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1. (WO2017112524) TOPSIDE OIL PRODUCTION EQUIPMENT SYSTEM FOR REDUCTION IN SPACE AND WEIGHT
Latest bibliographic data on file with the International Bureau

Pub. No.: WO/2017/112524 International Application No.: PCT/US2016/066980
Publication Date: 29.06.2017 International Filing Date: 15.12.2016
IPC:
C10G 33/02 (2006.01) ,C10G 53/02 (2006.01)
C CHEMISTRY; METALLURGY
10
PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
G
CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
33
De-watering or demulsification of hydrocarbon oils
02
with electrical or magnetic means
C CHEMISTRY; METALLURGY
10
PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
G
CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
53
Treatment of hydrocarbon oils, in the absence of hydrogen, by two or more refining processes
02
plural serial stages only
Applicants:
CAMERON SOLUTIONS, INC. [US/US]; 1333 West Loop South Suite 1700 Houston, TX 77027, US
Inventors:
SPRENKEL, Marcus, D.; US
SAMS, Gary, W.; US
MANDEWALKAR, S. Pavankumar, B.; US
CAIRES FERNANDEZ, Luis, Eduardo; US
Agent:
ROSSLER, Paul, E.; US
Priority Data:
14/977,93122.12.2015US
Title (EN) TOPSIDE OIL PRODUCTION EQUIPMENT SYSTEM FOR REDUCTION IN SPACE AND WEIGHT
(FR) SYSTÈME D'ÉQUIPEMENT DE PRODUCTION DE PÉTROLE EN SURFACE POUR RÉDUIRE L'ESPACE ET LE POIDS
Abstract:
(EN) A system and method for dehydrating crude oil on a floating production storage and offloading installation include a separator vessel (20) to receive an incoming produced water stream (15), followed by a flash vessel (30), a treatment block, a crude oil storage tank (60), and an electrostatic treater (70). The treatment block includes a low pressure degasser (40) followed by a compact electrostatic separator pre-treater (50) or a compact electrostatic separator pre- treater (50) followed by a low pressure degasser (40). The flash vessel (30) and/or the low pressure degasser (40) may employ an inlet cyclonic distributor and demisting cyclones, while the electrostatic treater may employ DUAL FREQUENCY® technology. The separator vessel (20) may be a single horizontal two-phase separator/degasser or two vertical two-phase separator/degassers that operate in parallel with each receiving approximately 50 percent of the incoming produced water stream. The final outlet stream preferably contains no more than 0.5 BS&W and 285 milligrams per liter salt.
(FR) L'invention concerne un système et un procédé de déshydratation de pétrole brut sur une installation flottante de production de stockage et de déchargement comprenant une cuve de séparation (20) servant à recevoir un courant d'eau produit entrant (15), puis une cuve de vaporisation (30), un bloc de traitement, un réservoir de stockage de pétrole brut (60) et un dispositif de traitement électrostatique (70). Le bloc de traitement comprend un dégazeur basse pression (40) puis un dispositif de prétraitement séparateur électrostatique compact (50), ou un dispositif de prétraitement séparateur électrostatique compact (50) puis un dégazeur basse pression (40). La cuve de vaporisation (30) et/ou le dégazeur basse pression (40) peuvent utiliser un distributeur cyclonique d'admission et des cyclones de désembuage, et le dispositif de traitement électrostatique peut employer la technologie DUAL FREQUENCY®. La cuve de séparation (20) peut être un unique séparateur/dégazeur horizontal à deux phases ou deux séparateurs/dégazeurs verticaux à deux phases qui fonctionnent en parallèle, chacun recevant environ 50 % du courant d'eau produit entrant. Le courant d'évacuation final ne contient de préférence pas plus de 0,5 BS&W et 285 milligrammes par litre de sel.
front page image
Designated States: AE, AG, AL, AM, AO, AT, AU, AZ, BA, BB, BG, BH, BN, BR, BW, BY, 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, HN, HR, HU, ID, IL, IN, IR, IS, JP, KE, KG, KH, KN, KP, KR, KW, KZ, LA, LC, LK, LR, LS, LU, LY, MA, MD, ME, MG, MK, MN, MW, MX, MY, MZ, NA, NG, 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, TH, TJ, TM, TN, TR, TT, TZ, UA, UG, US, UZ, VC, VN, ZA, ZM, ZW
African Regional Intellectual Property Organization (ARIPO) (BW, GH, GM, KE, LR, LS, MW, MZ, NA, RW, SD, SL, ST, SZ, TZ, UG, ZM, ZW)
Eurasian Patent Organization (AM, AZ, BY, KG, KZ, RU, TJ, TM)
European Patent Office (AL, AT, BE, BG, CH, CY, CZ, DE, DK, EE, ES, FI, FR, GB, GR, HR, HU, IE, IS, IT, LT, LU, LV, MC, MK, MT, NL, NO, PL, PT, RO, RS, SE, SI, SK, SM, TR)
African Intellectual Property Organization (BF, BJ, CF, CG, CI, CM, GA, GN, GQ, GW, KM, ML, MR, NE, SN, TD, TG)
Publication Language: English (EN)
Filing Language: English (EN)
Also published as:
SG11201805275SCN108431178KR1020180097634IN201817025007EP3394212MX2018007839
BR112018012608