-
Supplier: Accuris
Description: NICKEL, MOLYBDENUM, PHOSPHORUS, COBALT AND ALUMINUM IN FRESH CATALYSTS BY ICP-AES
-
Supplier: Accuris
Description: STANDARD TEST METHOD FOR TOTAL COBALT IN ALUMINA- BASE COBALT-MOLYBDENUM CATALYST BY THE POTENTIOMETRIC TITRATION METHOD
-
Supplier: ASTM International
Description: This method is for determining nickel, molybdenum, phosphorus and cobalt in fresh gamma-alumina supported catalysts; and nickel, molybdenum, phosphorus, cobalt and aluminum in fresh silica-alumina supported catalysts of known composition by Inductively
-
-
Supplier: ASTM International
Description: This method is for determining nickel, molybdenum, phosphorus and cobalt in fresh gamma-alumina supported catalysts; and nickel (Ni), molybdenum (Mo), phosphorus (P), cobalt (Co) and aluminum (Al) in fresh silica-alumina supported catalysts of known
-
Supplier: ASTM International
Description: 1.1 This test method covers the determination of cobalt (expressed as the oxide) in fresh cobalt-molybdenum catalyst, in the range of 0.5 to 10% cobalt oxide. 1.2 This standard does not purport to address all of the safety problems, if any associated with its use. It is
-
Supplier: Accuris
Description: STANDARD TEST METHOD FOR TOTAL COBALT IN ALUMINA-BASE COBALT-MOLYBDENUM CATALYST BY POTENTIOMETRIC TITRATION METHOD - INCLUDES STANDARD + REDLINE (PDF)
-
Supplier: ASTM International
Description: 1.1 This test method covers the determination of cobalt (expressed as the oxide) in fresh cobalt-molybdenum catalyst, in the range of 0.5 to 10?% cobalt oxide. 1.2 Units-The values stated in SI units are to be regarded as standard. No other units of measurement are
Find Suppliers by Category Top
More Information Top
Indicates content that may require registration and/or purchase.
-
Conceptual design of carbon nanotube processes
In the CNT-FBR process, carbon monoxide was reacted over a cobalt molybde- num catalyst in a fluidized bed reactor (FBR) at 950°C and 150 psi with a selectivity of 80% to single wall carbon nanotubes.
-
Production of aromatic hydrocarbons by the hydrogenative purification of liquid pyrolysis products
… the earlier techniques for treating liquid pyrolysis products an investigation was carried out of the hydrogenative improvement of these products by the two-stage method, using a palladium catalyst in the first stage and an aluminum- cobalt molybdenum catalyst in the second.
-
Coal to Olefins
For applications where it is desired to perform CO shift on raw syngas, a cobalt molybdenum catalyst can be used.
-
PRESSURIZED SOLID OXIDE FUEL CELL/GAS TURBINE POWER SYSTEM
The desulfurization process does not consume the cobalt molybde- num catalyst .
-
Effect of EDTA on hydrotreating activity of CoMo/γ-Al2 O3 catalyst
Supported nickel or cobalt molybde- num catalysts are used extensively in the hydrotreatment of petroleum feedstocks.
-
Interactions between catalytic hydrodesulfurization of thiophene and hydrodenitrogenation of pyridine
From studies on a supported nickel cobalt molybdenum catalyst at 750 to 1500 lb./sq.in.gauge, McIlvried (1971) concluded that the mechanism of pyridine denitrogenation is .
-
Catalytic carbon membranes for hydrogen production
cobalt molybdenum catalysts , which may be of interest based on other literature, are prepared by dissolving potassium acetate in ethanol and adding the appropriate quantity of this acetate/ethanol .
-
Applied over-all kinetics of hydrocracking of heavy petroleum distillates
The tabulated data for the parallel reaction scheme of crack- ing of feedstock and hydrodesulfurization show quite clearly that the hydrogenolysis (hydrodesulfurization) reactions on the alumino - cobalt molybdenum catalyst were mainly reactions on its active layer characterized by comparatively low activation energies …
-
Elucidation of hydrodesulfurization mechanism on molybdenum‐based catalysts using 35 S radioisotope pulse tracer methods
Keywords: presulfiding, 35S-labeled hydrogen sulfide, hydrodesulfurization, 35S-labeled dibenzothiophene, sulfur exchange, mechanism, labile sulfur, active site, cobalt molybdenum catalyst , alumina .
-
Ammonia
This process is a three-bed type reactor for hydrodesulfurizationthat converts the organic sulfur by reaction with hydrogen over a cobalt molybdenum catalyst to hydrogen sulfide and ad- BOrbB the hydrogen sulfide on zinc oxide.