of SYP & BH) | % | 1.9 | 1.805 | 1.855 | 2.039 | 2.03 | INPUT | — |
| 23 | Total Losses (With diversion of SYP & BH) | % | <7 | 5.726 | 6.015 | 7.11 | 5.923 | INPUT | — |
| 24 | Primary Mill Extraction | % | — | 74.08 | 73.15 | — | — | INPUT | — |
| 25 | Mill Extraction | % | 95.5 | 95.819 | 95.582 | 94.145 | 94.71 | INPUT | — |
| 26 | Reduced Mill Extraction (Mittal) | % | 96 | 96.117 | 96.06 | 94.725 | 95.248 | INPUT | — |
| 27 | Hours Worked to Actual | Hrs | 24 | 24 | 452 | 23.75 | 406.97 | INPUT | — |
| 28 | Hours Lost | Hrs | — | 0.8 | 13.94 | 0.25 | 45.12 | INPUT | — |
| 29 | % Capacity Utilization (24 Hrs)fx | % | 95 | 93.195 | 92.201 | 97.648 | 95.807 | CALCULATED | |
| 30 | Crushing rate (24 Hrs) - Including stoppages | MT/day | 15000 | 14,165.603 | 14,138.619 | 14,158.394 | 12,988.65 | INPUT | — |
| 31 | pH: Defecated juice | pH | 7.2 to 7.5 | 7.21 | — | 7.18 | — | INPUT | — |
| 32 | Primary Juice purity | % | — | 86.485 | 84.52 | — | — | INPUT | — |
| 33 | Power Generation (KWH)/T of cane | kWh/T | 72 | 71.977 | 70.981 | 70.983 | 73.071 | INPUT | — |
| 34 | Power Export (KWH)/T of cane | kWh/T | 40 | 42.697 | 41.78 | 41.39 | 43.633 | INPUT | — |
| 35 | Total Power Consumption / ton of cane (Sugar + Cogen) | kWh/T | 32 | 29.28 | 29.238 | 29.419 | 30.056 | INPUT | — |
| 36 | Sugar plant power consumption/ton of cane | kWh/T | 24 | 21.745 | 21.845 | — | — | INPUT | — |
| 37 | Cogen power consumption/ton of cane | kWh/T | 7 | 7.535 | 7.393 | 6.579 | 6.205 | INPUT | — |
| 38 | Steam Production % cane | % | — | 42.137 | 41.29 | 42.343 | 43.447 | INPUT | — |
| 39 | Steam % Cane (Process) | % | 38 | 35.23 | 34.91 | 36.037 | 35.538 | INPUT | — |
| — | Recovery in B- Heavy | % | — | 0.574 | 0.702 | 0.64 | 0.679 | INPUT | — |
| — | Recovery in Syrup Sent to distillery | % | — | 3.347 | 3.458 | 4.431 | 3.215 | INPUT | — |
| — | Recovery% Canefx | % | 11.5 | 11.981 | 10.653 | 9.99 | 9.916 | CALCULATED | |
| — | Crushing rate (24 Hrs) - Excluding stoppages | MT/day | 15000 | 14,654.072 | 14,588.54 | 14,615.116 | 14,354.003 | INPUT | — |
| — | pH: Clear Juice | pH | 6.9 to 7.1 | 7.05 | — | 6.98 | — | INPUT | — |
| — | pH: Spray Pond | pH | > 7.0 | 8.99 | — | 7.09 | — | INPUT | — |
| — | Mixed Juice purity | % | — | 85.368 | 83.24 | — | — | INPUT | — |
| — | Last Mill Juice purity | % | — | 73.023 | 72.272 | — | — | INPUT | — |
| — | Syrup Brix% | % | — | 56.5 | 55.824 | — | — | INPUT | — |
| — | B Heavy Purity | % | 56 | 47.664 | 49.617 | 51.797 | 49.695 | INPUT | — |