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Corporate Information

 
Press Release (Feb 29,2012)
Plant Status of Fukushima Daiichi Nuclear Power Station (as of 3:00 pm, February 29)
  
*Updates from previous press release are underlined. 
 
All 6 units of Fukushima Daiichi Nuclear Power Station have been shut down. 
 
Unit 1 (Shut down) 
-Explosive sound and white smoke were confirmed after the big quake 
 occurred at 3:36 pm on March 12, 2011. It was assumed to be hydrogen 
 explosion. 
-At 3:37 pm on March 25, 2011, we started injecting freshwater to the 
 reactor and are now injecting fresh water by a motor driven pump powered 
 by the off-site transmission line. 
-At 10:11 am on December 10, 2011, in addition to water injection from 
 water feeding system, we started water injection from piping of core 
 spray system to the reactor. 
 The current water injection amount from the reactor feed water system is 
 approx.4.6 m3/h and that from the core spray system is approx.1.8 m3/h. 
-At 1:31 am on April 7, 2011, we commenced injection of nitrogen gas into 
 Primary Containment Vessel. 
-At 11:22 am on August 10, 2011, we started cyclic cooling for the water 
 in the spent fuel pool by an alternative cooling equipment of the Fuel 
 Pool Cooling and Filtering System. 
-On October 28, 2011, we completed installation of the cover for the 
 Reactor Building in order to contain dispersion of radioactive substances. 
-At 4:04 pm on November 30, 2011, we started operation to inject nitrogen 
 into the reactor pressure vessel. 
-At 6:00 pm on December 19, 2011, a full-scale operation of the PCV gas 
 management system started. 
 
Unit 2 (Shut down) 
-At approximately 6:00 am on March 15, 2011, an abnormal noise began 
 emanating from nearby Pressure Suppression Chamber and the pressure 
 within the chamber decreased. 
-At 10:10 am on March 26, 2011, we started injecting freshwater to the 
 reactor and are now injecting fresh water by a motor driven pump powered 
 by the off-site transmission line. 
-At 2:59 pm on September 14, 2011, in addition to water injection from 
 feed water system, we started water injection from piping of core spray 
 system to the reactor. 
 The current water injection amount from the reactor feed water system is 
 approx.2.9 m3/h and that from the core spray system is approx.5.9 m3/h. 
-With regard to the water injection volume for Unit 2 reactor, which was 
 increased with temperature figure raising, we have gradually adjusted it 
 to the original volume before temperature increasing (Feed water system: 
 approx. 3.0m3/h, core spray system: approx. 6.0m3/h). During our 
 observing the plant parameter after decreasing the flow rate of feed 
 water system on February 22, we found that one thermometer in the lower 
 part of the RPV (top of the lower head 135°) indicated the different 
 movement from others. From 12:21 pm to 2:48 pm on February 23, we 
 investigated the concerned device. As the result of the measurement of DC 
 resistance, we found no breaking wire and availability of the thermometer. 
 But we confirmed that the DC resistance of it became higher than the 
 previous measurement test data. We will evaluate the soundness of the 
 concerned device and examine correspondence in future. We make sure no 
 re-criticality state because there were no significant changes at the 
 monitoring post and as the result of the sampling for the Gas Control 
 System of the Unit 2; we confirmed that the concentration of Xe-135 was 
 below the detectible limit. 
  ·At 11:00 am on February 29, the temperature of the lower part of the 
   RPV (top of the lower head 135°) : approximate 44.7 °C 
 (Reference) 
  ·At 11:00 am on February 29, the temperature of the lower part of the 
   RPV (top of the lower head 270°) : approximate 41.1 °C 
-At 5:21 pm on May 31, 2011, we started cyclic cooling for the water in 
 the spent fuel pool by an alternative cooling equipment of the Fuel Pool 
 Cooling and Filtering System. 
-At 8:06 pm on June 28, 2011, we started injecting nitrogen gas into the 
 Primary Containment Vessel. 
-At 6:00 pm on October 28, 2011, a full operation of the PCV gas control 
 system started. 
-At 10:46 am on December 1, 2011, we started the nitrogen injection to the 
 Reactor Pressure Vessel. 
-At 11:50 am on January 19, 2012, we started the operation of the spent 
 fuel pool desalting facility. 
 
Unit 3 (Shut down) 
-Explosive sound and white smoke were confirmed at approximately 11:01 am 
 on March 14, 2011. It was assumed to be hydrogen explosion. 
-At 6:02 pm on March 25, 2011, we started injecting fresh water to the 
 reactor and are now injecting fresh water by a motor driven pump powered 
 by the off-site transmission line. 
-At 2:58 pm on September 1, 2011, we started water injection by core spray 
 system in addition to water injection by the reactor feed water system 
 piping arrangement. 
 The current water injection amount from the reactor feed water system is 
 approx.1.7 m3/h and that from the core spray system is approx.5.1 m3/h. 
-At 7:47 pm on June 30, 2011, we started cyclic cooling for the water in 
 the spent fuel pool by an alternative cooling equipment of the Fuel Pool 
 Cooling and Filtering System. 
-At 8:01 pm on July 14, 2011, injection of nitrogen gas into the Primary 
 Containment Vessel started. 
-As installation works of the PCV gas control system was completed, we 
 started a test operation at 11:38 am on February 23, 2012. We confirmed 
 that an exhaust flow amount was stable at 33Nm3/h at 2:10 pm and started 
 an adjustment operation. 
-At 4:26 pm on November 30, 2011, we started operation to inject nitrogen 
 into the reactor pressure vessel. 
-At 3:18 pm on January 14, we started operation of the radioactive 
 material removal instrument for the spent fuel pool in Unit 3 
 
Unit 4 (Outage due to regular inspection) 
-At around 6 am on March 15, 2011, we confirmed the explosive sound and 
 the sustained damage around the 5th floor rooftop area of Reactor 
 Building. 
-At 12:44 pm on July 31, 2011, we started cyclic cooling for the water in 
 the spent fuel pool by an alternative cooling equipment of the Fuel Pool 
 Cooling and Filtering System. 
-At 10:58 am on November 29, 2011, in order to decrease more salinity, we 
 installed Ion exchange equipment and started the operation of such 
 equipment. 
-At this moment, we don't think there is any reactor coolant leakage 
 inside the primary containment vessel. 
 
Unit 5 (Outage due to regular inspection) 
-Sufficient level of reactor coolant to ensure safety is maintained. 
-At 5:00 am on March 19, 2011, we started the Residual Heat Removal System 
 Pump in order to cool the spent fuel pool. 
-At 2:45 pm on July 15, 2011, we started the operation of the original 
 Residual Heat Removal System (System B) by its original seawater pump. 
-At 10:11 am on December 22, 2011, since we finished the recovery work of 
 seawater pump (System B) of equipment water cooling system, we made a 
 trial run. At 11:25 am on the same day, we confirmed no abnormalities and 
 restarted the operation. 
 
Unit 6 (Outage due to regular inspection) 
-Sufficient level of reactor coolant to ensure safety is maintained. 
-At 10:14 pm on March 19, 2011, we started the Residual Heat Removal 
 System Pump of Unit 6 to cool down Spent Fuel Pool. 
-At 2:33 pm on September 15, 2011, we started separately cooling the 
 reactor through the Residual Heat Removal System and the spent fuel pool 
 through Equipment Cooling Water System and Fuel Pool Cooling System. 
 
Others 
-At around 10:00 am on June 13, 2011, we started the operation of the 
 circulating seawater purification facility installed at the screen area 
 of Unit 2 and 3. 
-At 8:00 pm on June 17, 2011, we started operation of Water Treatment 
 Facility against the accumulated water. At 6:00 pm on July 2, we started 
 the circulating injection cooling to inject the water, which was treated 
 by the accumulated water treatment system, to the reactors through the 
 buffer tank. 
-At 7:41 pm on August 19, 2011, we started treatment of accumulated water 
 by parallel operation of one line from the cesium adsorption instrument 
 to the decontamination instrument and the other treatment line of the 
 cesium adsorption instrument No.2. 
-At 2:06 pm on October 7, 2011, we started to spray purified accumulated 
 water brought from Unit 5 and 6 continually in order to prevent dust 
 scattering and potential fire outbreaks from the cut down trees. 
-On October 28, 2011, we started installation of the water proof wall at 
 the sea side, in front of the existing shore protection, Units 1-4, in 
 order to contain marine pollution by underground water. 
-At 12:25 pm on December 13, 2011, we started the re-circulating operation 
 of desalination facility (reverse osmosis membrane type) for the purpose 
 of suppression of condensed water after desalination treatment. 
-At 9:18 am on January 31, we started transfer of Sub-drain Water of Unit 
 6 to the temporary tank. We will conduct transferring to the temporary 
 tank appropriately. 
-At 1:56 pm on February 28, we started transfer the accumulated water from 
 the basement of turbine building of Unit 3 to Miscellaneous Solid Waste 
 Volume Reduction Treatment Building (High Temperature Incinerator 
 Building). 
-At 2:00 pm on February 28, we started transferring accumulated water from 
 basement of unit 2 turbine building to Centralized Radiation Waste 
 Treatment Facility Process Main building. 
-At 10:00 am to 4:00 pm on February 28, we transferred the accumulated 
 water from the basement of T/B, Unit 6 to the temporary tank. At 10:00 am 
 on February 29, we restarted the transfer. 
-As we confirmed that high radioactivity contaminated water is 
 accumulating in the pit of water circulating pump discharge valve of unit 
 3 pump chamber at the inspection of trench etc. conducted on January 19, 
 2012, from 8:51 am to 3:45 pm on February 28, 2012 we transferred 
 accumulated water from the pit to the basement of unit 2 turbine building. 
 At 8:17 am on February 29, we restarted the transfer. 
-At 8:37 am on February 29, the gradual decrease in the volume of treated 
 water was confirmed in the second cesium adsorption apparatus. In order 
 to conduct a backwashing of the filter, we suspended the apparatus. At 
 10:07 am, we restarted the apparatus. At 10:12 am, the water injection 
 volume reached at normal level (approx.34.4 m3/h). 
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