30萬(wàn)噸年丙烷脫氫制丙烯生產(chǎn)項(xiàng)目課件

30萬(wàn)噸/年丙烷脫氫制丙烯生產(chǎn)項(xiàng)目30萬(wàn)噸/年團(tuán)隊(duì)介紹Introduction

of

Group

Members工藝?yán)L圖廠區(qū)布置換熱網(wǎng)絡(luò)經(jīng)濟(jì)分析工藝設(shè)計(jì)設(shè)備校核三維配管設(shè)備設(shè)計(jì)安全環(huán)境文檔整理000102030405團(tuán)隊(duì)介紹Introduction

of

Group

Memb安全環(huán)保Safety&Environment答辯提綱ReplyOutline1項(xiàng)目背景ProjectBackground2工藝設(shè)計(jì)ProcessDesign3設(shè)備設(shè)計(jì)EquipmentDesign4工廠布置PlantLayout6經(jīng)濟(jì)分析EconomicAnalysis7項(xiàng)目總結(jié)5ProjectSummary安全環(huán)保Safety&Environment答辯提綱RePART1項(xiàng)目背景原料方案廠址選擇產(chǎn)品方案工藝選擇ProjectBackgroundPART1項(xiàng)目背景原料方案廠址選擇產(chǎn)品方案工藝選擇Proj1.1原料方案Raw

Material

我國(guó)本身的石油資源非常豐富，煉化企業(yè)在原油加工過(guò)程中會(huì)生產(chǎn)大量的C3餾分，液化石油氣中約占60%，它們一般是作為燃料使用或者放空燒掉，資源浪費(fèi)較為嚴(yán)重。項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)1.1原料方案我國(guó)本身的石油資源非常豐富，煉港口、航空、鐵路、公路40萬(wàn)噸聚丙烯項(xiàng)目1200+1000萬(wàn)噸/年煉油項(xiàng)目完善的公用工程一體化服務(wù)完善烯烴產(chǎn)業(yè)鏈惠州大亞灣石化園區(qū)地理位置交通運(yùn)輸下游去向原料供應(yīng)公用設(shè)施政策優(yōu)勢(shì)中海油惠州煉化項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)1.2廠址選擇SiteSelection港口、航空、鐵路、公路40萬(wàn)噸聚丙烯項(xiàng)目1200+1000萬(wàn)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)中海油惠州煉化LPG原料組成項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)1.2廠址選擇SiteSelection中海油惠州煉化LPG原料組成項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)近年來(lái)我國(guó)丙烯供需狀況1.3產(chǎn)品方案Product項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)近年項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)1.4工藝選擇ProcessSelection項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)1.PART2工藝設(shè)計(jì)ProcessDesign工藝模擬產(chǎn)品結(jié)構(gòu)工藝流程節(jié)能降耗模擬優(yōu)化工藝特點(diǎn)PART2工藝設(shè)計(jì)ProcessDesign工藝模擬產(chǎn)工藝流程Process項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)脫硫單元變壓吸附低溫分離多級(jí)壓縮急冷鍋爐丙烯精制塔脫乙烷塔脫丙烷塔丙烷脫氫選擇加氫C2,C3,H2循環(huán)C2,C3丙烷C3C2,C3無(wú)硫LPG含硫LPGC4液化氣去儲(chǔ)罐C2氣體去燃料氣系統(tǒng)富氫氣C1氣體去燃料氣系統(tǒng)堿渣、含硫空氣去三廢處理聚合級(jí)丙烯去儲(chǔ)罐C2,C3H2H2新鮮堿液循環(huán)堿液空氣預(yù)堿洗罐：H2S+2NaOH=Na2S+2H2O纖維膜接觸反應(yīng)器：RSH+NaOH=RSNa+H2O超重力反應(yīng)器：4RSNa+O2+2H2O=2RSSR+4NaOH冷卻水低壓蒸汽H2去總廠主反應(yīng)：C3H4+H2=C3H6副反應(yīng)：C3H6+H2=C3H8丙烷脫氫主反應(yīng)：C3H8=C3H6+H2丙烷脫氫副反應(yīng)：C3H8=C2H4+CH4C2H4+H2=C2H6C3H6=C3H4+H22.1工藝流程Process項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)原料資源化利用與總廠有效融合項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.2產(chǎn)品結(jié)構(gòu)Product總廠分廠聚合級(jí)丙烯0199.99%氫氣02C4液化氣03催化裂化01加氫裂化02延遲焦化03混合LPG58萬(wàn)噸/年返回總廠原料資源化利用與總廠有效融合項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置原料利用合理產(chǎn)品結(jié)構(gòu)合理原料單一，原子經(jīng)濟(jì)性高。綜合利用總廠出售的液化石油氣作為原料，實(shí)現(xiàn)丙烷資源化利用?？倧S提供原料，來(lái)源穩(wěn)定，規(guī)避市場(chǎng)風(fēng)險(xiǎn)，經(jīng)濟(jì)效益較高。主產(chǎn)聚合級(jí)丙烯，副產(chǎn)C4液化氣和H2。項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.3工藝特點(diǎn)ProcessCharacteristics原料利用合理產(chǎn)品結(jié)構(gòu)合理原料單一，原子經(jīng)濟(jì)性高。綜合利用總廠原料預(yù)處理工段氫氣分離及選擇加氫工段丙烷脫氫反應(yīng)工段項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)纖維膜接觸反應(yīng)器超重力反應(yīng)器丙烯精制熱泵雙塔丙烷脫氫反應(yīng)器變壓吸附等溫多級(jí)壓縮循環(huán)C2C3丙烯-乙烯復(fù)疊式制冷脫乙烷塔脫丙烷塔急冷鍋爐含硫LPGC4液化氣有機(jī)朗肯循環(huán)換熱器C1燃料氣氫氣選擇加氫反應(yīng)器循環(huán)氫氣C2氣體聚合級(jí)丙烯2.4工藝模擬ProcessSimulation原料預(yù)處理工段氫氣分離及丙烷脫氫反應(yīng)工段項(xiàng)目背景工藝設(shè)計(jì)設(shè)備項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.4工藝模擬ProcessSimulation原料預(yù)處理工段循環(huán)堿液含硫LPG含硫堿液無(wú)硫LPG氣體入口液體進(jìn)口氣體出口液體出口大量金屬纖維絲束，堿液形成液膜，增大接觸面積，提供較大的濃度差推動(dòng)力。相較于傳統(tǒng)氧化塔+沉降罐組合，降低了設(shè)備投資費(fèi)用，增大了接觸面積，并實(shí)現(xiàn)了反應(yīng)與分離的耦合。實(shí)現(xiàn)物流間換熱，降低總公用工程消耗量項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)采用徑向移動(dòng)床反應(yīng)器有利于催化劑循環(huán)再生降低設(shè)備投資并副產(chǎn)低壓蒸汽2.4工藝模擬ProcessSimulation丙烷脫氫反應(yīng)工段項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)采用項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)13℃-25℃-38℃-65℃-100℃丙烯、乙烯提供不同溫度的冷量，通過(guò)逐級(jí)制冷降低壓縮機(jī)的功耗。采用丙烯對(duì)乙烯進(jìn)行冷凝的復(fù)疊式制冷，減少公用工程消耗量。相較于丙烯-富氫氣制冷，減少了壓縮機(jī)和膨脹機(jī)的投資。2.4工藝模擬ProcessSimulation氫氣分離及選擇加氫工段項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)13項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)高效提純氫氣并副產(chǎn)C1燃料氣2.4工藝模擬ProcessSimulation氫氣分離及選擇加氫工段項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)高效項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)進(jìn)料板數(shù)的優(yōu)化餾出率的優(yōu)化回流比的優(yōu)化塔板數(shù)的優(yōu)化脫丙烷塔脫乙烷塔丙烯精制塔2.5模擬優(yōu)化ProcessOptimization項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)進(jìn)料項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.5模擬優(yōu)化ProcessOptimization項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.夾點(diǎn)溫差為14℃換熱網(wǎng)絡(luò)優(yōu)化項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.6節(jié)能降耗EnergySaving夾點(diǎn)溫差為14℃換熱網(wǎng)絡(luò)優(yōu)化項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置BeforeAfter換熱網(wǎng)絡(luò)優(yōu)化項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.6節(jié)能降耗EnergySavingBeforeAfter換熱網(wǎng)絡(luò)優(yōu)化項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工換熱網(wǎng)絡(luò)優(yōu)化熱泵精餾項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.6節(jié)能降耗EnergySaving換熱網(wǎng)絡(luò)優(yōu)化熱泵精餾項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保急冷塔流程圖急冷鍋爐流程圖投資費(fèi)用少年產(chǎn)低壓蒸汽10萬(wàn)噸換熱網(wǎng)絡(luò)優(yōu)化熱泵精餾急冷鍋爐項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)2.6節(jié)能降耗EnergySaving急冷塔流程圖急冷鍋爐流程圖投資費(fèi)用少年產(chǎn)低壓蒸汽10萬(wàn)噸換熱換熱網(wǎng)絡(luò)優(yōu)化熱泵精餾急冷鍋爐有機(jī)朗肯循環(huán)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)丙烯汽化器低溫氫氣汽輪機(jī)回?zé)崞鞅├淠髟鰤罕玫臀粺崮苡袡C(jī)工質(zhì)：丙烯2.6節(jié)能降耗EnergySaving換熱網(wǎng)絡(luò)優(yōu)化熱泵精餾急冷鍋爐有機(jī)朗肯循環(huán)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備PART3設(shè)備設(shè)計(jì)EquipmentDesign反應(yīng)器塔器換熱器加熱爐其他設(shè)備PART3設(shè)備設(shè)計(jì)EquipmentDesign反3.1反應(yīng)器Reactor本項(xiàng)目要求丙烷的單個(gè)反應(yīng)器單級(jí)轉(zhuǎn)化率為10%左右反應(yīng)器設(shè)計(jì)reactordesignOleflex工藝Oleflextechnology徑向移動(dòng)床movingbedreactorComsol反應(yīng)工程實(shí)驗(yàn)室Comsolreactionengineeringlaboratory反應(yīng)機(jī)理mechanism文獻(xiàn)資料documentkineticcurvefitting動(dòng)力學(xué)曲線擬合V=18.5m3項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)3.1反應(yīng)器本項(xiàng)目要求丙烷的單個(gè)反應(yīng)器單級(jí)轉(zhuǎn)化率為10%左右直徑2米，高7米轉(zhuǎn)化率=10.06%收率=9.11%項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)直徑2.1米，高6.3米轉(zhuǎn)化率=10.06%收率=9.41%直徑2.2米，高5.6米轉(zhuǎn)化率=10.06%收率=9.30%3.1反應(yīng)器Reactor直徑2米，高7米轉(zhuǎn)化率=10.06%項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)直徑2.1m床層高度6.3m壓降0.016MPa催化劑體積18.5m3項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)3.1反應(yīng)器Reactor直徑2.1m床層高度6.3m壓降0.016MPa催化劑體積1AspenPlus水力學(xué)參數(shù)KG-Tower+Matlab尺寸校核SW6-2011機(jī)械校核AutoCAD繪制裝配圖項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)3.2塔器TowerAspenPlus水力學(xué)參數(shù)KG-Tower+Matl3.2塔器Tower項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)Matlab塔結(jié)構(gòu)輔助設(shè)計(jì)代碼一覽T0102脫丙烷塔結(jié)構(gòu)示意圖四溢流塔盤(pán)結(jié)構(gòu)示意圖clc;clear;Ls=0.1358;%液體流量體積m3/sVs=1.0698;%輸入氣體體積流量m3/spl=418.1125;%輸入液體密度kg/m3pv=47.535;%輸入氣體密度kg/m3c=0.00383;%輸入混合液表面張力N/mHT=0.6;%輸入板間距mhL=0.08;%輸入板上液層高度ma=Ls*sqrt(pl./pv)./Vs;%史密斯關(guān)聯(lián)圖橫坐標(biāo)

b=HT-hL;C20=exp(-4.531+1.6562*b+5.5496*b.^2-6.4695*b.^3+(-0.474675+0.079*b-1.39*b.^2+1.3212*b.^3)*log(a)+(-0.07291+0.088307*b-0.49123*b.^2+0.43196*b.^3)*log(a)*log(a));C10=C20*((c./0.02)^0.2);%氣體負(fù)荷因子

umax=C10*(sqrt((pl-pv)./pv));%泛點(diǎn)氣速

u=0.8*umax;%適宜氣速

D1=sqrt(4*Vs./(pi*u))*10/2;%初算塔徑

D=ceil(D1)*2/10;%圓整后的塔徑

At=pi*D*D./4;%塔截面積

FI=0.25;%降液管總面積與塔截面積之比

Ad=At*FI;%降液管總面積

forx=0.0001:0.0001:pi./2As=((D./2)^2)*(x-sin(x)*cos(x));%邊降液管面積

l1=D*sin(x);%邊降液管弦長(zhǎng)

W1=(D./2)*(1-cos(x));%邊降液管寬度

Ac=Ad-2*As;%中心降液管面積

W2=Ac./D;%中心降液管寬度

l2=2*sqrt(((D./2)^2)-(W2./2)^2);%中心降液管弦長(zhǎng)

Ao=Ad./2;%偏心降液管面積

W=(D./2-W1)./2;%偏心降液管中心弦離圓心的距離

l=2*sqrt((D./2)^2-W^2);%偏心降液管中心弦長(zhǎng)

W3=Ao./l;%偏心降液管寬度

C=(D./2-W1-W3-0.5*W2)./2;%通道3、4的通道長(zhǎng)度

l3=2*sqrt(((D./2)^2)-(C+W3+0.5*W2)*(C+W3+0.5*W2));%偏心降液管外堰弦長(zhǎng)

l4=2*sqrt(((D./2)^2)-(C+0.5*W2)^2);%偏心降液管內(nèi)堰弦長(zhǎng)

A3=(l+l1)*C./2;%通道3的面積

A4=(D+l)*C./2;%通道4的面積

y=abs(A3./A4-2*As./Ac);

ify<0.001

break

endendx=x./(2*pi)*360;Q1=Ls*A3./(2*(A3+A4));%通道3中液體流量

Q2=Ls*A4./(2*(A3+A4));%通道4中液體流量

t1=As*HT./Q1;%邊降液管內(nèi)停留時(shí)間

t2=Ac*HT./(2*Q2);%中心降液管內(nèi)停留時(shí)間

t3=Ao*HT./(2*Q2);%偏心降液管內(nèi)停留時(shí)間

LW1=l2*(A3./A4);LW3=l4*A3./A4;LW2=LW1*A4./A3;how=0.00284*(3600*Q1./l1)^(2./3);hw=hL-how;偏心降液管中心弦偏心降液管3.2塔器項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)將AspenPlus模擬的全廠換熱網(wǎng)絡(luò)數(shù)據(jù)導(dǎo)入AspenEDR按照GB/T151-2014《熱交換器》標(biāo)準(zhǔn)進(jìn)行選型、校核項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)3.3換熱器Exchanger將AspenPlus模擬的全廠換熱網(wǎng)絡(luò)數(shù)據(jù)導(dǎo)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)工藝物流全部由輻射室加熱對(duì)流室產(chǎn)生3.8MPa中壓蒸汽作為動(dòng)力3.4加熱爐Furnace項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)工藝項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)泵選型部分一覽表壓縮機(jī)選型部分一覽表管道選型部分一覽表3.5其他設(shè)備OtherEquipments項(xiàng)目背景工藝設(shè)計(jì)設(shè)備設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)泵選PART4工廠布置PlantLayout廠區(qū)布置車(chē)間布置PART4工廠布置PlantLayout廠區(qū)布置車(chē)間布N4.1廠區(qū)布置PlantLayout項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)廠前區(qū)裝卸區(qū)總面積96200m2綠化率16.2%370m260m罐區(qū)生產(chǎn)區(qū)輔助生產(chǎn)區(qū)消防區(qū)預(yù)留地22.5°PN（建北）N4.1廠區(qū)布置項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)N4.1廠區(qū)布置PlantLayout項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)人流線Flowline物流線Supplyline消防站消防通道Fireexit逃生通道Escapeexit北大門(mén)南大門(mén)西大門(mén)東大門(mén)22.5°PN（建北）N4.1廠區(qū)布置項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)設(shè)備順從工藝設(shè)備布置緊湊檢修空間安全通道EL0.000平面布置項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)4.1車(chē)間布置WorkshopLayout設(shè)備順從工藝設(shè)備布置緊湊檢修空間安全通道EL0.000平面布項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)項(xiàng)目背景設(shè)備設(shè)計(jì)工藝設(shè)計(jì)工廠布置安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)PART5安全環(huán)保Safety＆EnvironmentSIS設(shè)計(jì)自動(dòng)控制環(huán)境評(píng)價(jià)三廢處理PART5安全環(huán)保Safety＆Environmen項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)T0102脫丙烷塔控制方案5.1自動(dòng)控制AutomaticControl溫度壓力流量液位項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)T0項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)E0108換熱器控制方案5.1自動(dòng)控制AutomaticControl項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)E0

項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)比值控制方案5.1自動(dòng)控制AutomaticControl丙烷循環(huán)H2NNFNNF丙烷循環(huán)H2項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)HAZOP分析LOPA分析SIL驗(yàn)證辨識(shí)加熱爐主要危險(xiǎn)事件將安全儀表功能分配到保護(hù)層驗(yàn)證SIL等級(jí)5.2SIS設(shè)計(jì)SISDesign項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)HARisksystem、Aloha軟件模擬防護(hù)、應(yīng)急措施項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)5.3環(huán)境評(píng)價(jià)EnvironmentEvaluationRisksystem、Aloha軟件模擬防護(hù)、應(yīng)急措施項(xiàng)目背5.3環(huán)境評(píng)價(jià)EnvironmentEvaluation液化氣儲(chǔ)罐項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)丙烯儲(chǔ)罐噪聲評(píng)價(jià)5.3環(huán)境評(píng)價(jià)液化氣儲(chǔ)罐項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全達(dá)標(biāo)排放項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目總結(jié)二硫化物氯化物煙塵廠家回收堿洗后高空排放廢氣氯鹽廢水少量硫化物蒸發(fā)脫鹽A/O污水處理廢液失活催化劑惰性瓷球堿渣WAO+SBR廠家回收再利用廢渣5.3三廢處理WasteTreatment達(dá)標(biāo)排放項(xiàng)目背景設(shè)備設(shè)計(jì)工廠布置工藝設(shè)計(jì)安全環(huán)保經(jīng)濟(jì)評(píng)價(jià)項(xiàng)目PART6經(jīng)濟(jì)分析EconomicEvaluation動(dòng)態(tài)評(píng)價(jià)靜態(tài)評(píng)價(jià)投資分析不確定性分析PART6經(jīng)濟(jì)分析E