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1、文文 件件 种种 类类 版本 Rev 日期 Date 状态 Status 编写 Drafted by 校核 Checked by 审核 Reviewed by 批准 Approved by 修改说明 Modification-Observation A 2010-3-31 PRE 首次 FANGCHENGGANG NUCLEAR POWER PHASE (21000MW) PROJECT 文件编码文件编码 DOC. NO BL 9 17TEU 002 DNFF 45 GN 题目题目 TITLE: System Manual-TEU Chapter 2, 3, 4, 5 Function, Ge

2、neral Design, Description and Definition of Equipment, Operating Parameters 工程号工程号 Project NO BL 文件类型文件类型 Document Type 子项号子项号 Sub-Item NO 设计阶段设计阶段 Engineering Phase C 参考文件参考文件编码编码 Reference Document PK817TEU002B30245GN Rev E Document Category A: Identical B: Modified C: New 工程设计 甲级 号：A144008121 工程咨

3、询 甲级 工咨甲 22420070005 CNPDC 中广核工程设计中广核工程设计 National A grade engineering designing, Certification NO: A144008121 CHINA NUCLEAR POWER DESIGN COMPANY, (SHENZHEN) National A grade engineering consulting, Certification NO: 22420070005 内部编码内部编码Internal Code This document is the property of CNPDC It must no

4、t be used、reproduced、transmitted or disclosed without the prior written permission of CNPDC 本文件之产权属于中广核工程设计 。未获本公司 ，任何人不得擅自使用、 、传递或泄露该文件。 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A and Definition of Equipment, Operating Parameters 版本版本 REVISION RECORD 版本版本 Rev 日

5、期日期 Date 状态状态 Status 编写编写 Drafted by 校核校核 Checked by 审核审核 Reviewed by 批准批准 Approved by 修改修改说明说明 Modification-Observation System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A and Definition of Equipment, Operating Parameters 文件修改文件修改 MODIFICATION RECORD 版本版本 Rev 日期日期 Date

6、章节章节 ITEM 页码页码 PAGE 修改范围及依据修改范围及依据 MODIFICATION A 2010-3-31 首次 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 1/5 and Definition of Equipment, Operating Parameters CONTENTS MODIFICATION RECORD . 2 CONTENTS. 1 2 FUNCTION . 1 2.1 FUNCTION . 1 2.1.1 2.1.2 2.1.3 2.1.4 2

7、.1.5 General . 1 Waste storage and monitoring. 2 Treatment by filtration . 2 Treatment by evaporation . 2 Treatment by demineralization . 3 2.2 SAFETY FUNCTION . 3 3 GENERAL DESIGN . 4 3.1 DESIGN BASES AND SAFETY CRITERIA . 4 3.2 EQUIPMENT DESIGN . 7 3.2.1 3.2.2 3.2.3 Head storage . 7 Neutralizing s

8、tation . 7 Waste evaporator. 7 3.2.3.1 RECIRCULATION PUMP . 7 3.2.3.2 HEATER . 8 3.2.3.3 EVAPORATOR . 8 3.2.3.4 DECONTAMINATION COLUMN . 8 3.2.3.5 CONDENSER. 9 3.2.3.6 ACCESSIBILITY TO EQUIPMENT . 9 3.2.3.7 LOCAL SAMPLING . 9 3.2.4 Demineralizer . 10 3.2.4.1 TREATMENT CHANNEL . 10 System Manual-TEU

9、Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 2/5 and Definition of Equipment, Operating Parameters 3.2.4.2 LOCAL SAMPLING . 10 3.2.5 TEU-TES connections . 10 3.2.5.1 EVAPORATION CONCENTRATE REMOVAL . 10 3.2.5.2 SPENT RESIN TRANSFER. 10 3.2.6 3.2.7 3.2.8 3.2.9 3.2.10 3.2.11 Protecti

10、on of circuits containing concentrate solutions . 11 Anti-foam . 11 Distillate monitor . 11 Filters . 11 Pumps . 12 Demineralizers . 12 3.3 CHOICE OF MATERIAL-CONSTRUCTION . 12 3.3.1 3.3.2 3.3.3 3.3.4 Equipment in contact with fluids to be treated or treated fluids . 12 Equipment in contact with ser

11、vice fluids . 13 Barrier, ion exchange or filtration materials . 13 Construction . 13 4 DESCRIPTION AND DEFINITION OF EQUIPMENT . 13 4.1 DESCRIPTION. 13 4.1.1 4.1.2 4.1.3 Unit relative to the head storage . 14 Unit relative to the chemical neutralization station . 15 Unit relative to the decontamina

12、tion (by evaporation) station . 15 4.1.3.1 EVAPORATION FEED PUMP 9TEU005PO. 15 4.1.3.2 EVAPORATION FEED PUMP 9TEU013PO. 15 4.1.3.3 EVAPORATION AND DECONTAMINATION STATION . 16 4.1.3.4 LOCAL SAMPLINGS . 17 4.1.4 4.1.5 4.1.6 Unit relative to the demineralization station . 18 Unit relative to the filtr

13、ation station . 18 Unit relative to treated water monitoring . 18 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 3/5 and Definition of Equipment, Operating Parameters 4.1.7 Interfaces with other systems . 19 4.2 CHARACTERISTICS . 19 4.2.1 Characteristics of fluids t

14、o be treated . 19 4.2.1.1 PROCESS DRAINS . 19 4.2.1.3 CHEMICAL EFFLUENTS. 20 4.2.1.4 TEP WASTE . 21 4.2.1.5 EXTRA STORAGE . 21 4.2.2 4.2.3 4.2.4 Characteristics of solutions after treatment . 21 Characteristics of utilities. 22 Equipment characteristics . 22 4.2.4.1 EQUIPMENT CHARACTERISTICS ASSOCIA

15、TED WITH HEAD STORAGE . 22 4.2.4.2. EQUIPMENT CHARACTERISTICS ASSOCIATED WITH FILTRATION STATION . 24 4.3 LAYOUT . 28 5 OPERATING PARAMETERS . 31 5.1 NORMAL OPERATION . 31 5.1.1 Holdup . 31 5.1.1.1 PROCESS DRAINS . 31 5.1.1.2 FLOOR DRAINS. 31 5.1.1.3 CHEMICAL EFFLUENTS. 31 5.1.2 Normal operating con

16、ditions of the waste evaporator . 31 5.1.3 Operating conditions, startup and normal stopping of the demineralization station . 32 5.1.4 Distillate monitor . 33 5.2 PARTICULAR STEADY OPERATION . 33 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 4/5 and Definition of

17、Equipment, Operating Parameters 5.2.1 Hold up . 33 5.2.1.1 TREATMENT OF TEP DEGASSED PRIMARY WASTE . 33 5.2.1.2 TREATMENT OF TEP CONCENTRATE MONITOR TANK CONTENTS (9TEP007BA) . 33 5.2.1.3 TREATMENT OF CONTENTS OF A TER TANK BY THE WASTE EVAPORATOR . 34 5.2.1.4 TREATMENT OF SEL TANK CONTENTS BY THE W

18、ASTE EVAPORATOR . 34 5.2.1.5 TREATMENT OF SRE TANK CONTENTS . 34 5.2.1.6 TREATMENT OF DISTILLATE MONITORING TANK CONTENTS (9TEU009BA AND 9TEU 010BA) . 34 5.2.2 Treatment of the contents of 9TEU016BA and 9TEU017BA extra storage 35 5.2.3 Neutralization . 35 5.3 PARTICULAR TRANSIENT OPERATION . 36 5.3.

19、1 5.3.2 5.3.3 5.3.4 5.3.5 Aerated TEG defect . 36 RRI isolation valve on condenser 9TEU001CS. 36 Tripping distillate pump 9TEU007PO . 36 Heater thermal shock . 36 Long duration SED failure on tank 9TEU015BA related to the mechanical seals of recirculation pump 9TEU006PO . 37 5.4 STARTUP AND NORMAL S

20、HUTDOWN . 37 5.4.1 Start-up . 37 5.4.1.1 REACHING HOT STANDBY . 37 5.4.1.2 OPERATION . 38 5.4.2 Normal shutdown . 38 5.4.2.1 HOT STANDBY - MODE 6 . 39 5.4.2.2 SHUTDOWN - MODE 0 . 39 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 5/5 and Definition of Equipment, Oper

21、ating Parameters 5.4.3 Automatic shutdown . 39 5.5 OTHER OPERATIONS . 40 5.5.1 5.5.2 5.5.3 5.5.4 5.5.5 5.5.6 5.5.7 Transfer of concentrates to tank 9TES001BA . 40 Return of tank 9TES001BA contents for reprocessing . 40 Waste evaporator draining . 41 Anti-foam injection . 41 Transfer of resins toward

22、s 9TES002 BA or 9TES003BA . 41 Treatment of special solutions . 41 Transfer to 9TEU016BA or 9TEU017BA . 41 5.6 CONTROL PRINCIPLES . 42 5.6.1 5.6.2 5.6.3 5.6.4 5.6.5 5.6.6 5.6.7 5.6.8 5.6.9 Evaporator 9TEU001EV . 42 Condenser 9TEU001CS . 42 SVA condensate tank 9TEU014BA . 42 SVA steam supply flowrate

23、. 42 Anti-foam device. 43 Distillate conductivity . 43 Basic principles for demineralization control . 43 Storage (9TEU001BA to 9TEU006BA, 9TEU016BA, 9TEU 017BA) . 43 Distillate monitor (9TEU009BA and 9TEU010BA). . 43 System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 1

24、/43 and Definition of Equipment, Operating Parameters 2 FUNCTION 2.1 FUNCTION 2.1.1 General The Liquid Waste Treatment System (TEU) is common to both units. It stores, monitors and processes non-reusable liquid waste from the reactor coolant system. Liquid waste is collected mainly by the Nuclear Is

25、land Vent and Drain System (RPE) common to both units. The TEU system can also process waste from miscellaneous sources: - waste from Liquid Waste Discharge (TER) for reprocessing, - waste from Conventional Island Liquid Waste Discharge reprocessing, (SEL) for - laundry waste from the hot laundry co

26、llected by the Sewage Recovery System (SRE), - waste contained in the intermediate Recycle System (TEP), and in the concentrate tank of the Boron - The concentrate for reprocessing from Solid Waste Treatment System (TES). All these types of waste are separated into three categories: - - - process dr

27、ains, chemical effluents, floor drains. The sorting of effluents into different categories is carried out at the source by the RPE system to ensure that the radiological and chemical composition of effluents complies with the processing lines located downstream from the storage According to the cate

28、gory the criteria for effluent sorting are as follows: . - Process drains are generally active effluents of low chemical content (the threshold depends on economic factors, the aim being to minimize the global cost of treatment, solid waste management included). - Chemical effluents are generally ac

29、tive effluents of high chemical content. - Floor drains are generally less active effluents (activity level below release threshold) of varying chemical content. System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 2/43 and Definition of Equipment, Operating Parameters Th

30、e treatment facilities can be resumed by the following chart: 2.1.2 Waste storage and monitoring The treatment unit includes a selective head storage tank for waste of the three following categories: - - - process drains, chemical effluents, floor drains. Two additive extra storage are available for

31、 the different categories of effluents in case of treatment lines unavailability. Storage allows monitoring of the activity level and physico-chemical characteristics of waste, by sampling (REN). Such monitoring results in, either simple filtration followed by direct routing of the liquid waste to t

32、he TER demineralization. , or where necessary treatment by evaporation or A neutralizing station is linked to the chemical, floor drain and extra storage has the following functions: - adjusting the pH of liquid waste before treatment in the waste evaporator to: . It . . increase the solubility of c

33、oncentrated waste, improve the quality of the waste - concrete conditioning (TES), - adjusting the pH of waste for direct discharge to within acceptable limits (generally 5.5 to 9). 2.1.3 Treatment by filtration In this case the waste is filtered on a cartridge filter, then routed to the TER monitor

34、ing before release. 2.1.4 Treatment by evaporation for In this case, after filtration, the waste is treated by a waste evaporator in order to separate it into two distinct liquid phases: - the concentrate containing almost all the active salts in solution and the particles in ACTIVITY LOW 9.25106Bq/

35、m3 HIGH 9.25 106Bq/m3 Chemical content low Filtration Demineralization Chemical content high Filtration Evaporation System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 3/43 and Definition of Equipment, Operating Parameters suspension, - a physically and chemically pure d

36、istillate. The concentrates are routed towards the TES system storage tank to be drummed. After monitoring by sampling, the distillates are routed to the TER . Otherwise they are recycled upstream from the evaporator for reprocessing. 2.1.5 Treatment by demineralization Process drains are generally

37、treated, after filtration, by two demineralizers in series. After treatment, the waste is stored with distillates. 2.2 SAFETY FUNCTION The TEU system has no direct safety function. However, it has an important role in the protection of the population against ionizing radiation because it decontamina

38、tes all radioactive liquid waste to limit the discharge activity. In addition the system is surrounded by all means of radioprotection required for the safety of operating nel: shielding walls, remote control, remote maintenance (for example: water flushing for spent resin), pneumatic valves, remote

39、 hand actuators, and so on. System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 4/43 and Definition of Equipment, Operating Parameters 3 GENERAL DESIGN 3.1 DESIGN BASES AND SAFETY CRITERIA The Liquid Waste Treatment System (TEU) is designed in accordance with the followi

40、ng criteria. 1. SAFETY CRITERIA 1.1. Reference station 1.2. PRC criteria 1.3. French criteria LNPS units 3 & 4 PSAR section 11.2.1 R subsection 2.3.7 2. CLASSIFICATION BLX30000002DOZJ03GN 3. ENGINEERING CODES AND STANDARDS - Reference to particular engineering rules and standards ASME VIII, TEMA

41、 , CODAP 4. FUNCTIONAL CRITERIA 4.1. R conditions in case of total loss of the system 4.2. Active component redundance 4.3. Emergency power supply Electrical redundance RFS 1.3.a not required No Not required 5. ENVIRONMENT AND INSTALLATION 5.1. Separation of redundant components - Active components

42、- Passive components 5.2. External attacks against which the system is protected - LOCA - Steam break - Pipe whip - Turbine missiles . high trajectory . low trajectory - Miscellaneous missiles - Airplane crash - Safe shutdown earthquake - Floods Not applicable Not applicable Not applicable No, low p

43、robability Not applicable Not necessary Not necessary Partially (see classification list) Yes System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 5/43 and Definition of Equipment, Operating Parameters The waste is selectively collected and processed differently according

44、 to category. Process drains are generally treated by demineralization if their chemical characteristics comply with the rules described above (see chapter 2 2.1). Otherwise, process drains with high chemical content, inconsistent with treatment by demineralization are treated by evaporation. Chemic

45、al effluents are generally treated by evaporation but when their specific activity is below the permissible value, they can be released by simple filtration. Floor drains are generally released after filtration. In case of high activity level, they are treated by evaporation. Head storage includes f

46、our groups of : - Drying - Noxious vapours or gases (other than those caused by fire) - Liquids (escaping from breaks in the piping) - Ionizing radiation - Explosions: from in-site - Particular precautions against fire - Tornado and induced missiles 5.3. Attacks on other systems - Pipe whip - Missil

47、es - Noxious vapours or gases (other than those caused by fire) - Flooding liquids - Ionizing radiation - Explosion - Fire No No No Yes Not necessary No No No No Yes Yes Yes No No 6. OPERATING CRITERIA 6.1. In service inspection 6.2. Periodic tests 6.3. Zoning 6.4. Protection against sabotage Yes. P

48、artially. No Yes Yes System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 6/43 and Definition of Equipment, Operating Parameters 2 35m3 : 2 20m3 2 20m3 2 100m3 - Process drains : 9TEU001BA, 9TEU 002BA - Chemical effluents 9TEU005BA, 9TEU006BA - Floor drains : 9TEU003BA, 9

49、TEU004BA - Extra storage : 9TEU016BA, 9TEU017BA each having a volume of 35m3. Monitoring storage is made of two distillate The extra storage or chemical effluent Furthermore these reprocessing. Because collect waste from the process drain in case of unavailability of can collect effluents from the S

50、EL or floor drain the treatment lines. or the TER for of the possibility of effluents mixing, the waste collected in these is treated by evaporation. When the specific activity is below the after filtering. give the possibility to acceptable value, these effluents can be released into TER Normally c

51、onnected to chemical drains treatment these have longer campaign of treatment for TEU evaporator. The average amount of waste to be treated for one unit is: - Process drains: 2250m3/year from the RPE divided up into: . 1250m3/year resin sluice water, . 1000m3/year of primary leakage, rinsings and dr

52、ains. The radioactivity contained in 2250m3/year of process drains is equivalent to that contained in 500 m3 of deaerated reactor coolant (DRC). - Chemical effluents: 1500m3/year The radioactivity contained in 1500m3/year of chemical effluents is equivalent to that contained in 1000m3 of deaerated r

53、eactor coolant (DRC). - Floor drains: 5000m3/year The radioactivity contained in 5000m3/year of floor drains is equivalent to that contained in 55m3 of deaerated reactor coolant (DRC). In addition 1250m3 of service effluents can be routed to the floor drain TER Service effluents come from showers or

54、 laundry. The filtration treatment flowrate is 27.2m3/h. The demineralization treatment flowrate is 10m3/h. The evaporation treatment flowrate is 3.15t/h. or the System Manual-TEU Chapter 2, 3, 4, 5 Function, General Design, Description Rev A 7/43 and Definition of Equipment, Operating Parameters 3.

55、2 EQUIPMENT DESIGN 3.2.1 Head storage The eight head storage contents of one of the two receiving incoming waste. are arranged in four groups of two so that the may be monitored and treated when the other one is A mixing device limits accumulation of solid particles at the bottom in the provides cor

56、rect sampling. and Suspended particles are retained by filters located upstream from the waste evaporator or upstream from the demineralizers or, naturally, on the filtration line. The process drain, chemical effluents, the floor drain and extra storage located in rooms designed to retain waste in c

57、ase of tank failure. are Process drain 9TEU001BA and 9TEU002BA are kept permanently under sub-atmospheric pressure (absolute pressure about 0.096 MPa) by the Gaseous Waste Treatment System (TEG aerated subsystem) fans to limit the gas contamination of the rooms and to change the air above water surf

58、ace to prevent formation of an explosive mixture by hydrogen degassing. The other storage are at atmospheric pressure. If needed, it is possible to route the waste, via a filter, towards TER storage later treatment. 3.2.2 Neutralizing station for Neutralization, which is done in storage must be very

59、 accurate. for floor drains and chemical drains, The amount of chemical reagent to be injected is computed from the results of tank sampling. The neutralization pumps are adjustable flowrate volumetric metering feed pumps. There is no neutralization in the process drains storage . The extra storage

60、are equipped with chemical additive pipes. 3.2.3 Waste evaporator The evaporator may process fouling solutions; it is of vertical forced circulation heater design. 3.2.3.1 Recirculation pump This pump operates at a high circulation flowrate (approximately 500m3/h) which provides: System Manual-TEU Chapt