Patent SG-11201806319Y-A (SG)
Title: Process and installation for the conversion of crude oil to petrochemicals having an improved product yield
Inventor: WARD ANDREW MARK
IPC: C10G69/14
Filed: 2017-01-27
Abstract: INTERNATIONAL APPLICATION PUBLISHED UNDER THE PATENT COOPERATION TREATY (PCT) (19) World Intellectual Property -, Organization MD 1111101110101011111 HO 11111 0111011110110011110111 RIMINI III International Bureau 0.. .... .. (10) International Publication Number (43) International Publication Date ..... .....!;,' WO 2017/133975 Al 10 August 2017(10.08.2017) WIPO I PCT (51) International Patent Classification: AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, ClOG 69/00 (2006.01) C1 0G 69/14 (2006.01) BZ, CA, CH, CL, CN, CO, CR, CU, CZ, DE, DJ, DK, DM, DO, DZ, EC, EE, EG, ES, FI, GB, GD, GE, GH, GM, GT, (21) International Application Number: HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KH, KN, PCT/EP2017/051750 KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, (22) International Filing Date: MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, 27 January 2017 (27.01.2017) NI, NO, NZ, OM, PA, PE, PG, PH, PL, PT, QA, RO, RS, RU, RW, SA, SC, SD, SE, SG, SK, SL, SM, ST, SV, SY, (25) Filing Language: English TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, (26) Publication Language: English ZA, ZM, ZW. (30) Priority Data: (84) Designated States (unless otherwise indicated, for every 16154556.1 5 February 2016 (05.02.2016) EP kind of regional protection available): ARIPO (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, (71) Applicant: SABIC GLOBAL TECHNOLOGIES B.V. TZ, UG, ZM, ZW), Eurasian (AM, AZ, BY, KG, KZ, RU, [NL/NL]; Plasticslaan 1, 4612 PX Bergen op Zoom (NL). TJ, TM), European (AL, AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, (72) Inventors: WARD, Andrew Mark; c/o SABIC Intellect- LV, MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, ual Property Group, P.O. Box 3008, 6160 GA Geleen SM, TR), OAPI (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, (NL). OPRINS, Arno Johannes Maria; c/o SABIC Intel- lectual Property Group, P.O. Box 3008, 6160 GA Geleen GW, KM, ML, MR, NE, SN, TD, TG). (NL). SCHAERLAECKENS, Egidius Jacoba Maria; c/o Published: SABIC Intellectual Property Group, P.O. Box 3008, 6160 — GA Geleen (NL). VELASCO PELAEZ, Raul; c/o SABIC with international search report (Art. 21(3)) Intellectual Property Group, P.O. Box 3008, 6160 GA — before the expiration of the time limit for amending the Geleen (NL). claims and to be republished in the event of receipt of amendments (Rule 48.2(h)) (81) Designated States (unless otherwise indicated, for every kind of national protection available): AE, AG, AL, AM, (54) Title: PROCESS AND INSTALLATION FOR THE CONVERSION OF CRUDE OIL TO PETROCHEMICALS HAVING AN IMPROVED PRODUCT YIELD (57) : The present invention relates to an integrated 24 process to convert crude oil into petrochemical products 21 comprising crude oil distillation, hydrocracking and steam 34 cracking, which process comprises subjecting the crude oil 31 ‘ - , 4 to crude oil distillation to produce gases fraction, naphtha, kerosene, gasoil and resid; subjecting resid to resid upgrad- 10 4 1 22 3,_ ing to produce LPG, light-distillate and middle-distillate; subjecting at least a portion of one or more of the group consisting of middle-distillate produced by resid upgrading, — .. — .. — .. 42 kerosene and gasoil to middle-distillate hydrocracking to LPG, light hydrowax; produce -distillate and and subjecting at least a portion of one or more the of group consisting of 23 ‘-, light-distillate by resid upgrading, light-distillate produced 51 ...S...,.. r ... tm 33 — ...---... 43 `-, produced by middle-distillate hydrocracking and hydrowax to steam cracking. Furthermore, the present invention relates installation for 1 ws/ 5 to a process performing the process of the present invention. The process and process installation of ir) the present invention allows the conversion of crude oil into petrochemical products having an improved carbon-effi- IN 01 ciency, while maintaining a high ethylene yield and a fa- vourable ethylene : propylene ratio. M M 1-1 ......... Figure 1 IN Il © ei O