1、11.5t/h112.7-(LXT乙烯裝置總貌圖33. 9kPa石油 9. lt/h 石腦油 9.8t/h汽油分is 塔DA1O柴汕 136t/h 丿JO敦幅油21.31:202叫184. 5*C產(chǎn)品至虢區(qū) 6t/h申烯產(chǎn)品至虢區(qū)1 13. Ot/h裂解煥料DA1O229. rc983, 5kPa機(jī) GB2O15, 887rpm37. 6C攀解潢汕 T3, 104Kg/hDA 10385. 2-C緘洗塔 DA2O3農(nóng)解F壓縮機(jī)GB2O145必X>氣甲淬kPa乙烘轉(zhuǎn)化_$J1 bacixMoi-8. 3-C乙憶鈾ta塔 DA4O335.A 205. 0*C B 79. 8-C35.1, 9

2、90. lkPa>4 -20. 2*C42. 8*C甲烷2#內(nèi)烯祐 tflff DA4O81,612. lkPa41.5*C衲慍塔 DA4O765.4'CA 20. 6-CB 60. 2C高壓脫丙 烷塔DA 1460l,4126kPa丙磁找 136. 8*C13.3t/hDC4O2 DA202進(jìn)料脫乙烷烙DA4O17.6t/h氫氣 323Kg/h48.4t/h16.3t/h545- 4kPa1-130. 6'CFF2O1低壓脫丙DA4O458. rc197t/h .稅卬繪塔 DA3011& 3t/hl9t/h裂解汽迪579.6kPa I J 2A301n L-Jf

3、-51.3Cll,492Kg/h混合碳四.6kPa162. 7"C9. 6t/h踹闕康料油乙 668Ke/h3, 948K“h輕婭4. 3t/h484mol%-2 I 07mjnH2CBA101/10 2裂解爐27KMh )K0h JlOKg/l2, 190Kg/l鍋爐給水BFW2, 047Kg/h2, 001Kg/h1, 851Kg/hb 846Kg/hnos1 229. 5*C<855. 2*Co265. rc205. 5'CCG去1#裂解爐BA1O1834. 8'C834. 6'C855. 0*C855.4'Cb 048Kg/h側(cè)鬆燃料UF

4、Gl,422Kg/h77kPa底部燃料任FG超扁壓汽包FAlOlCG去DA1O1JDA11O2油急冷器 HB1O1A脫過(guò)拚爲(wèi)EA1O1B17.9t/hlL510Mpa0389. 2*C437. rc檢熱錨爐 EA1O1A"98. 5'CSS16.9t/h3, 156KE/U1O 仃 & 417Kt/h 12. ot/h 2,656K“h嫌料油輕矩152. (TC2.5%1.2t/h鍋爐給水BFW汽DSV194. 5-C19.6t/h1, 971Kg/h1, 965Kg/hb 852Kg/h1, 850Kg/h251K0h245Kg/h 1.SQWK&/1694

5、K0h2“ 771KE/h835. rc835. 2*C835. rc835. 2-C-1.635mmH2O2#裂解爐BA 10211.582Mpay481. rc18.8t/h377. 8*C400. 8*CBH1O2A/B835.C ,廢熱弼爐EA102AP日色剛爐 EA102BD.超必壓汽過(guò)FA1O21, 180Kg/h J248kPQ側(cè)壁燃料PFGl,441Kg/h J701cPa廉部燃料UFG油急冷器HBIO2B汕急內(nèi)耀 HB1O2A217. 0*C217. rcCG去DAI 102，CG去DAIO1142. 0*C15t/hBA103/104裂解爐1.8%<4,322Kg/h

6、3, 776Kg/h3, 587Kg/h2, 825Kg/h鍋爐給水BFW凍料油3, 208Kg/h3, 143411Kg/h3, 116Kg/h3, 095Kg/h152. 0-C14t/h1.7%<184. 0*C3, 489Kg/h3, 490Kg/h3, 258Kg/h3,437Kg/h鍋爐給水BFW汽DS1, 998Kg/h1, 974Kg/h2, OOlKg/h1, 999Kg/h17.0t/h18. lt/h11. 509Mna11,499Mpa816. O"C843. 5*C37mjnH2O-1. 7 39mmH2O3&裂解爐BA1O3仆裂解爐BA1Q4

7、506. 2 C508. CTC超髙壓 蒸汽SS超高壓 蒸汽SS366. 3'C373. 6'C384. rc393. VC214. rc215. rc376. 3 C383. 5*CCG去DAIO1815. 9 C815. 8*C816. 0*C815. 8-C215. rc214.7-C廢卻創(chuàng)爐 EA1O4A/B廢劭鍋爐 EA103A/B汕急冷湃=HB1O4 八/BCG去DA1OIl,011Kg/h 丿99磯底濟(jì)燃料冗FG1, 203Kg/h1236kPa劇擊燃料冗FGl,419Kg/h .67. lkPa底部燃料VFG闕高壓汽包PA 103油急旳器rHB103A/BH 越

8、寫壓汽包I FA1047S脫id拾蠱13H1O4A/B 1X丿V517.4'C844. 0"C843. 6'C841. 9'C844.4-C煙燃料氣FG6.3t/h1, 329Kg/h (84 9kPa15. 5t/h凍料油BA105/106裂解爐120. 8'C2. 158mol<195. 2-C15t/h3, 233Kg/h3,440Kg/h4, 349Kg/h3, 825Kg/h鍋爐給水BFW2, 134Kg/h2, 095. 687Kg/h2, 158Kg/h2、095Kg/h134.5*C 1.4% <4,906Kg/h4,491

9、Kg/h4,565Kg/h4,961Kg/h嫌料油19t/h鍋爐給水BFW稀釋蒸汽DS3, 546Kg/h3,447Kg/h3, 549Kg/h3,494Kg/h10.4t/hw11.515Mpa511.4C834.1 C834. 9'C832. 5'C835. 5eC833. 6'C廢熱鍋爐EA1O5A/B400. 0*C427. 5'C818. 5eC818. 2*C817. 8*C818. 3eCH1O5A/B脫討熱器 BH】0682iunH2O5Q裂解爐BA1O5940Kg/h J1.7kPa側(cè)壁燃料氣FG1, 147Kg/h15-6t/h t90,Ok

10、Pa底溫燃料花FG熱汽SS*214. 8-C214. 8*C-2.z38mmH206說(shuō)解爐BA10622. 9t/h11.254MDa屜高壓汽 包FA106524. 9'C514. 2*C514. 6-C511.9'C818. rcP區(qū)熱謂爐 EA106A/B512. 6*C517. rc529. 8'C516. rc油免旳器、1, 586Kg/h側(cè)壁燃料氣FG2, 254Kg/h J9ClkPa底部燃料冗FG216. 8-C216.4'CCG去DA1O1HB1O5A/B18. 3t/hCG去DA1O129. rc急冷水系統(tǒng)裂解氣至FA201M總為水EA1132

11、并急冷水EA11434. 8kPa2、839Kg/h284C1.2kPa米hDAlOl的裂解氣220.lkPa690, 5t/h48.0-C109.工藝水汽檢511.0kPa汽煒513.9kPa38. 3kPaDA1O3187. TCDS至裂解爐中!£眾汽./稀件60. lt/h50. lt/hQi令油H彳打莖汽稀Ff塚汽發(fā)生EA117塔再沸器EA12O竦汽撿熱淞EA115丄藝水 汽提塔 DA1O4換迪器EA118A/B/C/D0EA12185. 2'C工藝水汽提塔進(jìn)料象GALO6A/B稀釋雄汽發(fā)生器進(jìn)料*(iA107A/BGA1O4A/B/C裂解汽油至EA42O996Kg/

12、htit污冷卻器EA116316t/h ms汽汕分!8塔冋越 IG八105八/B/C至DA1O1何流l964Kg/h 扌甲275, 883. 278rpm裂解代壓習(xí)機(jī)29. (TCGB201系統(tǒng)12345|77.2t/h39. 0-C21. 2*C31. 5 C30. 3986. 3*C血段后冷卻器84. TC182.5kPa80. 8-C465. 3kPa81.7-C983. 3kPa93. rc1, 870. OkPaEA2()«78. 8t/hEA203 A/R三園后冷34. Ok bQ三燈排Hl三 ELKA:段吸入雄287.2Kg/h37. 7'C急冷塔DA 103M

13、LEA2CM裂解氣束 自急冷塔 DA103卻辭 EA2O5裂解PEA206J四應(yīng)門冷邂料2# 偵熱器 EA21015. 0eC十矗爲(wèi)進(jìn)料1#網(wǎng)熱器EA2HA: 20& 5'CB: 16. 2'C段吸入越GA2O6A/B聚丙烯返何氣汽油汽捉塔 rDA1201£A201EAFA37. 9*CA373. lkP：P188.lkP：EA2O7*冷凝液加 ML £215黑解P 十枷藩FF2Q1A/DF燥器流 岀物葆冷 器EA220礙洗塔DA203賊洗塔 D/X203凝液諷提塔DA202提塔DA20248. 2t/h-9 CTCEA409 ，16.4t/h、EA

14、1315X6裂解代壓縮機(jī)四段吸入ME1 FA205GE201系統(tǒng)三塔流程37. 6'C裂解久斥縮 機(jī)四段吸入MIFA205裂解冗壓縮機(jī)7. 8t/h950. 5kPa2、503Kg/h27. 8'ClJ 304Kg/h超髙壓績(jī)江排污冷卻器EA109污水處理7. 2kPa59. CTCEA212A/B75. reU.6t/h 低壓稅內(nèi)烷塔EA1263DA2O3 >50%£*曲破酒as”；*GA2O2£2韓弱毗謹(jǐn)循環(huán)乂GA2IOA/B£N堿液循皿樂GA2O3A/B裂解氣斥縮機(jī)兀段吸入嫌FA206低斥脫丙烷塔DA4O4裂解氣爪縮機(jī)三段吸入罐F 八

15、203餐解氣加熱器EA206廢ai去廢堿液凝聚器FA801I, l93Kg/h斯鮮堿自GA2O47,225rpmGB501系統(tǒng)1, 580. 009kPa84. 633*CFA5051502t/h .E/501/150151.947kPa108.8t/h -37. 5*C154.787kPa26. lt/h -26.4*C：A1315X<0EA410fEA?07mi入誦134.4t/h 512.595kPa0.4*CEA60216.9t/h 9.7*CEA7Q4V丿1-EA6O4k亠，0EA4O3EA422EA1422FA4O9FA 1409EA315X15X 4QEA411FA41OK

16、A141OFA502:“吸Alt0EA1315X -FA503三段吸AMEA435EA304EA210KA14741315XEA1315X vFA50dEA315XGA5020FF4O1£A4()“/14()8TGB601系統(tǒng)N2乙烯分離單元碳二系統(tǒng)冷箱EA315X/1315XEA4O2至高壓脫丙烷塔 DAI 460L 990, lkPa|-2o. rcL2L0t/h冷凝器EA4O335. 6t/h粗氫氣3Kg/h氫氣65Kg/h25. 8kPa16. rc42. l C下燥器進(jìn)料“ 預(yù)熱器EA211脫乙烷塔 DA401EA4O1/14O1GAV01A/B/C63. 6'C脫

17、乙烷塔FA4011, 709. 9kPa綠汕嫌iff底象GA4O2A/B乙煥轉(zhuǎn)化器逬 岀料換熱召 EA4O4綠油謎FA4O2乙燒轉(zhuǎn)化器 進(jìn)料加熱器EA405A： 204. 6'CB:79. 8-CA: 187. 5*CB:52. 5'CA：185. 3*CB95.4C乙快轉(zhuǎn)化器 中間冷卻科 EA406A/B2Kg/h27Kg/h氧氣乙烷58.3kPsJ134t/g EA41O1.612.1a335Kg/hOA301 .乙煤軸倔塔回流肚FA4O3GA403A/E/C29. 7t/h乙烯產(chǎn)品去貯罐丿 DA4O3450.265kPa循環(huán)乙烷去EA3066, 828Kg/h3. 661

18、Kg/h循環(huán)乙燒去EA1315Xta塔-&4CEA1462A/B分離單元碳三系統(tǒng)EA1460l,4055CI6kPa-3877CH250Kg/h 32,8t/hl.#QNkPa158t/h65. 8*C13. 3t/h569. 7kP.6kPa67. 2*CA:38.4*CB: 38. 8*C脫乙烷塔 DA4O1回流雄 FAM6OEA411DA146O回適短GAM60A/B冋血鍵FA4O4必/低壓脫丙烷 塔釜換坯邂EA1464DA2025. 2 C13. 5t/h45. 5CEA412A/B低壓脫 內(nèi)烷塔 DA4O4 -H18. Ot/h 70. 6'CGA411A/B16.

19、Ot/h丙烯于FF4O236.8*012.450. 065kPa內(nèi)一坯轉(zhuǎn)化邂 I論H:物分為紳FA415A:-0.4kP? B：39. 7kP;丙_1劣轉(zhuǎn)1L2LDC402A：20. 6'CB:60. 2*C19.6t/hFA204431.2Kg/h14.lt/hGA41OA/B46. 0*CFA4O6再沸器EA416丙烯產(chǎn)品去貯罐滋丙憂13. lt/h 精ta塔DA4O8121.2t/h裂解乳油15. 3t/h5& 2C 痕烷塔DA4O5EA418W14. 6t/hEA419冋流線 FA4OXGA4O9A/B404,5kPa4.2CGA412A/B108. 8*C-0. 2t

20、/hlL 523Kg/h汽油產(chǎn)皿內(nèi)碳四產(chǎn)品CA14O8A/B混合碳四去貯罐18. 8kPa57.4*C循環(huán)丙烷去裂解爐回iOC GA413A/B2內(nèi)惴DA4O7l,9325Kg/EA115/1415600. 5kPaFA3O518.9t/h甲烷制冷 a 壓縮機(jī)GB3029T9V4«區(qū)F換敗妙3”皿工換熱£EA315XEA314X老冷箱2"尾U換熱理EA312X宀"換熱帶A21IX脫甲烷塔頂流出物3, 895. OkPa至EA1315X宅EA214再生9 5t/h年EO/EG 53Kg/h氣P甲烷壬FG 3,200Kg/h12至FG 26Kg/h甲烷外送1

21、723kPa74甲燈化反應(yīng)器DC301258. 丁C至PE-3Kg/h273. 2-C弦氣于想51Kg/h 簽嚇301x60EVUJa:L 畫331Kg/l9. 3t/h29. 4t/h-16. 2 C自DA301釜DA401 EA220-70. 0-C61.5t/h曲料0戀Iff FA304C-133J3,310. 3kPj-96. 2'CFA309乙 105Kg/h3J45Kg/hDA30L脫卬烷塔進(jìn) 料/烙須冷凝器EA310X脫甲烷塔冋流褲FA3O6,233Kg/1, 849Kg/h941Kg/h2 a逍料分DA30VDA301-167. 1C3#進(jìn)料分紋PP烷分離除FA307D

22、A3O1DA30 II叫流至EA214再生新冷箱和脫甲烷塔LP屮燒至FGH2 至 FGHDA30l-164. 3Cc-112.2n尾F按熱盟NO2 EA1314X/EA1312X卅圧吒換熱爲(wèi)NO.2EA1311XpA4(M 0.2'CIKg/h脫申烷塔 進(jìn)斛/塔li 冷凝益 NO.2 EA1310X4斗魁氣換熱泄NQ.2 EA1315X"130. 5'C 545. 6kPa23. 8kPa至EA312乍裂解 ZCREA4O9進(jìn)料來(lái)口冷箱 系統(tǒng)并分掲罐EA3O730. 8eC-11.2-C脫甲烷塔1#訥 料裸內(nèi)器鏟11 11. 2CIKg/h3,316. Ika-93.

23、-68. 8'CBL甲燒塔C24. lt/h磁甲烷烙3# 進(jìn)料分曲雄FA1306脫甲矩塔2W 進(jìn)料分虜雄FA13O5換抱器 EA1316X裂解氣自EAI309X脫屮寰塔異 進(jìn)料分蟲繼FA13O4脫甲烷塔3轉(zhuǎn) 進(jìn)料深為謎 EAI309XEA1318-66. 8-C-55. 9*C-57.4*C裂解花-55. 8-Cr59.6*C-41. 6'C樓卬烷塔 DA301.-44. VCP：A3()6-35.4'CDA3O1DA3O1EA1317REA1315X3#進(jìn)樣深卜:A309X2, 624Kg/h658Kg/h114Kg/hDA3O1DA3O1至FA1304、至 FA3O

24、4-51.3；EA308X謖料深逢器EA13O8X|EA315X/EA1315X"13()7裂解汽油58. 635-i5工嘰""宀h8483t/h脫戊烷塔冷凝器 EA70113.984t/h64. 089-C112.822'C脫戊烷培脫戊烷堆再沸瀋畢產(chǎn)冊(cè)GA701A/B"7014, 365. 368Kg/h35.444 "C509.360kPa-2.590kPsI 101.473'C再沸耀EA7MA/BH20汽提塔DA7036. 009Kg/h裂解汽油加氫碳I脫除塔冷凝器-68.668kPaEA7O355. 586,'-

25、18.997kPi11. 773/片F(xiàn)A202130. 974'C146. 040-CGA703A/BEA706礙I樓陰塔 DA702:冋施瑞FA7O20 器 EA7O4FA7O4段進(jìn)料fi 沖 KFA7O5和丿4 加 熱器 EA7OH632Kg/h238kPa47. 500Kg/hDC7O147. 976'C10. 245t/h32.934t/hGA7O2A/B1, 068 145Kg/h C9C10產(chǎn)氣 礁十產(chǎn)品冷卻越EA7O7GA7O5A/R22.691Kg/hH2S汽擇塔進(jìn)料/器EA7120混蛀芒品冷知活戌FA70610. 152t/h 混合苯產(chǎn)品24.835kPa2,

26、 770.007kPd2,498.481Kg/h薦用閃菇二段反應(yīng)器DC7O2進(jìn)山料攤EA7O9:段反應(yīng)器 流;11物冷檢器EA71Q279t/h.279©30. 9'C2, 913.425kPa41. rcH 2, 976.312kPa4&GA7O6術(shù)環(huán)壓縮 機(jī)吸入雄FA7O7段反應(yīng) 閃魚鍵FA1709仍環(huán)壓編機(jī)GB701A/B298159.81TCF1A7 *4由.849'CIIO. 983MpaF1.343t/h3, 349. 795kPa HS650.305'CGBT20128. 067t/h68. 275'C-71.840kPa公用工程11.044MpaCW23.494'