EP 2440867 A4 20180418 - HYDROCARBON GAS PROCESSING
Title (en)
HYDROCARBON GAS PROCESSING
Title (de)
BEHANDLUNG VON KOHLENWASSERSTOFFGAS
Title (fr)
TRAITEMENT DE GAZ D'HYDROCARBURES
Publication
Application
Priority
- US 2010029331 W 20100331
- US 68961610 A 20100119
- US 18636109 P 20090611
- US 71739410 A 20100304
Abstract (en)
[origin: WO2010144172A1] A process and an apparatus are disclosed for the recovery of propane, propylene, and heavier hydrocarbon components from a hydrocarbon gas stream in a compact processing assembly. The gas stream is cooled, expanded to lower pressure, and supplied as the bottom feed to an absorbing means inside the processing assembly. A first distillation liquid stream is collected from the lower region of the absorbing means and supplied as the top feed to a mass transfer means inside the processing assembly. A first distillation vapor stream is collected from the upper region of the mass transfer means and cooled sufficiently to at least partially condense it, forming a residual vapor stream and a condensed stream. The condensed stream is supplied as the top feed to the absorbing means. A second distillation vapor stream is collected from the upper region of the absorbing means and directed into one or more heat exchange means inside the processing assembly to heat it while cooling the first distillation vapor stream. The heated second distillation vapor stream is combined with any of the residual vapor stream and the combined stream is directed into the one or more heat exchange means inside the processing assembly to heat it while cooling the gas stream. A second distillation liquid stream is collected from the lower region of the mass transfer means and directed into a heat and mass transfer means inside the processing assembly to heat it and strip out its volatile components. The quantities and temperatures of the feeds to the absorbing means are effective to maintain the temperature of the upper region of the absorbing means at a temperature whereby the major portions of the desired components are recovered in the stripped second distillation liquid stream.
IPC 8 full level
C10G 5/06 (2006.01); F25J 3/00 (2006.01); F25J 3/02 (2006.01)
CPC (source: EP KR US)
B01D 5/00 (2013.01 - KR); C10G 5/06 (2013.01 - EP US); F25J 3/00 (2013.01 - KR); F25J 3/0209 (2013.01 - EP US); F25J 3/0219 (2013.01 - EP US); F25J 3/0233 (2013.01 - EP US); F25J 3/0238 (2013.01 - EP US); F25J 3/0242 (2013.01 - EP US); C10G 2400/20 (2013.01 - EP US); F25J 2200/02 (2013.01 - EP US); F25J 2200/30 (2013.01 - EP US); F25J 2200/70 (2013.01 - EP US); F25J 2200/78 (2013.01 - EP US); F25J 2200/80 (2013.01 - EP US); F25J 2205/04 (2013.01 - EP US); F25J 2210/06 (2013.01 - EP US); F25J 2210/12 (2013.01 - EP US); F25J 2240/02 (2013.01 - EP US); F25J 2270/12 (2013.01 - EP US); F25J 2270/60 (2013.01 - EP US); F25J 2290/40 (2013.01 - EP US); F25J 2290/42 (2013.01 - EP US); Y02C 20/20 (2013.01 - US)
Citation (search report)
- [XYI] US 2006032269 A1 20060216 - CUELLAR KYLE T [US], et al
- [Y] US 3625017 A 19711207 - HOFFMAN MICHAEL L
- [YA] US 6205813 B1 20010327 - SHAH MINISH MAHENDRA [US], et al
- [A] WO 9615414 A1 19960523 - ELCOR CORP [US]
- [Y] US 2008115532 A1 20080522 - JAGER MARCO DICK [NL]
- See references of WO 2010144172A1
Designated contracting state (EPC)
AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HR HU IE IS IT LI LT LU LV MC MK MT NL NO PL PT RO SE SI SK SM TR
DOCDB simple family (publication)
WO 2010144172 A1 20101216; AR 076383 A1 20110608; AU 2010259245 A1 20120223; AU 2010259245 A2 20120510; AU 2010259245 B2 20160929; CA 2764282 A1 20101216; CA 2764282 C 20160105; CN 102803881 A 20121128; CN 102803881 B 20150819; CO 6480937 A2 20120716; EA 025641 B1 20170130; EA 201270003 A1 20120730; EP 2440867 A1 20120418; EP 2440867 A4 20180418; JP 2012529621 A 20121122; JP 5552160 B2 20140716; KR 101680922 B1 20161129; KR 20120028359 A 20120322; MX 2011013071 A 20120201; MX 344122 B 20161206; MY 161443 A 20170414; PE 20121402 A1 20121026
DOCDB simple family (application)
US 2010029331 W 20100331; AR P100101345 A 20100422; AU 2010259245 A 20100331; CA 2764282 A 20100331; CN 201080025495 A 20100331; CO 11177221 A 20111222; EA 201270003 A 20100331; EP 10786524 A 20100331; JP 2012514955 A 20100331; KR 20127000145 A 20100331; MX 2011013071 A 20100331; MY PI2011005771 A 20100331; PE 2011002074 A 20110331