30results about How to "High removal depth" patented technology

The invention relates to a multi-element alloy getter for purifying krypton and xenon, and a preparation method of the getter, and the getter can be used for solving the problems that the existing getter is poorer in pertinence, insufficient in handling capacity, high in energy consumption, easy in pulverization and short in service life, and the like. The multi-element alloy getter comprises the following components: 50-65% of zirconium, 10-20% of aluminum, 5-10% of iron, 2-10% of titanium, 3-5% of lanthanum, 3-5% of silicon and the balance of unavoidable impurities. The method comprises the steps of pretreatment of alloy simple substances, alloy smelting and alloy crushing. The getter can meet the purity requirement of high-purity krypton and xenon (99.999%), is large in fluctuation ranges of anti-raw gas fluorocarbon and oxygen nitrogen compound, large in raw gas impurity adsorption capacity, high in raw gas impurity removal depth, wide in service temperature range (300-1000 DEG C) and long in service life, and is not pulverized.

The invention discloses a combined process for conversion of residual oil. The combined process comprises the following steps: (1) allowing a residual oil raw material to enter into a solvent deasphalting unit so as to obtain deasphalted oil and de-oiled asphalt; (2) mixing the de-oiled asphalt obtained in step (1) with heavy distillate oil of a catalytic cracking unit and allowing an obtained mixture to enter into a fluidized bed hydrotreatment unit for fluidized bed hydrotreatment; (3) mixing an effluent of fluidized bed hydrotreatment obtained in the step (2) with the deasphalted oil and carrying out fixed bed hydrotreatment, wherein generated oil of an effluent of fixed bed hydrotreatment is used as a raw material for the catalytic cracking unit; and (4) mixing the de-oiled asphalt with a catalytic heavy fraction obtained after dry gas, liquefied gas and catalytic gasoline are separated from an effluent of a catalytic cracking reaction and subjecting an obtained mixture to fluidized bed hydrotreatment. Compared with the prior art, the combined process provided by the invention has the advantages of wide sources of the raw materials, low equipment investment, stable operation, a long operation period and a good synergistic and coordination effect.

The present invention discloses a residual oil hydrogenation treatment and catalytic cracking combination method. According to the method, the residual oil hydrogenation treatment process comprises two hydrogenation protection reactors, wherein the two hydrogenation protection reactors are arranged in parallel connection, the feed material of the first hydrogenation protection reactor is the residual oil raw material, and the feed material of the second hydrogenation protection reactor is the catalytic cracking heavy fraction; the effluents of the two reactors are mixed, and the resulting mixture enters a hydrogenation treatment reaction zone to carry out a hydrogenation reaction; the effluent of the hydrogenation reaction is subjected to gas-liquid separation, wherein the resulting gas phase is circularly adopted for the hydrogenation reaction, and the liquid phase directly enters a catalytic cracking apparatus without fractionation; the effluent of the catalytic cracking reaction is separated to obtain dry gas, liquefied gas, catalytic cracking gasoline, and catalytic cracking heavy fraction after catalytic cracking of the gasoline, wherein the catalytic cracking heavy fraction is adopted as the feed material of the second hydrogenation protection reactor. With the method, the operating period of the residual oil hydrogenation apparatus can be prolonged, the maximum amount of the catalytic cracking gasoline can be produced, and the equipment investment can be saved.

The invention discloses a carbon four-component selective hydrogenation catalyst and a preparation method taking into account the depth of butadiene removal and the yield of 1-butene. The carbon four-component selective hydrogenation catalyst consists of active components, selectivity The active component is Pd, the selective additives are Ru and Ag, and the support carrier is γAl 2 o 3 , CeO 2 -ZrO 2 and attapulgite; the Pd is 0.05% to 1.5% of the mass of the support carrier, the selective additives Ru and Ag are respectively 0.05 to 2% of the mass of the support carrier, and the γAl in the support carrier 2 o 3 , CeO 2 -ZrO 2 , The quality of attapulgite is 50~60%, 30~40%, 10~20% respectively.

The invention relates to a renewable microporous-mesoporous composite material adsorbent, a preparing method thereof and applications of the adsorbent. The method includes steps of firstly preparing a modified FAU molecular sieve secondary unit; preparing a mesoporous gel mixture; mixing the modified FAU molecular sieve secondary unit with the mesoporous gel mixture; then performing microwave crystallization at 60-120 DEG C; washing, centrifuging and drying the mixture; then performing thermal oxidation treatment to remove a demolding agent, namely to prepare a recoverable microporous-mesoporous composite material; and preparing the composite material into the adsorbent having a certain particle size distribution through tabletting molding or extrusion molding or ball rolling molding. Compared with the prior art, the composite material adsorbent has characteristics of a high synthesis speed, low energy consumption, and the like. Compared with alcohol ether adsorbents at present, the composite material adsorbent is high in impurity adsorption depth, high adsorption capacity, and low in heat effect and has good physical and chemical properties.