Đánh giá định lượng rủi ro nhà máy sản xuất nhựa polypropylen dung quất bằng phần mềm mô phỏng safeti 6 54

ĐẠI HỌC QUỐC GIA TP HỒ CHÍ MINH TRƯỜNG ĐẠI HỌC BÁCH KHOA ¶· LÊ THỊ HUYỀN TRANG ĐÁNH GIÁ ĐỊNH LƯỢNG RỦI RO NHÀ MÁY SẢN XUẤT NHỰA POLYPROPYLEN DUNG QUẤT BẰNG PHẦN MỀM MƠ PHỎNG SAFETI 6.54 Chun ngành: CƠNG NGHỆ HĨA HỌC Mã số: 605275 LUẬN VĂN THẠC SĨ TP HỒ CHÍ MINH, tháng 12 năm 2009 LUẬN VĂN THẠC SĨ CƠNG TRÌNH ĐƯỢC HỒN THÀNH TẠI TRƯỜNG ĐẠI HỌC BÁCH KHOA ĐẠI HỌC QUỐC GIA TP HỒ CHÍ MINH Cán hướng dẫn khoa học : TS GV Huỳnh Quyền ThS GVC Hoàng Minh Nam Cán chấm nhận xét : (Ghi rõ họ, tên, học hàm, học vị chữ ký) Cán chấm nhận xét : (Ghi rõ họ, tên, học hàm, học vị chữ ký) Luận văn thạc sĩ bảo vệ HỘI ĐỒNG CHẤM BẢO VỆ LUẬN VĂN THẠC SĨ TRƯỜNG ĐẠI HỌC BÁCH KHOA, ngày 28 tháng 01 năm 2010 Trang i LUẬN VĂN THẠC SĨ TRƯỜNG ĐẠI HỌC BÁCH KHOA KHOA CƠNG NGHỆ HĨA HỌC CỘNG HOÀ Xà HỘI CHỦ NGHIà VIỆT NAM Độc Lập - Tự Do - Hạnh Phúc -oOo Tp HCM, ngày tháng năm NHIỆM VỤ LUẬN VĂN THẠC SĨ Họ tên học viên: Lê Thị Huyền Trang Ngày, tháng, năm sinh: 13/11/1981 Phái: Nữ Nơi sinh: Quảng Trị Chuyên ngành: CƠNG NGHỆ HĨA HỌC MSHV: 00506101 1- TÊN ĐỀ TÀI: Đánh giá định lượng rủi ro nhà máy sản xuất nhựa Polypropylen Dung Quất phần mềm mô SAFETI 6.54 2- NHIỆM VỤ LUẬN VĂN: đánh giá xác suất rủi ro cá nhân xác suất rủi ro tập thể tiềm tàng trình vận hành nhà máy Các kết rủi ro sau so sánh với tiêu chuẩn rủi ro chấp nhận để xác định thiết bị, khu vực có mức độ rủi ro cao, từ đưa biện pháp nhằm giảm thiểu rủi ro thiết lập hệ thống quản lý an toàn để kiểm soát rủi ro 3- NGÀY GIAO NHIỆM VỤ : 2/2009 4- NGÀY HOÀN THÀNH NHIỆM VỤ : 15/12/2009 5- HỌ VÀ TÊN CÁN BỘ HƯỚNG DẪN (Ghi đầy đủ học hàm, học vị ): TS GV Huỳnh Quyền Th.S GVC Hoàng Minh Nam Nội dung đề cương Luận văn thạc sĩ Hội Đồng Chuyên Ngành thông qua CÁN BỘ HƯỚNG DẪN (Họ tên chữ ký) CHỦ NHIỆM BỘ MÔN QUẢN LÝ CHUYÊN NGÀNH KHOA QL CHUYÊN NGÀNH (Họ tên chữ ký) (Họ tên chữ ký) Trang ii LUẬN VĂN THẠC SĨ LỜI CÁM ƠN Từ đáy lịng xin cảm ơn Ba Mẹ dạy bảo để trưởng thành ngày hơm Hồn thành luận văn này, trước tiên, xin bày tỏ lời cảm ơn sâu sắc đến thầy TS Huỳnh Quyền hướng dẫn, truyền thụ kiến thức chuyên môn quý bắu giúp có định hướng khoa học đắn q trình thực đề tài Tôi xin bày tỏ lời cảm ơn chân thành đến thầy Hoàng Minh Nam cho tơi lời khun, lời nhận xét, góp ý sâu sắc giúp đề tài hồn thiện Tơi xin bày tỏ lịng cảm ơn đến Cơng Ty Det Norske Veritas (DNV) tạo điều kiện thuận lợi để tơi hồn thành tốt luận văn Tơi xin cám ơn ông Derek Hoare đồng ý cho sử dụng kiến thức, nghiên cứu phần mềm công ty DNV luận văn Tôi xin cám ơn đồng nghiệp Lee Cho Hing truyền thụ kiến thức trình đánh giá định lượng rủi ro để tơi hồn thành tốt Luận văn Tơi xin trân trọng cảm ơn đồng nghiệp anh Hoàng Văn Tân người nhiệt tình bảo, cố vấn kỹ thuật suốt q trình thực đề tài Tơi xin cảm ơn đồng nghiệp anh Trần Đức Lai hướng dẫn tận tình cách sử dụng phần mềm SAFETI Tơi xin gửi lời tri ân đến quý Thầy Cô ngồi khoa Hóa Học trường Đại học Bách khoa Tp Hồ Chí Minh truyền thụ cho tơi kiến thức vô hữu dụng Tôi xin gửi lời cám đến Anh Chị, bạn học lớp Cao học giúp đỡ trình học tập Tôi vô biết ơn người thân gia đình đặc biệt người Chồng u q ln giúp đỡ động viên tơi suốt q trình học -o0o - Trang iii LUẬN VĂN THẠC SĨ TÓM TẮT LUẬN VĂN THẠC SĨ Đề tài “Đánh giá định lượng rủi ro nhà máy sản xuất nhựa Polypropylene Dung Quất phần mềm mô SAFETI 6.54” nghiên cứu quy trình cơng nghệ sản xuất nhà máy Polypropylene Dung Quất Từ xác đinh mối nguy hiểm cháy nổ, độc hại tiềm tàng trình vận hành nhà máy Xác đinh liệt kê trường hợp cố xảy nhà máy Từ trường hợp cố xác định, đề tài tính tốn tần số dựa vào sở liệu tần số tai nạn thiết bị gới mô hậu phần mềm PHAST 6.54 Sau kết hợp tần số hậu để tính xác suất rủi ro cá nhân rủi ro tập thể phần mềm SAFETI 6.54 Các kết rủi ro tính bao gồm: rủi ro cá nhân khu vực (LSIR), rủi ro cá nhân tính năm (IRPA), xác suất tổn thất sinh mạng tiềm tàng (PLL), rủi ro tập thể So sánh kết rủi ro tính với tiêu chuẩn rủi ro để xác định khu vực hoăc thiết bị có mức rủi ro cao, để từ có biện pháp giảm thiểu rủi ro khu vực thiết bị ABSTRACT The thesis undertake a Quantitative Risk Assessment (QRA) for all planned process facilities for Dung Quat Polypropylene Plant (DQPP) The study evaluates the level of individual risk as well as societal risk by the operation of the DQPP facilities and compare this level of risk to the recommended risk acceptance criteria The risk results may also be used to assist to identify process system safety critical elements, thus providing focus to Safety Management system initiatives to control the risk Trang iv LUẬN VĂN THẠC SĨ MỤC LỤC DANH MỤC CÁC THUẬT NGỮ, CHỮ VIẾT TẮT VII DANH MỤC CÁC HÌNH VỄ, ĐỒ THỊ X DANH MỤC CÁC BẢNG BIỂU XII ĐẶT VẤN ĐỀ 14 MỤC TIÊU NGHIÊN CỨU CỦA ĐỀ TÀI 15 TỔNG QUAN 15 I.1 TỔNG QUAN CÁC SỰ CỐ XẢY RA TRONG NHÀ MÁY LỌC – HÓA DẦU: 17 I.2 TỔNG QUAN PHƯƠNG PHÁP ĐÁNH GIÁ ĐỊNH LƯỢNG RỦI RO (QRA): 22 I.3 TỔNG QUAN PHẦN MỀM MÔ PHỎNG ĐÁNH GIÁ ĐỊNH LƯỢNG RỦI RO SAFETI 6.54 [04] 35 I.4 TỔNG QUAN CÔNG NGHỆ SẢN XUẤT POLYPROPYLENE TẠI NHÀ MÁY DUNG QUẤT 37 NGHIÊN CỨU ĐÁNH GIÁ ĐỊNH LƯỢNG RỦI RO NHÀ MÁY DQPP 41 II.2 THIẾT LẬP CÁC QUY TẮC VÀ GIẢ ĐỊNH [18], [24], [29] 42 II.3 NHẬN DIỆN CÁC MỐI NGUY VÀ XÁC ĐỊNH CÁC TRƯỜNG HỢP SỰ CỐ [11], [24], [29] 42 II.4 MỘT SỐ LOẠI TRỪ [24], [29]: 43 a) Hệ thống đuốc: 43 b) Hệ thống vận chuyển sản phẩm: 43 c) Mối nguy trình vận chuyển: 43 d) Các rủi ro liên quan đến an toàn nghề nghiệp 43 II.5 MÔ PHỎNG HẬU QUẢ BẰNG PHẦN MỀM PHAST 43 II.6 PHÂN TÍCH TẦN SỐ 44 II.6.1 Thiết bị công nghệ: 44 II.7 TÍNH TỐN RỦI RO BẰNG PHẦN MỀM SAFETI 45 II.7.1 Xây dựng kiện 45 II.7.2 Điều kiện khí 48 II.7.3 Các tiêu chuẩn ảnh hưởng đến người 48 II.7.4 Tính tốn rủi ro rủi ro cá thể 48 II.7.6 Tính tốn rủi ro rủi ro tập thể 49 II.7.7 Dữ liệu dân số 50 II.7.8 Đánh giá rủi ro 50 II.7.9 Các biện pháp giảm thiểu rủi ro 52 II.7.10 Phân tích lợi ích – phí tổn 52 II.7.11 Tính tương đối tính toán 53 KẾT QUẢ TÍNH TỐN 54 III.1 CÁC ĐƯỜNG MỨC RỦI RO CÁ THỂ 55 III.2 RỦI RO CÁ THỂ TRÊN NĂM 58 III.3 TỔN THẤT SINH MẠNG TIỀM TÀNG 59 III.4 Đồ THỊ F-N 62 III.5 CÁC THIẾT BỊ QUAN TRỌNG 62 KẾT LUẬN & KIẾN NGHỊ 63 IV.1 KẾT LUẬN 64 Tính tốn rủi ro cá thể cộng đồng 64 Rủi ro cá thể nhân viên nhà máy 65 Tổn thất sinh mạng tiềm tàng (PLL) 65 Rủi ro tập thể (đồ thị F-N) 65 IV.2 KIẾN NGHỊ 65 Kiến nghị chung 65 Tổng quan biện pháp giảm rủi ro 66 Đề nghị hướng nghiên cứu tiếp đề tài 67 Trang v LUẬN VĂN THẠC SĨ PHỤ LỤC I 68 CÁC QUY TẮC VÀ GIẢ ĐỊNH 68 A.1.1 ĐỊNH NGHĨA CÁC TRƯỜNG HỢP SỰ CỐ 69 A.1.2 DỮ LIỆU VỀ DÂN SỐ 69 A.1.3 DỮ LIỆU THỜII TIẾT 72 A.1.4 MÔ PHỎNG HẬU QUẢ 73 A.1.5 XÁC SUẤT CÂY SỰ KIỆN 75 A.1.6 ĐÁNH GIÁ ẢNH HƯỞNG 77 PHỤ LỤC II 80 CÁC TRƯỜNG HỢP SỰ CỐ 80 A.2.1 ĐẶT TÊN CHO CÁC TRƯỜNG HỢP SỰ CỐ 81 A.2.2 TÓM TắT CÁC TRƯờNG HợP Sự Cố 82 PHỤ LỤC III 87 MÔ PHỎNG HẬU QUẢ 87 A.5.1 GIớI THIệU 88 A.5.2 Cháy tia : 88 A.5.3 Fireball : 91 A.5.4 Cháy vùng (Pool fire) 96 A.5.5 Cháy bùng (Flash fire) 98 A.5.6 Nổ: 101 PHỤ LỤC IV 105 ĐẾM THIẾT BỊ 105 PHỤ LỤC V 115 TÍNH TỐN TẦN SỐ 115 A.5.1 CƠ Sở Dữ LIệU TầN Số Sự Cố CủA MộT Số THIếT Bị CƠ BảN [38] 116 A.5.2 TầN Số ĐốI VớI CÁC TRƯờNG HợP Sự Cố 117 PHỤ LỤC VI 120 CÁC BẢN VẼ P&IDS 120 LÝ LỊCH TRÍCH NGANG 123 H Trang vi LUẬN VĂN THẠC SĨ DANH MỤC CÁC THUẬT NGỮ, CHỮ VIẾT TẮT Viết tắt Tiếng Anh Tiếng Việt ALARP As Low As Reasonably Practicable Thấp hợp lý với thực tế chấp nhận AT-CAT AT-CAT Catalyst Xúc tác AT-CAT BLEVE Boiling Liquid Expanding Vapour Explosion Nổ chất lỏng sôi giản nở thành (thường có dạng hình cầu) BL Battery Limit Đường ranh giới nhà máy DQR nhà máy DQPP CBA Cost Benefit Analysis Phân tích Lợi ích – Phí tổn CCTV Closed Circuit Television Hệ thống camera theo dõi khép kín CIA Chemical Industry Association Tổ chức hóa học cơng nghiệp COMAH Control of Major Accident Hazard(s) Kiểm soát mối nguy tai nạn CPF Cost of Preventing Fatality Phí tổn nhằm ngăn chặn tử vong xảy DNV Det Norske Veritas Tổ chức đăng kiểm quốc tế Det Norske Veritas DQR Dung Quat Refinery Nhà máy lọc dầu Dung Quất DQPP Dung Quat Polypropylene Plant Nhà máy sản suất Polypropylene Dung Quất ESD Emergency Shut-Down Đóng ngắt khẩn cấp ESDV Emergency Shut-Down Valve Van đóng ngắt khẩn cấp F-N Curve Frequency-Number of fatalities Curve Đồ thị trình bày xác suất xảy cố gây N tử vong cho cộng đồng HCRD Hydrocarbon Release Database Cơ sở liệu rò rỉ Hydrocarbon Fireball Fireball Nổ chất lỏng sơi giản nở thành (thường có dạng hình cầu) HSE Health and Safety Executive (UK) Ban thực hành sức khỏe môi trường Anh HVAC Heating, Ventilation and Air Conditioning Hệ thống thơng gió điều hịa Trang vii LUẬN VĂN THẠC SĨ Viết tắt Tiếng Anh Tiếng Việt IR Individual Risk Rủi ro cá nhân IRPA Individual Risk Per Annum Rủi ro cá nhân năm LFL Lower Flammable Limit Giới hạn cháy LoC Loss of Containment Thất lỏng khí từ bồn chứa đường ống tai nạn xảy LSIR Location Specific Individual Risk Rủi ro cá nhân khu vực cụ thể LPG Liquified Petroleum Gas Khí dầu mỏ hóa lỏng (C3+C4) MAH Major Accident Hazard Các mối nguy tai nạn lớn MOV Motor Operated Valve Van vận hành băng tín hiệu điện NGL Natural Gas Liquid(s) Khí thiên nhiên dạng lỏng NNF Normally No Flow Khơng có lưu chất điều kiện thường P&ID Piping and Instrument Diagram Bản vẽ sơ đồ đường ống thiết bị OF-CAT OF-CAT catalyst Xúc tác OF-CAT PCR Process Control Room Phòng điều khiển PEAR People, Environment, Asset and Reputation Con người, môi trường, tài sản danh tiếng PF Proportion Factor Thừa số tỉ lệ PFD Process Flow Diagram Bản vẽ sơ đồ dịng cơng nghệ PHAST Process Hazard Analysis Software Tools Phần mềm phân tích mối nguy cơng nghệ PL Propylene Propylene PLL Potential Loss of Life Tổn thất sinh mạng tiềm tang SAFETI Software for Assessment of Flammable, Explosive, and Toxic Impact Phần mềm đánh giá rủi ro cháy nổ độc hại QRA Quantitative Risk Assessment Đánh giá định lượng rủi ro RRM Risk Reduction Measure Biện pháp giảm thiểu rủi ro SCE Safety Critical Element Yếu tố an toàn chủ chốt Trangviii LUẬN VĂN THẠC SĨ Viết tắt Tiếng Anh Tiếng Việt SS Substation Phân xưởng phụ trợ TNT Trinitrotoluene Chất nổ Trinitrotoluene TK-CAT TK-CAT catalyst Xúc tác TK-CAT VCE Vapour Cloud Explosion Sự nổ đám mây VPF Value of Preventing Fatality Giá trị việc ngăn chặn tử vong FDSJFD Trang ix D-101 07140-100-25-R110 DWG NO B2 ITEM NO SERVICE NAME B2 / 6.00 / 65 TYPE DESIGN CAPACITY (m3/hr) D.P (kg/cm2g) D.T (˚ C) INSUL TYPE / 0.10 AMB / NI 10 11 NOTES AS SHORT AS POSSIBLE AT-CAT FEED PUMP B2 0.0007~0.0064 661.0 CAPACITY (m3/hr) DIFFERENTIAL HEAD(m) INSUL TYPE CARTRIDGE 0.008 6.0 P-101A /B ITEM NO SERVICE NAME AT-CAT FILTER SERVICE NAME 700.0 x 800.0 0.40 F-101 ITEM NO AT-CAT HOLDING DRUM SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE BELOW D-101 LOWER T.L DELETED NI 65 NI B2 FILTER BY-PASS INSTALLED ABOVE F-101 PUMP SUCTION BELOW F-101 TOP H H 1/4"-AT-11005-W0JP-NI B2 1/2"-AT-10002-Q0JPP-NI NO POCKET NC O NC 2"x1/2" NOTE NOTE B2 B2 B2 LG 1101 B2 FT 1102 L B2 UX 103/205 B2 E SP D038 1/2"-AT-11005-W0JP-NI B2 B2 XZL O 1106 A C BS NC Q0JP W0JP H B2 Q0JP W0JP B2 XZL O 1106 B C B2 XHS O 1106 B C 1"x1/2" 1"x1/2" NOTE NOTE BS BS B2 HOLDS NOTE W0JP Q0JP PSV SIZE TO BE CONFIRMED BY PUMP VENDOR NOTE NOTE 111 FLUSHING OIL FROM P-113 DOCUMENT CLASS : Z 2" W/E 70.0 PAH 1103 B HOLD B1 01 F&G NOTE B2 MGL RUN 101 A DF 204 A REV PS W/E 1103 B PSV 1102 B UZ 204 A KS 114 UX 103 DFAH 204 A B2 DF B2 UX 103/205 MGL 101 B RUN 204 B UZ 204 B UX 103 DFAH 204 B KS 114 B2 PETROVIETNAM B DUNG QUAT REFINERY MANAGEMENT BOARD HYUNDAI ENGINEERING CO., LTD 1/2"-FLO-14105-Q0JP-NI DRAWN BY DATE HEC CLASSIFICATION NO 10 AT-CAT FEED SYSTEM 1/2 DATE 08.07.31 J.O.R A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J APPROVED BY TITLE: 08.07.31 S.Y.P CHECKED BY APPD DQR A CHKD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: F&G NOTE DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) 70.0 P-101B NOTE DATE W/E HOLD M P-101A 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 SP BS PSV 1102 A B2 C 1"-FLO-14105-Q0JP-NI B2 BS PS W/E 1103 A M UX 103/205 PT 1102 B D D009 Q0JP Q0JPP PAH 1103 A 1/2"-AT-11004-W0JP-NI BS 2" 1105 A C B2 XHS O 1105 B C UX 103 PSTV FC BS 1/2"-FLO-11012-Q0JP-NI 1/2"-FLO-11011-Q0JP-NI 1/2"-AT-11005-W0JP-NI LL PSTV FC BS Q0JPP Q0JP 1/2"-FLO-11010-Q0JP-NI 1/2"-FLO-11009-Q0JP-NI 1102 A SP B2 B 100 TO AT-CAT LINE FLUSHING UX 103 O XV 1105 B D008 O C XHS B2 NC L LL XHS 1103 C 3/4"x1/2" PT B2 H PI 1102 B L XZL O 1105 B C B2 B2 A SELECTOR B B2 B2 B2 XV 1106 B D011 (B) 1/2"-FLO-11013-Q0JP-NI B2 O XV 1105 A BS BS B2 PI 1107 XZL 1103 UX 103 XZL O 1105 A C BS UX 103 H PI 1102 A L HS P101 B2 NOTE UX 103/205 SP B2 (A) B2 B2 NC B2 B2 B2 NOTE LL DFAH 203 B2 B2 HS O 1106 A C B2 NOTE 1"-AT-11003-Q0JPP-NI B2 NC PT 1107 NOTE 1"-AT-11002-Q0JPP-NI B2 Q0JPP Q0JP B2 B2 D010 1108 BS BS DF 203 NOTE NC UZ 203 XV 1103 B2 PT D007 BS NOTE F&G UX 102/103 Q0JPP Q0JP Q0JP Q0JPP D004 D004 BS C NC PSTV FC B2 BS F-101 NC O NC SP SP B2 SP BS 3/4" XZL 1102 BS XV 1106 A SP UX 103 NOTE NOTE BS NC Q0JPP Q0JP B2 C B2 D005 Q0JPP Q0JP C FC PSTV UX 103 1"-AT-11001-Q0JPP-NI O BS XHS 1102 XV 1102 L LL BS B2 1" B2 SP BS 3" 1" 3" NOTE PI 1108 B2 BS MINIMUM 1500MM FROM GRADE 1/2"-FLO-11014-Q0JP-NI B2 PSTV FC UX 103/205 PSTV FC D 1/2"-AT-11008-W0JP-NI D006 B2 1" FIC 1102 BS L B2 KS 114 B2 NC SP D038 BS NC 1/2" E HH H SP 1/2"-FLO-14105-Q0JP-NI LI W0JP BS B2 Q0JP CM 1-1/2" 4" 1-1/2"x1" NOTE 1/2"-FLO-11007-Q0JP-NI BS 1101 B GWR 2" 111 FLUSHING OIL TO D-102 BS UX 102 HH 1/2"-FLO-11006-Q0JP-NI LT 1101 B D-101 Q0JP Q0JPP NC 1"-AT-11001-Q0JPP-NI 1-1/2" NOTE BS 3"x1" NOTE NC NOTE B2 XV 1101 3" F 1/2"-FLO-11005-Q0JP-NI B2 B2 111 VENT GAS TO D-103 1/2"-FLO-10004-Q0JP-NI 0.3 % MIN SLOPE NO POCKET 1/2"x1/4" 2" PG 1101 BS C B2 BS B2 LT 1101 A GWR 0.3 % MIN SLOPE NO POCKET 1/2"-VG-11003-Q0JP-NI D003 B2 O HH L LL SP UX 103 UX 102 2"-VG-11001-Q0JP-NI 1/2"-FLO-11004-Q0JP-NI C HH LI H 1101 A L PI 1109 G NOTE 1/2"-AT-10007-Q0JPP-NI B2 O UX 103 B2 1/2"-FLO-11003-Q0JP-NI B2 XHS 1101 Q0JP Q0JPP 1-1/2"x1/2" NO POCKET LL B2 DETAIL "A" NOTE 1/2"-FLO-11002-Q0JP-NI BS 0.3 % MIN SLOPE XZL 1101 B2 NC FO F PT 1106 BS L LL LL B2 Y006 Q0JPP Q0JP 1"x1" UX 102 1"x1/2" PI 1106 BS NC NOTE SOFT SEAT CHECK VALVE 1/2"-VG-11002-Q0JP-NI Q0JPP Q0JP XZL 1109-B C B2 XV 1109-B INLET FROM TOP 300 mm ABOVE D-101 TOP PT CONNECTION TO AIR TUBE TRACING NOTE SP Q0JPP Q0JP B2 300 MM MIN VERT FC FC BS UX 102 NC O C BS B2 XHS 1109 XV 1109-A PT 1109 LN 024 3/4"-LN-02405-A1AA-NI 1/2"-LN-02405-Q0JP-NI XZL O 1109-A C A1AA Q0JP 3/4"-LN-02405-Q0JP-NI B2 B2 B2 G 100 FLUSHING OIL FROM D-111 3/4"x1/2" FG 1101 NO POCKET 210 AT-CATALYST TO D-201 B2 PCV 1103 NC 100 AT-CATALYST FROM D-111 PG 1102 NOTE 6 AT-CAT LINE ON PIPE RACK HAS TO BE SUPPORTED ON ANGLE STEEL "L" SHAPE AS MECHANICAL PROTECTION SEE DETAIL "A" SCALE JOB NO - 07140 DRAWING NUMBER 07140-100-25-R110 11 REV B2 A1 841x594 DWG NO 07140-200-25-R220 B2 ITEM NO ITEM NO Z-213A /B CATALYST FEED PIPES SERVICE NAME P-200 ITEM NO Z-214 SERVICE NAME R-200 DISCHARGE PIPE SERVICE NAME CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE SERVICE NAME NI 11 NOTES R-200 JACKET WATER CIRCULATION PUMP CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE / 42.00 / 25 10 P-204 ITEM NO 168.0 x 21000.0 0.87 / 55.00 -45 / 150 SERVICE NAME PREPOLY REACTOR SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE 250.00 5.0 R-200 ITEM NO R-200 PUMP AS SHORT AS POSSIBLE LOCATE THE VALVE FAR ENOUGH FROM REACTOR TO PERMIT COMPLETE PIPING DISASSEMBLING IN SPOOL PIECE & ELBOWS AREA FOR EASIER REACTOR MAINTENANCE 40.00 20.0 CC B2 FULL BORE BALL VALVE B2 H H 2"-BDH-25001-B1GRS-NI 6"-BDH-22001-V0JPS-NI B2 B2 B2 B2 O KS 204 C B2 NOTE B2 G US 001 FI 2202 H 53.5 1" NC FC 1" XV 2201 H 6"x4" TI 1" 2203 RTD H TIC 2202 PSV 2201 B2 V0JPS B1GRS B2 D0 V0 JP JP S XZL 2201 4" TI 2204 45 ˚ L RTD B2 NOTE LO TE NO 10 L B2 UTILITY CONNECTION IS TO BE PROVIDED (HN, LN) SKIN TEMPERATURE 10 PIPING SPECIAL ITEMS DESC ITEM NO 1-1/2"-SLU-22002-V0JPS-NI DRIP RING SP-D015 1"-BDH-22002-B1GRS-NI SP-D016 1"-SLU-22001-V0JPS-CC SP-P002 1"-PL-23008-D0JP-HC SP-P003 1/2"-PL-22001-D0JP-CC SP-P024 1" UTILITY CONN 1"-PL-23008-D0JP-HC B2 1"-PL-23008-D0JP-HC NC 1" MEPR(MELTING ELECTRO PNEUMATIC RELAY) SHALL BE INSTALLED ON HV-2203 240 FROM R-201 PSV-2401A,B R-202-PSV-2501A,B NOTE NOTE 10 PV 2201 CC PROVIDE SUFFICIENT HEIGHT ABOVE FLOOR FOR INSTALLATION/OPERATION OF PISTON VALVE 45 ˚ 1-1/2"-BDH-22002-B1GRS-NI NC L INLET FROM TOP 240 HP FROM R-201 PV-2401, HV-2405A,B , R-202 PV-2501, B2 B2 1" NOTE 16"-BDH-25002-V0JPS-NI NOTE 11/2 "x1 " 240 TO R-201 MAX SLOPE C FC NC Z-214 US 001 V0JPS B1GRS O XHS 2201 B2 DELETED CC 1"-HN-02406-D1AP-NI NOTE 10 HN 024 PISTON VALVE 230 FROM D-202 SERVICE LINE NO G B2 B2 B2 PZI 2201 TT 2202 F FT 2202 B2 3"-RWS-02110-A1AW-CC 4"-RWS-22002-A1AW-CC B2 3"x2" 3"x2" 3/4" RTD B2 4" B2 HH H L B2 50 % MIN SLOPE 3/4"-Z-213A NOTE Z-213A TT 2201 A RTD NOTE B2 B2 XHS O 2202 A C UX 206/207 XV 2202 A FC XHS 2202 B 1" FC 1-1/2" NC B2 B2 B2 B2 B2 XZL O 2202 B C B2 1-1/2" S B2 FV 2201 B2 D 3/4" D 3/4" L PG 2203 NC D 16"-BDH-25002-V0JPS-NI NOTE XV 2203 NOTE 10 NC V0JPS D0JP B2 XZL O 2203 C B2 B2 UX 207 NOTE PG 2202 XHS 2203 B2 FLOOR 1"-PL-20005-D0JP-NI FC TSO 1" HH H 2" B2 B2 NOTE L TI 2201 B PT 2201 B NOTE 10 B2 1"-PL-20005-D0JP-NI 1"x3/4" 3/4" IA E L 4" B2 1" NOTE FO NC 1" SEAL PRESS P&ID 221 FT 2201 200 PROPYLENE FROM F-201A,B B2 EXT P-200 1"-PL-22002-D0JP-NI FIC 2201 UX 207 TAHH 2201 B EXT' 1-1/2" C HH H 2201 B B2 M UX 207 HH 2201 B RTD 2" PT 2201 A B2 TT 1" UX 206/207 2202 A C RUN B2 PI 4" B2 O XZL B2 MGL P200 PAHH 2201 B B2 XV 2202 B B2 D B2 B2 4"-RWS-22001-A1AW-CC V0JPS B1GRS D 3/4" CC 600 HP TO D-601 B2 DELETED DELETED 2"-BDH-25001-B1GRS-NI T001 P-204 HOLDS 45 ˚ B2 SP 1"-SLU-22001-V0JPS-CC TIC 2201 210 FROM Z-203A KS 204 HH B2 NOTE Z-213B US 001 UX 207 B2 50 % MIN SLOPE 3/4"-Z-213B L B2 3"-RWR-22001-A1AW-CC LO HH H PIC 2201 600 HP TO D-602,601 D 3/4" M C CSO 210 FROM Z-203B CC CC 1/2"-PL-22001-D0JP-CC E H TI 2206 2" RWR 021 R-200 FO D F B2 D NOTE RWS 021 3/4" 4" D RTD TV 2202 4" 3/4" B2 US 001 MGL P204 DOCUMENT CLASS: Z RUN 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 B1 01 REV 1"-BDH-22003-B1GRS-NI DATE B2 3/4"-BDL-22001-A1GR-NI D0JP 200 PROPYLENE FROM F-201A, B A1GR BDL 023 NOTE APPD DUNG QUAT POLYPROPYLENE PROJECT NC 1" CHKD VIETNAM OIL AND GAS GROUP (c/o DQR) PROJECT: B DRWN DESCRIPTION PETROVIETNAM FLUSHING PROPYLENE 1-1/2"-PL-20010-D0JP-NI 1-1/2"-PL-20010-D0JP-NI B DUNG QUAT REFINERY MANAGEMENT BOARD DQR 240 PROPYLENE TO FLUSHING LICENSOR: MITSUI CHEMICAL, INC HYUNDAI ENGINEERING CO., LTD DRAWN BY A DATE HEC CLASSIFICATION NO 10 PREPOLYMERIZATION-1/2 DATE 08.07.31 J.O.R A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J APPROVED BY TITLE: 08.07.31 S.Y.P CHECKED BY SCALE JOB NO - 07140 REV DRAWING NUMBER 07140-200-25-R220 11 B2 A1 841x594 SERVICE NAME INSERT AT THE LOWEST TRANSFER LOOP POINT AVOID POCKETS ON REACTOR JACKET VENT PIPES NI 1-1/2"-PL-23005-D0JP-HC B2 B2 B2 L RTD 6" US UX 001 R-201 205 B 200 TO FICA-2003 NOTE NC NC 2401 AB 205 B B2 14" 1" B2 3" B2 H TI 2401 A C HC 2404 B HZL D 3/4" NC 2" XZL O 2407 B C NOTE B2 FO HV 2404 B B2 D0JP V0JPS NOTE 15 NOTE 11 B2 2" 2" NOTE 15 B2 B2 B2 NOTE 2"-SLU-24002-V0JPS-NI 271 TO TIC-2713 B2 RUN P201 B2 US HC 001 2404 A FIC 2401 UX 208 IA DELETED 1"-PL-20004-D0JP-NI 1"-PL-20004-D0JP-NI 3/4" D PG 2401 B2 B2 B2 HZL O 2404 A C NOTE FC TSO 1" 3/4" D 3/4" B2 NOTE 14 SP-P004 1-1/2"-PL-24008-D0JP-HC SP-P005 1"-PL-24007-D0JP-H SP-P006 2"-SLU-24001-V0JPS-NI SP-P007 3"-SLU-24005-V0JPS-NI SP-P008 UTILITY STATION FOR HN SP-P009 1/2"-PL-24002-D0JP-NI F SP-P010 3"-SLU-24004-V0JPS-NI SP-P011 1/2"-PL-24003-D0JP-NI SP-P012 1/2"-PL-24004-D0JP-NI SP-P013 1/2"-PL-24005-D0JP-NI SP-P025 1-1/2"-PL-20010-D0JP-NI SP-P026 3"-SLU-24001-V0JPS-NI E B2 3/4" D 200 PROPYLENE FROM F-201B C 3/4"-BDL-24001-A1GR-NI B2 BDL 023 DOCUMENT CLASS: Z 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 B1 B2 4"-SLU-25005-V0JPS-NI B2 B2 2"-SLU-24001-V0JPS-NI 01 250 SLURRY FROM BELT CONNECTION REV DATE DRWN DESCRIPTION CHKD APPD VIETNAM OIL AND GAS GROUP (c/o DQR) 250 SLURRY TO BELT CONNECTION DUNG QUAT POLYPROPYLENE PROJECT PROJECT: 250 SLURRY TO D-301 PETROVIETNAM B DUNG QUAT REFINERY MANAGEMENT BOARD DQR 1-1/2"-PL-20010-D0JP-NI B2 2"-SLU-24001-V0JPS-NI FT 2401 FV 2401 3/4"-PL-24009-D0JP-NI A 3"-SLU-24001-V0JPS-NI SP-D023 P-201 MOTOR INSTRUMENTATION TO BE DEVELOPED WITH VENDOR INFORMATION B2 1/2" 1"x1/2" L 1/2"-PL-24006-D0JP-NI 2"-SLU-24002-V0JPS-NI SP-D022 B2 DELETED 2"-BDH-24005-B1GRS-NI 2"-SLU-24003-V0JPS-NI SP-D021 B2 H FLUSHING PROPYLENE V0JPS B1GRS 2"-SLU-24004-V0JPS-NI SP-D020 HOLDS MGL NOTE V0JPS B1GRS 1-1/2"-BDH-24001-B1GRS-NI SP-D019 D NOTE V0JPS B2 271 FROM P-205 SP-D018 B2 NC NC B2 2"x1" 271 TO E-208 1-1/2"-BDH-24004-B1GRS-NI UX 208/209/210 P-201 2" B2 NOTE NOTE 15 NOTE 15 2"x1" B2 NC NOTE 15 NOTE 1-1/2"-PL-20010-D0JP-NI NC 1" NC D0JP 1"-JW-24003-A1AW-NI PISTON VALVE HOLD NC B2 CSO V0JPS NOTE 6"-SLU-25005-V0JPS-NI CSO D0JP B2 3"-JW-24002-A1AW-NI B2 RTD FC UX 210 1/2"-PL-24004-D0JP-NI H TI 2409 XZL O 2407 A C 2"-SLU-24003-V0JPS-NI 1/2"-PL-24003-D0JP-NI B2 NC B2 NOTE 273 TO D-203 273 TO D-203 273 TO D-203 SERVICE LINE NO SP-D017 B2 M FO NC XHS O 2407 B C UX 210 XHS 2407 A C B2 O B2 NOTE NOTE 1"-JW-24001-A1AW-NI SEAL PRESS P&ID NO 242 HV 2404 A B2 EXT' XV 2407 A B2 NOTE 1"-PL-23006-D0JP-HC 220 PROPYLENE FROM F-201A/B V0JPS D0JP 1-1/2" B2 D 3/4" PY 2401 A 3" NOTE D0JP L NOTE 1/2" A1GR 230 PROPYLENE FROM D-202 D 3/4" DIC 2401 PT 2401 A TAHH 2402 B XV 2407 B O NC B2 NOTE 14 NC BDL 023 FC TSO B2 3" NC FC NC NOTE 15 1/2"-PL-24002-D0JP-NI S 3/16"-BDL-24002-A1GR-NI FC 1" TI 2402 B B2 FV 2402 1-1/2"-PL-24001-D0JP-NI H 3/4" 2404 B C NOTE IA FT 2402 B2 D0JP V0JPS NOTE 15 NC B2 US 001 NC 2"-SLU-24004-V0JPS-NI L O 2" D0JP XV 2401 B2 EXT' 2" 6" FC NOTE NOTE 3"-SLU-24005-V0JPS-NI US 231 DRIP RING PA2HH 2401 A UX 211 S H B2 H TI RTD 2402 A 1" NOTE 10 3/4" 1" B2 UX 311 PT 2401 B 1" NC V0JPS UX 208 B2 FIC 2402 1" SPECIAL ITEM NO B2 B2 NOTE 10 NC NOTE 15 3" B2 B2 B 3/4" NOTE 15 B2 300 FROM B2 FIC-3001 3/4" NC 1" B2 DESC PIC H 2401 A L 14"-JW-27101-A1AW-NI RTD TT 2402 B RTD 14" 2"-SLU-24001-V0JPS-NI TT 1" 2401 B RTD MAX SLOPE KS 211 KS 205 A 15 PIPING SPECIAL ITEMS 3" NOTE 15 14" H PI 2401 B L NOTE 12, 15 XZL 2401 B2 B2 G 14 MIN DISTANCE BETWEEN BLOCK VALVE AND GLOBE VALVE SHALL BE 1000 mm UX 210 1" B2 MEPR(MELTING ELECTRO PNEUMATIC RELAY) SHALL BE INSTALLED ON XV-2407A,B,C B2 INLET FROM TOP 12 UTILITY CONNECTION IS TO BE PROVIDED (HN) 3/4" 14" 250 HP FROM SV-2501A~C 11 SEE P&ID NO 243 FOR MORE DETAIL NOTE 14" 1"-HN-02407-D1AP-NI B2 DT 2401 C 1/2"-PL-24005-D0JP-NI TIC H 2401 B L C O CAMFLEX VALVES SHALL BE INSTALLED WITH THE BALL LOCATED UPWARD 13 SKIN TEMPERATURE B2 NUC B2 (DENSITY) B2 14" 14" B2 XHS PZI HC 3/4" 1" NOTE 10 NOTE 10 2401 US 001 B1GRS V0JPS 2401 AA B2 16"-BDH-25002-B1GRS-NI H B2 FULL BORE BALL VALVE NOTE 15 NOTE 15 B2 DELETED 10 SEE P&ID NO 241 FOR MORE DETAIL C B2 14" O NC FC 1-1/2" XV 2405 A D0JP V0JPS E 6"-SLU-20003-V0JPS-NI NC 250 PROPYLENE TO R-202 TOP PA3HH 2401 A UX 207 O 3/4" 3" TI RTD 2404 A L LOCATE THESE VALVES FAR ENOUGH FROM REACTOR BTM TO PERMIT COMPLETE DISASSEMBLING OF PIPING IN SPOOL PIECES AND ELBOWS AREAS FOR EASIER REACTOR MAINTENANCE 250 HP FROM R-202 TOP 14"-JW-24004-A1AW-NI B2 HN 024 NC 1-1/2" FC B2 HC B2 B2 B2 B2 B2 XHS 2406 B2 1" B2 B2 NOTE 13 V0JPS D0JP B2 XZL 2406 3/4" PV 2401 AA B2 XV 2406 1-1/2" FC PV 2401 AB B2 US 001 MAX SLOPE 220 FROM R-200 6" 1-1/2" B2 B2 1-1/2" SP 8"x6" NOTE 15 F FC V0JPS B1GRS B2 V0JPS B1GRS XV 2405 B FC NC US 001 B2 NOTE HOLD PSV 2401 B 51.0 B2 KS 205 A B2 B2 2405 B C NOTE 15 D0JP V0JPS B2 KS 2405 A C B2 O XZL B2 O XZL 51.0 B2 XHS O 2405 B C PZI B2 PSV 2401 A 8"x6" TRIM SPEC : V0JPS-HC Z-214 B2 1"-PL-24008-D0JP-HC V0JPS B1GRS SP NOTE B2 8"-BDH-24003-B1GRS-NI 1"-PL-24007-D0JP-H TI 2404 B XHS O B2 2405 A C 8"-BDH-24002-B1GRS-NI B2 NOTE 13 2"-BDH-25001-B1GRS-NI B2 NOTE 1-1/2"-BDH-24001-B1GRS-NI B2 1-1/2"-BDH-24004-B1GRS-NI 16"-BDH-25002-B1GRS-NI G 230 SLURRY FROM F-201A/B B2 2"-BDH-25001-B1GRS-NI NOTE B2 220 HP TO D-601 C NOTES AS SHORT AS POSSIBLE 7000.00 16.0 B2 220 HP TO D-601/602 11 R-201 PUMP CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE / 55.00 -45 / 150 HC 10 P-201 ITEM NO 609.6 x 31500.0 40.00 1-1/2"-PL-23005-D0JP-HC 230 PROPYLENE FROM D-202 D SERVICE NAME 1ST LOOP REACTOR SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P (kg/cm2g) D.T (˚ C) INSUL TYPE H R-201 ITEM NO Z-214 R-200 DISCHARGE PIPE SERVICE NAME D0JP A1GR 07140-200-25-R240 DWG NO ITEM NO LICENSOR: 250 PROPYLENE TO R-202 MITSUI CHEMICAL, INC 600 HP TO D-601 HYUNDAI ENGINEERING CO., LTD 243 PROPYLENE TO Z-205A 10 DRAWN BY DATE S.Y.P 08.07.31 CHECKED BY DATE K.S.J 08.07.31 APPROVED BY DATE J.O.R 08.07.31 TITLE: A PIPING & INSTRUMENT DIAGRAM 1ST BULK POLYMERIZATION 1/4 HEC CLASSIFICATION NO SCALE JOB NO DRAWING NUMBER - - 07140 07140-200-25-R240 11 REV B2 A1 841x594 P-202 07140-200-25-R250 DWG NO CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE NI 8"-BDH-25005-B1GRS-NI 240 HP TO D-601, 602 1-1/2"-BDH-25003-B1GRS-NI B2 NOTE 14 TI 2504 A L RTD 1-1/2"x1" 1-1/2"-PL-23005-D0JP-HC LOCATE THESE VALVES FAR ENOUGH FROM REACTOR BTM TO PERMIT COMPLETE DISASSEMBLING OF PIPING IN SPOOL PIECES AND ELBOWS AREAS FOR EASIER REACTOR MAINTENANCE NC 2" NC NOTE 16 NC B2 FC B2 US 001 KS 207 A B2 DIC 2501 XPI 2501 A PV 2501 B 6" B2 8"x6" SP B1GRS V0JPS NOTE B2 FLASH PIPE SHALL HAVE LESS BENDS AS POSSIBLE PROVIDE FLANGED COUPLINGS EVERY 6m MAX SPRING LOADED CHECK VALVE WITH ΔP OF 5kg/cm2 10 INLET FROM TOP 11 SEE P&ID NO 251 FOR MORE DETAIL B2 KS 207 B B2 XZL O 2505 B C PSV 2501 B 51.0 B2 B2 B2 B2 R-202 6" FC B2 NC PV 2501 B B2 13 UTILITY CONNECTION IS TO BE PROVIDED (HN) B2 US 001 US 001 B2 PA3HH 2501B PA2HH 2501 B UX 214 UX 215 14 SKIN TEMPERATURE 15 MIN DISTANCE BETWEEN BLOCK VALVE AND GLOBE VALVE SHALL BE 1000 mm B2 HC 16 PIPING SPECIAL ITEMS B2 NOTE 16 1-1/2" PIC H 2501 B L KS 207 B DESC NOTE 3/4" 1" PG 2502 B2 HOLD UX 212/213/214 B2 MGL P-202 B2 HZL RUN O 2503 A C P202 NC 1"x1/2" B2 1"-PL-23011-D0JP-NI D 3/4" 1" D 3/4" 1" B2 B2 B2 D0JP A1GR FE 2501 FC TSO 3/4" B2 3/4"-BDL-25001-A1GR-NI NOTE 15 B2 D 3/4" HC US 2503 A 231 BDL 023 3" B2 2" 3" NOTE 16 NC FO NC NOTE FCNOTE 16 NC B2 UX 212 UX 214 XZL 2507 A C XHS O 2507 A C B2 2507 B C V0JPS B1GRS FO NC 2" B2 B2 2"-SLU-24001-V0JPS-HC US 231 1"-HN-02408-D1AP-NI 4" B2 1" 3" XV 2508 B B2 FC LV 2301 UX 212 XZL O 2508 B C B2 XHS O 2508 B C UX 214 B2 XHS O 2507 B C 3"-SLU-25004-V0JPS-HC SP-P018 1/2"-PL-25003-D0JP-NI SP-P019 1/2"-PL-25002-D0JP-NI SP-P020 UTILITY STATION FOR HN SP-P021 1/2"-PL-25001-D0JP-NI SP-P022 1/2"-LA-15015-V0JPS-ET E LZI 2301 D B2 HOLDS B2 DELETED DELETED 2" EXT' P-202 MOTOR INSTRUMENTATION TO BE DEVELOPED WITH VENDOR INFORMATION PG 2501 B B2 V0JPS B1GRS C DOCUMENT CLASS: Z 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 B1 01 REV D0JP V0JPS NOTE DATE 600 SLURRY TO D-601 CHKD APPD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: NOTE 16 NOTE 3"-SLU-25001-V0JPS-NI DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) 300 SLURRY TO D-301 PETROVIETNAM B DUNG QUAT REFINERY MANAGEMENT BOARD DQR LICENSOR: FIC 2502 D 3/4" S H L HYUNDAI ENGINEERING CO., LTD IA 2502 FV DRAWN BY CM APPROVED BY DATE HEC CLASSIFICATION NO 10 A PIPING & INSTRUMENT DIAGRAM 2ND BULK POLYMERIZATION-1/3 08.07.31 J.O.R 1/2" TITLE: DATE 08.07.31 K.S.J B2 DATE 08.07.31 S.Y.P CHECKED BY FC D 3/4" 1/2" B2 1/2"-PL-25004-D0JP-NI SP-P017 MITSUI CHEMICAL, INC FT 2502 1"-PL-25005-D0JP-HC SP-P016 B2 1-1/2"-PL-20010-D0JP-NI FLUSHING PROPYLENE 1/2"-LA-15015-D0JP-ET 1"-PL-23005-D0JP-HC SP-P015 B2 2"-SLU-25002-B1GRS-NI NOTE B2 NC 231 LN 024 NOTE 10 NOTE 211 UX 212 1-1/2"-BDH-25006-B1GRS-NI SP-P014 IA 3"x2" US NC B2 SP-D030 F NOTE NC NOTE 16 FC NC B2 KS 3"-SLU-25001-V0JPS-NI S B2 NOTE 16 NOTE B 2"-SLU-25002-V0JPS-HC SP-D029 272 FROM P-206 B2 NOTE 1/2"-PL-25004-D0JP-NI 1/2"-PL-25003-D0JP-NI 6"-SLU-250005-V0JPS-NI 3"-SLU-25004-V0JPS-HC O 2"-SLU-25002-V0JPS-NI SP-D028 272 TO E-209 272 TO TIC-2723 UX 212 EXT' NC 2" 1" NC B2 B2 IA 230 FROM LIC-2301 NOTE XZL TIC 2501 B L NOTE 13,16 3" B2 O S B2 B2 B2 V0JPS D0JP 14"-JW-27201-A1AW-NI B2 XV 2507 B NOTE 16 TT RTD 2501 B D0JP B2 B2 NOTE NOTE XV 2507 A B2 EXT' 2" B2 14"-JW-25003- -NI 1/2"-PL-25001-D0JP-NI FV 2501 M 6" 3"-SLU-25004-V0JPS-HC SP-D027 PISTON VALVE 273 TO D-203 NOTE S FT B2 RTD 2501 A 3"-JW-25001- -NI HH H NC IA HV 3" 2503 A 3/4" NOTE L L NOTE PT 2501 B NC 2501 UX 212 2501 A 2509 3/4" TAHH 2502B PT 2"-SLU-25003-V0JPS-HC H H CSO NOTE H 3/4"-PL-901533-D0JP-NI FIC PI 1" 1" TI 2502 B UX 215 NOTE 16 SEAL PRESS P&ID 252 MAX SLOPE TI 2501 150 LIQUID ADDITIVE FROM P-111A, B NOTE 11 NOTE 16 V0JPS D0JP 4"-SLU-23001-V0JPS-NI B2 240 PROPYLENE FROM F-201A, B RTD NOTE 4" D 240 SLURRY FROM R-201 1" 3/4" 4"-SLU-25005-V0JPS-NI 230 SLURRY FROM D-202 240 SLURRY FROM BELT CONNECTION 3/4" 1" NOTE 11 V0JPS TI 2502 A RTD SP-D026 273 TO D-203 14" NOTE 16 E NOTE 11 B2 TT RTD 2502 B 1-1/2"-BDH-25003-B1GRS-NI 2501 B H B2 B2 3"-SLU-25001-V0JPS-NI NOTE 11 D 1-1/2" H 230 PROPYLENE FROM F-201A, B H TI 2501 A B2 14" B2 14" V0JPS D0JP 14" 1"-JW-25002- -NI RTD 1/2"-PL-25002-D0JP-NI B2 HC TI 2503 HC HC SERVICE LINE NO SP-D025 273 TO D-203 PY 3" 3" 1"-JW-25004- -NI NOTE D 1" 14" 1" 14" 3" 3" 240 SLURRY TO BELT CONNECTION 1-1/2" 14" 3" D NOTE 16 3/4" D 2"-SLU-25002-V0JPS-HC 3/4" CSO NOTE 14" SPECIAL ITEM NO DRIP RING F 1" G 12 REQUIRED ELECTRICAL TRACING TEMPERATURE : 50 ℃ B2 NOTE 16 NOTE 10 NC FC 1-1/2" XV 2505 B NC B2 H MEPR(MELTING ELECTRO PNEUMATIC RELAY) SHALL BE INSTALLED ON XV-2507A,B,C B2 CAMFLEX VALVES SHALL BE INSTALLED WITH THE BALL B2 LOCATED UPWARD 1-1/2"-BDH-25006-B1GRS-NI B2 DT 2501 L SP 1-1/2" B2 B2 NOTE 14 TI RTD 2504 B L B2 FULL BORE BALL VALVE XHS 2505 B B2 NC NUC B2 (DENSITY) H V0JPS B1GRS 8"x6" XV 2505 A 1-1/2" FC B2 51.0 DELETED 2" B2 PSV 2501 A B2 XZL O 2505 A C B2 B2 D0JP NC NOTE 16 B1GRS NOTE 10 1"-PL-23005-D0JP-HC 1"-PL-25005-D0JP-HC A AVOID POCKETS ON REACTOR JACKET VENT PIPES NOTE B2 KS 207 A B2 US 001 230 FIC-2301 C AS SHORT AS POSSIBLE 16"-BDH-25002-B1GRS-NI XHS O B2 2505 A C 11 NOTES SIZE DIA x LENGTH (mm) 609.6 (O.D) x 31500.0 40.00 CAPACITY (m3) D.P (kg/cm2g) / 55.00 D.T (˚ C) -45 / 150 INSUL TYPE HC 7000.00 16.0 10 2ND LOOP REACTOR 2"-BDH-25001-B1GRS-NI 240 HP TO D-601 G R-202 SERVICE NAME 8"-BDH-25004-V0JPS-NI 240 PROPYLENE FROM D-202 ITEM NO R-202 PUMP D0JP B1GRS B2 ITEM NO SERVICE NAME H SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-200-25-R250 11 B2 A1 841x594 E-303 DWG NO 07140-300-25-R320 B2 ITEM NO B2 T-301 ITEM NO SERVICE NAME T-301 REBOILER TYPE HEAT DUTY (kW) CALANDRIA 348.7 TUBE / 25.0 -45 / 120 / 25.0 -45 / 120 / 25.00 -45 / 120 E-301 60.00 95.0 B2 D.P (kg/cm2g) D.T (˚ C) INSUL TYPE HC / 25.0 -45 / 120 / 20.0 -45 / 120 B2 NOTES AS SHORT AS POSSIBLE BEM, HOR 93.3 SHELL D.P (kg/cm2g) D.T (˚ C) INSUL TYPE NI 11 E-308 TYPE HEAT DUTY (kW) B2 TUBE SHELL 10 T-301 VENT CONDENSER SERVICE NAME BES, HOR 2106.3 TYPE HEAT DUTY (kW) B2 NI ITEM NO PROPYLENE CONDENSER SERVICE NAME B2 HC ITEM NO T-301 REFLUX PUMPS CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE / 18.00 / 52 P-302A /B SERVICE NAME 1200.0 x 14300.0 16.8000 SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE ITEM NO RECYCLE PROPYLENE SCRUBBER SERVICE NAME B2 SHELL D.P (kg/cm2g) D.T (˚ C) INSUL TYPE INSTALL ON HORIZONTAL PIPE / 20.0 -45 / 120 / 25.0 -45 / 120 INLET/OUTLET FROM TOP B2 TUBE MIN 1" PIPE JACKET LENGTH 10m MIN 1/2" PIPE JACKET LENGTH 10m MIN 2" PIPE JACKET LENGTH 10m B2 CC H 1/2"-PL-32013-B1GR-NI US 236 B2 PV 3201 B2 B2 PG 3203 8"-PL-30001-B1GR-PP B1AP B1GR NOTE B2 S101 8" NOTE 24" TI H 3205 B2 B2 NC S B2 501 PROCESS WATER FROM P-501A/B FV 3208 B2 4"-PRW-50111-A1AP-HC MIN D 3/4" 4"x2" FC 4"x2" A1AP 3" B2 B2 V 3/4" V NC 3/4" P023 D D NOTE FZI 3205 1" 1-1/2" 1" SP D032 D031 4"x2" FO 4"x2" D 3/4" B2 B2 B2 3" 4"-RWR-32001-A1AW-CC RWS 021 FT 3207 LG 3202 3/4 D B2 3/4"-CWR-32002-A1AW-NI ATM TO SAFE LOCATION 2" D 3/4" 10"-CWR-32001A1AW-NI FV 3207 CWR 021 10"x8" FO 10"x8" D B2 3/4" 8" A1AW LT 3202 LI 3202 A1AW D H B2 L RTD TI 3208 H HOLDS BDL 023 H B1GR A1GR RTD DELETED B1GR A1GR B2 D 3/4" 1"-BDL-32007-A1GR-NI BDL 023 10"-CWS-02130-A1AW-NI CWS 021 DOCUMENT CLASS: Z B2 B1 01 REV NC 1"-BDL-32006-B1GR-NI B2 3/4" 3/4" D 1/2" PG 3202 A B2 NC SP P-302A T004 PG 3202 B B2 D D 1/2" 3/4" NOTE D DATE BDL 023 US 233 1/2" NC S B2 M B2 KS 221 B2 B2 DUNG QUAT POLYPROPYLENE PROJECT PROJECT: NC B2 SP PETROVIETNAM T005 3/4" D B DUNG QUAT REFINERY MANAGEMENT BOARD DQR A1GR B1GR MGL 3302 A R S MITSUI CHEMICAL, INC A1GR US 236 D 1"-BDL-32005-A1GR-NI KS 221 3/4" BDL 023 B1GR B2 M MGL R 3302 B HYUNDAI ENGINEERING CO., LTD B2 S US 236 SEAL PRESS P&ID 360 DRAWN BY DATE S.Y.P 08.07.31 CHECKED BY DATE K.S.J 08.07.31 APPROVED BY 10 A PIPING & INSTRUMENT DIAGRAM PROPYLENE SCRUBBING DATE HEC CLASSIFICATION NO TITLE: 08.07.31 J.O.R APPD VIETNAM OIL AND GAS GROUP (c/o DQR) 1/2" NC B2 SEAL PRESS P&ID 360 NOTE CHKD LICENSOR: IA DRWN DESCRIPTION B2 P-302B 3/4" 1"-BDL-32009-B1GR-NI B2 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 1"-BDL-32006-B1GR-NI B2 C 2"-PL-32029-B1GR-NI 8"-PL-32003-B1GR-NI 4"-PL-32004-B1GR-NI B2 DELETED B2 BDL 023 NC 1/2"-PL-32009-B1GR-NI RWR 021 B2 A 1/2"-LA-15016-DOJP-ET B2 NOTE S101 12" 8" TI 3204 NOTE NC FV 3205 PSV 3202 3" B2 2" 2" SC 32 B1GR A1GR 1"-SLU-32001-B0JPS-NI SP H RTD 2" D 3/4" B2 F B2 12" B1GR A1GR NOTE 1-1/2" B2 CL 022 150 LIQUID ADDITIVE FROM P-111A/B L 1"-BDL-32002-A1GR-NI B2 B1GR H NC SP B2 T LIC 3201 B2 SP 4" V B TI 3207 E-301 E-303 FC FT 3208 LT 3201 1"-BDL-32003-A1GR-NI DOJP B1GR B2 2" 3/4" IA 2" 60˚ 4" NC US 236 3/4" L 3/4"-CL-32001-A1AS-PP H 4"-PRW-50111-B1GR-HC FIC 3208 A1AP B1GR 4"-PRW-32001-A1AP-PP 501 PROCESS WATER TO T-501 B2 2" LG 3201 2" 3/4" 4"-PRW-32001-B1GR-HC US 001 B2 (ST) TRIM SPEC : B1GR12" 4" #1 2"-SL-32005-A1AS-HS 1"-SLU-32001-B0JPS-SJ MIN 3/4" B2 4"-RWS-02111-A1AW-CC B2 V FV 3209 B2 3/4"-RWR-32002B1AW-NI D 3/4" NOTE V 3/4" 60˚ 1-1/2" C 4" 3207 BDL 023 3" B2 RTD CL 022 3" D 3/4" B2 E B2 T B2 NC 4" 3/4 D 8.0 FIC 4" M.H NC 3/4" SP B2 B2 3" TRIM SPEC : B1GR-HC B2 3/4"-CL-32002-A1AS-PP NOTE D A1GR A1GR 3"x2" E-308 D 3/4" 3/4" T-301 3/4" V B1GR A1GR RTD 8"x6" 1-1/2"-PL-32011-B1GR-NI D 3/4" CC 4" B2 NC 300 PROPYLENE FROM D-301 HC NC NOTE 3202 6"-PL-30001-B1AP-PP HG M ET PR PL N ATM TO SAFE LOCATION RTD RTD V 3/4" 2" NC H TI 3"-PL-35007-B1AP-H 3"-SL-32004-A1AS-HS 1/2"-PL-32008-BOJPS-ST 350 PROPYLENE FROM PK-301 1-1/2"x1" B2 2"x1-1/2" NC B2 1-1/2"-SLU-32001-B0JPS-SJ B2 B2 NC NC Y036 2"x1-1/2" FC TSO D 3/4" V 3/4" FT 3209 B1GR A1GR CL 022 #23 FO 3203 2"-PL-32012-B1GR-NI 2"x1-1/2" AI 3201 TI 3209 PSV 3203 MIN M S101 FG 3205 B 3"x2" 3" FT 3201 NOTE H TI B2 US FIC 3206 4"-PL-32017-B1GR-NI B2 3/4" SP FG 3205 A 10" FV 3201 B2 3/4"-CL-32003-A1AS-PP T SP B2 24" M.H L B2 G 2" B2 3209 NO POCKET BDL 023 001 2"-PL-32019-B1GR-ST 1/2" NOTE H FIC 3201 3/4"-BDL-32010-A1GR-NI B1GR BOJPS 3/4" 4" B2 2"-SLU-32001-B0JPS-SJ 3"-SL-32003-A1AS-HS US 001 B2 AT 3001 NO POCKET 10"-PL-32001-B1GR-NI NOTE PP HC B2 B2 EXT' 2" B2 EXT' 2" PDT 1/2" 3203 PGC INST H2 CH4 C2H4 C2H6 C3H6 C3H8 N2 8"-PL-32002-B1GR-NI PT 3204 RTD PDI H 3203 (ST) TT 3201 3204 2"x1" FC 2"x1" TSO B2 1/2" 3201 L FT 3205 (ST) (ST) PT 3201 SEE 501 TI H 3203 L RTD PG 3201 NOTE A1GR B1GR PI B2 NO POCKET TIC L 2"-SL-32002-A1AS-HS 2"-SLU-32001-B0JPS-PP H 2"-SL-32001-A1AS-HS FIC 3205 PT 3203 PIC 3201 L 4"-PL-32014-B1GR-NI PIC H 3203 L D 3/4" B1AW A1AW 3/4" 3/4"-PL-32021-B1GR-NI (ST) PCV 3205 AE 3201 B2 2"-BDL-32008-A1GR-NI 2"-PL-32019-B1GR-ST NO POCKET H US 001 B2 6"x2" D 3/4" FV 3204 B1AW A1AW B2 B2 2"-SL-02217-A1AS-HS 1/2"-PL-32008-B1GR-ST 2" LO PSV 1/2 F 25.0 3201 FT 3204 L LO BDL 023 2"x1" FC 2"x1" 3/4" V B2 310 SLURRY TO F-301 D 1/2" V 2"-SL-02217-A1AS-HS FI H 3202 L B2 FIC 3204 (ST) 6"-BDL-32001-A1GR-NI H US 001 NC PV 3203 A1GR B1GR 3206 PG 3204 LO 4"x1-1/2" FT B2 B1AW A1AW NOTE D 3/4" 3" FOR SAMPLING DETAILS SEE P&ID NO 07140-000-25-R006 A1GR B2 B2 B1GR 3202 BDL 023 LO FT L NC MIN DISTANCE BETWEEN BLOCK VALVE AND GLOBE VALVE SHALL BE 1000 mm 330 PROPYLENE TO D-302 3/4"-BDL-32009-A1GR-NI D 3/4" NC FIC 3206 4"x3" FC 4"x3" TSO B2 D 3/4" H HOLE Φ13mm AT LOW POINT 750 PROPYLENE TO T-720A/B B2 B1GR A1GR NO POCKET 1"-PL-32007-B1GR-ST G E 4"-PL-32006-B1GR-NI 4"-PL-32005-B1GR-NI 310 PROPYLENE TO D-303 F NC IA NOTE SL 022 UTILITY CONNECTION IS TO BE PROVIDED (HN) S 2"-PL-32016-B1GR-ST 300 PROPYLENE TO D-301 OUTLET H REQUIRED : ELECTRICAL TRACING TEMPERATURE : 50℃ 12"x10" 300 PROPYLENE TO FT-3001 SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-300-25-R320 11 B2 A1 841x594 DWG NO 07140-300-25-R330 B2 SHELL D.P (kg/cm2g) D.T (˚ C) INSUL TYPE H FV / 25.0 -45 / 120 / 20.0 -45 / 180 / 25.00 -45 / 120 BEM, HOR 136.6 B2 SHELL TUBE TYPE B2 HEAT DUTY (kW) / 18.00 40 / 60 B2 HC HC D.P (kg/cm2g) D.T (˚ C) INSUL TYPE 10 11 NOTES P-301A/B ITEM NO SERVICE NAME P-301A,B COOLER SERVICE NAME 3200.0 x 7400.0 68.00 E-305 ITEM NO PROPYLENE FEED DRUM SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE BKU, HOR 407.7 B2 TUBE TYPE HEAT DUTY (kW) D-302 SERVICE NAME PROYLENE VAPORIZER SERVICE NAME ITEM NO E-302 ITEM NO B2 4m MIN ABOVE GRADE TO BE FINALIZED DURING DETAIL ENGINEERING PROPYLENE FEED PUMP CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE 90.00 700.0 OUTLET FROM TOP NI INLET FROM BOTTOM / 43.0 / 120 / 55.0 -45 / 120 1m MAX ABOVE GRADE NI MIN DISTANCE BETWEEN BLOCK VALVE AND GLOBE VALVE SHALL BE 1000 mm H UTILITY CONNECTION IS TO BE PROVIDED (HN, LN) B2 HOLE Φ13mm AT LOW POINT 1"-PL-33020-B1GR-NI 1-1/2"-PL-33004-B1GR-ST 1"-CWR-33003-A11F-NI B2 LO 1/2" V 24" A1GR B1GR 1/2" V B2 4"-BDL-33010-A1GR-NI PSV 1/2 F 3302 B 25.0 B2 3"-PL-33002-B1GR-HC HH HH H PI 3304 PT 4"-SL-02218-A1AS-HS 3304 2"-PL-33003-B1GR-NI 1" 6" TRIM SPEC : B1GR-HC FC TSO NOTE 1"-BDL-33011A1GR-NI B2 3303 400 mm B2 B2 B2 B2 XHS O 3301 C US 237 XZL 3301 B2 O C PT PIC 3303 3303 B1GR KS 222 MGL RUN P301 A US NOTE S SP B2 B2 T006 3/4" B2 LO D1GR A1AW B2 SEE 501 PI 3302 L D B2 3/4" 3/4" HOLDS 2"x1-1/2" FC TSO D 3/4" B2 TO BE CONFIRMED BY ANALYZER VENDOR INFORMATION B2 NC 6"-PL-33012-D1GR-NI NOTE D 3/4" RUN US 237 M KS 222 MGL P301 B C US 237 M T006 SC 35 D 3/4" SEAL PRESS P&ID 360 B2 B2 DOCUMENT CLASS: Z BY VENDOR NOTE 1"x3/4" D 3/4" 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 B1 01 REV DATE 1"-BDL-33009-A1GR-NI PETROVIETNAM B2 DUNG QUAT REFINERY MANAGEMENT BOARD MITSUI CHEMICAL, INC SEAL PRESS P&ID 360 HYUNDAI ENGINEERING CO., LTD B2 B2 DRAWN BY DATE APPROVED BY 10 REACTORS FEED DRUM DATE 08.07.31 A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J TITLE: 08.07.31 S.Y.P CHECKED BY B LICENSOR: NOTE D 3/4" APPD DQR HEC CLASSIFICATION NO CHKD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: BDL 023 J.O.R DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) 1"-BDL-33009-B1GR-NI 3/4"-BDL-33009-B1GR-NI NOTE 1"-BDL-33001-B1GR-NI P-301B D B2 P-301A 2" B2 PG 3302 B SP D 3/4" B2 3/4"-BDL-33002-B1GR-NI DELETED NC 8"-PL-33010-B1GR-NI NC NC AT C3H6 3302 B C3H8 C4H8 A1GR B1GR 1"-BDL-33001-A1GR-NI 1" NC PGC B2 PT 3302 A1GR D 2"x1-1/2" 2"-PL-33001-B1GR-NI BDL 023 TI 3304 RTD FT 3301 NOTE B2 D1GR L B2 HOLD 1/2" (ST) INST B2 8"-PL-33008-B1GR-NI PV 3303 CL 022 B2 H AE 3301 E B2 H2 B2 Y080 1-1/2"-CL-33001-A1AS-PP FIC 3301 D NC IA B1GR A1AS 3/4" PG 3302 A 3"x2" B2 US 001 D 1-1/2"-PL-33013-D1GR-NI 1-1/2"-CL-33001-B1GR-PP B2 3/4" NC 238 B2 B2 4" 3305 PCV 6"x4" D B2 DELETED E-302 T 3/4" 4"x3" FC 4"x3" TSO PR PL BN 1/2"-BDL-33008-D1GR-NI PG 3303 SP H AI 3301 B2 BDL 023 3" D 6"-PL-33011-D1GR-NI BDL 023 B2 6"x4" D1GR A1GR BDL 023 B2 NOTE FV 3301 B1GR A1GR 1-1/2"-BDL-33007-A1GR-NI 4" 1-1/2" A XV 3301 HC 4" S010 3301 4"x3" 4"-SL-02218-B1GR-HS SP B2 NOTE A1GR TI 1" D 3/4" B1GR LG RTD 1-1/2" SC 37 B2 B2 2" D-302 2"-PL-33001-B1GR-NI US A1AS 3" CWS 021 B2 B2 SC 34 D LC 238 D 3/4" 1" PSV 1/2 F 3302 A 25.0 3/4" LO 2"-PL-33017B1GR-NI 1/2" V A1GR B1GR 3/4" 1-1/2" 4" 6"-PL-75008-B1GR-NI B B2 HC 24" B2 B2 3/4" D SL 022 M.H 2" NC 4"-BDL-33012A1GR-NI C M.H LV 3301 B2 1-1/2" D1GR B1GR NOTE (ST) B2 LO D 3/4" B2 LT 3301 F 3" PG 3301 FC D B2 6" PT 3301 B2 8" 1-1/2"-PL-33006-B1GR-HC 751 PROPYLENE FROM T-721A/B BDL 023 4" 3" 3" 750 PROPYLENE TO T-702A,B TOP B2 3"x2" NC 1-1/2"-PL-33005-B1GR-HC 230 PROPYLENE TO D-202 TOP B2 LIC 3301 L 6" 3"-CWS-02107-A1AW-NI 3/4"-BDL-33013-D1GR-NI E 2" H NOTE 3/4" D 3/4"-PL-33011-A1GR-NI B2 NC B2 US 001 D 3/4" 1/2"-BDL-33006-A1GR-NI 3302 HG PR PL BN RTD L 3" E-305 6"-PL-33016-D1GR-NI LO CWR 021 3"-CWR-33001-A1AW-NI 1/2"-BDL-33012-A1GR-NI C3H6 B2 3302 A C3H8 C4H8 8"-BDL-33003-A1GR-NI TI 3302 V D1GR A1AW BDL 023 H PI 3301 A1GR B1GR 6" NOTE B2 NOTE D ATM 3/4" 3/4"-CWR-33002A1AW-NI D1GR A1GR B2 H2 PSV 3301 V 3/4" 6"-PL-33015-D1GR-NI NOTE B2 AT AI 3J4 25.0 B2 1-1/2"-PL-33013-D1GR-NI NOTE 3302 PGC 2"-PL-33002-B1GR-HC SC 36 B2 AE F 2"-HN-02401-D1AP-NI HOLD PSV 3303 3/4" NC B2 6"x4" B2 3306 PCV 1/2" 3/4 D 9.2 B2 HN 024 4"-PL-32005-B1GR-NI INST (ST) 320 PROPYLENE FROM P-302A/B B2 G B1GR A1GR G FOR PGC ROOM DETAIL, SEE P&ID NO 07140-500-25-R-501 520 PROPYLENE TO PK-502 6"-PL-33011-D1GR-NI 200 PROPYLENE TO F-201A,B FOR SAMPLING DETAILS SEE P&ID NO 07140-000-25-R006 350 PROPYLENE TO C-301 SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-300-25-R330 11 B2 A1 841x594 P-304 07140-300-25-R340 DWG NO B2 ITEM NO SERVICE NAME E-304 ITEM NO SERVICE NAME 20.00 20.0 TYPE HEAT DUTY (kW) HC B2 D.P (kg/cm2g) D.T (˚ C) INSUL TYPE H T-302 P-303 ITEM NO SERVICE NAME 1000.0 x 8500.0 SIZE DIA x LENGTH (mm) CAPACITY D.P (kg/cm2g) D.T (˚ C) INSUL TYPE / 8.0 / 120 / 5.0 / 120 LOW PRESSURE PROPYLENE SCRUBBER SERVICE NAME BES, VERT 57.6 B2 TUBE SHELL ITEM NO RECYCLE GAS COOLER T-302 REFLUX PUMP CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE HC 3" 3"-CWS-02112-A1AW-NI 3/4" B2 3/4" 3" BDL 023 NO POCKET 12"-PL-34001-A1AP-NI D G 1/2" V B2 LO 3"-BDL-34002-A1APS-NI A1APS A1AP D TG 3402 TRIM SPEC : A1AP- ST 11 TI H 3401 PP 12" 2"-BDL-34002-A1AP-NI F B2 1" NO POCKET D-304 1" B2 B2 300# B2 B2 NC B2 LG 2" 2"x1-1/2" LI H 3401 L (ST) LT 3401 B2 B2 3403 D B2 E 3/4" (ST) LG 3401 3" B2 3" NC M.H 1" SC 36 D B2 3/4" B2 B2 300# 1"-LA-15006-A1AP-ET NOTE HC ET B2 1-1/2"-WO-34001-A1AP-NI 6" 1-1/2" NC 1-1/2"-O-35005-B1AP-NI HOLD TG 3401 5.0 B2 150 LIQUID ADDITIVE FROM P-110 D 650 WASTE OIL TO D-609 HOLDS B2 PSV SIZE TO BE FINALIZED BY PUMP VENDOR 350 WASTE OIL FROM PK-301 W/E B2 B2 SP T008 (ST) HC 6"-O-34005-A1AP-ST HC Y037 B2 1-1/2"-O-34001-A1AP-NI C 3/4" D M B2 US 001 MGL P304 RUN 1-1/2"-O-34003-A1AP-ST C PSV 3403 PG 3404 SP P-304 A1AP B1AP 2m MIN NC PG 3402 132 OIL FROM P-115 NC 2" NOTE 1"-O-13205-A1AP-PP PP HC D HC HH H 1-1/2" 1" 1-1/2"-O-34002-A1AP-HC 2" B2 B2 FT 3401 B2 B2 B2 B2 E 1" LI UX 239 300# 300# B2 3" 3403 HH 3" 3402 12" B2 LT NC 3/4" A1AP A1APS NOTE 1" FI 3401 L TRIM SPEC : A1AP-NI 3" 12" B2 PG 3401 NC 12"-PL-31008-A1AP-PP 350 PROPYLENE TO PK-301 B2 T-302 3" 3"-O-34006-A1AP-ST D 3/4" LO LO 1" 1" 2"-PL-34003-A1AP-PP 310 PROPYLENE FROM F-302A/B 12"-PL-34002-A1AP-NI NO POCKET NC RTD B2 3403 3/4" 1" 3"-BDL-34001-A1APS-NI V 1/2" LO PG B2 D E-304 BDL 023 1/2 F PSV 5.0 3401 350 PROPYLENE GAS FROM C-301 1/2 F PSV 5.0 3402 B2 V 12" F 3/4" D 3/4" D P-303 DOCUMENT CLASS: Z M US 001 B2 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 MGL P303 B1 RUN 01 REV SEAL PRESS P&ID 361 SL 022 DATE 1"-SL-02225-A1AS-HS 1-1/2"-O-34004-A1AP-ST 1-1/2"-O-34003-A1AP-SJ 1-1/2"-O-34003-A1AP-ST DRWN DESCRIPTION CHKD APPD VIETNAM OIL AND GAS GROUP (c/o DQR) DUNG QUAT POLYPROPYLENE PROJECT PROJECT: B H B2 CWS 021 B2 B2 3"-CWR-34001-A1AW-NI 3/4" B2 FOR SAMPLING DETAILS SEE P&ID NO 07140-000-25-R006 NI 1"-PL-35012-A1AP-NI 3/4"-CWR-34002-A1AW-NI G HOLE Φ13mm AT LOW POINT B2 1"-CWR-34003-A1AW-NI NOTE B2 ATM TO SAFE LOCATION LO 3/4" UTILITY CONNECTION TO BE PROVIDED (MN) 0.50 / 1.00 40 / 80 PSV 3403 D CWR 021 / 5.00 / 120 PP 3/4 D 9.2 NOTES REQUIRED ELECTRICAL TRACING TEMPERATURE : 50℃ 1000.0 x 3000.0 2.60 SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE / 120 PP 11 C-301 SUCTION KNOCK-OUT DRUM SERVICE NAME 1.00 24.0 10 D-304 ITEM NO OIL LOADING PUMP CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE / 5.00 3"-SL-34001-A1AS-HS B ST HS 2m JACKET LENGTH NC 3/4" PETROVIETNAM B2 LICENSOR: MITSUI CHEMICAL, INC T HYUNDAI ENGINEERING CO., LTD 3/4"-CL-34001-A1AS-PP DRAWN BY A DUNG QUAT REFINERY MANAGEMENT BOARD DQR B2 DATE CHECKED BY HEC CLASSIFICATION NO 10 RECYCLE GAS SCRUBBING DATE 08.07.31 J.O.R A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J APPROVED BY TITLE: 08.07.31 S.Y.P CL 022 SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-300-25-R340 11 B2 A1 841x594 07140-300-25-R350 DWG NO B2 B2 C-301-D1 (W/E) ITEM NO SERVICE NAME SERVICE NAME C-301 SNUBBER SIZE DIA x LENGTH (mm) CAPACITY (m3) (kg/cm2g) O.P D.P O.T (˚ C) D.T INSUL TYPE x / 5.00 / 120 / / NI C-301-E1 (W/E) / / D.P (kg/cm2g) D.T (˚ C) INSUL TYPE NI H / 5.0 / 120 / 9.2 / 120 RECIPRO TYPE DESIGN CAPACITY (Nm3/hr) SUC PRESS (kg/cm2g) DISCH PRESS.(kg/cm2g) INSUL TYPE TUBE B2 SERVICE NAME 1668.0 0.5 ~ 1.00 22.00 NI B2 SERVICE NAME x / / NI 1"-CWR-35008-A1AW-NI PSV 3504 B2 NOTE ATM TO SAFE LOCATION SG 3502 x PP 3/4 D 9.2 B2 HOLE Φ13mm AT LOW POINT B2 B2 C-301-E1 TI H 3501 B2 B2 E RTD HH H B2 PSV 3501 D 3" B2 B2 LG 3502 B2 LT 3501 LI 3501 B2 B2 1" C-301-D2 B2 TRIM SPEC : A1AP-NI NC A1AP B1AP 3/4" 3/4" V 3/4" B2 PI 3506 A1APS B1AP B2 HH H PT 3506 3"-PL-35015-B1AP-HC HH US 239 3"-PL-35007-B1AP-HC B2 B2 1"-PL-35008-B1AP-HC PG 3504 4"x3" F 750 PROPYLENE TO T-720A/B 320 PROPYLENE TO T-301 310 PROPYLENE TO D-303 V E 4" 1" 3" B2 B2 1" 3" LT 3503 LI 3503 HOLD H B2 B2 1" D RTD PK-301 B2 PP LG 3505 HH H TG 3504 NC A1AP B1AP TT 3504 B2 4"-PL-35007-B1AP-PP 3/4" TI 3504 B2 3/4" D -PL-35011-B1AP-PP 1" US 239 1"-WO-35002-A1AP-NI C HH H 3" 1" 3/4" D V 1/2" 3/4" TT 3502 -PL-35002-A1AP-NI -PL-35001-A1AP-NI 1"-WO-35001-A1AP-NI 3/4" B2 D A1APS A1AP -PL-35010-B1AP-PP 1" 340 WASTE OIL TO P-303 25.0 PSV 3502 LO LO B2 TG 3502 FO 3501 HOLD V 1/2" LO TI 3502 -PL-35003-A1AP-NI HH US 239 B2 B2 HOLD B2 B2 D 3/4" RTD CWS 021 C-301-D4 1"-WO-35004-B1AP-NI NC B2 1" B2 3"-CWS-20114A1AW-NI HOLD C-301-D1 FO C-301-D3 B2 B2 B2 3/4" 3"-CWR-35001-A1AW-NI NOTE 1" NOTE D W/E B2 PV 3503 B1AP A1AP NOTE NO POCKET F B2 BDL 023 3"-BDL-35001-A1APS-NI V 3/4" CWS 021 3"-CWS-02132-A1AW-NI HOLD B2 PG 3503 CWR 021 B2 D NC 1/2" HOLD G 6" 3"-PL-35009-B1AP-PP SG 3501 3" D B2 TRIM SPEC : B1AP-PP HOLDS 1-1/2"-WO-35005-B1AP-NI B2 PSV SIZE TO BE FINALIZED BY VENDOR INFORMATION DELETED UTILITY LINE SIZE FOR PACKAGE TO BE FINALIZED BY VENDOR INFORMATION BDL 023 1"-BDL-35003-A1APS-NI NC NC V ATM TO SAFE LOCATION 3/4"-CWR-35004-A1AW-NI 1"-WO-35003-B1AP-NI 3/4" CWR 021 3"-CWR-35006-A1AW-NI 6"-PL-35009-A1AP-NI V NC TG 3501 NOTE 3/4" V PG 3501 12" 12"-PL-34002-A1AP-NI D PG 3502 B2 B2 -PL-35006-B1AP-PP PT 3504 1" RTD 340 PROPYLENE FROM D-304 PI 3504 3/4" -PL-35004-A1AP-NI PT 3502 H -PL-35005-B1AP-PP PT 3503 PI H 3502 L LL 3/4" HH LL 1"-CWR-35005-A1AW-NI HH TI H 3506 US 239 H C-301-E2 PSV 3503 LO PIC H 3503 L INTERCONNECTING PIPING/TUBING/WIRING BETWEEN THE SKIDS (TOTAL SKIDS WITH LCP & GAUGE BOARD BEING FREE STANDING) TO BE BY OTHERS (NOT BY COMPRESSOR VENDOR) PACKAGE INCLUDING CONTROL IS ON HOLD FOR VENDOR INFORMATION A1APS B2 6" B2 B1AP 3/4 D 9.2 UTILITY CONNECTION IS TO BE PROVIDED (MN) HOLD LO B2 OUTLET FROM BOTTOM / / B2 3" G B2 INLET FROM TOP / 25.00 / 120 6"-PL-35010-A1AP-NI US 001 DELETED B2 D B2 3/4" 3/4"-CWR-35007-A1AW-NI LO B2 B2 NOTES C-301 KNOCK-OUT DRUM SIZE DIA x LENGTH (mm) CAPACITY (m3) (kg/cm2g) O.P D.P O.T (˚ C) D.T INSUL TYPE / / NI 3/4" V 11 C-301-D4 (W/E) ITEM NO C-301 KNOCK-OUT DRUM SIZE DIA x LENGTH (mm) CAPACITY (m3) (kg/cm2g) O.P D.P O.T (˚ C) D.T INSUL TYPE 10 B2 C-301-D2 (W/E) ITEM NO RECYCLE GAS COMPRESSOR SERVICE NAME TYPE HEAT DUTY (kW) SHELL C-301 (W/E) ITEM NO C-301 INTER COOLER SERVICE NAME x / / B2 ITEM NO C-301 SNUBBER SIZE DIA x LENGTH (mm) CAPACITY (m3) (kg/cm2g) O.P D.P O.T (˚ C) D.T INSUL TYPE B2 B2 C-301-D3 (W/E) ITEM NO B2 C DOCUMENT CLASS: Z 1ST B1 BDL 023 1-1/2"-BDL-35002-A1APS-NI STAGE CSO PCV 3504 PG 3505 H PDA 3501 L 01 REV PDT 3501 HS 3501 C-301 1"-MN-33020-B1GR-NI DATE 0/50/100 LOAD MN 024 1-1/2"-MN-02478-B1GR-NI HOLD B2 DUNG QUAT POLYPROPYLENE PROJECT PROJECT: NC CWS 021 SG 3503 2"-CWS-02113-A1AW-NI B2 HOLD 2"-CWR-35003-A1AW-NI HOLD B2 B2 B2 B2 CWR 021 PETROVIETNAM B LICENSOR: SERVICE NAME TI H 3503 A US 239 MGL C301 ITEM NO RECYCLE GAS BYPASS COOLER SHELL D.P (kg/cm2g) D.T (˚ C) INSUL TYPE B2 SERVICE NAME CAPACITY (Nm3/hr) TYPE HEAT DUTY (kW) RUN MITSUI CHEMICAL, INC B2 C-301-E2 (W/E) ITEM NO RTD PK-301 HYUNDAI ENGINEERING CO., LTD RECYCLE GAS COMPRESSOR UNIT 1668.00 DRAWN BY TUBE / 5.0 / 120 CHECKED BY / 9.2 / 120 APPROVED BY DATE 10 RECYCLE GAS COMPRESSION DATE HEC CLASSIFICATION NO A PIPING & INSTRUMENT DIAGRAM 08.07.31 J.O.R NI TITLE: 08.07.31 K.S.J B2 DATE 08.07.31 S.Y.P DUNG QUAT REFINERY MANAGEMENT BOARD DQR B2 APPD VIETNAM OIL AND GAS GROUP (c/o DQR) M CHKD -LN-35001-A1AA-NI B2 DRWN DESCRIPTION NC B 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 1"-PL-35012-A1AP-NI 340 PROPYLENE GAS TO D-304 330 CLEAN PROPYLENE GAS ATM TO SAFE LOCATION 2ND SCALE JOB NO - 07140 REV DRAWING NUMBER 07140-300-25-R350 11 B2 A1 841x594 07140-500-25-R510 DWG NO PK-501 B2 ITEM NO C-501-E1 (W/E) SHELL D.P (kg/cm2g) D.T (˚ C) INSUL TYPE 4.0 NI SERVICE NAME 1000.0 x 1200.0 1.20 / 6.00 / 80 NI / 6.00 / 80 B2 TYPE HEAT DUTY (kW) / 4.00 / 10 NI NOTES MINIMUM 2.5M FROM D-505 UPPER SIDE BEM, HOR 9.3 B2 SHELL TUBE D.P (kg/cm2g) D.T (˚ C) INSUL TYPE B2 NI 11 OFF GAS COOLER SERVICE NAME 350.0 x 600.0 0.07 10 E-504 ITEM NO WATER COLLECTOR SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE / / D-504 ITEM NO GAS/WATER SEPARATOR SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE / 8.0 / 80 C-501-D1 (W/E) B2 SERVICE NAME TUBE / 6.0 / 80 ITEM NO BEM, HOR TYPE HEAT DUTY (kW) 800.0 0.1 LIQUID RING COOLER SERVICE NAME LIQUID RING TYPE DESIGN CAPACITY (kg/hr) SUC PRESS (kg/cm2g) DISCH PRESS.(kg/cm2g) INSUL TYPE B2 ITEM NO STEAMER OFF GAS COMPRESSOR SERVICE NAME 800.0 CAPACITY (kg/hr) C-501 (W/E) ITEM NO STEAMER OFF GAS COMPRESSOR SERVICE NAME LOCATED D-507, LV-5102 & LV-5104 300mm MIN BELOW N.L.L INTO C-501-D1 BOOT / 8.0 / 80 / 6.2 / 80 B2 UTILITY CONNECTION IS TO BE PROVIDED (MN) HOLE Φ 13 mm AT LOW POINT CC H H 4"-BDL-50001-A1APS-ST B2 PI 5102 L LL HH TI 5101 US 504 HH PI 5103 3/4" D 2" D 3/4" 3" B2 3"-PL-51006-A1AP-NI D B2 D PT 5102 TT 5101 C-501 TG 5101 PT 5103 B2 RTD 501 PROPYLENE FROM T-501 M B2 NC 6"-PL-50102-A1AP-PP E B2 6" M.H 3" 2" MGL C501 300# 3" 1-1/2" 2" B2 (ST) H LI 5101 B2 2" LT 5101 L LL LG 5101 3/4" B2 B2 FO 5101 SP LT 5102 B2 B2 INT 1" B2 3" LIC 5102 H L B2 D D-509 1" B2 B2 M.H SP Y044 LN 024 FG 5102 B2 20" B2 3"X1" LT 5103 B2 LG 5103 300# E 3" Z-502 1"-LN-02440-A1AA-NI B2 1" 3" 1"-LN-02440-Q0JP-NI 3/4" D B2 1-1/2" B2 2" 3/4" 2"x1" D GWR LT 2"x1" LI 5103 H 5104 2" INT H LIC 5104 US 001 L 1"-WO-51002-A1AP-NI D D 3/4" B2 NOTE 2" 300# HOLDS 2" 1"-PRW-51003-A1AP-NI V 3/4" LG 5104 1" DELETED 2" C-501-E1 SG 5101 B2 GWR B2 3" B2 B2 3" 1-1/2"x1" 2" B2 B2 3" FC 1" NOTE 300# TRIM SPEC : A1APS-NI B2 B2 1" 1-1/2" (ST) 2" -PRW-51002-A1AP-NI D D B2 D 3/4" US 001 300# FG 5101 PK-501 B2 1" LG 5102 TRIM SPEC : A1AP- ST RUN 3/4" B2 2" LV 5104 B2 2"-PL-51007-A1AP-PP C-501-D1 2" 1" 3/4" D 1" B2 LL (ST) F NC PG 5102 3" G V 1/2" D 3/4" 3"X1 1/2" US 504 LG 5106 LO 6"-PL-51001-A1AP-PP PG 5103 H NO POCKET NO POCKET 1" NOTE B2 1D2 6.0 2" 2" 1-1/2" LI 5106 300# D-507 D 3/4" B2 ST TRIM SPEC : A1AP- -PRW-51001-A1AP-NI 2" 3/4" 2" DELETED D 2"x1" PACKAGE INCLUDING CONTROL IS ON HOLD FOR VENDOR INFORMATION CSO PG 5101 B2 PSV 5101 (ST) B2 LT 5106 CSO HOLD A1AP A1APS PT 5101 B2 NO POCKET LO 5101 L -PL-51002-A1AP-NI FO 3/4" 1-1/2"-PL-51003-A1AP-NI PIC F -PL-51002-A1AP-NI HH H NOTE B2 B2 2" 2" 2" RWS 021 2"-RWS-02108-A1AW-CC 3/4" 2" (ST) 1" TRIM SPEC : A1APS- ST 2" NO POCKET PV 5101 B2 D-508 E-504 3" RWR 021 NC US 001 D-504 HH H 2"-RWR-51001-A1AW-CC A1AA Q0JP US 508 HH H HH 2" CC 520 LP BLOW DOWN TO S-601 2"-BDL-51003-A1APS-NI LL B2 G V 3/4" B2 V B2 1/2" 3/4"-RWR-51002-A1AW-NI ATM TO SAFE LO LOCATION 3"-PL-51005-A1AP-NI 2"-PL-51004-A1AP-ST 520 PROPYLENE TO T-503A/B NOTE B2 2"-BDL-51001-A1APS-NI TI H 5102 L RTD 3/4 D 8.0 B2 2"-BDL-51002-A1APS-NI PSV 5102 1"-RWR-51003-A1AW-NI 2"-BDL-51004-A1APS-ST NO POCKET 1"-WO-51001-A1AP-NI 501 LP BLOW DOWN FROM T-501 3/4" D 3/4" B2 D Y043 2" 1"-CL-63011-A1AS-NI HOLD 3/4" B2 D D-510 B2 H.H SP Y045 FG 5103 3"X1" B2 D-507 A SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE / 4.00 / 45 NI B2 SERVICE NAME x / 6.00 / 80 D-508 ITEM NO WATER/ORGANIC SEPARATOR B2 300.0 x 1000.0 / 1.80 / 80 B2 / 0.03 / 45 NI ITEM NO SERVICE NAME Z-502 (W/E) D-509 NITROGEN SPARGER ITEM NO / 1.80 / 80 / 0.10 / 45 SERVICE NAME Z-503 (W/E) D-510 NITROGEN SPARGER NI B2 SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE H US 5105 L 001 FC B DUNG QUAT REFINERY MANAGEMENT BOARD LICENSOR: MITSUI CHEMICAL, INC LV 5105 HYUNDAI ENGINEERING CO., LTD DRAWN BY APPROVED BY DATE HEC CLASSIFICATION NO 10 A PIPING & INSTRUMENT DIAGRAM STEAMER OFF GAS RECOVERY-1/2 08.07.31 J.O.R B2 TITLE: DATE 08.07.31 K.S.J / 0.10 / 45 DATE 08.07.31 S.Y.P NI APPD DQR CHECKED BY B2 PETROVIETNAM 1-1/2"x1" B2 x / 1.80 / 80 CHKD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: B2 HYDROCARBONS SEPARATOR B2 D D-510 ITEM NO SERVICE NAME x SIZE DIA x LENGTH (mm) CAPACITY (m3) D.P O.P (kg/cm2g) D.T O.T (˚ C) INSUL TYPE B2 B2 D-509 WASTE OIL COLLECTING DRUM SERVICE NAME DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) 1-1/2" 1-1/2"x1" DATE B2 LIC ITEM NO CONDENSATE DRAIN POT B1 01 1"-LN-02241-Q0JP-NI B2 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.07.08 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 REV 3/4" B2 SERVICE NAME 1" Z-503 1"-WW-51001-A1AP-NI ITEM NO LG 5105 2" 10" 1"-LN-02241-A1AA-NI CWS 021 LT 5105 TRIM SPEC : A1AP-NI B2 B CWR 021 DOCUMENT CLASS: Z 2" B2 LN 024 B2 1" 1"-PRW-51004-A1AP-NI A1AA Q0JP LO D 3/4" 1" FC HOLD B2 3/4"-CWR-51002-A1AW-NI B2 C 3"X1" 1" HOLD ATM TO SAFE LOCATION NOTE 3/4 D 9.2 -CWS-02125-A1AW-NI PSV 5103 NOTE HOLD 1"-CWR-51003-A1AW-NI LV 5102 PACKAGE VENDOR -CWR-51001-A1AW-NI 630 STEAM CONDENSATE FROM E-605 A1AS A1AP C SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-500-25-R510 11 B2 A1 841x594 B2 DWG NO 07140-700-25-R730 B2 B2 F-712 ITEM NO HIGH PRESSURE HYDROGEN FILTER SERVICE NAME H TYPE DESIGN CAPACITY (m3/hr) D.P (kg/cm2g) D.T (˚ C) INSUL TYPE PK-702 ITEM NO SERVICE NAME CARTRIDGE 3.0 55.0 HYDROGEN COMPRESSION UNIT SERVICE NAME 15.0 CAPACITY (kg/hr) C-702A-D1/B-D1 C-702A-D1/B-D1 (W/E) ITEM NO B2 / 65 NI / / NI SERVICE NAME 15.0 30.0 51.0 NI NOTES C-702A/B AFTER COOLER SERVICE NAME x SHELL / / D.P (kg/cm2g) D.T (˚ C) INSUL TYPE NI B2 TUBE / 55.0 / 120 / 43.0 / 65 H NI D0JP D1AH 1"-H-73009-D0JP-NI HOLE Φ 13 MM AT LOW POINT B2 TYPE HEAT DUTY (kW) / 55.00 / DELETED -H-73102-B1AH-NI 731 HYDROGEN FROM PK-701 1"-H-73008-D1AH-NI NC BDL 023 V G F-712 MGL C702 A PK-702 US 203 RUN BDL 023 B2 US 203 HH HH PIC H 7301 L B2 US 001 1"-BDL-73001-A1AH-NI 3/4" 1"-BDL-73002-A1AH-NI 200 HYDROGEN TO R-200, R-201, R-202 11 C-702A/B-E1 (W/E) ITEM NO C-702A/B AFTER SNUBBER SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE RECIPRO TYPE DESIGN CAPACITY (kg/hr) SUC PRESS (kg/cm2g) DISCH PRESS.(kg/cm2g) INSUL TYPE 10 B2 C-702A-D2/B-D2 C-702A-D2/B-D2 (W/E) ITEM NO HYDROGEN COMPRESSORS SERVICE NAME x / 44.00 / 65 C-702A /B (W/E) ITEM NO C-702A/B SUCTION SNUBBER SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE G D 3/4" PT PV 7301 7301 1"-H-73010-B1AH-NI FO F D B2 B2 B2 B1AH D1AH PI H 7304 A L LL PG 7301 A PT 7304 A TT 7301 B2 -H-73102-B1AH-NI US 001 B2 C-702A-D1 E 1"-CWS-73002A1AW-NI B2 D 3/4" M ATM TO SAFE LOCATION -H-73006-D1AH-NI B2 HOLD HOLD CWR 021 B3 V D 3/4" HOLD CWR 021 3/4" D HOLD B2 1-1/2"-CWR-73003-A1AW-NI TG 7301 A B2 B3 PI H 7304 B L LL A1AH D1AH PG 7302 A 3/4" SG 7301A HOLD D HOLD 1-1/2" B2 PT 7304 B B2 C -H-73001-B1AH-NI D DELETED CWS 021 DELETED 3/4" UTILITY LINE SIZE FOR PACKAGE TO BE FINALIZED BY VENDOR INFORMATION B2 3/4" DELETED D C MGL DOCUMENT CLASS: Z C702 B RUN C-702B-D1 B2 B2 1-1/2"-CWS-02108-A1AW-NI C-702A-D2 PG 7301 B HOLDS 3/4" -H-73007-D1AH-NI -H-73002-B1AH-NI LL FO C-702A/B-E1 PSV 7301 55.0 1-1/2"-CWS-02128-A1AW-NI US 203 TV 7301 W/E C-702A W/E NC CWS 021 3/4" D 3/4"-CWS-73001A1AW-NI B2 B2 B2 D E 3/4 D 9.2 1-1/2"-CWR-73001-A1AW-NI 1"-LN-02449-A1AA-NI B2 PSV 7302 NOTE FO 7301 A LN 024 H TIC 7301 L RTD LO LL F -H-73005-B1AH-NI US 203 3/4" D 3/4" US 203 M 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.07.08 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 B2 B1 01 FO 7301 B B2 LN 024 REV -H-73003- -NI 1"-BDL-73003-A1AH-NI HOLD B BDL 023 B2 B2 CWR 021 1-1/2"-CWR-73002-A1AW-NI HOLD 7302 B B PETROVIETNAM DUNG QUAT REFINERY MANAGEMENT BOARD DQR HOLD 3/4" B2 TG 7301 B SG 7301B B2 LICENSOR: MITSUI CHEMICAL, INC -H-73004-D1AH-NI 1-1/2" C-702B-D2 D HYUNDAI ENGINEERING CO., LTD B2 3/4" DRAWN BY A DATE APPROVED BY HEC CLASSIFICATION NO 10 HYDROGEN FEED SYSTEM DATE 08.07.31 J.O.R A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J TITLE: 08.07.31 S.Y.P CHECKED BY APPD PG C-702B W/E 1-1/2"-CWS-02109-A1AW-NI CHKD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: B2 CWS 021 DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) B2 B2 1"-LN-02450-A1AA-NI DATE SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-700-25-R730 11 B2 A1 841x594 DWG NO 07140-700-25-R731 B2 B2 PK-701 ITEM NO HYDROGEN PURIFICATION PACKAGE SERVICE NAME SERVICE NAME 130.00 CAPACITY (Nm3/hr) PK-701-Z2 (W/E) ITEM NO SERVICE NAME HYDROGEN PREHEATER CAPACITY (Nm3/hr) B2 B2 PK-701-E1 (W/E) ITEM NO SERVICE NAME SULFUR GUARD B2 PK-701-Z3 (W/E) ITEM NO CO AND CO2 GUARD SERVICE NAME 10 HYDROGEN COOLER PK-701-F1 (W/E) ITEM NO SERVICE NAME 11 B2 B2 PK-701-E2 (W/E) ITEM NO CAPACITY (Nm3/hr) CAPACITY (Nm3/hr) HYDROGEN FILTER NOTES PK-701-Z1 (W/E) ITEM NO MEMBRANE SERVICE NAME HOLE Φ 13mm AT LOW POINT FOR SAMPLING DETAILS SEE P&ID NO 07140-000-25-R006 CAPACITY (Nm3/hr) B2 H H 2"-H-73102-B1AH-NI 730 HYDROGEN TO PK-702 G G FIC 7311 TIC 7316 PK-701 PSV 7312 NOTE ATM TO SAFE LOCATION F CWR 021 -CWR-73102-A1AW-NI BDL -BDL-73104-A1AH-NI F PSV 7311 V 1/2" HOLD SC 70 LO 1"-HN-02412-D1AP-NI LO E D LO SG 7311 HOLD HN 024 3/4" 3/4 D 9.2 3/4" D V PDI 7313 NC NC PK-701-F1 TT 7316 010 HYDROGEN FROM B/L PK-701-Z2 TAHH TAH LG 7311 TT TT 7311 RTD W/E 7311 E RTD PK-701-Z3 TIC 7314 D FV 7311 FT PG 7311 TIC 7311 PG 7312 2"-H-73102-B1AH-NI 3/4" FOR PURGE 2"-H-01001-B1AH-NI NOTE 7314 FT 7311 FIC 7311 PT 7311 PI 7311 D PK-701-E2 HEATER PK-701-E1 TIC 7312 H TIC 7313 L H TIC 7315 L HOLDS H PK-701-Z1 L UTILITY LINE SIZE FOR PACKAGE TO BE FINALIZED BY VENDOR INFORMATION PG TT MN 024 7312 RTD -MN-02410-A1AA-NI PG TG 7311 7311 TT TT 7313 RTD B2 DELETED 7312 7315 RTD DELETED 2"-BDL-73101-A1AH-NI HOLD HOLD DELETED 023 PERMEATE OUTLET TO FLARE PACKAGE CONTROL AND FINAL CONFIGURATION ARE ON HOLD FOR VENDOR INFORMATION C C CWS 021 PDI PDI 7311 7312 DOCUMENT CLASS: Z 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.07.08 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 -CWS-73101-A1AW-NI B1 HOLD 01 REV DATE DRWN DESCRIPTION CHKD APPD VIETNAM OIL AND GAS GROUP (c/o DQR) DUNG QUAT POLYPROPYLENE PROJECT PROJECT: B PETROVIETNAM B DUNG QUAT REFINERY MANAGEMENT BOARD DQR LICENSOR: B2 MITSUI CHEMICAL, INC HYUNDAI ENGINEERING CO., LTD DRAWN BY A DATE APPROVED BY HEC CLASSIFICATION NO 10 HYDROGEN PURIFICATION DATE 08.07.31 J.O.R A PIPING & INSTRUMENT DIAGRAM DATE 08.07.31 K.S.J TITLE: 08.07.31 S.Y.P CHECKED BY SCALE JOB NO - 07140 DRAWING NUMBER REV 07140-700-25-R731 11 B2 A1 841x594 P-992 07140-990-25-R990 CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE 60.00 432.0 NI NI B2 H 10"-FL-99018-A1GR-NI / 23.00 -20 / 65 LOCATE THE PUSH BUTTON SWITCH NEAR THE PUMP START/STOP SWITCH / 15.50 / 40 A1GR B1GR D 3/4" LO B2 2" FC D B2 3/4" 6"-PL-99002-B1GR-NI B2 B2 LI US 991 B2 3" LT 9902 B2 TE 9903 9901 A LI 9902 B2 W/E B2 W/E HH HH F PIC 9901 H TI 9904 NOTE PT 9901 LI 9903 NOTE 3" 3/4" D B2 M1 G L1 B2 B2 L V B2 TE 9904 LI US 993 B2 B2 B2 PG 9902 M1 G 2"-PL-99026-B1GR-NI PT 9902 3/4" B2 V F B2 TK-991B LI 9904 LL TRIM SPEC : B1GR-NI NOTE B2 FT 9903 FQI 9903 NOTE D 3/4" 3"-PL-99004-B1GR-NI 9904 C XHS O 9904 C XZSL 9904 D 3/4" KS FIC 9901 3"-PL-99006B1GR-NI B2 FV 9901 T028 D B2 PSV 9907 2" PG T029 P-991A 3/4" D B2 SP D 3/4" 9903 B2 1" LO 3/4"-PL-99003-B1GR-NI NC NOTE 11 1"-FL-99008-A1GR-NI D FT 9901 B2 PT 9906 L TI 9905 FQI 9902 TT 9905 FT 9902 3/4 D 51.0 V 1/2" 3/4" C DOCUMENT CLASS : Z 08.07.31 IFD UPDATED (PID REVIEW INCORPORATED) S.Y.P K.S.J J.O.R ISSUED FOR HAZOP & PID REVIEW 08.05.30 S.Y.P K.S.J J.O.R ISSUED FOR APPROVAL 08.04.30 S.Y.P K.S.J J.O.R B2 LO B1 D 01 REV B2 DATE B2 A US 001 UX 993/994 M B2 4"-PL-99022-B1GR-NI 3/4" B2 4" US 991/993 KS 991 NC US 991/993 UX 993/994 PG SP T030 P-991B B2 9904 PETROVIETNAM RUN MGL P991 A RUN UX 993/994 M MGL US 001 HYUNDAI ENGINEERING CO., LTD US 991/993 B2 DRAWN BY US P991 B RUN 001 10 DATE S.Y.P 08.07.31 CHECKED BY DATE K.S.J 08.07.31 APPROVED BY DATE TITLE: A PIPING & INSTRUMENT DIAGRAM PROPYLENE STORAGE SPHERES 08.07.31 J.O.R HEC CLASSIFICATION NO S.Y.P SCALE JOB NO DRAWING NUMBER - - 07140 07140-990-25-R990 K.S.J DUNG QUAT REFINERY MANAGEMENT BOARD DQR MGL P992 B B2 KS 991 B2 APPD 3/4"-PL-99014-B1GR-NI NOTE M CHKD DUNG QUAT POLYPROPYLENE PROJECT PROJECT: 6"-PL-99020-B1GR-NI 4"-PL-99022-B1GR-NI NOTE DRWN DESCRIPTION VIETNAM OIL AND GAS GROUP (c/o DQR) D 4"-PL-99018-B1GR-NI NOTE B2 B2 NC 3/4" 3/4" A1GR B1GR CSO D 3/4" PI 9906 B2 A1GR B1GR CSO CSO 2" 1" NOTE 11 2" A1GR B1GR CSO D NC CSO D NC 3/4" NC P-992 SP A1GR B1GR D 6"-PL-99012-B1GR-NI B2 PG 3/4" 3/4" CSO D 9907 D D 3/4" CSO 3/4" 6"-PL-99010-B1GR-NI 3/4" CSO B2 CSO CSO A1GR B1GR D 3/4" 3/4"-PL-99024B1GR-NI D NC 1/2" 3/4"-PL-99023-B1GR-NI 1"-FL-99015-A1GR-NI NOTE 11 LO 1"-FL-99012-A1GR-NI B1GR A1GR NOTE 3/4" B2 B2 V 3/4" B2 HOLDS DELETED NOTE 11 2" D 750 PROPYLENE TO DRYER/COS REMOVAL TOWER 3/4" D 1"x3/4" B2 D LO 2"x1-1/2" B2 2"x1-1/2" FO 3"x2" 1"-FL-99013-A1GR-NI B2 B2 3/4" D 1"x3/4" PSV 9906 B2 991 B2 3/4 D 51.0 B2 B2 C B2 V 1/2" 3/4"-PL-99017-B1GR-NI D 3/4" LO 3/4" 6"-PL-99016-B1GR-NI D D 3/4 D 51.0 1"-FL-99010-A1GR-NI 9904 B2 3/4" PSV 9905 A1GR B1GR 9906 D XZL B1GR A1GR 9906 NOTE NOTE 10 TI NOTE 10 TT 3/4" 6"-PL-99054-B1GR-NI 001 O XZS B2 US UX 994 3/4"-PL-99008-B1GR-NI B2 B2 1"-FL-99016-A1GR-NI 3/4"-PL-99013-B1GR-NI NOTE 1, B2 1"-FL-99011-A1GR-NI B2 O XZL 9903 C B2 3/4" PI 9908 XHS O 9903 C D 3/4" XZS 9903 6"-PL-99012-B1GR-NI D PT 9908 NOTE 1, B2 B1GR A1GR 1/2" V V 1/2" 6"-PL-01001-B1GR-NI B2 UX 993 001 LO D 9902 US 3/4 D 51.0 XV 9904 LO LO C 3/4" XZSL 4"-PL-99021-B1GR-NI 010 PROPYLENE TO REFINERY PLANT XZL O 9902 C PSV 9904 B2 E 2"-PL-99004-B1GR-NI D O B2 XV 9903 NOTE O XHS 9904 C B2 NOTE 10 9901 C B2 XZS 9902 001 XHS 9902 3/4 D 51.0 023 FL 14"-FL-99001-A1GR-NI FB TSO PSTV D 6"-PL-99015-B1GR-NI FC TSO FC PSTV 3/4" FB O TG 9904 B B2 LO XZL NOTE 1, B2 PSV 9903 B2 A1GR B1GR 9901 US UX 993 NOTE XHS O 9903 C 3/4"-PL-99011-B1GR-NI XHS O 9901 C 6"-PL-01001-B1GR-NI XV 9902 6"-PL-99010-B1GR-NI XZS 010 PROPYLENE FROM REFINARY PLANT 9902 C 1"-FL-99009-A1GR-NI NOTE 1, FB TSO 001 NOTE XHS O 1"-FL-99007-A1GR-NI XV 9901 UX 991 A M2 NC NOTE B2 D 3/4" PSTV B2 D B2 B2 PSTV US 4" B2 B1GR A1GR B2 XHS O 9901 C B2 A M2 NC NOTE TG 9903 B FC FC E D LO 4" NOTE B B2 3/4" L2 L2 B2 G B2 L1 LT 9904 11 MINIMUM DISTANCE BETWEEN BLOCK AND GLOBE VALVE SHALL BE 1000mm L CSO D 9903 A LI 9904 TRIM SPEC : B1GR-NI NOTE B2 W/E W/E H 1"-FG-01002-A2AD-NI 023 FUEL GAS FROM BATTERY LIMIT A1GR B1GR 1" PIC 9902 NOTE V LT 9903 HH TK-991A 10 VALVES INTERLOCKED TO ENSURE THAT ONE(1) VALVE IS IN SERVICE FOR EACH SPHERE AT ANY TIME 3/4" H HH UX 993 B2 6" LI 9902 LL PG 9901 B2 L B2 6" B2 B2 INSTALLED HORIZONTALLY 2"x1-1/2" 6"-PL-99007-B1GR-NI B2 2"-PL-99025-B1GR-NI CSO TO BE READABLE FROM MANUAL VALVE FC D B2 D 3" LT 9901 L UX 991 NOTE 3/4" NC LI 9901 3/4" CONNECTION FROM OUTLET OF SPHERE UP TO AND INCLUDING THE FIRST BLOCK VALVE SHALL BE FIELD WELDED VALVE B2 PV 9902 A1GR B1GR 6"-PL-99051-B1GR-NI 6"-PL-99005-B1GR-NI 3"-PL-75010-B1GR-NI NOTE V 3"-PL-75011-B1GR-NI TSO FB 750 PROPYLENE FROM T-720A/B V TI H 9903 FREE DRAINING TO THE HEADER 4"x2" 3K4 23.0 LO G NOTE B2 B2 B2 4"-FL-99005-A1GR-NI H PRESSURE COMPENSATION TO TANK GAUGING SYSTEM PSV 9902 1/2" B2 WATER SPRAY SYSTEM SHALL BE PROVIDED SEE FIRE WATER DISTRIBUTION DWG FOR WATER SUPPLY HEADER CONNECTION B2 LO PV 9901 B2 INPUT TO DCS THRU TANK GAGING SYSTEM B2 A1GR B1GR 3K4 23.0 2"x1-1/2" 1/2" V B2 4"x2" B2 B2 LOCATE THE VALVE AS CLOSE AS POSSIBLE TO THE STORAGE TANK NI 4"-FL-99002-A1GR-NI 2"x1-1/2" A1GR B1GR PSV 9901 11 NOTES B2 LO 10 10"-FL-99017-A1GR-NI B2 B2 12900.0 x 1124.00 SIZE DIA x LENGTH (mm) CAPACITY (m3) O.P (kg/cm2g) D.P O.T (˚ C) D.T INSUL TYPE 50.00 266.0 PROPYLENE STORAGE SPHERE SERVICE NAME PROPYLENE SPHERE PUMP NOTE 10 B2 CAPACITY (m3/hr) DIFFERENTIAL HEAD (m) INSUL TYPE SERVICE NAME TK-991A /B ITEM NO P-991A/B ITEM NO OFF-SPEC PROPYLENE RETURN PUMP NC DWG NO ITEM NO SERVICE NAME 2" 11 REV B2 A1 841x594 LUẬN VĂN THẠC SĨ JLIỆU THAM KHẢO [01] Aasif Vindhani, “A brief report on Huge Fire At IOC Oil Depot, Jaipur, India On 29 Oct.-2009”, QP Refinery, Qatar, 2009 [02] AICHE “Guidelines for Chemical Process Quantitative Risk Analysis” 2nd Edition AICHE, 2000 [03] Cox, A.W., Lees, F.P & Ang, M.L., “Classification of Hazardous Locations”, Institution of Chemical Engineers, Rugby, UK, 1990 [04] DNV “SAFETI manual” DNV, 2007 [05] DNV, “Quantitative Risk Assessment of Dung Quat Refinery, revision 1” – 2006 [06] DNV, “ARF Technical Notes, T14 Process Equipment failure Frequencies”, Rev 3, 20 December 2006 [07] DNV, “ARF Technical Notes, T14 Section – Process Equipment failure Frequencies, Process Vessel”, Rev 2, December 2000 [08] DNV, “ARF Technical Notes, T14 Section 17 – Process Equipment failure Frequencies, Transfer Equipment”, Rev 1, 23 December 1999 [09] DNV, “ARF Technical Notes, T17 – Risk Criteria”, Rev 1, 1998 [10] DNV, “ARF Technical Notes, T15 – Human Impact Criteria”, Rev 01, 31 March 1998 [11] DNV, “ARF Technical Notes, T13 – Failure selection onshore”, DNV, 1998 [12] DNV, “ARF Technical Notes, T18 – Data source for QRA”, DNV, 2002 [13] DNV, “ARF Technical Notes, T19 – Background risk data”, DNV, 2002 [14] DNV, “ARF Technical Notes, T21 – Fireball/Bleve modeling”, DNV, 2003 [15] DNV, “Technical Note T16 – SAFETI Parameters” [16] DNV, “Guideline Onshore QRA using SAFETI”, DNV, 1998 [17] DNV, “Consequence handbook”, DNV, 2008 [18] DNV, “Guide to finding and using reliability data for QRA”, DNV, 2009 [19] E Skramstad, “Guideline Quantitative Risk Assessment (QRA) Principales” DNV, 1998 [20] Lee Cho Hing “QRA training course material” DNV, 2009 [21] Lee Cho Hing “Process safety management”, DNV, 2009 [22] http://en.wikipedia.org/wiki/Piper_Alpha [23] Hyundai “07140-000-GI-0005, PP Plant process description”, Hyundai, 2008 [24] Hyundai “Process Flow Diagram” – 07140-000-20-R001~R012 and 07140-000-20R030~R031”, revision B1, Hyundai, 2008 [25] Hyundai “Material Balance - 07140-000-21-R001”, revision C1, Hyundai, 2008 [26] Hyundai “Material Safety Data Sheet (MSDS) - 07140-000-RP-R101”, revision 01, Hyundai, 2008 [27] Hyundai “Emergency Isolation Philosophy – 07140-8110-PD-0003”, revision B1, Hyundai, 2008 [28] Hyundai “Cause & Effect Chart – 07140-000-24-R001”, revision 01, Hyundai, 2008 Trang 121 LUẬN VĂN THẠC SĨ [29] Hyundai “Piping & Instrument Diagrams”, revision B1, Hyundai, 2008 [30] Hyundai “Basic Engineering Design Data (BEDD) – 07140-8820-SP-0001”, revision B1, Hyundai, 2008 [31] Hyundai “Design of Blast Resistant Control Building – 07140-8300-SP-0004”, revision B1, 2008 [32] Hyundai “Building Functional Specification - 07140-8300-SP-0101”, revision B1, 2008 [33] Hyundai “Hazardous Area Classification report – 07140-000-HS-F001”, revision C1 [34] Hyundai “Plot Plan Drawings”, 2008 [35] Hyundai “Equipment Location Plan (ELP) drawings”, 2008 [36] Hyundai, “Process description – 07140-000-GI-0005”, 2008 [37] Tập đồn dầu khí Việtnam, “hướng dẫn xử lý rủi ro đối phó với tình trạng khẩn cấp hoạt động dầu khí”, June 2002 [38] “UK HSE Frequency database”, UK, 2004 [39] CIA, “Guidance for the Location and Design of Occupied Buildings on Chemical Manufacturing sites”, (Version 2) CIA/CISHEC, 2003 G Trang 122 LUẬN VĂN THẠC SĨ LÝ LỊCH TRÍCH NGANG Họ tên: Lê Thị Huyền Trang Ngày, tháng, năm sinh: 13/11/1981 Nơi sinh: Quảng trị Địa liên lạc: 14 Trưng Nữ Vương, Khu 7, TT Phú Bài, Huyện Hương Thủy, TT Huế QUÁ TRÌNH ĐÀO TẠO 1999 – 2004 : Sinh viên trường Đại học Bách khoa Đà Nẵng 2007 – 2009 : Học viên Cao học trường Đại học Bách khoa Tp Hồ Chí Minh Q TRÌNH CƠNG TÁC 2004 – 2006 : Công ty Rostaing Technic 2006 – 2007 : Công ty Sơn Becker 2007 – 2009 : Công ty Det Norske Veritas Trang 123 ... THẠC SĨ Đề tài ? ?Đánh giá định lượng rủi ro nhà máy sản xuất nhựa Polypropylene Dung Quất phần mềm mô SAFETI 6.54? ?? nghiên cứu quy trình cơng nghệ sản xuất nhà máy Polypropylene Dung Quất Từ xác đinh... tài ? ?Đánh giá định lượng rủi ro nhà máy sản xuất nhựa Polypropylene Dung Quất phần mềm SAFETI 6.54? ?? đánh giá xác suất rủi ro cá nhân xác suất rủi ro tập thể tiềm tàng trình vận hành nhà máy Các... 1- TÊN ĐỀ TÀI: Đánh giá định lượng rủi ro nhà máy sản xuất nhựa Polypropylen Dung Quất phần mềm mô SAFETI 6.54 2- NHIỆM VỤ LUẬN VĂN: đánh giá xác suất rủi ro cá nhân xác suất rủi ro tập thể tiềm