Spreadsheet: 843129d1695074550-extract-information-from-on-file-to-another-with-power_bi-or-formulas-action-items
Sheet: Action Item 

This is an example of the 45 files with 1200 plus rows.
Site | Industrial Complex /AKZ | Process Step | Process Step /AKZ | Subprocess Step | Subprocess AKZ | Node | Deviation | Cause | Consequences /Causal Chain | C | L | RR | M requ. | Main Idea | TAG | Description | Fct | Description2 | D/Q | M | Cat | St | Setpoint | Actuator/SOP | S-Action | S-P | Action | Respronsibility | Status
1. Central Plant |  | 1. MY Station | 42 | 1. General |  | 1. General | 1. In terms of general aspects | 1. downstream: | see Unit
 |  |  |  |  |  |  | 2. Power failure | 1. Compressors | In case of power failure compressors will stop, but flow will continue to proceed towards NaSH unit. Sufficient time left to shut down wells.
 |  |  |  |  |  |  |  | 2. Controls | No power backup in the control room. Everthing at the sour gas booster station is manual.
 |  |  |  |  |  |  |  | 3. Flare | The flare will not be operational as the gas towards the pilots will be shut down. In case of high pressure at the same time potential for H2S sent towards atmosphere. | [NAME] | L3 | D | I |  |  |  |  |  |  |  |  |  |  |  |  |  | 1. Evaluate need to implement power back up for the flare. Esp. in case of power shortage at the NaSH unit and at the sour gas booster station (at the same time). -->prevent relief of sour gas towards atmosphere not beeing flared. Update hazard discussion in way towards A4 .
 |  |  |  |  |  |  | 3. Leakages | 1. Corrosion operator error | Potential for fatalities due to gas release containing toxic H2S | C2 | [NAME] | D | I | Detect gas leakages | 1745-003 | H2S High Concentration Detector | AHH | Alarm H2S detection. Alarm/Danger will acutate flashing light, furthermore audible alarm. SOP describes behaviour in case of an alarm.  - Use of PPE, including respiratory protection, when responding to potential H2S leak. |  | I | PCT | U | 10 ppm | SOP |  |  | 2. Manage gas detectors AI-60-3711/3712/3713/3714 as i- class measures.
This is the example of where I want to place the extracted rows.
Site | Industrial Complex /AKZ | Process Step | Process Step /AKZ | Subprocess Step | Subprocess AKZ | Node | Deviation | Cause | Consequences /Causal Chain | C | L | RR | M requ. | Main Idea | TAG | Description | Fct | Description2 | D/Q | M | Cat | St | Setpoint | Actuator/SOP | S-Action | S-P | Action | Respronsibility | Status
 |  |  |  |  |  |  |  | 3. Flare | The flare will not be operational as the gas towards the pilots will be shut down. In case of high pressure at the same time potential for H2S sent towards atmosphere. | [NAME] | L3 | D | I |  |  |  |  |  |  |  |  |  |  |  |  |  | 1. Evaluate need to implement power back up for the flare. Esp. in case of power shortage at the NaSH unit and at the sour gas booster station (at the same time). -->prevent relief of sour gas towards atmosphere not beeing flared. Update hazard discussion in way towards A4 .
 |  |  |  |  |  |  | 3. Leakages | 1. Corrosion operator error | Potential for fatalities due to gas release containing toxic H2S | C2 | [NAME] | D | I | Detect gas leakages | 1745-003 | H2S High Concentration Detector | AHH | Alarm H2S detection. Alarm/Danger will acutate flashing light, furthermore audible alarm. SOP describes behaviour in case of an alarm.  - Use of PPE, including respiratory protection, when responding to potential H2S leak. |  | I | PCT | U | 10 ppm | SOP |  |  | 2. Manage gas detectors as i- class measures.