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I-Catalyst

  • I-catalyst yokushintsha kwezinga lokushisa eliphansi

    I-catalyst yokushintsha kwezinga lokushisa eliphansi

    I-catalyst yokushintsha kwezinga lokushisa eliphansi:

     

    Isicelo

    I-CB-5 ne-CB-10 isetshenziselwa Ukuguqulwa ekuhlanganiseni nasekukhiqizeni i-hydrogen izinqubo

    Kusetshenziswa amalahle, i-naphtha, igesi yemvelo kanye negesi yasensimini kawoyela njengemithombo yokudla, ikakhulukazi kuma-axial-radial low lokushisa shift converters.

     

    Izici

    I-catalyst inezinzuzo zomsebenzi ekushiseni okuphansi.

    Ukuminyana kwenqwaba ephansi, i-Copper ephakeme ne-Zinc surface namandla omshini angcono.

     

    Izakhiwo zomzimba namakhemikhali

    Uhlobo

    CB-5

    CB-5

    I-CB-10

    Ukubukeka

    Amaphilisi amnyama angama-cylindrical

    Ububanzi

    5mm

    5mm

    5mm

    Ubude

    5mm

    2.5mm

    5mm

    Ukuminyana ngobuningi

    1.2-1.4kg/l

    Amandla e-Radialcrushing

    ≥160N/cm

    ≥130 N/cm

    ≥160N/cm

    I-CuO

    40±2%

    ZnO

    43±2%

    Izimo zokusebenza

    Izinga lokushisa

    180-260°C

    Ingcindezi

    ≤5.0MPa

    Isivinini sesikhala

    ≤3000h-1

    I-Steam Gas Ratio

    ≥0.35

    Faka i-H2Scontent

    ≤0.5ppmv

    I-Inlet Cl-1okuqukethwe

    ≤0.1ppmv

     

     

    I-ZnO desulfurization Catalyst enekhwalithi ephezulu kanye nentengo yokuncintisana

     

    I-HL-306 isetshenziswa ekususeni i-sulfurization yamagesi aqhekeka ezinsalela noma ama-syngas kanye nokuhlanzwa kwamagesi okuphakelayo

    izinqubo ze-organic synthesis. Ilungele kokubili izinga lokushisa eliphezulu (350–408°C) nangaphansi (150–210°c) ukusetshenziswa.

    Ingakwazi ukuguqula isibabule semvelo esilula kuyilapho imunca isibabule esingaphili emgudwini wegesi. Ukusabela Main of the

    inqubo desulfurization imi kanje:

    (1) Ukusabela kwe-zinc oxide ne-hydrogen sulfide H2S+ZnO=ZnS+H2O

    (2) Ukusabela kwe-zinc oxide ngezinye izinhlanganisela ezilula zesibabule ngezindlela ezimbili ezingenzeka.

    2.Izakhiwo Zomzimba

    Ukubukeka ama-extrudates amhlophe noma aphuzi
    Usayizi wezinhlayiya, mm Φ4×4–15
    Ukuminyana ngobuningi, kg/L 1.0-1.3

    3.Izinga Lekhwalithi

    amandla okuchoboza, N/cm ≥50
    ukulahlekelwa ekulahlekelweni, % ≤6
    Umthamo wesibabule, wt% ≥28(350°C)≥15(220°C)≥10(200°C)

    4. Isimo Esijwayelekile sokuSebenza

    I-Feedstock: i-synthesis gas, igesi yenkundla kawoyela, igesi yemvelo, igesi yamalahle. Ingaphatha umfudlana wegesi ngesibabule esingaphili njengephezulu

    njengo-23g/m3 enedigri yokuhlanza egculisayo. Ingase futhi ihlanze ukusakaza kwegesi kufika ku-20mg/m3 kokulula kangako

    i-organic sulfur njenge-COS ukuya ngaphansi kuka-0.1ppm.

    5.Iyalayisha

    Ilayisha ukujula: I-L/D Ephakeme (min3) iyanconywa. Ukucushwa kwama-reactor amabili ochungechungeni kungathuthukisa ukusetshenziswa

    ukusebenza kahle kwe-adsorbent.

    Ilayisha inqubo:

    (1)Hlanza i-reactor ngaphambi kokulayisha;

    (2)Beka amagridi amabili angenabala anosayizi omncane we-mesh kune-adsorbent;

    (3)Layisha ungqimba ongu-100mm we-Φ10—20mm wamaphanorama-refractory kumagridi angenabala;

    (4)Skrini i-adsorbent ukuze ususe uthuli;

    (5)Sebenzisa ithuluzi elikhethekile ukuqinisekisa ukusatshalaliswa ngokulinganayo kwe-adsorbent embhedeni;

    (6)Hlola ukufana kombhede ngesikhathi sokulayisha. Lapho kudingeka ukusebenza kwangaphakathi kwereactor, Ipuleti lokhuni kufanele lifakwe kwi-adsorbent ukuze opharetha ame kulo.

    (7)Faka Igridi engagqwali enosayizi omncane we-mesh kune-adsorbent kanye nongqimba oluyi-100mm lwe-Φ20—30mm refractory sphere phezulu kombhede we-adsorbent ukuze uvimbele ukungena kwe-adsorbent futhi uqinisekise.

    ngisho nokusatshalaliswa komfudlana wegesi.

    6.Ukuqala

    (1)Shintsha uhlelo nge-nitrogen noma amanye amagesi angasebenzi kuze kube yilapho ukugcwala komoyampilo egesini kuba ngaphansi kuka-0.5%;

    (2)Shisisa kuqala umfudlana wesiphakeli nge-nitrogen noma igesi yokuphakelayo ngaphansi kwengcindezi ezungezile noma ephakeme;

    (3)Isivinini sokushisa: 50°C/h ukusuka kumazinga okushisa asekamelweni kuya ku-150°C (nge-nitrogen); 150°C amahora angu-2 (uma isisetshenziswa sokushisisa sinjalo

    ishintshelwe kwigesi yokudla), 30°C/h ngaphezu kuka-150°C kuze kufike izinga lokushisa elidingekayo.

    (4) Lungisa ingcindezi kancane kancane kuze kufinyelelwe ukucindezela kokusebenza.

    (5) Ngemuva kokushisisa kwangaphambili nokuphakama komfutho, isistimu kufanele iqale isetshenziswe ngomthwalo oyingxenye amahora angu-8. Bese uphakamisa i

    layisha kancane kancane lapho ukusebenza kuzinza kuze kube yilapho kusebenza ngokugcwele.

    7.Vala

    (1)Ukunikezwa kwegesi yokuvalwa okuphuthumayo (uwoyela).

    Vala ama-valve angenayo kanye ne-outlet. Gcina izinga lokushisa nengcindezi.Uma kunesidingo, sebenzisa i-nitrogen noma i-hydrogen-nitrogen

    igesi ukugcina ukucindezela ukuvimbela ukucindezela okubi.

    (2) Ukuguqulwa kwe-adsorbent ye-desulfurization

    Vala ama-valve angenayo kanye ne-outlet. Yehlisa kancane izinga lokushisa nokucindezela esimweni se-ambient. Bese wehlukanisa

    i-desulfurization reactor evela ohlelweni lokukhiqiza. Faka esikhundleni i-reactor ngomoya kuze kube yilapho kutholakala umoya-mpilo ongaphezu kwama-20%. Vula i-reactor bese ukhulula i-adsorbent.

    (3) Ukugcinwa kwezisetshenziswa (ukulungiswa kabusha)

    Qaphela inqubo efanayo njengoba kukhonjisiwe ngenhla ngaphandle kokuthi ukucindezela kufanele kwehliswe ku-0.5MPa/10min kanye nezinga lokushisa.

    kwehliswe ngokwemvelo.

    I-adsorbent engalayishiwe izogcinwa izendlalelo ezihlukene. Hlaziya amasampula athathwe kusendlalelo ngasinye ukuze unqume

    isimo kanye nempilo yesevisi ye-adsorbent.

    8.Ezokuthutha kanye nesitoreji

    (1) Umkhiqizo we-adsorbent upakishwe epulasitiki noma emiphongolweni yensimbi enolwelwesi lwepulasitiki ukuvikela umswakama kanye namakhemikhali.

    ukungcola.

    (2) Ukudilika, ukungqubuzana kanye nokudlidliza okunodlame kufanele kugwenywe ngesikhathi sokuthutha ukuze kuvinjelwe ukuguquguquka

    i-adsorbent.

    (3)Umkhiqizo we-adsorbent kufanele uvinjelwe ukuthintana namakhemikhali ngesikhathi sokuhamba nokugcinwa.

    (4) Umkhiqizo ungagcinwa iminyaka emi-3-5 ngaphandle kokuwohloka kwezakhiwo zawo uma uvalwe ngokufanelekile.

     

    Ukuze uthole imininingwane eyengeziwe mayelana nemikhiqizo yethu, sicela ungangabazi ukungithinta.

     

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  • I-Nickel Catalyst Njenge-Ammonia Ukubola I-Catalyst

    I-Nickel Catalyst Njenge-Ammonia Ukubola I-Catalyst

    I-Nickel Catalyst Njenge-Ammonia Ukubola I-Catalyst

     

    I-ammonia decomposition catalyst iwuhlobo lwesekhondi. i-react catalyst, esekelwe ku-nickel njengengxenye esebenzayo ene-alumina njengomthwali oyinhloko. Isetshenziswa kakhulu esitshalweni se-ammonia se-reformer yesibili ye-hydrocarbon nokubola kwe-ammonia

    idivayisi, isebenzisa i-hydrocarbon eyigesi njengempahla eluhlaza. Inokuqina okuhle, umsebenzi omuhle, namandla aphezulu.

     

    Isicelo:

    Isetshenziswa kakhulu esitshalweni se-ammonia se-reformer yesibili ye-hydrocarbon ne-ammonia yokubola,

    usebenzisa i-gaseous hydrocarbon njengento eluhlaza.

     

    1. Izakhiwo Zomzimba

     

    Ukubukeka Indandatho ye-raschig empunga
    Usayizi we-particle, mmDiameter x Ubude x Ubukhulu 19x19x10
    Amandla okuchoboza ,N/izinhlayiyana Ubuncane.400
    Ukuminyana ngobuningi, kg/L 1.10 – 1.20
    Ukulahlekelwa ekunciphiseni, wt% Ubukhulu.20
    Umsebenzi we-Catalytic 0.05NL CH4/h/g I-Catalyst

     

    2. Ukwakheka Kwamakhemikhali:

     

    Okuqukethwe kwe-Nickel (Ni), % Okuncane.14.0
    I-SiO2, % Ubukhulu.0.20
    I-Al2O3, % 55
    I-CaO, % 10
    I-Fe2O3, % Ubukhulu.0.35
    I-K2O+Na2O, % Ubukhulu.0.30

     

    Ukumelana nokushisa:ukusebenza isikhathi eside ngaphansi kwe-1200 ° C, ukungancibiliki, okungancibiliki, okungaguquki, ukuqina okuhle kwesakhiwo namandla aphezulu.

    Iphesenti lezinhlayiya zokuqina okuphansi (iphesenti elingaphansi kuka-180N/izinhlayiyana): max.5.0%

    Inkomba yokumelana nokushisa: ukunganamatheli nokuphuka emahoreni amabili ku-1300°C

    3. Isimo sokuSebenza

     

    Izimo zenqubo Ingcindezi, MPa Izinga lokushisa, °C Isivinini sesikhala se-Amonia, hr-1
    0.01 -0.10 750-850 350-500
    Izinga lokubola kwe-ammonia 99.99% (amaminithi)

     

    4. Impilo yesevisi: 2 iminyaka

     

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  • Ikhwalithi ephezulu ye-wholesale catalyst yemboni ye-hydrogenation

    Ikhwalithi ephezulu ye-wholesale catalyst yemboni ye-hydrogenation

    I-Hydrogenation industry catalyst

     

    Nge-alumina njengesithwali, i-nickel njengengxenye eyinhloko esebenzayo, i-catalyst Isetshenziswa Kakhulu kupharafini wendiza kuya ku-hydrogenation dearomatization, benzene hydrogenation kuya ku-cyclohexane, i-phenol hydrogenation kuya ku-cyclohexanol hydrotreating, i-hydrofining ye-industrial crude hexane, kanye ne-organic-rated hydrogensphant hydrocarbonation ye-unsa. ama-hydrocarbon anephunga elimnandi, njengamafutha amhlophe, i-lube oil hydrogenation. Ingase futhi isetshenziselwe i-desulfurization yesigaba se-liquid ephumelelayo, kanye ne-sulfur protective agent enqubweni yokuguqula i-catalytic. I-catalyst inamandla aphezulu, umsebenzi omuhle kakhulu, enqubweni yokucwenga i-hydrogenation, engenza i-hydrocarbon enamakha noma engagcwalisiwe yehle iye ezingeni le-ppm. I-catalyst iyancipha isimo esizinzisa ukwelashwa.

    Ngokuqhathanisa, i-catalyst esetshenziswe ngempumelelo ezitshalweni eziningi emhlabeni, ingcono kunemikhiqizo yasekhaya efanayo.
    Izakhiwo zomzimba namakhemikhali:

    Into Inkomba Into Inkomba
    Ukubukeka isilinda esimnyama Ukuminyana ngobuningi ,kg/L 0.80-0.90
    Usayizi wezinhlayiya, mm Φ1.8×-3-15 Indawo engaphezulu, m2/g 80-180
    Izingxenye zamakhemikhali I-NiO-Al2O3 Amandla okuchoboza ,N/cm ≥ 50

     

    Izimo zokuhlola umsebenzi:

    Izimo Zenqubo Ingcindezi yesistimu
    Mpa    		 I-Hydrogen Nitrogen space velocity hr-1 Izinga lokushisa
    °C    		 Isivinini se-Phenol isikhala
    hr-1    		 Isilinganiso se-hydrogen phenol
    mol/mol
    Ingcindezi evamile 1500 140 0.2 20
    Ileveli Yomsebenzi I-Feedstock: i-phenol, ukuguqulwa kwe-phenol min 96%

     

    Ukuze uthole imininingwane eyengeziwe mayelana nemikhiqizo yethu, sicela ukhululeke ukuxhumana nami.

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  • I-Sulfur Recovery Catalyst AG-300

    I-Sulfur Recovery Catalyst AG-300

    I-LS-300 iwuhlobo lwe-catalyst yokubuyisela isibabule enendawo enkulu ethize kanye nomsebenzi ophezulu weClaus. Ukudlala kwayo kusezingeni eliphezulu lamazwe ngamazwe.

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  • I-TiO2 Based Sulfur Recovery Catalyst LS-901

    I-TiO2 Based Sulfur Recovery Catalyst LS-901

    I-LS-901 iwuhlobo olusha lwe-TiO2 esekelwe i-catalyst enezithasiselo ezikhethekile zokuthola kabusha isulfure. Ukusebenza kwayo okuphelele kanye nezinkomba zobuchwepheshe sekufinyelele ezingeni elithuthukile emhlabeni, futhi isendaweni ehamba phambili embonini yasekhaya.

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  • I-AG-MS Spherical Alumina Carrier

    I-AG-MS Spherical Alumina Carrier

    Lo mkhiqizo uyizinhlayiya zebhola elimhlophe, elingenabuthi, alinambitheki, elingancibiliki emanzini ne-ethanol. Imikhiqizo ye-AG-MS inamandla amakhulu, izinga lokugqoka eliphansi, usayizi olungisekayo, ivolumu yembotshana, indawo ethile, ukuminyana kwenqwaba nezinye izici, ingalungiswa ngokuya ngezidingo zazo zonke izinkomba, isetshenziswa kabanzi ku-adsorbent, i-hydrodesulfurization catalyst carrier, i-hydrogenation denitrification. catalyst carrier, CO sulfur resistant transformation catalyst carrier kanye nezinye izinkambu.

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  • I-AG-TS Yasebenza I-Alumina Microspheres

    I-AG-TS Yasebenza I-Alumina Microspheres

    Lo mkhiqizo uyizinhlayiyana ezimhlophe zebhola elincane, elingenabuthi, alinambitheki, elingancibiliki emanzini ne-ethanol. Ukusekelwa kwe-AG-TS kwe-catalyst kubonakala ngokuyindilinga okuhle, izinga eliphansi lokugqoka kanye nokusabalalisa usayizi wezinhlayiyana ezifanayo. Ukusabalalisa usayizi wezinhlayiyana, ivolumu ye-pore kanye nendawo ethile yendawo ingalungiswa njengoba kudingeka. Ilungele ukusetshenziswa njengesithwali se-C3 ne-C4 dehydrogenation catalyst.

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  • I-AG-BT Cylindrical Alumina Carrier

    I-AG-BT Cylindrical Alumina Carrier

    Lo mkhiqizo uyisithwali se-alumina esimhlophe esiyicylindrical, esingenabuthi, asinambitheki, asincibiliki emanzini ne-ethanol. Imikhiqizo ye-AG-BT inamandla amakhulu, izinga lokugqoka eliphansi, usayizi olungisekayo, ivolumu yembotshana, indawo ethize, ukuminyana kwenqwaba nezinye izici, ingalungiswa ngokuya ngezidingo zazo zonke izinkomba, isetshenziswa kabanzi ku-adsorbent, i-hydrodesulfurization catalyst carrier, i-hydrogenation denitrification. catalyst carrier, CO sulfur resistant transformation catalyst carrier kanye nezinye izinkambu.

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