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I-Catalyst

  • I-catalyst yokutshintsha ubushushu obuphantsi

    I-catalyst yokutshintsha ubushushu obuphantsi

    Isixhobo sokutshintsha ubushushu obuphantsi:

     

    Isicelo

    I-CB-5 kunye ne-CB-10 isetyenziselwa uGuquko kwi-synthesis kunye neenkqubo zokuvelisa i-hydrogen

    Ukusebenzisa amalahle, i-naphtha, irhasi yendalo kunye nerhasi ye-oyile yentsimi njengezokutya, ngakumbi iziguquli zokutshintsha ubushushu be-axial-radial..

     

    Iimpawu

    I-catalyst ineenzuzo zomsebenzi kwiqondo lokushisa eliphantsi.

    Ubuninzi bobuninzi obusezantsi, iCopper ephezulu kunye nomphezulu weZinc kunye namandla angcono omatshini.

     

    Iimpawu zomzimba kunye neekhemikhali

    Uhlobo

    CB-5

    CB-5

    CB-10

    Imbonakalo

    Iipilisi ezimnyama ze-cylindrical

    Ububanzi

    5mm

    5mm

    5mm

    Ubude

    5mm

    2.5mm

    5mm

    Unizi lolwapho kuyiwa khona

    1.2-1.4kg / l

    Amandla eRadialcrushing

    ≥160N/cm

    ≥130 N/cm

    ≥160N/cm

    CuO

    40±2%

    ZnO

    43±2%

    Iimeko zokusebenza

    Ubushushu

    180-260°C

    Uxinzelelo

    ≤5.0MPa

    Isantya sesithuba

    ≤3000h-1

    Umlinganiselo wegesi yomphunga

    ≥0.35

    Faka i-H2Scontent

    ≤0.5ppmv

    Ingenisa uCl-1umxholo

    ≤0.1ppmv

     

     

    I-ZnO desulfurization Catalyst enomgangatho ophezulu kunye nexabiso elikhuphisanayo

     

    I-HL-306 iyasebenza kwi-desulfurization yentsalela yeegesi eziqhekekayo okanye i-syngas kunye nokucocwa kweegesi zesondlo

    iinkqubo ze-organic synthesis. Ilungele ukusetyenziswa kobushushu obuphezulu (350–408°C) nangaphantsi (150–210°c).

    Iyakwazi ukuguqula isulfure ephilayo elula ngelixa ifunxa isulfure ye-inorganic kumsinga werhasi. Impendulo engundoqo ye

    inkqubo desulfurization imi ngolu hlobo lulandelayo:

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

    (2) Ukusabela kwe-zinc oxide kunye nezinye iikhompawundi zesulfure ezilula ngeendlela ezimbini ezinokwenzeka.

    2.iiPropati zoMzimba

    Imbonakalo ezimhlophe okanye ukukhanya-tyheli extrudates
    Ubungakanani besuntswana, mm Φ4×4–15
    Ukuxinana ngobuninzi, kg/L 1.0-1.3

    3.Umgangatho woMgangatho

    amandla okutyumza, N/cm ≥50
    ilahleko ekuphelelweni, % ≤6
    Ukutyhoboza umthamo wesulfure, wt% ≥28(350°C)≥15(220°C)≥10(200°C)

    4. IMeko yokuSebenza eqhelekileyo

    I-Feedstock: irhasi ye-synthesis, irhasi yentsimi yeoli, igesi yendalo, irhasi yamalahle. Inokuphatha umjelo werhasi ngesulfure engaphiliyo iphezulu

    njengoko 23g/m3 kunye isidanga esanelisayo zokucoca. Iyakwazi nokuhlambulula umjelo werhasi ukuya kuthi ga kwi-20mg/m3 yelula ngolo hlobo

    sulphur ephilayo njenge-COS ukuya ngaphantsi kwe-0.1ppm.

    5.Ilayisha

    Ukulayisha ubunzulu: I-L/D ephezulu (min3) iyacetyiswa. Ulungelelwaniso lweereactor ezimbini kuthotho kunokuphucula ukusetyenziswa

    ukusebenza kakuhle kwe-adsorbent.

    Ilayisha inkqubo:

    (1)Coca i-reactor phambi kokulayisha;

    (2)Beka iigridi ezimbini ezingenakutyiwa ezinobukhulu obuncinci bemesh kune-adsorbent;

    (3)Layisha umaleko oyi-100mm we-Φ10—20mm iisphere ezizii-refractory kwiigridi ezingenasici;

    (4)Jonga i-adsorbent ukususa uthuli;

    (5)Sebenzisa isixhobo esikhethekileyo ukuqinisekisa ukuhanjiswa ngokulinganayo kwe-adsorbent ebhedini;

    (6)Hlola ukufana kwebhedi ngexesha lokulayisha. Xa kufuneka umsebenzi wangaphakathi wereactor, ipleyiti yomthi kufuneka ibekwe kwi-adsorbent ukuze umqhubi ame phezu kwayo.

    7

    nokusasazwa komsinga werhasi.

    6.Ukuqalisa

    (1)Tshintsha inkqubo nge-nitrogen okanye ezinye iigesi ezingasebenziyo de i-oxygen concentration kwigesi ibe ngaphantsi kwe-0.5%;

    (2)Tshisa umjelo wesondlo ngenitrogen okanye igesi yefidi phantsi koxinzelelo olungqongileyo okanye oluphakamileyo;

    (3)Isantya sokufudumeza: 50°C/h ukusuka kubushushu begumbi ukuya kwi-150°C (ngenitrogen); I-150 ° C ye-2 h (xa i-idium medium ishushu

    itshintshelwe kwigesi yokutya), 30°C/h ngaphezulu kwe-150°C de ubushushu obufunekayo bufunyenwe.

    (4) Lungisa uxinzelelo ngokuthe chu de uxinzelelo lomsebenzi lufunyenwe.

    (5)Emva kokufudumeza kwangaphambili kunye nokuphakama koxinzelelo, inkqubo kufuneka iqale iqhutywe kwisiqingatha somthwalo we-8h. Emva koko phakamisa i

    layisha ngokuthe chu xa umsebenzi uzinza de usebenze ngokupheleleyo.

    7.Cima

    (1)Ubonelelo olungxamisekileyo lokuvala irhasi (i-oyile).

    Vala iivalvu zokungena neziphumayo. Gcina ubushushu kunye noxinzelelo. Ukuba kuyimfuneko, sebenzisa initrogen okanye ihydrogen-nitrogen

    igesi ukugcina uxinzelelo lokuthintela uxinzelelo olubi.

    (2) Ukutshintsha kwe-adsorbent ye-desulfurization

    Vala iivalvu zokungena neziphumayo. Yehlisa ngokuthe ngcembe iqondo lobushushu kunye noxinzelelo kwimeko ye-ambient. Emva koko wahlule i

    i-reactor desulfurization ukusuka kwinkqubo yemveliso. Buyisela ireactor ngomoya de uxinzeleko lweoksijini engaphezulu kwama-20% lufunyenwe. Vula i-reactor kwaye ukhuphe i-adsorbent.

    (3) Ukugcinwa kwezixhobo (ulungiso)

    Qwalasela inkqubo efanayo njengoko kubonisiwe ngasentla ngaphandle kokuba uxinzelelo kufuneka luthotywe nge-0.5MPa/10min kunye ne-temp.

    ithotywe ngokwemvelo.

    I-adsorbent engalayishwanga iya kugcinwa kwimigangatho eyahlukeneyo. Hlalutya iisampulu ezithathwe kumaleko ngamnye ukumisela

    ubume kunye nobomi benkonzo ye-adsorbent.

    8.Ukuthutha kunye nokugcinwa

    1

    ungcoliso.

    (2) Ukugingqika, ukungqubana kunye nokungcangcazela okunobundlobongela kufuneka kuphetshwe ngexesha lothutho ukunqanda ukugutyungelwa

    i-adsorbent.

    (3)Imveliso ye-adsorbent kufuneka ithintelwe ekudibaneni neekhemikhali ngexesha lokuthutha kunye nokugcinwa.

    (4) Imveliso ingagcinwa iminyaka emi-3-5 ngaphandle kokuwohloka kweempawu zayo ukuba itywinwe ngokufanelekileyo.

     

    Ukufumana iinkcukacha ezithe vetshe malunga neemveliso zethu, nceda ungalibazisi ukuqhagamshelana nam.

     

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  • I-Nickel Catalyst Njenge-Amoniya yokuBola kweCatalyst

    I-Nickel Catalyst Njenge-Amoniya yokuBola kweCatalyst

    I-Nickel Catalyst Njenge-Amoniya yokuBola kweCatalyst

     

    I-ammonia yokubola i-catalyst luhlobo lwe-sec. i-reaction catalyst, esekelwe kwi-nickel njengenxalenye esebenzayo kunye ne-alumina njengomphathi oyintloko. Isetyenziswa ikakhulu kwisityalo se-ammonia sohlaziyo lwesibini lwe-hydrocarbon kunye nokubola kwe-ammonia

    isixhobo, sisebenzisa i-hydrocarbon enegesi njengento ekrwada. Inozinzo oluhle, umsebenzi omhle, kunye namandla aphezulu.

     

    Isicelo:

    Isetyenziswa kakhulu kwisityalo se-ammonia sohlaziyo lwesibini lwe-hydrocarbon kunye nesixhobo sokubola kwe-ammonia,

    usebenzisa i-hydrocarbon enegesi njengemathiriyeli ekrwada.

     

    1. IiPropati zoMzimba

     

    Imbonakalo Isileyiti esingwevu raschig iringi
    Ubungakanani besuntswana, mmDiameter x Ubude x Ukutyeba 19x19x10
    Amandla okutyumza,N/isuntswana Min.400
    Ukuxinana ngobuninzi, kg/L 1.10 - 1.20
    Ilahleko ekuphelelweni, wt% Ubuninzi.20
    Umsebenzi weCatalytic 0.05NL CH4/h/g I-Catalyst

     

    2. Ukuqulunqwa kwemichiza:

     

    Umxholo weNickel (Ni), % Umz.14.0
    SiO2, % Ubuninzi.0.20
    Al2O3, % 55
    CaO, % 10
    Fe2O3, % Ubuninzi.0.35
    K2O+Na2O, % Ubuninzi.0.30

     

    Ukumelana nobushushu:ukusebenza kwexesha elide phantsi kwe-1200 ° C, ukunganyibiliki, ukungafihli, ukungahambi kakuhle, ukuzinza okuhle kunye namandla aphezulu.

    Ipesenti yezinto ezincinci ezisezantsi (ipesenti engaphantsi kwe-180N / i-particle): max.5.0%

    Isalathisi sokumelana nobushushu: ukungabambeleli kunye nokwaphuka kwiiyure ezimbini kwi-1300 ° C.

    3. Umqathango wokuSebenza

     

    Iimeko zenkqubo Uxinzelelo, MPa Iqondo lobushushu, °C Isantya sendawo yeammonia, hr-1
    0.01 -0.10 750-850 350-500
    Izinga lokubola kwe-ammonia 99.99% (min)

     

    4. Ubomi benkonzo: iminyaka emi-2

     

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  • Umgangatho ophezulu we-wholesale catalyst yoshishino lwe-hydrogenation

    Umgangatho ophezulu we-wholesale catalyst yoshishino lwe-hydrogenation

    I-Hydrogenation industry catalyst

     

    Nge-alumina njengomthwali, i-nickel njengeyona nto isebenzayo, i-catalyst isetyenziswa ngokubanzi kwi-aviation parafiation ukuya kwi-hydrogenation dearomatization, benzene hydrogenation ukuya kwi-cyclohexane, phenol hydrogenation ukuya kwi-cyclohexanol hydrotreating, i-hydrofining ye-industrial crude hexane, kunye ne-organic rated hydrogensphant hydrogensation ye-unsa. iihydrocarbons ezinevumba elimnandi, njengeoyile emhlophe, i-oyile ye-oyile ye-hydrogenation. Ingasetyenziselwa i-desulfurization yesigaba solwelo, kunye ne-agent ekhuselayo yesulfure kwinkqubo yokuguqulwa kwe-catalytic. I-catalyst inamandla aphezulu, umsebenzi ogqwesileyo, kwinkqubo yokusulungekisa i-hydrogenation, enokwenza i-hydrocarbon enevumba elimnandi okanye engaxutywanga phantsi ukuya kwinqanaba le-ppm. I-catalyst iyancipha urhulumente ozinzisayo unyango.

    Ngokuthelekisa, i-catalyst esetyenziswe ngempumelelo kwizityalo ezininzi kwihlabathi, ingcono kuneemveliso zasekhaya ezifanayo.
    Iimpawu zomzimba kunye neekhemikhali:

    Into Isalathiso Into Isalathiso
    Imbonakalo cylinder emnyama Ukuxinana ngobuninzi ,kg/L 0.80-0.90
    Ubungakanani besuntswana, mm Φ1.8×-3-15 Indawo engaphezulu,m2/g 80-180
    Amacandelo amachiza NiO-Al2O3 Amandla okutyumza ,N/cm ≥ 50

     

    Iimeko zovavanyo lomsebenzi:

    Iimeko zeNkqubo Uxinzelelo lwenkqubo
    Mpa    		 I-Hydrogen ye-Nitrogen yesantya sesithuba hr-1 Ubushushu
    °C    		 Isantya sendawo yePhenol
    hr-1    		 Hydrogen phenol ratio
    mol/mol
    Uxinzelelo oluqhelekileyo 1500 140 0.2 20
    Inqanaba lomsebenzi I-Feedstock: i-phenol, ukuguqulwa kwe-phenol min 96%

     

    Ukufumana iinkcukacha ezithe vetshe malunga neemveliso zethu, nceda uzive ukhululekile ukuqhagamshelana nam.

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  • I-Sulfur Recovery Catalyst AG-300

    I-Sulfur Recovery Catalyst AG-300

    I-LS-300 luhlobo lwe-sulfur recovery catalyst enendawo enkulu ethile kunye nomsebenzi ophezulu weClaus. Imisebenzi yayo ime kwinqanaba eliphezulu lamazwe ngamazwe.

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  • I-TiO2 Esekwe kwi-Sulfur Recovery Catalyst LS-901

    I-TiO2 Esekwe kwi-Sulfur Recovery Catalyst LS-901

    I-LS-901 luhlobo olutsha lwe-TiO2 esekelwe kwi-catalyst enezongezo ezikhethekileyo zokubuyisela isulfure. Imisebenzi yayo ebanzi kunye nezalathisi zobugcisa zifikelele kwinqanaba eliphezulu lehlabathi, kwaye ikwindawo ephambili kushishino lwasekhaya.

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  • I-AG-MS Spherical Alumina Carrier

    I-AG-MS Spherical Alumina Carrier

    Le mveliso yibhola emhlophe yebhola, i-non-toxic, i-tasteless, i-insoluble emanzini kunye ne-ethanol. Iimveliso ze-AG-MS zinamandla amakhulu, izinga lokunxiba eliphantsi, ubungakanani obuhlengahlengiswayo, umthamo wepore, indawo ethile yendawo, ubuninzi bobuninzi kunye nezinye iimpawu, zinokuhlengahlengiswa ngokweemfuno zazo zonke izikhombisi, ezisetyenziswa ngokubanzi kwi-adsorbent, i-hydrodesulfurization catalyst carrier, i-hydrogenation denitrification. catalyst carrier, CO sulfur resistant transformation catalyst carrier kunye nezinye iinkalo.

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  • I-AG-TS iAlumina Microspheres esebenzayo

    I-AG-TS iAlumina Microspheres esebenzayo

    Le mveliso yincinci emhlophe yebhola encinci, i-non-toxic, i-tasteless, i-insoluble emanzini kunye ne-ethanol. Inkxaso ye-AG-TS ye-catalyst ibonakaliswe yi-sphericity elungileyo, izinga eliphantsi lokunxiba kunye nokusabalalisa ubungakanani be-particle efanayo. Ukusabalalisa ubungakanani be-particle, umthamo we-pore kunye nommandla othile wendawo unokulungiswa njengoko kufuneka. Ifanelekile ukusetyenziswa njengomphathi weC3 kunye neC4 dehydrogenation catalyst.

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  • I-AG-BT Cylindrical Alumina Carrier

    I-AG-BT Cylindrical Alumina Carrier

    Le mveliso i-white cylindrical alumina carrier, ayinayo ityhefu, ayinancasa, ayinyibiliki emanzini kunye ne-ethanol. Iimveliso ze-AG-BT zinamandla amakhulu, izinga lokunxiba eliphantsi, ubungakanani obuhlengahlengiswayo, umthamo wepore, indawo ethile yendawo, ubuninzi bobuninzi kunye nezinye iimpawu, zinokuhlengahlengiswa ngokweemfuno zazo zonke izikhombisi, ezisetyenziswa ngokubanzi kwi-adsorbent, i-hydrodesulfurization catalyst carrier, i-hydrogenation denitrification. catalyst carrier, CO sulfur resistant transformation catalyst carrier kunye nezinye iinkalo.

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