Vis enkel innførsel

dc.contributor.authorBjerknes, V.nb_NO
dc.contributor.authorIversen, E.nb_NO
dc.contributor.authorBakke, T.nb_NO
dc.contributor.authorHelland, A.nb_NO
dc.contributor.authorSivertsen, B.nb_NO
dc.contributor.authorBekkestad, T.nb_NO
dc.contributor.otherBjerknes, V. - Project managernb_NO
dc.coverage.spatialVenezuelanb_NO
dc.date.accessioned2014-08-01T10:37:59Z
dc.date.available2014-08-01T10:37:59Z
dc.date.issued1995nb_NO
dc.identifier3270nb_NO
dc.identifier.isbn82-577-2793-8nb_NO
dc.identifier.issn1894-7948nb_NO
dc.identifier.urihttp://hdl.handle.net/11250/208308
dc.description.abstractThis preliminary EIA is a preconseption of the Vanadium and Nickel Recovery Processes, which will eventually be realized to extract 7.2tV as vanadium pentoxide and 1.3t Ni as nickelsulfide per day from fly ash, produced in a rate of 25 t/d in the CFAY plant. The daily effluent flow rate from the Vanadium recovery process is estimated to 240 m3, containing <200 mg TSP/l, <1 mg V/l and 16.2 g N/l, if untreated. The N- and V-content in the effluent may be recycling processes and diffenrent waste water treatment methods. the flue gas is estimated to contain 1500 ppm SOx (4290 mg/m³, emission rate 33 g/s), and 500 mg TSP/Nm3 (emission rate 2.3 g/s), provided baghouse treatment for particle reduction. The amounts of solid waste (sludge) from the vanadium recovery has not been quoted. The solid waste production of the nickel recovery process is estimated to 5, or alternatively 1.2 t/d, dependent on choice of additives. A landfill will have to be constructed to take care of the solid waste. Different mitigating actions are recommended to reduce gas emissions, effluent discharges, in particular the Nitrogen content, and the production rates and contaminant contents of solid waste, to ensure that legal and environmental acceptable limits are kept.nb_NO
dc.description.sponsorshipLagoven S.A. Refineria de Amuay, Judibana, Edo. Falcon, Venezuelanb_NO
dc.publisherNorsk institutt for vannforskningnb_NO
dc.relation.ispartofseriesNIVA-rapport;3270nb_NO
dc.rightsNavngivelse-IkkeKommersiell-DelPåSammeVilkår 3.0 Norgenb_NO
dc.rights.urihttp://creativecommons.org/licenses/by-nc-sa/3.0/no/nb_NO
dc.subjectolje og gassnb_NO
dc.titleEstudio de Impacto Ambiental de projecto VNRP. Preliminary Environmental Impact Assessment for a plant for the recovery of vanadium and nickel from Flexicoke (VNRP) at Refineria de Amuay, Venezuelanb_NO
dc.typeResearch reportnb_NO
dc.rights.holderNorsk institutt for vannforskning/Norwegian institute for water researchnb_NO
dc.subject.nsiVDP::Matematikk og naturvitenskap: 400nb_NO
dc.source.pagenumber64nb_NO
dc.subject.keywordenvironmental impactnb_NO
dc.subject.keywordassessmentnb_NO
dc.subject.keywordvanadiumnb_NO
dc.subject.keywordrecovertynb_NO
dc.subject.keywordnickelnb_NO
dc.subject.keywordrecoverynb_NO
dc.subject.keywordflexicokenb_NO
dc.relation.projectO-95032nb_NO


Tilhørende fil(er)

Thumbnail
Thumbnail

Denne innførselen finnes i følgende samling(er)

Vis enkel innførsel

Navngivelse-IkkeKommersiell-DelPåSammeVilkår 3.0 Norge
Med mindre annet er angitt, så er denne innførselen lisensiert som Navngivelse-IkkeKommersiell-DelPåSammeVilkår 3.0 Norge