新《污水處理施工方案資料》AO工藝設(shè)計(jì)計(jì)算8

《新《污水處理施工方案資料》AO工藝設(shè)計(jì)計(jì)算8》由會(huì)員上傳分享，免費(fèi)在線閱讀，更多相關(guān)內(nèi)容在工程資料-天天文庫(kù)。

Hydralic水力計(jì)算一(水處理主流程部分)平均設(shè)計(jì)流量Qave=0.463m3/s最大設(shè)計(jì)流量Qmax=#NAME?m3/s2023/2/181出水井,細(xì)格柵及旋流式沉砂池1.1位置名稱該項(xiàng)水頭損失該處水位備注出水井1778.300進(jìn)水泵壓力在此處釋放31.2位置名稱堰寬(m)流量(m/s)堰上水深(m)流量系數(shù)負(fù)荷(l/s.m)自由跌落該項(xiàng)水頭損失該處水位單泵1600cum/h出水井堰下薄壁平頂堰2.850.444#NAME?#NAME?1560.210#NAME?#NAME?2塊1.5米堰31.3位置名稱格柵寬流量(m/s)格柵間隙(mm)柵前水深柵前流速過柵流速柵后水深柵后流速該項(xiàng)水頭損失該處水位進(jìn)水渠細(xì)格柵1#NAME?10.0000.800#NAME?10.65#NAME?0.150#NAME?1.4位置名稱該項(xiàng)水頭損失該處水位旋流式沉砂池沉砂池0.120#NAME?31.5位置名稱堰寬(m)流量(m/s)堰上水深(m)流量系數(shù)負(fù)荷(l/s.m)自由跌落該項(xiàng)水頭損失該處水位沉砂池出水堰下薄壁平頂堰1.7#NAME?#NAME?#NAME?#NAME?0.180#NAME?#NAME?2組1.7米出水堰2自旋流式沉砂池出口至氧化溝322.1位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失Q=Qmax沉砂池出口進(jìn)口(進(jìn)管)600#NAME?#NAME?#NAME?1.00.5#NAME?由池子進(jìn)圓管,進(jìn)口沒修圓32.2位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失沉砂池至氧化溝直鋼管600#NAME?#NAME?141.0#NAME?#NAME?322.3位置名稱管徑流量(m/s)流速(m/s)數(shù)量損失系數(shù)V/2*g該項(xiàng)水頭損失沉砂池至氧化溝90鋼管彎頭600#NAME?#NAME?1.01.08#NAME?#NAME?2.4位置名稱該項(xiàng)水頭損失厭氧池(預(yù)留)厭氧池(預(yù)留)0.400322.5位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失氧化溝進(jìn)口出口(出管)600#NAME?#NAME?#NAME?11#NAME?流入水池2.6位置水頭損失合計(jì)該處水頭氧化溝液位#NAME?#NAME?32.7位置名稱堰寬(m)流量(m/s)堰上水深(m)流量系數(shù)負(fù)荷(l/s.m)自由跌落該項(xiàng)水頭損失堰下水頭氧化溝出水堰下薄壁平頂堰5#NAME?#NAME?#NAME?#NAME?0.200#NAME?#NAME?每系列1條5米堰3自氧化溝出水渠至沉淀池323.1位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失單系列Q=(Qmax+r*Qav)/2氧化溝出口進(jìn)口(進(jìn)管)800#NAME?#NAME?#NAME?1.00.5#NAME?由池子進(jìn)圓管34.2位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失氧化溝至沉淀池直鋼管800#NAME?#NAME?35.0#NAME?#NAME?324.3位置名稱管徑流量(m/s)流速(m/s)數(shù)量損失系數(shù)V/2*g該項(xiàng)水頭損失氧化溝至沉淀池90鋼管彎頭800#NAME?#NAME?1.01.05#NAME?#NAME?324.4位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失氧化溝至沉淀池出口(出管)800#NAME?#NAME?#NAME?11#NAME?流入進(jìn)水筒34.4位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失沉淀池進(jìn)水管進(jìn)水直鋼管2000#NAME?#NAME?6.0#NAME?#NAME?34.5位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失導(dǎo)流筒進(jìn)水直鋼管3000#NAME?#NAME?31.2#NAME?#NAME?4.6位置名稱合計(jì)堰上水頭沉淀池出水堰的堰上#NAME?#NAME?管路水頭損失合計(jì)35.9位置名稱堰數(shù)流量(m/s)單堰流量(l/s)堰上水深(m)自由跌落該項(xiàng)水頭損失堰下水頭沉淀池出水堰的堰下垂直三角堰942#NAME?#NAME?#NAME?0.164#NAME?#NAME?單池Q=Qmax/23管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失出水干管800#NAME?#NAME?200.0#NAME?#NAME?3管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失出水干管1000#NAME?#NAME?200.0#NAME?#NAME?總水頭損失#NAME?m水力計(jì)算二(污泥回流沉淀池至污泥泵房部分)最大回流量Qr=0.463m3/s1二沉池至移動(dòng)橋的集泥槽1.1位置名稱該處水位備注二沉池#NAME?沉淀池水位321.2位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失單池Q=Qr/2吸泥管進(jìn)口進(jìn)管5000.231#NAME?#NAME?1.01#NAME?33.2位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失排泥管直鋼管5000.231#NAME?36.0#NAME?#NAME?323.3位置名稱管徑流量(m/s)流速(m/s)數(shù)量損失系數(shù)V/2*g該項(xiàng)水頭損失排泥管90鋼管彎頭5000.231#NAME?0.01.01#NAME?#NAME?Page1

1Hydralic323.4位置名稱管徑流量(m/s)流速(m/s)數(shù)量損失系數(shù)V/2*g該項(xiàng)水頭損失排泥管45鋼管彎頭5000.231#NAME?0.00.51#NAME?#NAME?323.5位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失污泥泵房的進(jìn)口出口(出管)5000.231#NAME?#NAME?11#NAME?流入水池3.6位置名稱合計(jì)污泥泵房水位污泥泵房水位#NAME?#NAME?管路水頭損失合計(jì)二沉池至污泥泵站水頭損失合計(jì)#NAME?水力計(jì)算三(回流污泥出水井至氧化溝部分)最大回流量Qr=0.463m3/s1出水井至沉淀池1.1位置名稱該項(xiàng)水頭損失該處水位備注出水井#NAME?壓力進(jìn)水在此處釋放31.2位置名稱堰寬(m)流量(m/s)堰上水深(m)流量系數(shù)負(fù)荷(l/s.m)自由跌落該項(xiàng)水頭損失該處水位單泵出水井堰下薄壁平頂堰2.50.231#NAME?#NAME?930.270#NAME?#NAME?2塊2.5米堰321.3位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失吸泥管進(jìn)口進(jìn)管5000.231#NAME?#NAME?1.01#NAME?321.4位置名稱管徑流量(m/s)流速(m/s)數(shù)量損失系數(shù)V/2*g該項(xiàng)水頭損失排泥管90鋼管彎頭5000.231#NAME?1.01.01#NAME?#NAME?31.5位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失排泥管直鋼管5000.231#NAME?55.0#NAME?#NAME?321.6位置名稱管徑流量(m/s)流速(m/s)V/2*g數(shù)量阻力系數(shù)該項(xiàng)水頭損失氧化溝的進(jìn)口出口(出管)5000.231#NAME?#NAME?11#NAME?流入水池1.7位置名稱合計(jì)氧化溝氧化溝水位#NAME?#NAME?管路水頭損失合計(jì)二沉池至污泥泵站水頭損失合計(jì)#NAME?****回流污泥泵泵數(shù)量2臺(tái)用1臺(tái)備33單臺(tái)流量q=20000m/d=0.231m/s3=833.3m/h泵井內(nèi)水面高程h0=#NAME?m出水井水面高程h1=#NAME?m自由水頭h21.0=m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s損失系數(shù)損失300-500漸擴(kuò)管45010.231#NAME?0.5#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)損失系數(shù)損失(合計(jì))#NAME?揚(yáng)程合計(jì):#NAME?m選用泵型為350ZQB-70D****剩余污泥泵泵數(shù)量1臺(tái)用1臺(tái)備33單臺(tái)流量q=980m/14hr=0.019m/s3=70.000m/h污泥泵井內(nèi)水面高程h0=#NAME?m貯泥池出口高程h1=1777.5m較大估值自由水頭h21.5=m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s損失系數(shù)損失100-150漸擴(kuò)管15010.019#NAME?0.5#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)損失系數(shù)損失支管1503200.019#NAME?#NAME?#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s損失系數(shù)損失支管彎頭15030.019#NAME?0.9#NAME?止回閥門15010.019#NAME?2.5#NAME?閘閥15020.019#NAME?0.15#NAME?支管接干管15010.019#NAME?1.5#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)損失系數(shù)損失干管15000.039#NAME?#NAME?#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s損失系數(shù)損失干管彎頭15000.039#NAME?1.05#NAME?(合計(jì))#NAME?揚(yáng)程合計(jì):#NAME?mPage2

2Hydralic選用泵型為WQ70-12-5.5Page3

3Hydralic由池子進(jìn)圓管,進(jìn)口沒修圓連通管線校合34.2位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)生物池至沉淀池配水井直鋼管800#NAME?#NAME?143.0#NAME?34.2位置名稱管徑流量(m/s)流速(m/s)長(zhǎng)度m損失系數(shù)該項(xiàng)水頭損失#NAME?Page4

4inletpump污水處理廠計(jì)算書1.基本數(shù)據(jù)一進(jìn)水泵站計(jì)算1.1水量3重力流進(jìn)水日平均Qav=40000m/d=0.463日最小流量Qmin=40000m/d=0.46日變化系數(shù)Kz=#NAME?3日最大流量Q'max=Kz*Qav=#NAME?m/d=3=#NAME?m/s3選定最大流量Qmax=#NAME?m/d=#NAME?1.2進(jìn)水管(自進(jìn)水井至泵房粗格柵前)管線末端管底高程(m)H=1763.959m管線末端水面高程(m)Hw=1764.959m地面高程(m)Hd=1773.600m1.3粗格柵計(jì)算選用回轉(zhuǎn)式格柵,擬用宜昌市第二冷作機(jī)械廠的產(chǎn)品,共兩臺(tái)HF1000.格柵臺(tái)數(shù)量n=2套格柵間隙b=20mm格柵安裝角度a=70度單套設(shè)備寬Wo=1m設(shè)備總高H2=m單套設(shè)備總寬W2=1.35m渠道數(shù)n1=2條每條渠道寬W=1.08m每條渠道深H=9.541m導(dǎo)流槽長(zhǎng)度L1=H*ctg(a)+0.55=4.023m排渣高度(距渠底)H1=10.941m柵前水深h1=0.9m柵前流速V1=0.44m/s過柵流速V=0.8m/s3單套格柵過流量Qs=37200.0m/d過柵水頭損失dh=0.15m柵后水深h2=0.75m柵后流速V2=0.5m/s333柵渣產(chǎn)率f=0.100m/10m污水3柵渣產(chǎn)量Wf=Qav*f=4.000m按單渠過流平均流量校核柵前水深h1=0.90m柵前流速V1=0.44m/s過柵流速V=#NAME?m/s3單套格柵過流量Qs=Qav=#NAME?m/d過柵水頭損失dh=#NAME?m柵后水深h2=#NAME?m柵后流速V2=#NAME?m/sPage5

5inletpump1.4進(jìn)水提升泵(4萬(wàn))泵數(shù)量2臺(tái)用1臺(tái)備3單臺(tái)流量q=24000m/d=0.28泵數(shù)量1臺(tái)用1臺(tái)備3單臺(tái)流量q=14400m/d=0.173流量(4-8)合計(jì)Q=62400m/d=0.72泵數(shù)量0臺(tái)用1臺(tái)備3單臺(tái)流量q=31200m/d=0.363流量(8-16)合計(jì)Q=62400m/d=0.72*擬設(shè)計(jì)污水泵(1000m3/h)泵井內(nèi)水面高程h0=1764.809m出水井水面高程h1=1778.300m泵本身?yè)p失h2=0.5m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s300-500漸擴(kuò)管50010.278#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)支管500200.278#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s支管彎頭50010.278#NAME?止回閥門50000.278#NAME?支管接干管50010.278#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)干管90000.833#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s干管彎頭90000.833#NAME?閥門(合計(jì))其它損失1.0m揚(yáng)程合計(jì):#NAME?m選用泵型為WQ1000-16-75*已購(gòu)污水泵(600m3/h)泵井內(nèi)水面高程h0=1764.809m出水井水面高程h1=1778.300m泵本身?yè)p失h2=0.5m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s300-400漸擴(kuò)管40010.167#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)支管400200.167#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/sPage6

6inletpump支管彎頭40010.167#NAME?止回閥門40000.167#NAME?支管接干管40010.167#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)干管90000.500#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s干管彎頭90000.500#NAME?閥門(合計(jì))其它損失1.0m揚(yáng)程合計(jì):#NAME?m選用泵型為WQ600-20-55*擬設(shè)計(jì)污水泵(1300m3/h)泵井內(nèi)水面高程h0=1764.809m出水井水面高程h1=1778.300m泵本身?yè)p失h2=0.5m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s400-600漸擴(kuò)管50010.361#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)支管500200.361#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s支管彎頭50010.361#NAME?止回閥門50000.361#NAME?支管接干管50010.361#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)干管90001.083#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s干管彎頭90001.083#NAME?閥門(合計(jì))其它損失1.0m揚(yáng)程合計(jì):#NAME?m選用泵型為WQ1300-16-110*已購(gòu)污水泵(1600m3/h)泵井內(nèi)水面高程h0=1764.809m出水井水面高程h1=1778.300m泵本身?yè)p失h2=0.5m管路損失(鋼管)3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s400-600漸擴(kuò)管60010.444#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)支管600200.444#NAME?Page7

7inletpump3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s支管彎頭60010.444#NAME?止回閥門60000.444#NAME?支管接干管60010.444#NAME?3管件名稱管徑(mm)長(zhǎng)度(m)流量(m/s)流速(m/s)干管90001.333#NAME?3管件名稱管徑(mm)數(shù)量(個(gè))流量m/s流速m/s干管彎頭90001.333#NAME?閥門(合計(jì))其它損失1.0m揚(yáng)程合計(jì):#NAME?m選用泵型為WQ1600-20-134Page8

8inletpump3m/s3m/s3#NAME?m/h3m/sPage9

9inletpump1.4進(jìn)水提升泵(8萬(wàn))泵數(shù)量2臺(tái)用133m/s單臺(tái)流量q=24000m/d=泵數(shù)量2臺(tái)用133m/s單臺(tái)流量q=14400m/d=3m/s泵數(shù)量1臺(tái)用13單臺(tái)流量q=31200m/d=33m/s流量(8)合計(jì)Q=108000m/d=3m/s1.4進(jìn)水提升泵(16萬(wàn))泵數(shù)量2臺(tái)用13單臺(tái)流量q=24000m/d=泵數(shù)量2臺(tái)用13單臺(tái)流量q=14400m/d=損失系數(shù)損失泵數(shù)量2臺(tái)用130.5#NAME?單臺(tái)流量q=38400m/d=損失系數(shù)損失3#NAME?#NAME?流量(8-16)合計(jì)Q=153600m/d=損失系數(shù)損失0.9#NAME?2.5#NAME?1.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失1.05#NAME?0#NAME?損失系數(shù)損失0.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失Page10

10inletpump0.9#NAME?2.5#NAME?1.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失1.05#NAME?0#NAME?損失系數(shù)損失0.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失0.9#NAME?2.5#NAME?1.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失1.05#NAME?0#NAME?損失系數(shù)損失0.5#NAME?損失系數(shù)損失#NAME?#NAME?Page11

11inletpump損失系數(shù)損失0.9#NAME?2.5#NAME?1.5#NAME?損失系數(shù)損失#NAME?#NAME?損失系數(shù)損失1.05#NAME?0#NAME?Page12

12inletpumpPage13

13inletpump臺(tái)備30.28m/s臺(tái)備30.17m/s臺(tái)備30.36m/s31.25m/s臺(tái)備30.28m/s臺(tái)備30.17m/s臺(tái)備30.44m/s31.78m/sPage14

14inletwell二沉砂池計(jì)算1.基本數(shù)據(jù)1.1流量3日平均流量Qav=40000m/d=0.463日最小流量Qmin=40000m/d=0.46日變化系數(shù)Kz=#NAME?3日最大流量Qmax=Kz*Qav=#NAME?m/d=3=#NAME?m/s2進(jìn)水井及堰2.1進(jìn)水井尺寸3最大流量Qmax=#NAME?m/s3最小流量Qmin=0.46m/s進(jìn)水井格數(shù)n=1格進(jìn)水井堰板方向?qū)扡=1.5m進(jìn)水井長(zhǎng)W=1.2m進(jìn)水井高H=6m進(jìn)水最大上升流速V=Qmax/(n*w*L)=#NAME?m/s進(jìn)水最小上升流速V=Qmin/(n*w*L)=0.26m/s2.2矩形堰2.2.1薄壁平頂堰（不淹沒，無(wú)側(cè)面收縮，流速忽略）1/23/2使用公式：通過堰口的流量為Q=m*b*(2*g)*H流量系數(shù)為m=0.405+0.0027/H公式取值：堰數(shù)n1=2單堰寬b=1.5m3單堰流量Qma=Qmax/n1=#NAME?m/s2重力加速度g=9.81m/s使用試算方法得到以下結(jié)果：堰上水深H=#NAME?m流量系數(shù)為m=#NAME?堰負(fù)荷q=#NAME?l/(m*s)按單堰過流平均流量校核堰數(shù)n2=1單堰寬b=1.5m3單堰流量Q'=Qav/(n1-1)=0.463m/s2重力加速度g=9.81m/s使用試算方法得到以下結(jié)果：堰上水深H=#NAME?m流量系數(shù)為m=#NAME?堰負(fù)荷q=308.6l/(m*s)2.3渠道尺寸流量q=#NAME?cum/s水深h=0.500m渠寬w=0.900mPage15

15inletwell流速v=q/h/w#NAME?m/s2.機(jī)械格柵選用回轉(zhuǎn)式格柵,擬用宜昌市第二冷作機(jī)械廠的產(chǎn)品.每套由兩臺(tái)HF1000并聯(lián)而成.格柵臺(tái)數(shù)量n=2套格柵間隙b=10mm格柵安裝角度a=75度單套設(shè)備寬Wo=1m設(shè)備總高H2=m單套設(shè)備總寬W2=1m渠道數(shù)n1=2條每條渠道寬W=1m每條渠道深H=1.3m導(dǎo)流槽長(zhǎng)度L1=H*ctg(a)=0.616m排渣高度(距渠底)H1=2.3m柵前水深h1=0.8m柵前流速V1=#NAME?m/s過柵流速V=1.0m/s3單套格柵過流量Qs=#NAME?m/d過柵水頭損失dh=0.15m柵后水深h2=0.65m柵后流速V2=#NAME?m/s333柵渣產(chǎn)率f=0.050m/10m污水3柵渣產(chǎn)量Wf=Qav*f=2.000m按單渠過流平均流量校核柵前水深h1=0.90m柵前流速V1=0.51m/s過柵流速V=#NAME?m/s3單套格柵過流量Qs=Qav=40000.0m/d過柵水頭損失dh=#NAME?m柵后水深h2=#NAME?m柵后流速V2=#NAME?m/s3沉砂池:D=3.5m4.沉砂池出水堰計(jì)算1/23/2使用公式：通過堰口的流量為Q=m*b*(2*g)*H流量系數(shù)為m=0.405+0.0027/H公式取值：堰數(shù)n1=2單堰寬b=6m3單堰流量Qma=Qmax/n1=#NAME?m/s2重力加速度g=9.81m/s使用試算方法得到以下結(jié)果：堰上水深H=#NAME?m流量系數(shù)為m=#NAME?堰負(fù)荷q=#NAME?l/(m*s)三配水井計(jì)算Page16

16inletwell1/23/2使用公式：通過堰口的流量為Q=m*b*(2*g)*H流量系數(shù)為m=0.405+0.0027/H公式取值：堰數(shù)n1=3單堰寬b=3m3單堰流量Qma=Qmax/n1=#NAME?m/s2重力加速度g=9.81m/s使用試算方法得到以下結(jié)果：堰上水深H=#NAME?m流量系數(shù)為m=#NAME?堰負(fù)荷q=#NAME?l/(m*s)3管徑流量(m/s)流速(m/s)長(zhǎng)度m阻力系數(shù)1250.333#NAME?1.0#NAME?3管徑流量(m/s)流速(m/s)長(zhǎng)度m阻力系數(shù)1500.167#NAME?10.0#NAME?3管徑流量(m/s)流速(m/s)長(zhǎng)度m阻力系數(shù)1500.083#NAME?10.0#NAME?Page17

17inletwell3m/s3m/s3#NAME?m/hPage18

18inletwellPage19

19inletwell壓降mm#NAME?壓降mm#NAME?壓降mm#NAME?Page20

20A/O除磷工藝生物處理池設(shè)計(jì)計(jì)算1.基本數(shù)據(jù)1.1流量日平均流量Qav=90000cum/d日最小流量Qmin=90000cum/d日變化系數(shù)Kz=#NAME?日最大流量Qmax=Kz*Qav=#NAME?cum/d設(shè)計(jì)日流量Q=90000cum/d1.2水質(zhì)名稱及單位進(jìn)水出水設(shè)計(jì)出水BOD5(mg/l)1202010COD(mg/l)3006040SS(mg/l)150200TN(mg/l)403020NH3-N(mg/l)301210NO3-N(mg/l)011TP(mg/l)310.5SP(mg/l)2.51.5油類(mg/l)7010色度(倍)50PH值7.7平均最高溫(度)24平均最低溫(度)121.3參數(shù)選取1.3.1運(yùn)行參數(shù)△生物池中活性污泥濃度Xvss=2100mgMLVSS/l△揮發(fā)活性組份比例fvss=0.7(一般0.7~0.8)△污泥回流比r=0.75△混合液回流比R=21.3.2碳氧化工藝參數(shù)△污泥理論產(chǎn)泥系數(shù)Y=0.6mgVSS/mgBOD5(范圍0.4~0.8,一般0.6)△20℃時(shí)污泥自身氧化系數(shù)Kd20=0.061/d(范圍0.04~0.075,一般0.06)1.3.3硝化工藝參數(shù)△硝化菌在15℃時(shí)的最大比生長(zhǎng)速率μm(15)0.=471/d(范圍0.4~0.5,一般0.47或0.45)△好氧池中溶解氧濃度DO=2.0mg/l△NH4-N的飽和常數(shù)KN=T=Tmin=12℃KN=10^(0.051*T-1.158)=0.3mg/l△硝化菌理論產(chǎn)率系數(shù)Yn=0.15mgVSS/mgNH4－N(范圍0.04~0.29,一般0.15)△20℃時(shí)硝化菌自身氧化系數(shù)KdN20=0.041/d(范圍0.03~0.06,一般0.05)△安全系數(shù)SF=3.2(范圍1.5~4,一般2.5)△氧的飽和常數(shù)Ko=1.0mg/l(范圍0.25~2.46,一般1.0)1.3.4反硝化工藝參數(shù)△在20℃時(shí)的反硝化速率UDN(20)=0.111/d(范圍0.075~0.115,一般0.1)△厭氧池溶解氧濃度DOn=0.15mg/l1.3.5除磷工藝參數(shù)

21△

222好氧池設(shè)計(jì)計(jì)算(按低溫情況計(jì)算)2.1參數(shù)修正污水的最低平均水溫Tmin=12℃△污泥自身氧化系數(shù)Kd修正Kd(Tmin)=Kd20*1.05^(Tmin-20)=0.0411/d△硝化菌最大比生長(zhǎng)速率μm修正μm=μm(15)*e^[0.098*(Tmin-15)]*[1-0.833*(7.2-PH)]*[DO/(Ko+DO)]=0.3311/d△硝化菌自身氧化系數(shù)KdN修正KdN(Tmin)=KdN20*1.05^(Tmin-20)=0.0271/d2.2計(jì)算設(shè)計(jì)泥齡2.2.1最大基質(zhì)利用率k'=μm/Yn=2.211/d2.2.2泥齡計(jì)算△最小硝化泥齡tcmin由公式:1/tcmin=Yn*k'-kdN得:tcmin=1/(Yn*k'-kdN)tcmin1=/(Yn*k'-kdN)=3.29d△設(shè)計(jì)泥齡tc=SF*tcmin=10.5d2.3污泥負(fù)荷2.3.1硝化污泥負(fù)荷Un由公式:1/tc=Yn*Un-kdN得:Un=(1/tc+kdN)/YnUn=(1/tc+kdN)/Yn=0.81mgNH4-N/(mgMLVSS*d)2.3.2出水氨氮濃度Ne由公式:Un=k'*Ne/(Kn+Ne)得:Ne=Un*Kn/(k'-Un)Ne=Un*Kn/(k'-Un)=0.17mg/l2.3.3碳氧化污泥負(fù)荷Us由公式:1/tc=Y*Us-kd得:Us=(1/tc+kd)/YUs=(1/tc+kd)/Y=0.23mgBOD/(mgMLVSS*d)2.4好氧池容積2.4.1BOD氧化要求水力停留時(shí)間tb=(So-Se)/(Us*Xvss)=0.23d=5.57h2.4.1硝化要求水力停留時(shí)間△BOD5表觀產(chǎn)率系數(shù)Yobs=Y/(1+Kd*tc)=0.42mgVSS/mgBOD5△硝化細(xì)菌在微生物中的百分比f(wàn)n硝化的氨氮量Nd=TN0-0.122*Yobs*(So-Se)-Ne-0.016*Kd*tc*(So-Se)*Yobs=33.9mg/l硝化菌百分比f(wàn)n=Yn*Nd/(Yabs*(So-Se)+Yn*Nd+0.016*Kd*tc*(So-Se)*Yobs)=0.098△硝化水力停留時(shí)間tntn=(TNo-0.122*Yobs*(S0-Se)-Ne-0.016*Kd*tc*(So-Se)*Yobs)/(Usn*X*fn)=0.20d=4.8h2.4.2好氧池水力停留時(shí)間選定t=5.57h2.4.3好氧池容積Va=Q*t/24=20872.1cum2.5排泥量計(jì)算△污泥有機(jī)部分產(chǎn)量W1=Yobs*(So-Se)*Q/1000=4159.99kg/d△污泥惰性部分產(chǎn)量W2=ηss*SSo*Q/1000=3375.0kg/d總懸浮物TSS惰性組份比例ηss取25%△污泥硝化部分產(chǎn)量W3=Yn*(NH0-Nhe)*Q/(1+tc*KdN)=210.1kg/d△活性污泥總產(chǎn)量W'=W1/fvss+W2+W3-SSe*Q/1000=9527.9kg/d=9.5t/d△污泥的綜合產(chǎn)率W'/[(So-Se)*Q/1000)=0.96kgDS/kgBOD

23△初沉池污泥產(chǎn)量W”=Q*(SS0'-SSe')/1000=13500kg/d=13.52.6污泥中MLVSS比例fvss'=(W1/fvss)/W=0.62選定0.622.7污泥中MLSSX=MLVSS/fvss=3367mg/l選定3500mg/l實(shí)際污泥負(fù)荷0.1355kgBOD/kgSS.d2.8污泥體積取活性污泥含水率p=99.3%污泥濃度Nw=7.0kg/m3污泥體積Vs=W/Nw=1361m3/d=27.0l/s(14hr)2.9污泥濃縮脫水取污泥濃縮脫水機(jī)每日工作14小時(shí)每小時(shí)處理泥量82.2m3/h相當(dāng)于1645kg/h含水率體積m3流量m3/h流量l/s99.30%3290234.9865.394.00%383.827.417.680.00%115.18.222.3每公斤干泥加混凝劑PAM0.004kgPAM/kg干泥加藥量92kg/d=6.579kg/h2.10好氧池容積計(jì)算2.10.1傳統(tǒng)曝氣池設(shè)計(jì)水深H1=6m系列數(shù)S=3系列單渠道寬度B1=10m單系列好氧區(qū)面積A1=1159.6m2單系列好氧區(qū)長(zhǎng)度L1=116.0m缺氧區(qū)長(zhǎng)度L2=24m曝氣池總長(zhǎng)度L3=140.0m取L3=144m單系列曝氣池分格數(shù)3格單格曝氣池長(zhǎng)度L4=48m曝氣池超高H2=0.5m曝氣池總高H=6.5m設(shè)計(jì)進(jìn)水渠道寬度B2=2m設(shè)計(jì)出水渠道寬度B3=2m設(shè)單向池壁總厚度B4=1.5m曝氣池尺寸L×W×H=3－49.5×31.5×6.5m厭氧池尺寸L×W×H=3－30×7×6.5m2.11初沉池輻流式沉淀池設(shè)計(jì)有效水深H1=3.5m設(shè)計(jì)超高H2=0.5m設(shè)計(jì)緩沖層高度H3=0.5m設(shè)計(jì)污泥層高度H4=0.5m沉淀池池邊高度H=5m設(shè)計(jì)沉淀池直徑D=30m設(shè)計(jì)初沉池?cái)?shù)量3座平均流量時(shí)表面負(fù)荷q=1.77m3/m2.h設(shè)計(jì)規(guī)范1.5~3.0m3/m2.h平均流量時(shí)停留時(shí)間t=1.98h設(shè)計(jì)規(guī)范1.5~2.0h峰值流量時(shí)表面負(fù)荷q'=#NAME?m3/m2.h峰值流量時(shí)停留時(shí)間t'=#NAME?h初沉池尺寸3－Φ30×5.0m2.11二沉池輻流式沉淀池設(shè)計(jì)有效水深H1=3.5m

243缺氧池設(shè)計(jì)計(jì)算(按低溫情況計(jì)算)3.1參數(shù)修正污水的最低平均水溫Tmin=12℃△反硝化速率UDN修正UDN=UDN(20)*1.09^(Tmin-20)*(1-DOn)=0.0469mgNO3-N/mgMLVSS*d3.2反硝化池容積Vdn△反硝化氮量NDenitNDenit=TNo-TNe-0.12*W1/Q*1000=14.5mg/l(TNe為設(shè)計(jì)值)△容積VdnVdn=NDenit/(UDN*Xvss)=0.15d=3.52h△綜合回流比(R+r)=NDenit/TNe=0.72

254厭氧池設(shè)計(jì)計(jì)算(按低溫情況計(jì)算)4.1參數(shù)修正4.2厭氧區(qū)容積Vp=Q*tan/24=3000.0cum厭氧區(qū)名義水力停留時(shí)間tan=0.8hr4.3厭氧區(qū)實(shí)際水力停留時(shí)間tant=24*Vp/[(1+r)*Q]=0.5hr(滿足要求)4.4厭氧區(qū)釋放出PO4－P濃度CP1△PO4-P釋放速率系數(shù)kp=0.0236*So-0.036=2.80mgP/gMLSS*hr△CP1=CPo+kp*tant*X/1000=6.8mg/l4.5好氧區(qū)出水PO4－P濃度CP2△PO4-P吸收速率系數(shù)ku,取0.5l/gMLSS*hr△好氧區(qū)實(shí)際水力停留時(shí)間t2=t/(1+r+R)=1.48hr△由公式ln(Cp1/Cp2)=ku*X*t2/1000得:Cp2=Cp1*exp(-ku*X*t2/1000)=1.43mg/l4.6校核好氧區(qū)出水總磷濃度TPeTPe=(CP2+0.055)/0.671=2.22mg/l4.7校核污泥含磷率PxPx=(TPo-TPe)*Q/(W*1000)=1.70%基本滿足要求

265需氧量計(jì)算5.1有機(jī)物碳化需氧量O2－cO2-c=1.47*Q*(So-Se)/1000-1.42*W1=8645.8kgO2/d式中：<>BODu/BOD5=1.47<>理論上微生物自身氧化的好氧量1.42kgO2/kgVSS5.2硝化需氧量O2-nO2-n=4.6*[Q*(TNo-Ne)-0.12*W1]=14194.9kgO2/d式中：<>微生物細(xì)胞中N的比例為14/113=0.12kgN/kgVSS5.3反硝化可利用氧O2-dnO2-dn=2.85*[Q*(TNo-TNe)/1000-0.12*W1*fvss]=0.000kgO2/d(TNe使用要求值30mg/l)5.4總需氧量O2=O2_c+O2_n-O2_dn=22840.7kgO2/d=22.8tO2/d5.5去除每公斤BOD5的需氧量=O2*1000/[Q*(So-Se)]=2.31kgO2/kgBOD

276曝氣器計(jì)算水深?m6.1基礎(chǔ)數(shù)據(jù)6.1.1實(shí)際傳氧速率N(AOR)22840.7kgO2/d=951.7kgO2/h6.1.2污水剩余DO值(DO)2.0mg/L6.1.3標(biāo)準(zhǔn)狀態(tài)下清水中飽和溶解氧(CS,20度)9.17mg/L6.1.4當(dāng)?shù)睾０胃叨?00m6.1.5當(dāng)?shù)卮髿鈮篜a(kPa)(見給排水手冊(cè)一P81頁(yè))9.6mH2O=94.08Kpa6.1.6污水溫度(T)高溫24度低溫6.1.7T溫度時(shí)清水飽和溶解氧(簡(jiǎn)明排水設(shè)計(jì)手冊(cè)P6頁(yè))8.53mg/L6.1.8T、Pa時(shí)清水飽和溶解氧(CSW)7.926.2計(jì)算6.2.1微孔曝氣頭項(xiàng)目KKL215KKL215KKL215KKL215計(jì)算公式3單臺(tái)氣量(m/h.只)2222氧氣利用率(EA%)20232530設(shè)計(jì)有效水深(m)6.06.06.06.0實(shí)際傳氧效率α(KLa污/KLa清)0.800.800.800.80污水與清水的飽和溶解氧比值β0.900.900.900.90曝氣池逸出氣體的含氧率%(Ot)17.5416.9916.6215.69Ot=21×100（1－EA)/79+21(1－EA)2曝氣裝置處實(shí)際壓力Pb(kgf/cm)1.561.561.561.5624℃時(shí)曝氣池中平均溶解氧值CSM(mgO2/L)9.749.649.579.40CSM=CSW(Ot/42+Pb/2Pa)(T－20)24℃時(shí)f值(f＝N0：N＝SOR：AOR)1.541.561.581.61N=αN0×(βCSM－C0)×1.024/CS24℃時(shí)標(biāo)準(zhǔn)傳氧速率N0(SOR)(kg－O2/h)1465.521485.861499.891536.74N0=f×N324℃時(shí)供空氣體積Gs(m/h)24425.3521534.2019998.5417074.87Gs=N0/(0.3EA)12℃時(shí)曝氣池中平均溶解氧值CSM(mgO2/L)12.3712.2412.1511.9312℃時(shí)f值(f＝N0：N＝SOR：AOR)1.521.541.551.5912℃時(shí)標(biāo)準(zhǔn)傳氧速率N0(SOR)(kg－O2/h)1443.731462.571475.541509.55312℃時(shí)供空氣體積Gs(m/h)24062.1221196.6019673.9016772.8320℃時(shí)曝氣池中平均溶解氧值CSM(mgO2/L)10.4810.3610.2910.1020℃時(shí)f值(f＝N0：N＝SOR：AOR)1.541.561.581.6220℃時(shí)標(biāo)準(zhǔn)傳氧速率N0(SOR)(kg－O2/h)1468.621488.581502.351538.47320℃時(shí)供空氣體積Gs(m/h)24476.9321573.6220031.2817094.14按20℃時(shí)的SOR值和供空量計(jì)算曝氣裝置數(shù)量按單臺(tái)供氣量計(jì)算微孔曝氣頭數(shù)量(只)1223810787100168547每座曝氣池內(nèi)曝氣頭數(shù)量(只,共3座曝氣池)4079359633392849風(fēng)管阻力mmH2O800800800800曝氣裝置阻力mmH2O4504504504502標(biāo)準(zhǔn)大氣壓下的計(jì)算風(fēng)壓p'(kgf/cm)0.7450.7450.7450.7452按當(dāng)?shù)卮髿鈮盒拚L(fēng)壓p(kgf/cm)0.8020.8020.8020.802風(fēng)機(jī)效率η0.70.70.70.7風(fēng)機(jī)功率P(Kw)766.93675.96627.64535.61P=2.05(Gs×p)/(75×η)動(dòng)力效率(kg－O2/kw.h)2.743.153.424.10動(dòng)力效率＝N0/(P×η)總動(dòng)力效率(kg－O2/kw.h)1.912.202.392.87

288.接觸池8.1池容取接觸時(shí)間t'=30min接觸池容積V'=1875m3取接觸池?cái)?shù)n'=2座取接觸池深h=5.0m取單接觸池寬W=10m設(shè)計(jì)單接觸池長(zhǎng)L=23.4m取L=度接觸池實(shí)際容積V=2000m3mg/L8.2出水加氯量取每方水加液氯5gCl2/t水出水加氯量為450kgCl2/d=計(jì)算公式(T－20)N=αN0×(βCSW－C0)×1.024/CSN0=f×N

29水量及水質(zhì)處理廠服務(wù)人口(萬(wàn)人)人均綜合用水量升/(人.天)總供水量152704050014782500處理廠服務(wù)人口(萬(wàn)人)人均排水量升/(人.天)BOD1521022生活污染源排污量水量(萬(wàn)噸)BOD(噸)1149.751204.5工業(yè)污染源排污量工業(yè)項(xiàng)目水量(萬(wàn)噸)BOD(噸)云南省楚雄市醬菜廠0.607280.91092楚雄市食品工業(yè)公司0.43410.26046紅塔集團(tuán)卷煙廠4.06941.22082楚雄州食品公司0.99860.26046云南省楚雄市絲綢廠1.74472.86245楚雄市鹿城造紙廠14.558816.0101楚雄市眾達(dá)紙業(yè)公司11.291314.2458楚雄市廣鑫聯(lián)營(yíng)造紙廠2.29091.3836云南新華印刷二廠6.2453.747楚雄州彩印廠10.6楚雄州林產(chǎn)品工業(yè)公司0.220.132有色化工總公司0.54430.81645國(guó)營(yíng)云南燃料二廠4.168534.44楚雄仁恒化肥有限公司0.9891.4835楚雄東瓜氮肥廠0.14710.22065云南楚雄磷肥廠6.180479.3902楚雄雁塔藥業(yè)有限公司4.87255.0016楚雄市交通工具修理廠1.6150.969云南雄德鐵合金有限公司0.230.138大姚銅礦楚雄星泰公司10.6昆明水泥有限公司楚雄水泥廠8.739000000合計(jì)71.94588164.69301污染源計(jì)算水量(噸/天)BOD(mg/l)33471.1112.1設(shè)計(jì)值40000120Page30

30水量及水質(zhì)收集系數(shù)人均綜合排水量升/(總?cè)伺?天水)量0.82163240011826000CODTNTPSS4050.835CODTNTPSS2190273.7543.81916.25CODTNTPSSBOD1.82184001.21456按綜合排放二級(jí)標(biāo)準(zhǔn)計(jì)算1500.65115000.8682按綜合排放二級(jí)標(biāo)準(zhǔn)計(jì)算604.0694002.84858處理達(dá)標(biāo)300.65115000.8682按綜合排放二級(jí)標(biāo)準(zhǔn)計(jì)算606.361004.68實(shí)測(cè)20035.5780023.585實(shí)測(cè)18023.7430016.176實(shí)測(cè)1802.306006.939實(shí)測(cè)1807.4940012.49601.2002600.264000.44601.6329001.0886150114.8008.337實(shí)測(cè)602.967001.9781500.4413000.2942150396.9510012.3608實(shí)測(cè)15016.672003.849實(shí)測(cè)1502.4225000.4845600.345000.069601.5000.36000017.4780621.8712400118.3486CODTNTPSS230.222.43.6166.5240254180Page31

31水量及水質(zhì)CODTNTPSS3002001502001007015020030020040025040025040025012020012020012020030020020002003002003002006002003001501503015030150300200Page32

32Others龍川江規(guī)劃斷面核算相對(duì)高程絕對(duì)高程三十年一遇洪水位-1.631771.229規(guī)劃湖濱北路路中01772.859龍川江底高程-6.431766.429排污明渠底高-21770.859?龍川江北岸現(xiàn)況高程-0.5291772.33可研報(bào)告:防洪水位:1780.53~1772.004m進(jìn)管高程-8.91763.959m泵房底高程-11.11761.759m泵房頂部高程0.01772.859m型號(hào)500L=1.8K=0.5j=0.65進(jìn)水管中心0.65Page33

33power氧化溝主要設(shè)備一覽表序號(hào)設(shè)備名稱數(shù)量主要規(guī)格性能備注A1進(jìn)水泵站A1.1人工除污斜裝平面格柵1已建A1.2潛污泵2流量0.167m3/s,揚(yáng)程20mH2O,WQ600-20-55已購(gòu)A1.3潛污泵1流量0.444m3/s,揚(yáng)程20mH2O,WQ1600-20-132已購(gòu)A1.4潛污泵1流量0.444m3/s,揚(yáng)程16mH2O,WQ1600-16-110備用A1.5潛污泵1流量0.444m3/s,揚(yáng)程12mH2O,WQ1600-12-90排澇A1.6電動(dòng)葫蘆A2細(xì)格柵及沉砂池A2.1回轉(zhuǎn)式格柵2柵條間隙8mm，寬1.0m，渠高1.3mA2.2無(wú)軸螺旋輸送機(jī)1長(zhǎng)5m,內(nèi)徑320mm,不銹鋼A2.3旋流式沉砂池2流量460l/s，直徑3.5m,不銹鋼A2.4螺旋式砂水分離機(jī)2流量5~15l/s,不銹鋼A2.5鼓風(fēng)機(jī)2風(fēng)量2.5m3/min,風(fēng)壓50KPaA2.6疊量閘1W×H=800×1300mmA2.7疊量閘4W×H=1000×1300mmA2.8疊量閘1W×H=1200×1300mmA2.9板閘2W×H=700×1200mmA2.10閘門3DN600A2.11閘門1DN700A3Carrousel氧化溝A3.1表曝機(jī)4P＝55kw,充氧能力1.6~2.0kgO2/kwhA3.2表曝機(jī)(調(diào)速)2P＝55kw,充氧能力1.6~2.0kgO2/kwh,調(diào)速A3.3潛水?dāng)嚢铏C(jī)6P＝5.5kw,直徑1800mmA4沉淀池及污泥泵站A4.1半橋式刮泥機(jī)2沉淀池直徑D＝40mA4.2潛污泵(剩余污泥泵)2揚(yáng)程10m，流量20l/s,WQ70-12-5.5A4.3潛污泵(回流污泥泵)3揚(yáng)程3.3m，流量240l/s,350ZQB-70DA4.4鑄鐵閘門4DN500A5儲(chǔ)泥池A5.1潛水?dāng)嚢铏C(jī)1P＝2.2kwA6污泥脫水機(jī)房A6.1污泥濃縮機(jī)ROS2.22單臺(tái)21m3/h,進(jìn)泥含水率99.3%,出泥<94%A6.2污泥脫水機(jī)ROS3.12單臺(tái)5m3/h,進(jìn)泥含水率94%,出泥<80%A6.3制藥投藥裝置1單臺(tái)Q=2kgPAM/hA6.4加藥泵3單臺(tái)Q=0.4m3/h,h=10mA6.5送泥泵（計(jì)量泵）3單臺(tái)Q=25m3/h,h=10mA6.6屋頂軸流風(fēng)機(jī)3P＝0.5kwA6.7無(wú)軸螺旋輸送機(jī)2長(zhǎng)8m,內(nèi)徑320mmB儀表與自控B1儀表靜壓式液位計(jì)1進(jìn)水泵房B1.1超聲波液位計(jì)3細(xì)格柵進(jìn)水渠(1)污泥泵房(1)貯泥池(1)B1.3溫度計(jì)和PH計(jì)1細(xì)格柵進(jìn)水渠B1.4電磁流量計(jì)2DN600,氧化溝進(jìn)水管(2)B1.5電磁流量計(jì)2DN500,回流污管道(2)B1.6電磁流量計(jì)1DN150(剩余污泥)B1.7溶解氧分析儀4氧化溝B1.8侵入式污泥濃度計(jì)3氧化溝(2),污泥泵房(1)B2自控（PLC與自控系統(tǒng)）B2.1監(jiān)控系統(tǒng)，包括UPS等B2.2可編程控制器(PLC)B2.3電視攝像監(jiān)控系統(tǒng)C電氣設(shè)備（MCC）Page34

34powerC1.1MCCC1.2變壓器Page35

35power數(shù)量工作臺(tái)數(shù)備用臺(tái)每數(shù)臺(tái)額定功每率臺(tái)(k工w)作功率(總kw功)率(kw)總工作功率(kw)裝機(jī)功率（kw)1.001.000.000.000.000.000.000.002.002.000.0055.0047.71110.0095.43110.001.001.000.00132.00126.86132.00126.86132.001.000.001.00110.00101.490.000.00110.001.001.000.0090.0076.1190.0076.1190.002.002.000.002.202.204.404.404.401.001.000.000.750.750.750.750.752.002.000.000.000.000.000.000.002.002.000.000.370.370.740.740.742.001.001.003.502.903.502.907.003.001.002.001.101.101.101.103.301.001.000.001.101.101.101.101.104.004.000.0055.0055.00220.00220.00220.002.002.000.0055.0055.00110.00110.00110.006.006.000.005.505.5033.0033.0033.002.002.000.000.750.751.501.501.502.001.001.005.504.005.504.0011.003.002.001.0014.0013.2028.0026.4042.001.001.000.002.202.202.202.202.202.002.000.001.101.102.202.202.202.002.000.002.002.004.004.004.001.001.001.001.001.001.001.001.003.002.001.001.000.042.000.073.003.002.001.002.001.164.002.316.003.003.000.000.500.501.501.501.50758.49717.58896.6975.8571.76834.34789.34Page36

36powerPage37