pointdir.cfg

plc中基于数据采集、发送接收、驱动、写入数据库

BEGIN_HEAD
	VERSION OF CONFIGER 2.0
	PROJECT  河南辉县永昌化工有限公司10万吨/年硝酸DCS项目
	ON   2006年12月18日
	AT   9:14:58
END_HEAD

BEGIN_AX
1,200,FIRQ-101,外管来液氨流量,DCS,t/h,7.2,10,0
1,200,FRCRA-102,入氨过滤器气氨流量,DCS,Nm3/h,7.2,800,0
1,200,FIRA-103,入氨空混合器空气流量,DCS,Nm3/h,7.2,60000,0
1,200,FI-106-1,进锅炉冷壁段给水流量,DCS,m3/h,7.2,36,0
1,200,FI-106-2,进锅炉主蒸发段给水流量,DCS,m3/h,7.2,300,0
1,200,FI-121,出工艺水泵工艺水流量,DCS,t/h,7.2,6.0,0.6
1,200,FI-122,稀硝酸泵出口流量,DCS,t/h,7.2,1.6,0
1,200,FIRQ-141,进成品酸储槽算流量,DCS,kg/h,7.2,30000,0
1,200,FICA-142,入吸收塔工艺水流量,DCS,t/h,7.2,8,0
1,200,FI-143,至二次空气冷却器二次空气流量,DCS,MPa,7.2,15000,0
1,200,FISA-148,出吸收塔冷却循环水流量,DCS,t/h,7.2,50,0
1,200,FISA-161,锅炉水循环泵出口去废热锅炉水流量,DCS,m3/h,7.2,300,0
1,200,FISA-162,汽包出口至减温器蒸汽流量,DCS,t/h,7.2,25,0
1,200,FIR-163,至蒸汽透平过热器蒸汽流量,DCS,t/h,7.2,25,0
1,200,FIRQ-164,中压蒸汽至管网蒸汽流量,DCS,t/h,7.2,6,0
1,200,FIRQ-201,自管来网底压蒸汽总管流量,DCS,Nm3/h,7.2,5000,0
1,200,FIQ-202,至管网循环水总管流量,DCS,t/h,7.2,3500,0
1,200,FIQ-203,脱盐水总管流量,DCS,t/h,7.2,0.6,0
1,200,DT-141,硝酸密度,DCS,kg/m3,7.2,1.0,0
1,200,LICAS-101A,氨蒸发器EA103A液位,DCS,%,7.2,100,0
1,200,LICAS-101B,氨蒸发器EA103B液位,DCS,%,7.2,100,0
1,200,LICSA-121,氧化氮分离器液位,DCS,%,7.2,100,0
1,200,LISA-123,排酸槽液位,DCS,%,7.2,100,0
1,200,LICA-142,吸收塔液位,DCS,%,7.2,100,0
1,200,LIA-143,补充循环水槽液位,DCS,%,7.2,100,0
1,200,LICA-144,漂白塔液位,DCS,%,7.2,100,0
1,200,LIA-146,开工槽液位,DCS,%,7.2,100,0
1,200,LIA-147,尾气分离器液位,DCS,%,7.2,100,0
1,200,LIA-148A,成品槽A液位,DCS,%,7.2,100,0
1,200,LIA-148B,成品槽B液位,DCS,%,7.2,100,0
1,200,LICA-161,除氧器液位,DCS,%,7.2,100,0
1,200,LICSA-162,汽包液位,DCS,%,7.2,100,0
1,200,LICSA-164,排污罐液位,DCS,%,7.2,100,0
1,200,LICSA-166,管道蒸汽分离器液位,DCS,%,7.2,100,0
1,200,PIC-101,氨蒸发器NO2气氨压力,DCS,MPa,7.2,1,0
1,200,PICA-102,氨过热器出口气氨压力,DCS,MPa,7.2,1.0,0
1,200,PI-104,氨过热器入口气氨压力,DCS,MPa,7.2,1.0,0
1,200,PDIA-105,氨过滤器压差,DCS,KPa,7.2,10,0
1,200,PDIA-106,空气过滤器压差,DCS,KPa,7.2,4,0
1,200,PIR-108,氨空混合器入口空气压力,DCS,MPa,7.2,0.6,0
1,200,PDI-143,空压机出口与氧化氮压缩机入口差压,DCS,KPa,7.2,100,0
1,200,PICA-144,吸收塔冷却回水至补充循环水槽压力,DCS,MPa,7.2,0.8,0
1,200,PDI-148,吸收塔压差,DCS,KPa,7.2,100,0
1,200,PIC-161,除氧器上部压力,DCS,MPa,7.2,1.6,0
1,200,PI-162,汽包压力,DCS,MPa,7.2,6.0,0
1,200,PICA-163,中压蒸汽到管网压力,DCS,MPa,7.2,6.0,0
1,200,PIC-164,管网中压蒸汽至蒸汽分离器压力,DCS,MPa,7.2,6.0,0
1,200,PIA-201,低压蒸汽总管压力,DCS,MPa,7.2,1.6,0
1,200,PIA-202,中压蒸汽总管压力,DCS,MPa,7.2,6.0,0
1,200,PISA-203,仪表用空气压力,DCS,MPa,7.2,1.0,0
1,200,PIA-204,密封空气总管压力,DCS,MPa,7.2,0.6,0
1,200,PIA-205,循环总管至管网压力,DCS,MPa,7.2,0.8,0
1,200,TI-100-1,液氨温度1,DCS,℃,7.2,50,0
1,200,TI-100-2,液氨温度2,DCS,℃,7.2,50,0
1,200,TI-100-5,65%硝酸温度,DCS,℃,7.2,100,0
1,200,TI-100-6,空气温度,DCS,℃,7.2,150,0
1,200,TI-100-7,60%硝酸温度1,DCS,℃,7.2,100,0
1,200,TI-100-8,60%硝酸温度2,DCS,℃,7.2,100,0
1,200,TI-100-21,冷却水温度1,DCS,℃,7.2,50,0
1,200,TI-100-22,冷却水温度2,DCS,℃,7.2,50,0
1,200,TI-100-23,壁炉温度1,DCS,℃,7.2,300,0
1,200,TI-100-24,壁炉温度2,DCS,℃,7.2,300,0
1,200,TI-100-25,壁炉温度3,DCS,℃,7.2,300,0
1,200,TI-100-26,壁炉温度4,DCS,℃,7.2,300,0
1,200,TI-100-27,壁炉温度5,DCS,℃,7.2,800,0
1,200,TI-100-31,NOX气体温度,DCS,℃,7.2,800,0
1,200,TI-100-40,蒸汽温度,DCS,℃,7.2,800,0
1,200,TI-100-41,过热蒸汽温度1,DCS,℃,7.1,200,0
1,200,TI-100-42,过热蒸汽温度2,DCS,℃,7.2,100,0
1,200,TICA-101,气氨温度1,DCS,℃,7.2,150,0
1,200,TI-102,气氨温度2,DCS,℃,7.2,150,0
1,200,TIR-103,空气温度,DCS,℃,7.2,300,0
1,200,TI-105,液氨温度,DCS,℃,7.2,50,0
1,200,TIR-120-1,氨空混合气温度,DCS,℃,7.2,300,0
1,200,TIR-120-2,NOX气体温度1,DCS,℃,7.2,1000,0
1,200,TIR-121-1,NOX气体温度2,DCS,℃,7.2,1000,0
1,200,TIR-121-2,NOX气体温度3,DCS,℃,7.2,1000,0
1,200,TIR-121-3,NOX气体温度4,DCS,℃,7.2,1000,0
1,200,TIR-122-1,34%硝酸温度1,DCS,℃,7.2,50,0
1,200,TIR-122-2,34%硝酸温度2,DCS,℃,7.2,50,0
1,200,TIR-141,硝酸温度,DCS,℃,7.2,100,0
1,200,TIRA-161,除氧水温度,DCS,℃,7.2,150,0
1,200,TIRA-162,过热蒸汽温度1,DCS,℃,7.2,500,0
1,200,TIRCA-163,过热蒸汽温度2,DCS,℃,7.2,500,0
1,200,TIR-164,过热蒸汽温度3,DCS,℃,7.2,500,0
1,200,HIC-101,氨蒸发器E103A去E103B液氨切断,DCS,%,7.2,100,0
1,200,HIC-104,气氨放空阀,DCS,%,7.2,100,0
1,200,HIC-141,二次空气冷却器入口空气量遥控,DCS,%,7.2,100,0
1,200,HIC-161,过热中压蒸汽放空,DCS,%,7.2,100,0
1,200,HV-101,氨蒸发器E103A去E103B液氨切断,DCS,%,7.2,100,0
1,200,HV-104,气氨放空阀,DCS,%,7.2,100,0
1,200,HV-121,点火器前氢气切断,DCS,%,7.2,100,0
1,200,HV-141,二次空气冷却器入口空气量遥控,DCS,%,7.2,100,0
1,200,HV-161,过热中压蒸汽放空,DCS,%,7.2,100,0
1,200,TV-101,氨过热器EA104氨出口温度调节,DCS,%,7.2,100,0
1,200,TV-163,蒸汽分离器FA103过热蒸汽入口温度调节,DCS,%,7.2,100,0
1,200,PV-101A,氨蒸发器NO2气氨压力调节,DCS,%,7.2,100,0
1,200,PV-101B,氨蒸发器NO2气氨压力调节,DCS,%,7.2,100,0
1,200,PV-102,氨蒸发器出口气氨压力调节,DCS,%,7.2,100,0
1,200,PV-144,吸收塔冷却回水到补充循环水槽压力调节,DCS,%,7.2,100,0
1,200,PV-161,除氧器EG101上部压力调节,DCS,%,7.2,100,0
1,200,PV-163,副产蒸汽压力调节,DCS,%,7.2,100,0
1,200,PV-164,管网中压蒸汽至蒸汽分离器压力调节,DCS,%,7.2,100,0
1,200,LV-101A,氨蒸发器EA103A液位调节,DCS,%,7.2,100,0
1,200,LV-101B,氨蒸发器EA103B液位调节,DCS,%,7.2,100,0
1,200,LV-121,氧化氮分离器液位调节,DCS,%,7.2,100,0
1,200,LV-142,吸收塔液位调节,DCS,%,7.2,100,0
1,200,LV-144,漂白塔液位调节,DCS,%,7.2,100,0
1,200,LV-161,除氧器液位调节,DCS,%,7.2,100,0
1,200,LV-162,汽包液位调节,DCS,%,7.2,100,0
1,200,LV-164,排污罐FA106液位调节,DCS,%,7.2,100,0
1,200,LV-166,管道分离器FA109液位调节,DCS,%,7.2,100,0
1,200,FV-102,入氨过滤器气氨流量调节,DCS,%,7.2,100,0
1,200,FV-142,工艺水泵至吸收塔工艺水流量调节,DCS,%,7.2,100,0
1,200,EMV-101,进氨过滤器前氨事故切断,DCS,%,7.2,100,0
1,200,L-P101A,1#电机电流,DCS,A,7.2,10,0
1,200,L-P101B,2#电机电流,DCS,A,7.2,10,0
1,200,L-P102A,3#电机电流,DCS,A,7.2,10,0
1,200,L-P102B,4#电机电流,DCS,A,7.2,10,0
1,200,L-P103A,5#电机电流,DCS,A,7.2,10,0
1,200,L-P103B,6#电机电流,DCS,A,7.2,10,0
1,200,L-P104A,7#电机电流,DCS,A,7.2,10,0
1,200,L-P104B,8#电机电流,DCS,A,7.2,10,0
1,200,L-P106A,9#电机电流,DCS,A,7.2,10,0
1,200,L-P106B,10#电机电流,DCS,A,7.2,10,0
1,200,L-P107A,11#电机电流,DCS,A,7.2,10,0
1,200,L-P107B,12#电机电流,DCS,A,7.2,10,0
1,200,L-P108A,13#电机电流,DCS,A,7.2,10,0
1,200,L-P108B,14#电机电流,DCS,A,7.2,10,0
1,200,L-P109,15#电机电流,DCS,A,7.2,10,0
1,200,L-P110,16#电机电流,DCS,A,7.2,10,0
1,200,L-P111A,17#电机电流,DCS,A,7.2,10,0
1,200,L-P111B,18#电机电流,DCS,A,7.2,10,0
1,200,L-P112A,19#电机电流,DCS,A,7.2,10,0
1,200,L-P112B,20#电机电流,DCS,A,7.2,10,0
1,200,L-P113A,21#电机电流,DCS,A,7.2,10,0
1,200,L-P113B,22#电机电流,DCS,A,7.2,10,0
1,200,TVS-101,氨过热器EA104氨出口温度调节,DCS,%,7.2,100,0
1,200,TVS-163,蒸汽分离器FA103过热蒸汽入口温度调节,DCS,%,7.2,100,0
1,200,PVS-101A,氨蒸发器NO2气氨压力调节,DCS,%,7.2,100,0
1,200,PVS-101B,氨蒸发器NO2气氨压力调节,DCS,%,7.2,100,0
1,200,PVS-102,氨蒸发器出口气氨压力调节,DCS,%,7.2,100,0
1,200,PVS-144,吸收塔冷却会水到补充循环水槽压力调节,DCS,%,7.2,100,0
1,200,PVS-161,除氧器EG101上部压力调节,DCS,%,7.2,100,0
1,200,PVS-163,副产蒸汽压力调节,DCS,%,7.2,100,0
1,200,PVS-164,管网中压蒸汽至蒸汽分离器压力调节,DCS,%,7.2,100,0
1,200,LVS-101A,氨蒸发器EA103A液位调节,DCS,%,7.2,100,0
1,200,LVS-101B,氨蒸发器EA103B液位调节,DCS,%,7.2,100,0
1,200,LVS-121,氧化氮分离器液位调节,DCS,%,7.2,100,0
1,200,LVS-142,吸收塔液位调节,DCS,%,7.2,100,0
1,200,LVS-144,漂白塔液位调节,DCS,%,7.2,100,0
1,200,LVS-161,除氧器液位调节,DCS,%,7.2,100,0
1,200,LVS-162,汽包液位调节,DCS,%,7.2,100,0
1,200,LVS-164,排污罐FA106液位调节,DCS,%,7.2,100,0
1,200,LVS-166,管道分离器FA109液位调节,DCS,%,7.2,100,0
1,200,FVS-102,入氨过滤器气氨流量调节,DCS,%,7.2,100,0
1,200,FVS-142,工艺水泵至吸收塔工艺水流量调节,DCS,%,7.2,100,0
1,200,FIRQ-101Q,外管来液氨流量累计,DCS,t/h,7.2,1000000,0
1,200,FIRQ-141Q,进成品酸储槽算流量累计,DCS,kg/h,7.2,100000,0
1,200,FIRQ-164Q,中压蒸汽至管网蒸汽流量累计,DCS,t/h,7.2,1000000,0
1,200,FIRQ-201Q,自管来网底压蒸汽总管流量累计,DCS,Nm3/h,7.2,1000000,0
1,200,FIQ-202Q,至管网循环水总管流量累计,DCS,t/h,7.2,1000000,0
1,200,FIQ-203Q,脱盐水总管流量累计,DCS,t/h,7.2,1000000,0
1,200,FFNK,氨控比,DCS,%,7.2,1.0,0
1,200,D1NAO035,DPU1模拟量上网点035,BAK,%,7.2,0,100
 1,200,D1NAO036,DPU1模拟量上网点036,BAK,%,7.2,0,100
 1,200,D1NAO037,DPU1模拟量上网点037,BAK,%,7.2,0,100
 1,200,D1NAO038,DPU1模拟量上网点038,BAK,%,7.2,0,100
 1,200,D1NAO039,DPU1模拟量上网点039,BAK,%,7.2,0,100
 1,200,D1NAO040,DPU1模拟量上网点040,BAK,%,7.2,0,100
 1,200,D1NAO041,DPU1模拟量上网点041,BAK,%,7.2,0,100
 1,200,D1NAO042,DPU1模拟量上网点042,BAK,%,7.2,0,100
 1,200,D1NAO043,DPU1模拟量上网点043,BAK,%,7.2,0,100
 1,200,D1NAO044,DPU1模拟量上网点044,BAK,%,7.2,0,100
 1,200,D1NAO045,DPU1模拟量上网点045,BAK,%,7.2,0,100
 1,200,D1NAO046,DPU1模拟量上网点046,BAK,%,7.2,0,100
 1,200,D1NAO047,DPU1模拟量上网点047,BAK,%,7.2,0,100
 1,200,D1NAO048,DPU1模拟量上网点048,BAK,%,7.2,0,100
 1,200,D1NAO049,DPU1模拟量上网点049,BAK,%,7.2,0,100
 1,200,D1NAO050,DPU1模拟量上网点050,BAK,%,7.2,0,100
 1,200,D1NAO051,DPU1模拟量上网点051,BAK,%,7.2,0,100
 1,200,D1NAO052,DPU1模拟量上网点052,BAK,%,7.2,0,100
 1,200,D1NAO053,DPU1模拟量上网点053,BAK,%,7.2,0,100
 1,200,D1NAO054,DPU1模拟量上网点054,BAK,%,7.2,0,100
 1,200,D1NAO055,DPU1模拟量上网点055,BAK,%,7.2,0,100
 1,200,D1NAO056,DPU1模拟量上网点056,BAK,%,7.2,0,100
 1,200,D1NAO057,DPU1模拟量上网点057,BAK,%,7.2,0,100
 1,200,D1NAO058,DPU1模拟量上网点058,BAK,%,7.2,0,100
 1,200,D1NAO059,DPU1模拟量上网点059,BAK,%,7.2,0,100
 1,200,D1NAO060,DPU1模拟量上网点060,BAK,%,7.2,0,100
 1,200,D1NAO061,DPU1模拟量上网点061,BAK,%,7.2,0,100
 1,200,D1NAO062,DPU1模拟量上网点062,BAK,%,7.2,0,100
 1,200,D1NAO063,DPU1模拟量上网点063,BAK,%,7.2,0,100
 1,200,D1NAO064,DPU1模拟量上网点064,BAK,%,7.2,0,100
 1,200,D1NAO065,DPU1模拟量上网点065,BAK,%,7.2,0,100
 1,200,D1NAO066,DPU1模拟量上网点066,BAK,%,7.2,0,100
 1,200,D1NAO067,DPU1模拟量上网点067,BAK,%,7.2,0,100
 1,200,D1NAO068,DPU1模拟量上网点068,BAK,%,7.2,0,100
 1,200,D1NAO069,DPU1模拟量上网点069,BAK,%,7.2,0,100
 1,200,D1NAO070,DPU1模拟量上网点070,BAK,%,7.2,0,100
 1,200,D1NAO071,DPU1模拟量上网点071,BAK,%,7.2,0,100
 1,200,D1NAO072,DPU1模拟量上网点072,BAK,%,7.2,0,100
 1,200,D1NAO073,DPU1模拟量上网点073,BAK,%,7.2,0,100
 1,200,D1NAO074,DPU1模拟量上网点074,BAK,%,7.2,0,100
 1,200,D1NAO075,DPU1模拟量上网点075,BAK,%,7.2,0,100
 1,200,D1NAO076,DPU1模拟量上网点076,BAK,%,7.2,0,100
 1,200,D1NAO077,DPU1模拟量上网点077,BAK,%,7.2,0,100
 1,200,D1NAO078,DPU1模拟量上网点078,BAK,%,7.2,0,100
 1,200,D1NAO079,DPU1模拟量上网点079,BAK,%,7.2,0,100
 1,200,D1NAO080,DPU1模拟量上网点080,BAK,%,7.2,0,100
 1,200,D1NAO081,DPU1模拟量上网点081,BAK,%,7.2,0,100
 1,200,D1NAO082,DPU1模拟量上网点082,BAK,%,7.2,0,100
 1,200,D1NAO083,DPU1模拟量上网点083,BAK,%,7.2,0,100
 1,200,D1NAO084,DPU1模拟量上网点084,BAK,%,7.2,0,100
 1,200,D1NAO085,DPU1模拟量上网点085,BAK,%,7.2,0,100
 1,200,D1NAO086,DPU1模拟量上网点086,BAK,%,7.2,0,100
 1,200,D1NAO087,DPU1模拟量上网点087,BAK,%,7.2,0,100
 1,200,D1NAO088,DPU1模拟量上网点088,BAK,%,7.2,0,100
 1,200,D1NAO089,DPU1模拟量上网点089,BAK,%,7.2,0,100
 1,200,D1NAO090,DPU1模拟量上网点090,BAK,%,7.2,0,100
 1,200,D1NAO091,DPU1模拟量上网点091,BAK,%,7.2,0,100
 1,200,D1NAO092,DPU1模拟量上网点092,BAK,%,7.2,0,100
 1,200,D1NAO093,DPU1模拟量上网点093,BAK,%,7.2,0,100
 1,200,D1NAO094,DPU1模拟量上网点094,BAK,%,7.2,0,100
 1,200,D1NAO095,DPU1模拟量上网点095,BAK,%,7.2,0,100
 1,200,D1NAO096,DPU1模拟量上网点096,BAK,%,7.2,0,100
 1,200,D1NAO097,DPU1模拟量上网点097,BAK,%,7.2,0,100
 1,200,D1NAO098,DPU1模拟量上网点098,BAK,%,7.2,0,100
 1,200,D1NAO099,DPU1模拟量上网点099,BAK,%,7.2,0,100
 1,200,D1NAO100,DPU1模拟量上网点100,BAK,%,7.2,0,100 
 1,200,wh,wend,c,%,7.2,0,100
1,200,11111,E501出口压力,TBL,MPa,7.2, 3, 0 
END_AX

BEGIN_DX
1,200,ZSO-101A,氨蒸发器EA103A液位阀开,EGD,F,T
1,200,ZSC-101A,氨蒸发器EA103A液位阀关,EGD,F,T
1,200,ZSO-101B,氨蒸发器EA103B液位阀开,EGD,F,T
1,200,ZSC-101B,氨蒸发器EA103B液位阀关,EGD,F,T
1,200,ZSO-102,入氨过滤器气氨流量阀开,EGD,F,T
1,200,ZSC-102,入氨过滤器气氨流量阀关,EGD,F,T
1,200,ZSO-104,气氨放空阀开,EGD,F,T
1,200,ZSC-104,气氨放空阀关,EGD,F,T
1,200,ZSO-121,点火器前氢气切断阀开,EGD,F,T
1,200,ZSC-121,点火器前氢气切断阀关,EGD,F,T
1,200,ZSO-142,吸收塔液位调节阀开,EGD,F,T
1,200,ZSC-142,吸收塔液位调节阀关,EGD,F,T
1,200,ZSO-144,漂白塔液位调节阀开,EGD,F,T
1,200,ZSC-144,漂白塔液位调节阀关,EGD,F,T
1,200,ZSO-161,除氧器液位调节阀开,EGD,F,T
1,200,ZSC-161,除氧器液位调节阀关,EGD,F,T
1,200,ZSO-163,蒸汽分离器FA103过热蒸汽入口温度调节阀开,EGD,F,T
1,200,ZSC-163,蒸汽分离器FA103过热蒸汽入口温度调节阀关,EGD,F,T
1,200,EZSO-101,进氨过滤器前氨事故切断阀开,EGD,F,T
1,200,EZSC-101,进氨过滤器前氨事故切断阀关,EGD,F,T
1,200,ZS-141,吸收塔工艺法状态,EGD,F,T
1,200,LS-141,尾气预热器液位报警,EGD,F,T
1,200,LS-163,汽包液位报警、联锁,EGD,F,T
1,200,LS-167A,磷酸钠溶解槽液位联锁、报警,EGD,F,T
1,200,LS-167B,磷酸钠溶解槽液位联锁、报警,EGD,F,T
1,200,LS-168,联胺溶解槽液位联锁、报警,EGD,F,T
1,200,PB-101,氧化炉旁按钮状态,EGD,F,T
1,200,PB-102,吸收塔旁按钮状态,EGD,F,T
1,200,PB-103,氧化炉就地盘按钮1状态,EGD,F,T
1,200,PB-104,氧化炉就地盘按钮2状态,EGD,F,T
1,200,PB-105,氧化炉就地盘按钮1状态,EGD,F,T
1,200,R-P101A,1#电机运行信号,EGD,F,T
1,200,F-P101A,1#电气故障信号,EGD,F,T
1,200,R-P101B,2#电机运行信号,EGD,F,T
1,200,F-P101B,2#电气故障信号,EGD,F,T
1,200,R-P102A,3#电机运行信号,EGD,F,T
1,200,F-P102A,3#电气故障信号,EGD,F,T
1,200,R-P102B,4#电机运行信号,EGD,F,T
1,200,F-P102B,4#电气故障信号,EGD,F,T
1,200,R-P103A,5#电机运行信号,EGD,F,T
1,200,F-P103A,5#电气故障信号,EGD,F,T
1,200,R-P103B,6#电机运行信号,EGD,F,T
1,200,F-P103B,6#电气故障信号,EGD,F,T
1,200,R-P104A,7#电机运行信号,EGD,F,T
1,200,F-P104A,7#电气故障信号,EGD,F,T
1,200,R-P104B,8#电机运行信号,EGD,F,T
1,200,F-P104B,8#电气故障信号,EGD,F,T
1,200,R-P106A,9#电机运行信号,EGD,F,T