123456789101112131415161718192021222324252627282930313233343536373839404142434445464748495051525354555657585960616263646566676869707172737475767778798081828384858687888990919293949596979899100101102103104105106107108109110111112113114115116117118119120121122123124125126127128129130131132133134135136137138139140141142143144145146147148149150151152153154155156157158159160161162163164165166167168169170171172173174175176177178179180181182183184185186187188189190191192193194195196197198199200201202203204205206207208209210211212213214215216217218219220221222223224225226227228229230231232233234235236237238239240241242243244245246247248249250251252253254255256257258259260261262263264265266267268269270271272273274275276277278279280281282283284285286287288289290291292293294295296297298299300301302303304305306307308309310311312313314315316317318319320321322323324325326327328329330331332333334335336337338339340341342343344345346347348349350351352353354355356357358359360361362363364365366367368369370371372373374375376377378379380381382383384385386387388389390391392393394395396397398399400401402403404405406407408409410411412413414415416417418419420421422423424425426427428429430431432433434435436437438439440441442443444445446447448449450451452453454455456457458459460461462463464465466467468469470471472473474475476477478479480481482483484485486487488489490491492493494495496497498499500501502503504505506507508509510511512513514515516517518519520521522523524525526527528529530531532533534535536537538539540541542543544545546547548549550551552553554555556557558559560561562563564565566567568569570571572573574575576577578579580581582583584585586587588589590591592593594595596597598599600601602603604605606607608609610611612613614615616617618619620621622623624625626627628629630631632633634635636637638639640641642643644645646647648649650651652653654655656657658659660661662663664665666667668669670671672673674675676677678679680681682683684685686687688689690691692693694695696697698699700701702703704705706707708709710711712713714715716717718719720721722723724725726727728729730731732733734735736737738739740741742743744745746747748749750751752753754755756757758759760761762763764765766767768769770771772773774775776777778779780781782783784785786787788789790791792793794795796797798799800801802803804805806807808809810811812813814815816817818819820821822823824825826827828829830831832833 |
- {
- "norm": "xxxtp",
- "system": "作为一位经验丰富的污水处理厂专家,请根据以下污水处理厂的关键指标数据,回答后续的一系列问题。\n对于每个问题,请给出最符合当前数据的选项作为答案:\n污水处理厂的关键指标数据如下:\n\n<begin>\n出水总磷:当前值为{{TP_off}}mg/L,标准值为{{TP_off_name}}mg/L ,管控值为{{TP_off_con}}mg/L。\n进水总磷:当前的值为{{TP_in}}mg/L,设计值为{{TP_in_name}}mg/L。\n进水TDS:当前的值为{{TDS_in}}mg/L,管控值为{{TDS_in_name}}mg/L。\n进水水温:当前值是{{T}}℃。
进水pH:当前值是{{pH}}。\n进水碳磷比:是{{c}},稳态值是{{BTP_wending}}。\n{% for item in doana_items -%}\n厌氧池{{loop.index}}溶解氧:当前值是{{item.DO_ana}}mg/L,稳态值是{{item.DO_ana_wentai}}mg/L。\n{%- endfor %}\n{% for item in sv_items -%}\n池{{loop.index}}污泥沉降比:当前的值为{{item.SV}}%,管控值为{{item.SV_con}}%。\n{%- endfor %}\n{% for item in svi_items -%}\n池{{loop.index}}污泥体积指数:当前的值为{{item.SVI}}mL/g,管控值为{{item.SVI_con}}mL/g。\n{%- endfor %}\n<line>\n化学除磷率{{TP_LV_continuity}}下降。\n出水总磷{{cs_continuity}}连续两个相邻检测数据超标。\n进水总量与设计值的比较是{{cs_all_compare}}\n<end>\n\n出水总磷是否存在连续两次超标?(存在/不存在)。\n进水总磷高于设计值?(低于设计值/高于设计值但是低于110%/高于设计值110%)。\n各个厌氧池的溶解氧当前值是否超出各自的稳态值? (都未超出/至少一个池子有超出)\n各个池子的污泥沉降比和污泥体积指数是否大于其对应的管控值?(都未大于 /至少一个池子有大于)\n进水水温是否低于10℃?(是/否)。\n进水TDS是否超出管控值?(超出/未超出)。\n进水pH是否低于6.5?(是/否)。\n进水总量与设计值的比较是?(小于设计值/大于但未超过110%/超过110%)。\n进水碳磷比是否低于稳态值?(是/否)。\n化学除磷率是否存在下降?(存在/不存在)。\n\n请基于专业知识和经验,给出你的判断,无需列出判断依据。让我们认真审视数据,给出客观准确的评估。只需给出问题后括号内的选项即可,无需解释。",
- "prompt": "<begin>\n除磷药剂投加量: 当前值是{{cltjl}},建议调整值是{{cltjl_wentai}}。\n{% for item in doo_items -%}\n好氧池{{loop.index}}溶解氧:当前值是{{item.DO_O}},建议调整值是{{item.DO_O_wentai}}。\n{%- endfor %}\n{% for item in mlss_items -%}\n池{{loop.index}}生化池污泥浓度 MLSS:当前值{{item.MLSS}},建议调整值{{item.MLSS_wentai}}。\n{%- endfor %}\n进水水量:当前值是{{Q_in}},建议调整值是{{Q_in_wentai}}。\n干污泥量: 当前值是{{gwnl}},建议调整值是{{gwnl_wentai}}。<end>",
- "boot": [
- "2_2",
- "2_6",
- "2_15",
- "2_19",
- "2_27",
- "2_30"
- ],
- "questions": [
- {
- "id": "2_2",
- "mainType": "alert",
- "mainContent": "出水总磷在线仪表是正常的吗?",
- "options": [
- {
- "option": "正常",
- "next": [
- "4_2"
- ]
- },
- {
- "option": "不正常",
- "next": [
- "4_5"
- ]
- }
- ]
- },
- {
- "id": "2_6",
- "mainType": "text",
- "mainContent": "进水总磷高于设计值?",
- "options": [
- {
- "option": "低于设计值",
- "next": [
- "4_6"
- ]
- },
- {
- "option": "高于设计值但是低于110%",
- "next": [
- "4_9"
- ]
- },
- {
- "option": "高于设计值110%",
- "next": [
- "4_12"
- ]
- }
- ]
- },
- {
- "id": "2_15",
- "mainType": "text",
- "mainContent": "进水碳磷比是否低于稳态值?",
- "options": [
- {
- "option": "否",
- "next": [
- "4_15"
- ]
- },
- {
- "option": "是",
- "next": [
- "4_16"
- ]
- }
- ]
- },
- {
- "id": "2_17",
- "mainType": "alert",
- "mainContent": "厌氧池硝酸盐氮是否大于1.5mg/L",
- "options": [
- {
- "option": "否",
- "next": [
- "4_17"
- ]
- },
- {
- "option": "是",
- "next": [
- "4_18"
- ]
- }
- ]
- },
- {
- "id": "2_19",
- "mainType": "text",
- "mainContent": "各个厌氧池的溶解氧当前值是否超出各自的稳态值",
- "options": [
- {
- "option": "都未超出",
- "next": [
- "4_19"
- ]
- },
- {
- "option": "至少一个池子有超出",
- "next": [
- "4_20"
- ]
- }
- ]
- },
- {
- "id": "2_21",
- "mainType": "text",
- "mainContent": "进水水温是否低于10℃?",
- "options": [
- {
- "option": "否",
- "next": [
- "4_21"
- ]
- },
- {
- "option": "是",
- "next": [
- "4_22"
- ]
- }
- ]
- },
- {
- "id": "2_23",
- "mainType": "text",
- "mainContent": "进水pH是否低于6.5?",
- "options": [
- {
- "option": "否",
- "next": [
- "4_23"
- ]
- },
- {
- "option": "是",
- "next": [
- "4_24"
- ]
- }
- ]
- },
- {
- "id": "2_25",
- "mainType": "text",
- "mainContent": "进水TDS是否超出管控值?",
- "options": [
- {
- "option": "未超出",
- "next": [
- "4_25"
- ]
- },
- {
- "option": "超出",
- "next": [
- "4_26"
- ]
- }
- ]
- },
- {
- "id": "2_27",
- "mainType": "text",
- "mainContent": "各个池子的污泥沉降比和污泥体积指数是否大于其对应的管控值?",
- "options": [
- {
- "option": "都未大于",
- "next": [
- "4_27"
- ]
- },
- {
- "option": "至少一个池子有大于",
- "next": [
- "4_29"
- ]
- }
- ]
- },
- {
- "id": "2_30",
- "mainType": "text",
- "mainContent": "化学除磷率是否存在下降?",
- "options": [
- {
- "option": "不存在",
- "next": [
- "4_30"
- ]
- },
- {
- "option": "存在",
- "next": [
- "4_31"
- ]
- }
- ]
- },
- {
- "id": "2_32",
- "mainType": "alert",
- "mainContent": "设备与电气类是否有故障发生?",
- "options": [
- {
- "option": "否",
- "next": [
- "4_32"
- ]
- },
- {
- "option": "是",
- "next": [
- "4_33"
- ]
- }
- ]
- },
- {
- "id": "3_2",
- "mainType": "text",
- "mainContent": "正常",
- "options": [
- {
- "option": "出水总磷是否存在连续两次超标?",
- "next": [
- "5_2",
- "5_3"
- ]
- }
- ]
- },
- {
- "id": "3_5",
- "mainType": "text",
- "mainContent": "不正常",
- "options": []
- },
- {
- "id": "3_6",
- "mainType": "text",
- "mainContent": "低于设计值",
- "options": [
- {
- "option": "进水总量与设计值的比较是?",
- "next": [
- "5_6",
- "5_7",
- "5_8"
- ]
- }
- ]
- },
- {
- "id": "3_9",
- "mainType": "text",
- "mainContent": "高于设计值但是低于110%",
- "options": [
- {
- "option": "进水总量与设计值的比较是?",
- "next": [
- "5_9",
- "5_10",
- "5_11"
- ]
- }
- ]
- },
- {
- "id": "3_12",
- "mainType": "text",
- "mainContent": "高于设计值110%",
- "options": [
- {
- "option": "进水总量与设计值的比较是?",
- "next": [
- "5_12",
- "5_13",
- "5_14"
- ]
- }
- ]
- },
- {
- "id": "3_15",
- "mainType": "text",
- "mainContent": "否",
- "options": []
- },
- {
- "id": "3_16",
- "mainType": "text",
- "mainContent": "是",
- "options": []
- },
- {
- "id": "3_17",
- "mainType": "text",
- "mainContent": "否",
- "options": []
- },
- {
- "id": "3_18",
- "mainType": "text",
- "mainContent": "是",
- "options": []
- },
- {
- "id": "3_19",
- "mainType": "text",
- "mainContent": "都未超出",
- "options": []
- },
- {
- "id": "3_20",
- "mainType": "text",
- "mainContent": "至少一个池子有超出",
- "options": []
- },
- {
- "id": "3_21",
- "mainType": "text",
- "mainContent": "否",
- "options": []
- },
- {
- "id": "3_22",
- "mainType": "text",
- "mainContent": "是",
- "options": []
- },
- {
- "id": "3_23",
- "mainType": "text",
- "mainContent": "否",
- "options": []
- },
- {
- "id": "3_24",
- "mainType": "text",
- "mainContent": "是",
- "options": []
- },
- {
- "id": "3_25",
- "mainType": "text",
- "mainContent": "未超出",
- "options": []
- },
- {
- "id": "3_26",
- "mainType": "text",
- "mainContent": "超出",
- "options": []
- },
- {
- "id": "3_27",
- "mainType": "text",
- "mainContent": "都未大于",
- "options": [
- {
- "option": "生化池是否有大量泡沫、浮泥等不正常现象?",
- "next": [
- "5_27",
- "5_28"
- ]
- }
- ]
- },
- {
- "id": "3_29",
- "mainType": "text",
- "mainContent": "至少一个池子有大于",
- "options": []
- },
- {
- "id": "3_30",
- "mainType": "text",
- "mainContent": "不存在",
- "options": []
- },
- {
- "id": "3_31",
- "mainType": "text",
- "mainContent": "存在",
- "options": []
- },
- {
- "id": "3_32",
- "mainType": "text",
- "mainContent": "否",
- "options": []
- },
- {
- "id": "3_33",
- "mainType": "text",
- "mainContent": "是",
- "options": []
- },
- {
- "id": "4_2",
- "mainType": "text",
- "mainContent": "出水总磷是否存在连续两次超标?",
- "options": [
- {
- "option": "存在",
- "next": [
- "6_2"
- ]
- },
- {
- "option": "不存在",
- "next": [
- "6_3"
- ]
- }
- ]
- },
- {
- "id": "4_5",
- "mainType": "export",
- "mainContent": "状态:出水总磷在线仪表不正常。\n解决方案:\n请使用如下排查方式进行:\n1、是否存在设备故障,水样通路、检测药剂更换等问题;\n2、查询仪表代维公司是否在进行周/月度/季度的质控核查或比对,如果在进行核查或比对,通过后,需完成监测平台标记记录;若比对时间超过6h或更长时间,需完成主管局备案并监测平台标记,必要时采取第三方取样人工监测,监测周期间隔不大于6 h,数据报送每天不少于4次(具体按属地监管要求执行),监测技术要求参照HJ91.1执行;",
- "options": []
- },
- {
- "id": "4_6",
- "mainType": "text",
- "mainContent": "进水总量与设计值的比较是?",
- "options": [
- {
- "option": "小于设计值",
- "next": [
- "6_6"
- ]
- },
- {
- "option": "大于但未超过110%",
- "next": [
- "6_7"
- ]
- },
- {
- "option": "超过110%",
- "next": [
- "6_8"
- ]
- }
- ]
- },
- {
- "id": "4_9",
- "mainType": "text",
- "mainContent": "进水总量与设计值的比较是?",
- "options": [
- {
- "option": "小于设计值",
- "next": [
- "6_9"
- ]
- },
- {
- "option": "大于但未超过110%",
- "next": [
- "6_10"
- ]
- },
- {
- "option": "超过110%",
- "next": [
- "6_11"
- ]
- }
- ]
- },
- {
- "id": "4_12",
- "mainType": "text",
- "mainContent": "进水总量与设计值的比较是?",
- "options": [
- {
- "option": "小于设计值",
- "next": [
- "6_12"
- ]
- },
- {
- "option": "大于但未超过110%",
- "next": [
- "6_13"
- ]
- },
- {
- "option": "超过110%",
- "next": [
- "6_14"
- ]
- }
- ]
- },
- {
- "id": "4_15",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_16",
- "mainType": "export",
- "mainContent": "状态:进水碳磷比失衡。\n解决方案:\n1、强化水质变化数据分析,提前预警管控\n开展水质溯源进行源头控制;合理调整C/P或利用精准投药系统实时动态调节,同步对除磷药剂投加点位可通过小试和生产性试验证进一步优化。\n2、工艺调整\nA²O等连续流工艺可将生化系统的过渡段调整为厌氧段运行,同时优化多点进水和回流分配,提高厌氧释磷的底物浓度和反应速率,一个厌氧停留时间后检测校核调整效果;",
- "options": []
- },
- {
- "id": "4_17",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_18",
- "mainType": "export",
- "mainContent": "状态:厌氧池硝酸盐氮浓度偏高。\n解决方案:\n1、厌氧区硝态氮存在消耗有机基质而抑制PAO对磷的释放,从而影响在好氧条件下聚磷菌对磷的吸收,一般控制在1.5mg/L以下,在保障脱氮的前提下,可以适当降低外回流量,避免过量硝酸盐底物回流至前端厌氧区,同时优化多点进水和回流分配,提高厌氧稀磷的底物浓度和磷的释放效率。",
- "options": []
- },
- {
- "id": "4_19",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_20",
- "mainType": "export",
- "mainContent": "状态:厌氧池溶解氧偏高;\n解决方案:\n由于出水混合液 DO 控制过高,内外回流将高DO 带回了厌氧池,厌氧段DO高于0.2mg/L,难以形成厌氧环境,抑制释磷反应,微生物活性下降,可采用以下方式解决:\n1、供风量过高导致的好氧混合液DO过高\n首先查看风机状态,尝试降低已运行风机风量(调整幅度每次5%(根据实际情况可适当调整),有气量计量的以读数为准,没有的按照变频器的频率和额定风量核算,以气水比的数值和实际溶解氧校核);其次,可以通过放空阀进行气量放空。A²O等连续流工艺调整后3~5小时后检测DO校核。\n2、供风量充足,解决由于生化池液位差异引起生化池气量分配不均导致的混合液回流DO过高\n调整各系统进水和污泥回流阀门,尽可能保障运行工况一致,进行各系统供气总阀和局部阀的调整,A²O等连续流工艺调整3~5小时后检测DO校核。\n3、二沉池长时间DO过低,造成总磷的二次释放\n合理控制好氧末端DO,将二沉池DO刮吸泥机等运转正常,避免厌缺氧导致磷释放。",
- "options": []
- },
- {
- "id": "4_21",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_22",
- "mainType": "export",
- "mainContent": "状态:进水水温过低。\n解决方案:\n由于水温低于10℃,聚磷菌在低温时生长速度会减慢,生物除磷速率将会迅速下降,微生物活性下降,可采用以下方式解决:\n1、强化温降数据收集与分析,提前预警管控一般在10月中旬及3月下旬进入变温期或换季期间,做好温降曲线的统计和绘制工作,秋季进水水温连续3天低于15℃,或春季进水水温连续3天高于12℃时,加强相关指标的检测频次和分析,提前采取运行管理措施和工艺调整\n2、工艺调整\n①适当加大剩余污泥排放量,缩短污泥龄,一般以除磷为目的的生物处理系统的泥龄控制在7天左右,但要综合考虑系统脱氮能力,生化池污泥泥龄一般控制在20天左右。\n②根据不同工艺历年来生产运行经验和污泥负荷核算,A²O及改良工艺控制秋冬季低温期污水处理厂污泥浓度控制在4000~6000mg/L。",
- "options": []
- },
- {
- "id": "4_23",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_24",
- "mainType": "export",
- "mainContent": "状态:进水pH过低。\n解决方案:\n最适宜pH值为6.5-8,pH值低于6.5时,吸磷率急剧下降,pH下降引起的释放是破坏性的“酸溶”效应,pH下降引起的厌氧释放量越大,好氧吸磷能力就越低,微生物活性下降,可采用以下方式解决:\n1、启动水质溯源,同步投加碱调节pH,确保系统各生化段pH在合理范围内;\n2、解决高氨氮硝化反应过多消耗碱度或进水碱度降低导致系统缓冲液体系失衡\n①根据回流混合液硝酸盐浓度和缺氧池碱度核算后,投加工业碱调节pH。",
- "options": []
- },
- {
- "id": "4_25",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_26",
- "mainType": "export",
- "mainContent": "状态:进水TDS超过管控值。\n解决方案:\n以进水TDS数据表征有毒物质,由于有毒物质进入系统导致微生物活性下降,可采用以下方式解决:\n1、向行业主管部门报备、开展水质溯源、启动应急预案等工作\n配合主管部门的调查认定,最短时间内完成源头控制,争取第一时间内最大限度降低处理负荷;或利用初沉池、水解酸化池等预处理设施投加絮凝剂提高进水絮凝效果,尽可能减少可沉降性毒性物质进行系统。\n2、开展毒性抑制定性分析\n根据属地重点工业企业排水清单和溯源结果,重点对重金属、典型芳香类化合物等及时开展毒性检测分析,同步进行小试抑制试验,确定进水毒性抑制和生化系统恢复潜力\n3、毒性小试实验方案\n将现有生化系统活性厌氧段污泥分别与异常进水和正常进水混合,保证污泥浓度一致条件下,开启六连搅拌器,缓慢搅拌,搅拌时间模拟厌氧段停留时间,每 2h 取样 1 次,按上述比例24h 换水 1 次(换水量为 50%),连续运行 72h,观察总磷去除效率,根据实验结果确定:① 探究污水对厌氧释磷的毒性抑制作用;② 探究解决当前生化池毒性抑制问题的适宜应对策略。\n4、恢复毒性抑制的关键工艺调整\n根据毒性抑制试验结果,系统总磷去除率不再继续降低,应尽可能最短时间完成优质外源活性污泥接种,随着驯化成熟,总磷去除率不断升高,可同步加大剩余污泥排放,进行新老活性污泥的置换,根据实际情况也可尝试定向微生物菌剂投加等措施,缩短系统恢复时间。同时在调整期间提高相应参数、指标的检测频次和分析。\n5、长时间毒性冲击系统,应对措施\n系统濒临瘫痪,无法短期完成恢复的,及时启动专家论证程序,联动省市主管部门,落实具体方案,将生态环境损害降至最低,免于环保问责或处罚。",
- "options": []
- },
- {
- "id": "4_27",
- "mainType": "alert",
- "mainContent": "生化池是否有大量泡沫、浮泥等不正常现象?",
- "options": [
- {
- "option": "没有",
- "next": [
- "6_27"
- ]
- },
- {
- "option": "有",
- "next": [
- "6_28"
- ]
- }
- ]
- },
- {
- "id": "4_29",
- "mainType": "export",
- "mainContent": "状态:污泥沉降比或污泥体积指数超过了管控值。\n解决方案:\n由于污泥膨胀、老化、解絮等导致微生物活性下降,导致出水带泥,总磷不受控,可采用以下方式解决:\n1、强化污泥SV、SVI和镜检的污泥性状分析,按照污泥膨胀、老化、解絮等对症管控措施,及时完成工艺调整,将污泥负荷控制在设计管控目标内。\n2、系统恢复应急期调整\n①重新进行活性污泥接种和驯化;\n②根据生化反应中出现问题选择相适应的微生物菌剂、污泥调理剂进行系统定向强化\n3、短期内无法解决恢复时,应及时完成主管部门报备和专家论证等免责程序,并启动应急预案。",
- "options": []
- },
- {
- "id": "4_30",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_31",
- "mainType": "export",
- "mainContent": "状态:化学除磷效率下降导致超标。\n解决方案:\n1、进水磷组分发生变化,立即进行磷组分检测和不同除磷药剂的小试定量试验,指导实际生产除磷药剂投加调整和优化;\n2、药剂投加量不足以小试试验定量为指导,实际生产适当提高投加系数,一般不高于1.5倍为宜,根据投加点位的不同,按投加后系统停留时间为单位,进行效果校核调整,药剂投加量提升的同时,提高剩余污泥排放量,避免长期大量除磷药剂回流系统,影响生物除磷。",
- "options": []
- },
- {
- "id": "4_32",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "4_33",
- "mainType": "export",
- "mainContent": "状态:设备与电气类有故障发生。\n解决方案:\n由于设备与电气类故障问题,影响活性污泥系统稳定,导致超标,可采用以下方式解决:\n1、及时解决外回流泵、二沉池刮泥机、排泥泵、污泥脱水系统等故障,保障活性污泥的生长处于合理周期内;\n2、及时解决搅拌器、推流器等故障问题造成的生化系统活性污泥混合流化不充分或堆积问题影响生物除去效率;\n3、解决电气自控类的关键控制电器元件、传感器等故障导致的系统运行失控风险,需保障水量和风量开关控制阀门等关键设备的电气控制元器件的稳定运行;",
- "options": []
- },
- {
- "id": "5_2",
- "mainType": "text",
- "mainContent": "存在",
- "options": []
- },
- {
- "id": "5_3",
- "mainType": "text",
- "mainContent": "不存在",
- "options": [
- {
- "option": "请第一时间取样与实验室人工或智能检测化验比对,是否超标了",
- "next": [
- "7_3",
- "7_4"
- ]
- }
- ]
- },
- {
- "id": "5_6",
- "mainType": "text",
- "mainContent": "小于设计值",
- "options": []
- },
- {
- "id": "5_7",
- "mainType": "text",
- "mainContent": "大于但未超过110%",
- "options": []
- },
- {
- "id": "5_8",
- "mainType": "text",
- "mainContent": "超过110%",
- "options": []
- },
- {
- "id": "5_9",
- "mainType": "text",
- "mainContent": "小于设计值",
- "options": []
- },
- {
- "id": "5_10",
- "mainType": "text",
- "mainContent": "大于但未超过110%",
- "options": []
- },
- {
- "id": "5_11",
- "mainType": "text",
- "mainContent": "超过110%",
- "options": []
- },
- {
- "id": "5_12",
- "mainType": "text",
- "mainContent": "小于设计值",
- "options": []
- },
- {
- "id": "5_13",
- "mainType": "text",
- "mainContent": "大于但未超过110%",
- "options": []
- },
- {
- "id": "5_14",
- "mainType": "text",
- "mainContent": "超过110%",
- "options": []
- },
- {
- "id": "5_27",
- "mainType": "text",
- "mainContent": "没有",
- "options": []
- },
- {
- "id": "5_28",
- "mainType": "text",
- "mainContent": "有",
- "options": []
- },
- {
- "id": "6_2",
- "mainType": "export",
- "mainContent": "状态:基本确认出水总磷超标了\n解决方案:\n1、出水总磷指标超限值标准,立即启动应急预案开展相关工艺调整,与行业主管部门报备并建立联动机制,落实具体方案,将生态环境损害降至最低,免于环保问责或处罚。",
- "options": []
- },
- {
- "id": "6_3",
- "mainType": "alert",
- "mainContent": "请第一时间取样与实验室人工或智能检测化验比对,是否超标了",
- "options": [
- {
- "option": "超标",
- "next": [
- "8_3"
- ]
- },
- {
- "option": "不超标",
- "next": [
- "8_4"
- ]
- }
- ]
- },
- {
- "id": "6_6",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "6_7",
- "mainType": "export",
- "mainContent": "状态:进水总磷未超设计值,但进水总磷总量超过进水总磷总量设计值小于等于进水总磷总量设计值的110%\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、工艺调整优化等工作。\n①污泥浓度控制调整:增加剩余污泥排放量,降低系统污泥浓度,每次调整幅度控制不超过常态稳定时的10%,A²O等连续流工艺均以日为单位,检测校核调整效果。\n②回流量调整:适当提高外回流比,外回流比不宜超过150%;合理控制好氧末端溶解氧DO不超过2mg/L,总氮可控的前提下适当降低内回流比保障厌氧释磷环境,A²O等连续流工艺以生化池停留时间为单位,检测校核调整效果。",
- "options": []
- },
- {
- "id": "6_8",
- "mainType": "export",
- "mainContent": "状态:进水总磷未超设计值,但进水总磷总量超过进水总磷总量设计值的110%\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、启动应急预案等工作。\n①优先采取降负荷运行方式:具备条件且无环保风险的前提下,按照污染物负荷总量核算运行负荷或根据应急预案执行。\n②不具备降负荷条件时,可以利用厂内初沉池、水解酸化等预处理设施池容,对超标水进行错峰调蓄,最大限度保障生化系统进水水质均衡。\n③当系统长时间受到超标冲击,远超系统处理能力时,系统面临瘫痪风险,根据现场实际情况,可选择性进行系统保留和放弃,即停进水闷曝内循环系统和进水运行负荷系统;\n④运行负荷调整涉及管网的污水溢流问题,事关环保风险责任,因此启动应急预案落实负荷调整时要完成主管报备,必要时同步联动专家论证程序,确保合法合规。",
- "options": []
- },
- {
- "id": "6_9",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "6_10",
- "mainType": "export",
- "mainContent": "状态:进水总磷未超设计值110%,进水总磷总量超过进水总磷总量设计值但小于等于进水总磷总量设计值的110%\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、工艺调整优化等工作。\n①污泥浓度控制调整:增加剩余污泥排放量,降低系统污泥浓度,每次调整幅度控制不超过常态稳定时的10%,A²O等连续流工艺均以日为单位,检测校核调整效果。\n②回流量调整:适当提高外回流比,外回流比不宜超过150%;合理控制好氧末端溶解氧DO不超过2mg/L,总氮可控的前提下适当降低内回流比保障厌氧释磷环境,A²O等连续流工艺以生化池停留时间为单位,检测校核调整效果。",
- "options": []
- },
- {
- "id": "6_11",
- "mainType": "export",
- "mainContent": "状态:进水总磷未超设计值110%,进水总磷总量超过进水总磷总量设计值的110%。\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、启动应急预案等工作。\n①优先采取降负荷运行方式:具备条件且无环保风险的前提下,按照污染物负荷总量核算运行负荷或根据应急预案执行。\n②不具备降负荷条件时,可以利用厂内初沉池、水解酸化等预处理设施池容,对超标水进行错峰调蓄,最大限度保障生化系统进水水质均衡。\n③当系统长时间受到超标冲击,远超系统处理能力时,系统面临瘫痪风险,根据现场实际情况,可选择性进行系统保留和放弃,即停进水闷曝内循环系统和进水运行负荷系统;\n④运行负荷调整涉及管网的污水溢流问题,事关环保风险责任,因此启动应急预案落实负荷调整时要完成主管报备,必要时同步联动专家论证程序,确保合法合规。",
- "options": []
- },
- {
- "id": "6_12",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "6_13",
- "mainType": "export",
- "mainContent": "状态:进水总磷超设计值110%,进水总磷总量超过进水总磷总量设计值但小于等于进水总磷总量设计值的110%。\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、工艺调整优化等工作。\n①污泥浓度控制调整:增加剩余污泥排放量,降低系统污泥浓度,每次调整幅度控制不超过常态稳定时的10%,A²O等连续流工艺均以日为单位,检测校核调整效果。\n②回流量调整:适当提高外回流比,外回流比不宜超过150%;合理控制好氧末端溶解氧DO不超过2mg/L,总氮可控的前提下适当降低内回流比保障厌氧释磷环境,A²O等连续流工艺以生化池停留时间为单位,检测校核调整效果。",
- "options": []
- },
- {
- "id": "6_14",
- "mainType": "export",
- "mainContent": "状态:进水总磷超设计值110%,进水总磷总量超过进水总磷总量设计值的110%。\n解决方案:\n1、向行业主管部门报备、开展水质溯源进行源头控制、启动应急预案等工作。\n①优先采取降负荷运行方式:具备条件且无环保风险的前提下,按照污染物负荷总量核算运行负荷或根据应急预案执行。\n②不具备降负荷条件时,可以利用厂内初沉池、水解酸化等预处理设施池容,对超标水进行错峰调蓄,最大限度保障生化系统进水水质均衡。\n③当系统长时间受到超标冲击,远超系统处理能力时,系统面临瘫痪风险,根据现场实际情况,可选择性进行系统保留和放弃,即停进水闷曝内循环系统和进水运行负荷系统;\n④运行负荷调整涉及管网的污水溢流问题,事关环保风险责任,因此启动应急预案落实负荷调整时要完成主管报备,必要时同步联动专家论证程序,确保合法合规。",
- "options": []
- },
- {
- "id": "6_27",
- "mainType": "export",
- "mainContent": "",
- "options": []
- },
- {
- "id": "6_28",
- "mainType": "export",
- "mainContent": "状态:生化池出现大量泡沫、浮泥等不正常现象。\n解决方案:\n由于生化池出现大量泡沫、浮泥等不正常现象,可能是污泥膨胀、老化、解絮等导致微生物活性下降,导致出水带泥,总磷不受控,可采用以下方式解决:\n1、强化污泥SV、SVI和镜检的污泥性状分析,按照污泥膨胀、老化、解絮等对症管控措施,及时完成工艺调整,将污泥负荷控制在设计管控目标内。\n2、系统恢复应急期调整\n①重新进行活性污泥接种和驯化;\n②根据生化反应中出现问题选择相适应的微生物菌剂、污泥调理剂进行系统定向强化\n3、短期内无法解决恢复时,应及时完成主管部门报备和专家论证等免责程序,并启动应急预案",
- "options": []
- },
- {
- "id": "7_3",
- "mainType": "text",
- "mainContent": "超标",
- "options": []
- },
- {
- "id": "7_4",
- "mainType": "text",
- "mainContent": "不超标",
- "options": []
- },
- {
- "id": "8_3",
- "mainType": "export",
- "mainContent": "状态:人工化验比对,出水总磷超标了\n解决方案:\n1、出水总磷指标超限值标准,立即启动应急预案开展相关工艺调整,与行业主管部门报备并建立联动机制,落实具体方案,将生态环境损害降至最低,免于环保问责或处罚。",
- "options": []
- },
- {
- "id": "8_4",
- "mainType": "export",
- "mainContent": "状态:人工化验出水不超标\n解决方案:化验室检测未超标,暂时关闭报警,持续观察出水水质;",
- "options": []
- }
- ]
- }
|