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8/13/2019 HP Gas Processes HB 2012
http://slidepdf.com/reader/full/hp-gas-processes-hb-2012 1/2
This essential industry handbook contains flow diagrams
and descriptions of more than 130 commercially viable
gas processing technologies from 50 licensors. Featured
developments include drying, treating, contaminantremoval, cleanup, hydrogen, liquefied natural gas,
syngas, sulfur and gas-to-liquids. Each process description
includes a four-color flow diagram, as well as application,
operation, economic yield and licensor information. The
processes are indexed by process and contributing company.
This valuable reference tool should be available to every
engineer in the natural gas industry and will be distributed to all
paid subscribers of Hydrocarbon Processing magazine in specific
industries. Closing date for sponsorship is June 1, 2012.
Special supplement printed in September 2012
Gas ProcessesHandbook 2012
8/13/2019 HP Gas Processes HB 2012
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Premier Sponsors of Hydrocarbon Processing’s Gas Processes Handbook CD-ROM
Logo on CD-ROM sleeve (front) under Premier Sponsors Logo on splash screens under Premier Sponsors Active link from logo to website Listing of all processes from sponsor in handbook Posting at HydrocarbonProcessing.com for three years Five articles from Hydrocarbon Processing or articles
or papers from conferences, to be selected by sponsorfor inclusion on CD-ROM
A full-page, full-color ad in the July issue of HydrocarbonProcessing
50 copies of CD-ROM for sales purposes
This is a nonexclusive sponsorship (limited to five).Prices start at $16,390* gross agency commissionable.
Standard Sponsors of Hydrocarbon Processing’s Gas Processes Handbook CD-ROM Logo on CD-ROM sleeve (back) under Sponsors Logo on splash screens under Sponsors Active link from logo to website Listing of all processes from sponsor in handbook Two articles from Hydrocarbon Processing or articles or papers from conferences, to be selected by
sponsor for inclusion on CD-ROM Posting at HydrocarbonProcessing.com for three years
25 copies of CD-ROM for sales purposes
This is a nonexclusive sponsorship.Prices start at $4,540* gross agency commissionable.
*Contact your sales representative about available frequency discounts and full details.
Closing date for sponsorships is June 1, 2012
Sponsorships are secured on a first-response basis and are limited. Please indicate below your preferredsponsorship.
This is to confirm that _____________________________________ company will serve as a sponsor for theHydrocarbon Processing Gas Processes Handbook on CD-ROM to be published in September 2012.
Sponsorship Preference:❏ Premier Sponsor❏ Standard Sponsor
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Gas Processes 2009Gas Processes 2009 Company IndexProcess CategoriesHome
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Nitrogen recycle LNG liquefer
Application: Liquefaction of natural gas for peak shaving, product distri-bution or floating production storage and offloading (FPSO) applications.
Description: Natural gas is pretreated to remove water and carbon diox-ide (CO2). A fraction of the pretreated natural gas is used to regeneratethe CO2 /water (H2O) removal system. The remaining gas is cooled andthe heavier hydrocarbons (HC) removed in a knock-out (KO) drum ormulti-stage separation device. The resulting vapor product is then con-densed to produce LNG. Boil-off gas (BOG) from the LNG storage andthe collected heavier HCs are warmed in the exchangers and mixed withthe CO2 /H2O-laden regeneration gas. The resulting gas stream is thenreturned to the feed gas supply or a low-pressure fuel system.
Cooling is provided by a nitrogen (N2) recycle refrigeration system,which utilizes an N2 recycle compressor, an N2 compander and a cold boxthat houses the liquefaction heat exchangers. N 2 is compressed in the N2 recycle compressor and cooled in an aftercooler. A compander incorporatesa compression stage and an expansion stage on a single shaft. N2 droppingfrom high to low pressure across the expander wheel provides refrigerationand generates rotational force which is absorbed by the compressor wheelproviding a portion of the total nitrogen compression required. A portion ofthe N2 stream is expanded in the compander, providing part of the refrig-eration requirement. The remaining N2 is expanded with an expansion valveand provides the rest of the refrigeration required for liquefaction.
There are many variations in the specific configuration of the N 2 refrigeration cycle (pressures, number of expanders, expander arrange-ments, etc.). The configuration is driven by the need to develop the mostcost-effective solution for the plant size, final refrigeration temperaturerequired and project-specific economic evaluation criteria.
Economics: N2 recycle plants typically offer a lower capital solution forsmall plant applications and provide an attractive liquefication process op-tion for applications where hydrocarbon refrigerants may be undesirable.
Installations: Two units in operation in peak-shaving applications. Sixnitrogen recycle units under construction for LNG subcooling.
Reference: Bronfenbrenner, J. C. and W. R. Miller, “On a smaller scale,”LNG Industry , Winter 2008.
Licensor: Air Products and Chemicals, Inc.
LNGstorage
H2O/CO2removal
Liquefactionexchangers
Boil-off/react gas
to flow-by/fuel
BOGcompressor
LIC
Heavy HCK.O.drum
Feedgas
N2compressor
N2compander
Aftercooler Aftercooler
SPONSORSHIP RESERVATIONS AND MATERIALS DUE BY JUNE 1, 2012.
TO CONFIRM YOUR RESERVATION, FAX THIS FORM TO +1 (713) 525-4615 ATTN: CHERYL WILLIS
Gas ProcessesHandbook 2012