CN103771443B

CN103771443B - The method of modifying of Y zeolite and the preparation method of catalytic cracking catalyst

Info

Publication number: CN103771443B
Application number: CN201210398974.0A
Authority: CN
Inventors: 张杰潇; 周灵萍; 张蔚琳; 田辉平; 朱玉霞; 许明德
Original assignee: Sinopec Research Institute of Petroleum Processing; China Petroleum and Chemical Corp
Current assignee: Sinopec Research Institute of Petroleum Processing; China Petroleum and Chemical Corp
Priority date: 2012-10-19
Filing date: 2012-10-19
Publication date: 2016-03-23
Anticipated expiration: 2032-10-19
Also published as: CN103771443A

Abstract

The invention discloses the method for modifying of Y zeolite and the preparation method of catalytic cracking catalyst.The method of modifying angle employed between multiple bearing of trend and the axial direction of middle cylinder of this Y zeolite is the stoving oven of the flight at acute angle or obtuse angle, the roasting condition of improvement and second time give-and-take conditions, and the maturing temperature of described Y zeolite is 400 to being less than 500 DEG C; Described second time is exchanged for and washes with water or acid solution washing, and the temperature that described second time exchanges is 20-70 DEG C.Y zeolite prepared by aforesaid method has lower Na ₂o content, and the catalytic cracking catalyst obtained by this Modified Zeolite Y has better catalytic performance.

Description

The method of modifying of Y zeolite and the preparation method of catalytic cracking catalyst

Technical field

The present invention relates to a kind of method of modifying of Y zeolite and the preparation method of catalytic cracking catalyst.

Background technology

Catalytic cracking catalyst is secondary processing process important in refining of petroleum---the catalyzer that catalytic cracking process uses.In catalytic cracking catalyst, Y zeolite is a kind of application material widely, is also very important active ingredient simultaneously.The performance of Y zeolite directly has influence on the reactivity worth of catalytic cracking catalyst.In order to improve the result of use of Y zeolite, according to different needs, different modifications can be carried out to reach the requirement of use to Y zeolite.Existing many technology propose the method to Y zeolite modification.

Usually, in the preparation of catalytic cracking catalyst, require the Na of catalytic cracking catalyst ⁺content meets the requirement that catalytic cracking is produced.And the Na in catalytic cracking catalyst ⁺usually brought into by Y zeolite component, therefore reduce Na in Y zeolite component ⁺it is just particularly important that content meets demand of industrial production to final catalytic cracking catalyst use.Generally by the Y zeolite that Hydrothermal Synthesis is produced, due to Na ⁺content height is also often called NaY molecular sieve.Reduce the Na in Y molecular sieve ⁺content, by ammonium salt solution exchange, roasting, with NH ₄ ⁺part replaces Na ⁺, then wash removal and carry out, obtain Na ⁺the Y zeolite of the modification that content reduces.Better Na in Y molecular sieve is reduced in order to reach ⁺effect, industrial usual employing twice exchange and bakes to burn the article process, namely twice ammonium salt exchanges.

Roasting reduces Na in Y zeolite ⁺the important step of content, its effect makes Y zeolite generation dealuminzation, dehydroxylation, silicon migration, deamination, crystalline rearrangement react and cause part Al-O to be replaced by Si-O, thus make that the structure cell of Y zeolite shrinks, silica alumina ratio improves, structural stability improves, and also makes Na simultaneously ⁺the position exchanged by difficulty migrates to the position easily exchanged, and therefore roasting effect is to the Y zeolite performance of modification, especially Na ⁺exchange to remove the quality of degree most important.

Na in reduction Y zeolite ⁺in the process of content, the roasting quality of Y zeolite is mainly relevant with the stoving oven used.In prior art, for material, as the powder such as catalyzer, Y zeolite, visual plant that is in enormous quantities, baked for producing continuously is rotary type stoving oven.In roasting process, stoving oven is reached maturing temperature by heating, and at this temperature, material by stoving oven, completes the roasting of material within the regular hour.Material joins in cylindrical shell by opening for feed, and along with the rotation of cylindrical shell, material is reversed.The inner barrel of general rotary type stoving oven has the structure such as flight, weir plate, and flight is to parallel and along the axially extended straight plate of cylindrical shell, weir plate is the annular plate along cylindrical shell circumference with drum shaft.Flight in cylindrical shell helps material turning, and weir plate prevents that material is too fast passes through stoving oven.The installation of cylindrical shell must have certain inclination angle, and namely opening for feed is higher than discharge port, thus makes material rely on the effect of gravity, is moved, realizes automatic discharging, complete serialization automatic-baking by opening for feed to discharge port.But the stoving oven of prior art can not control material from the process being fed to discharging, the discharging time of material is random mean value, and the real residence time difference specific to each material is just very large, therefore causes the roasting quality of material inconsistent.In addition, in this stoving oven middle cylinder body, space utilization is insufficient, and roasting heating efficiency is low.But in roasting process, ensure that material all stands identical roasting time, make material roasting even, to material, particularly to the stably manufactured of Y zeolite and catalytic cracking catalyst, obtain good roasting quality particularly important, therefore control material even at roasting kiln roasting, stand identical and enough roasting time, become the key that quality of material controls.Control the even roasting of material in addition, also need more effectively to utilize an intracorporeal space and roasting heat.

CN2861917Y discloses a kind of continuous rotation roasting furnace, and principal character is, be made up of cylindrical shell and spirochete, spirochete is arranged on inner barrel, in aggregates to discharge port shape from opening for feed with cylindrical shell.During use, cylindrical shell forwards to together with spirochete.The tube structure of this continuous rotation roasting furnace when spirochete is screw-blade as shown in Figure 2.This utility model can control and ensure that roasting material has identical roasting time and quality preferably, but due to gravity, material is always deposited in the Lower Half of cylindrical shell, an intracorporeal space can not be full of, the upset of material is also insufficient, and roasting heat is under-utilized, affects roasting quality.

CN101149214A discloses a kind of rotary tube type roasting furnace, primarily of feeding tube, charging end socket, body of heater, revolution boiler tube, boiler tube revolution transmission system, shedding mechanism and temperature controlling system composition, wherein body of heater is made up of heating system, thermal insulation layer and burner hearth, revolution boiler tube is arranged in burner hearth, it is characterized in that, described revolution boiler tube is separated at least two cavitys along boiler tube tube wall, and each cavity communicates vertically.During use, treat that roasting material is sent in revolution boiler tube.The stoving oven that this invention provides, for improving same volume calcination process amount and reducing energy consumption, does not provide the method improving roasting effect.

CN2611844Y discloses a kind of electrical heating rotary cylinder roasting furnace, mainly be made up of feed box, stove cylinder, material feeding box, transmission system, support roller gear wheel group, support roller group, temp measuring system, it is characterized in that, stove cylinder passes across burner hearth, high-temperature sealing material is adopted to seal between burner hearth and stove cylinder, embed pressing plate, make sealing material be close to hearth wall; Stove cylinder, built with temp measuring system, is fixed together with feed box; Inboard wall of burner hearth lays high-temperature refractory, and electric stove wire is equipped with in bottom; Burner hearth adopts split type; There are feed box and material feeding box in two ends, stove cylinder left and right, feed box and have feed box to seal between material feeding box and stove cylinder and material feeding box seals, and support roller group and support roller gear wheel component occupy in the both sides of burner hearth.This invention aims to provide employing Electric heating, reduces fuel oil to the pollution of environment, can also realize the automatic control of computer operation to revolving drum roasting in-furnace temperature.This utility model does not provide the method can improving molecular sieve roasting effect, barrel space and roasting Btu utilization.

US5997289 discloses a kind of equipment for particulate material process, this equipment comprises the rotating cylinder of horizontal extension, at least one position of described cylinder inner wall at least arranges two row's waviness battens, the horizontal axis orthogonal of described batten and described cylinder, each described batten is that V-shape is installed, the space being aligned of summit between the described batten of two rows of described V-shape, described cylinder has gas feed, material inlet, outlet for product, and the mechanism that described cylinder is rotated by described zenith directions.This invention improves the mixed effect of material particles, but does not improve the consistence of material roasting.

As can be seen here, in Y zeolite modification and catalytic cracking catalyst preparation, Na is reduced ⁺content is the key of producing qualified product.Roasting is one of them important preparation link, is Na ⁺exchange the influence factor of removal degree, wherein stoving oven is most important to roasting quality effect.The stoving oven used in the industrial production of existing Y zeolite " two hand over a roasting ", can not provide good roasting to control, as roasting time controls and material roasting homogeneity, cause Y zeolite roasting effect poor, affect final Na ⁺the reduction of content.In addition also there is the problem of inner barrel space and roasting Btu utilization difference in existing stoving oven.In order to obtain the roasting effect of hope, produce Na ⁺the Y zeolite that content is qualified, prior art is taked to improve maturing temperature and is greater than 500 DEG C, carries out the method that second time ammonium salt exchanges, but causes temperature high energy consumption large, the shortcoming of at least twice ammonia nitrogen waste water at 80-90 DEG C.

The Na of the Y zeolite of modification ⁺content is defective, affects the preparation of catalytic cracking catalyst and the performance of catalyzer further.In prior art, normal needs improves maturing temperature in catalyst preparing, and high-temperature wash and increasing bath water amount reach and reduce Na in catalyzer further ⁺content reaches the requirement of industrial application, to keep the performance of catalyzer.Usually prepare the maturing temperature of catalytic cracking catalyst higher than 400 DEG C, the temperature of water washing is 70-80 DEG C, water in washing: agent (weight) is than being usually greater than 20:1.Therefore, cause energy consumption in the preparation of catalytic cracking catalyst high, the problem that washing water loss is large.

In sum, there is Na in reduction Y zeolite and catalytic cracking catalyst ⁺the problem of content weak effect.This wherein the step such as roasting, washing to Na ⁺the reduction impact of content is larger.The weak effect such as roasting, washing, not only Na in prior art ⁺content reduces weak effect, and in producing, energy consumption is high, ammonia nitrogen waste water discharge is many, and catalyst detergent water loss is large.

Summary of the invention

The object of the invention is to overcome in Y zeolite modification and catalytic cracking catalyst preparation and there is the problem reducing sodium ions content weak effect, the method for modifying of Y zeolite and the preparation method of catalytic cracking catalyst are provided.

The present inventor finds under study for action, in the method for modifying of Y zeolite, by using the stoving oven improved, can control the roasting time of Y zeolite well, the roasting effect obtained.Lower maturing temperature can be used, and adopt the second time of low temperature washing or acid solution washing to exchange, the Na on Y zeolite ⁺can be exchanged better, realized the Na of Y zeolite ⁺content reduces.And in the preparation of catalytic cracking catalyst, be the improvement of roasting effect equally, lower maturing temperature and low temperature, low-water wash can be used, the catalyst n a of acquisition ⁺content is low, and catalytic performance improves.In above-mentioned modification and preparation process, production energy consumption reduces, and ammonia nitrogen waste water discharge reduces, and bath water amount also reduces, and achieves consumption reduction and reduces discharging.

To achieve these goals, the invention provides a kind of method of modifying of Y zeolite, the method comprises carries out first time exchange, drying, roasting, second time exchange and filtration successively by Y zeolite, carry out the stoving oven that first time exchanges, the roasting of dried described Y zeolite uses successively to comprise body of heater 1 and be arranged on the cylindrical shell 2 in described body of heater 1, described cylindrical shell 2 comprises feed end 24, middle cylinder 20 and discharge end 25 successively; The inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4; Angle between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, and does not contact between adjacent two flights 3; Carry out that first time exchanges, the roasting of dried described Y zeolite comprises carrying out successively that first time exchanges, dried described Y zeolite sends in the described cylindrical shell 2 that is in maturing temperature from the opening for feed 21 of described cylindrical shell 2, and discharge from discharge port 22 successively; Carry out that first time exchanges, the temperature of the roasting of dried described Y zeolite is 400 to being less than 500 DEG C successively; Described second time is exchanged for and washes with water or acid solution washing, and the temperature that described second time exchanges is 20-70 DEG C.

Present invention also offers a kind of preparation method of catalytic cracking catalyst, the method comprises: Y zeolite is carried out modification, obtain the Y zeolite of modification, and with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of the modification of 5-50 % by weight, 0.5-50 % by weight carries out plastic with the clay mixture of the binding agent of oxide basis and 5-90 % by weight, and the plastic product obtained is carried out drying successively, roasting, washing, obtain product of roasting, the temperature of the roasting of dried described plastic product is 350-400 DEG C, described product of roasting washs successively, filter and drying, the washing of described product of roasting is washing, the temperature of the washing of described product of roasting is 20-45 DEG C, be 5-20:1 for the water of the washing of described product of roasting and the weight ratio of described product of roasting, the method of modifying of the Y zeolite that described method of Y zeolite being carried out modification provides for the invention described above.

Present invention also offers a kind of preparation method of catalytic cracking catalyst, the method comprises: with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of 5-50 % by weight, 0.5-50 % by weight carries out plastic successively with the clay mixture of the binding agent of oxide basis and 5-90 % by weight, dry, roasting, obtain calcining matter, carry out plastic successively, the temperature of the roasting of dried described mixture is 350-400 DEG C, described calcining matter washs successively, filter and drying, the washing of described calcining matter is washing, the temperature of the washing of described calcining matter is 20-45 DEG C, be 5-20:1 for the water of the washing of described calcining matter and the weight ratio of described calcining matter, carry out successively plastic, dried described mixture roasting use stoving oven comprise body of heater 1 and be arranged on the cylindrical shell 2 in described body of heater 1, described cylindrical shell 2 comprises feed end 4, middle cylinder 20 and discharge end 25 successively, the inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4, angle between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, and does not contact between adjacent two flights 3, carry out plastic successively, the roasting of dried described mixture comprises carrying out plastic successively, dried described mixture is sent in the described cylindrical shell 2 that is in maturing temperature from the opening for feed 21 of described cylindrical shell 2, and discharge from discharge port 22.

In the method for modifying of Y zeolite provided by the invention, flight 3 and weir plate 4 are set on the inwall of the middle cylinder 20 of stoving oven, and edge is from feed end 24 to the direction of discharge end 25, the bearing of trend of flight 3 and the axial shape of middle cylinder 20 at a certain angle, when middle cylinder 20 drives flight 3 and weir plate 4 rotates to the motion generation effect of Y zeolite, increase the back-mixing of Y zeolite, thus make the Y zeolite carrying out roasting in middle cylinder 20, from opening for feed 21 to the process of discharge port 22, the motion conveying of Y zeolite is subject to the control of flight 3 and weir plate 4, reach the object improving roasting.The rotating speed of adjustment middle cylinder 20 just can control Y zeolite and move in cylindrical shell 2 time of carrying, and also just controls the time that Y zeolite stands roasting; Rotating speed is certain, and the roasting time of Y zeolite in stoving oven just determines, and in result Y zeolite, each several part is all subject to identical calcination process, obtains same roasting effect.In addition, due to the setting of flight 3 and weir plate 4 enable Y zeolite under the drive of flight 3 and weir plate 4 with the whole contact internal walls of cylindrical shell 2, while such Y zeolite is controlled conveying, also be forced to stir and the roasting heat that provides of the inwall of the internal space and middle cylinder 20 that make full use of middle cylinder 20, obtain better Y zeolite roasting effect.The Na of the Y zeolite Z1 of modification in embodiment 1 ₂o content is 1.2 % by weight.Adopt the stoving oven and lower maturing temperature that improve, and second time is exchanged for the lower water washing of temperature or acid solution washing, and unconventional ammonium salt exchanges, enforcement of the present invention can obtain the qualified Y zeolite Industrial products that sodium ions content reduces, also can realize reducing energy consumption, reduce the discharge of ammonia nitrogen waste water.

In the preparation method of a kind of catalytic cracking catalyst provided by the invention, because the sodium ions content of the Y zeolite of modification is low, the sodium ions content of the catalytic cracking catalyst prepared is also low.The Na of the catalytic cracking catalyst C1 of preparation in embodiment 5 ₂o content is 0.07 % by weight.Thus improving the performance of catalytic cracking catalyst, the pore volume as C1 is 0.40mLg ^-1be 283m with specific surface area ²g ^-1, the catalytic cracking catalyst D3 comparing ratio 3 preparation obviously increases, and the micro-activity of C1 is 82%(800,4h simultaneously) also significantly improve.

The Y zeolite of the modification that the sodium ions content prepared with the method for modifying of Y zeolite provided by the invention reduces, carry out the preparation of catalytic cracking catalyst provided by the invention, because the sodium ions content in the Y zeolite of modification is low, again due to prepare catalytic cracking catalyst roasting in have employed the stoving oven of improvement, thus make the preparation process of catalytic cracking catalyst adopt lower maturing temperature to reduce energy consumption, also make the washing temperature in washing and the washing water yield all reduce.

In the preparation method of another kind of catalytic cracking catalyst provided by the invention, use the stoving oven improved, maturing temperature reduces, and save energy consumption, the wash temperature that is correspondingly in the suds and bath water amount also all reduce, and decrease water content consumption.

Therefore, the method of modifying of Y zeolite provided by the invention and the preparation method of catalytic cracking catalyst, improve preparation flow, employ the stoving oven that roasting effect is improved, solve sodium ions content in Y zeolite and catalytic cracking catalyst and reduce the problem of weak effect; And make in the final catalytic cracking catalyst obtained, pore volume and specific surface area obviously increase, and micro-activity significantly improves, and the Catalytic Cracking Performance of acquisition is better.In addition, method provided by the invention also achieves the water loss reducing energy consumption, reduce ammonia nitrogen waste water discharge and catalyst detergent.

Other features and advantages of the present invention are described in detail in embodiment part subsequently.

Accompanying drawing explanation

Accompanying drawing is used to provide a further understanding of the present invention, and forms a part for specification sheets, is used from explanation the present invention, but is not construed as limiting the invention with embodiment one below.In the accompanying drawings:

Fig. 1 is the structural representation of a kind of preferred implementation of the stoving oven that the present invention adopts;

Fig. 2 is the structural representation of the another kind of preferred implementation of the stoving oven that the present invention adopts;

Fig. 3 is the structural representation of the another kind of preferred implementation of the stoving oven that the present invention adopts;

Fig. 4 is the structural representation of the cylindrical shell of existing a kind of stoving oven;

Fig. 5 is the structural representation of the cylindrical shell of existing another kind of stoving oven;

Fig. 6 is the schematic flow sheet of Y zeolite modification;

Fig. 7 is schematic flow sheet prepared by a kind of catalytic cracking catalyst;

Fig. 8 is schematic flow sheet prepared by another kind of catalytic cracking catalyst.

Description of reference numerals

1-body of heater; 10-thermostat; 11-thermal insulation layer; 12-zone of heating; 13-burner hearth; 2-cylindrical shell; 20-middle cylinder; 21-opening for feed; 22-discharge port; 23-connecting steering mechanism; 24-feed end; 25-discharge end; 3-flight; 4-weir plate.

Embodiment

Below the specific embodiment of the present invention is described in detail.Should be understood that, embodiment described herein, only for instruction and explanation of the present invention, is not limited to the present invention.

In the present invention, be not specifically noted, " internal diameter " and " external diameter " of use is all be diameter.

The invention provides a kind of method of modifying of Y zeolite, the method comprises carries out first time exchange, drying, roasting, second time exchange and filtration successively by Y zeolite, as Figure 1-3, carry out the stoving oven that first time exchanges, the roasting of dried described Y zeolite uses successively to comprise body of heater 1 and be arranged on the cylindrical shell 2 in described body of heater 1, described cylindrical shell 2 comprises feed end 24, middle cylinder 20 and discharge end 25 successively; The inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4; Angle between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, and does not contact between adjacent two flights 3; Carry out that first time exchanges, the roasting of dried described Y zeolite comprises carrying out successively that first time exchanges, dried described Y zeolite sends in the described cylindrical shell 2 that is in maturing temperature from the opening for feed 21 of described cylindrical shell 2, and discharge from discharge port 22 successively; Carry out that first time exchanges, the temperature of the roasting of dried described Y zeolite is 400 to being less than 500 DEG C successively; Described second time is exchanged for and washes with water or acid solution washing, and the temperature that described second time exchanges is 20-70 DEG C; The temperature of preferred roasting is 400-490 DEG C, and the temperature that described second time exchanges is 30-60 DEG C.

According to the present invention, the roasting time of carrying out exchange, dried described Y zeolite for the first time successively can be 0.5-5 hour, and the roasting time of preferred described Y zeolite is 1-4 hour.

A preferred embodiment of the invention, described Y zeolite modification is carried out according to flow process as shown in Figure 6 in the present invention, comprise and the aqueous solution of Y zeolite and ammonium salt carried out first time and exchange, then drying, roasting is carried out, product of roasting and water or acid solution are carried out second time exchange, then filter second time and exchange product, obtain the Y zeolite of modification.

Described first time exchanges the method that ammonium salt can be adopted to exchange, described first time exchanges can carry out in making beating tank, such as described Y zeolite to be added in the making beating tank filling water and to add ammonium salt, the weight ratio of water and Y zeolite is 3-8:1, preferred described water is deionized water, described ammonium salt can be ammonium sulfate, and the weight ratio of ammonium sulfate and Y zeolite is 0.2-3:1.

According to the present invention, the temperature that described first time exchanges is 60-100 DEG C, and the time that described first time exchanges is 1-3 hour.

According to the present invention, the drying of the described Y zeolite after first time exchanges can adopt the method for this area routine to implement.Particularly, the drying of the described Y zeolite after first time exchanges can be carried out in flash distillation dryer, and dry temperature is 120-200 DEG C, and the dry time is 1-2 hour.

According to the present invention, the roasting carrying out exchange, dried described Y zeolite for the first time successively having carried out first time exchange, dried described Y zeolite as treating the roasting that the Y zeolite of roasting carries out, having carried out in stoving oven as Figure 1-3.

According to the present invention, when described flight 3 is arranged in described middle cylinder 20, described flight 3 is not parallel or vertical with the axis of described middle cylinder 20, but shape is at a certain angle.The bearing of trend of described flight 3 is to the direction that discharge port 22 extends from opening for feed 21, the axis of described middle cylinder 20 refers to the direction from opening for feed 21 to discharge port 22, the angle formed between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, in order to description of the invention, the angle that described corner dimension all gets the acute angle of formation represents, preferred described angle is for being greater than 0 ° and being less than or equal to 45 °; More preferably, described angle is 10-30 °.

According to the present invention, described cylindrical shell 2 is the conventional cylindrical shell in this area, and such as described cylindrical shell 2 can comprise feed end 24, middle cylinder 20 and discharge end 25.Described middle cylinder 20 is equal with the length of described body of heater 1, and in the inside of described body of heater 1, described feed end 24 and described exit end 25 are positioned at described middle cylinder 20 two ends, stretch out described body of heater 1 two ends and not in the inside of described body of heater 1.On described feed end 24 and described discharge end 25, correspondence offers opening for feed 21 and discharge port 22 respectively, and further preferred described opening for feed 21 is opened in the top of described feed end 24, and described discharge port 22 is opened in the bottom of described discharge end 25.Described feed end 24, described discharge end 25 and described middle cylinder 20 3 sections of internal diameters are identical.Described middle cylinder 20 is both ends open, and described feed end 24 and described discharge end 25 are one end open, and the other end is closed.Described feed end 24 is all connected with described middle cylinder 20 by connecting steering mechanism 23 with the open at one end of described discharge end 25.Described connecting steering mechanism 23 ensures that described feed end 24, described discharge end 25 are connected with described middle cylinder 20 and No leakage, can make that described middle cylinder 20 rotates under the driving of connecting steering mechanism 23 and described feed end 24 and discharge end 25 do not rotate simultaneously.Connecting steering mechanism 23 can be such as boiler tube revolution transmission system 4 disclosed in CN101149214A.During baking operation, the driving of connecting steering mechanism 23 makes middle cylinder 20 rotate, and controls turning direction and make material acted on by flight 3 to realize back-mixing as far as possible.

According to the present invention, the inwall of described middle cylinder 20 is provided with described flight 3 and described weir plate 4.Described flight 3 and described weir plate 4 are the structure outstanding towards the internal space of described middle cylinder 20.Described flight 3 makes to treat that the Y zeolite of roasting is forced in the inside of described middle cylinder 20 to stir, and the Y zeolite that described weir plate 4 prevents from treating roasting is too fast passes through stoving oven.Described flight 3 can be identical with well known by persons skilled in the art with described weir plate 4 set-up mode, and such as, described flight 3 can be extended along the axis of described middle cylinder 20, and described weir plate 4 can be arranged with the axial vertical of described middle cylinder 20.Homogeneity and stability that described flight 3 and described weir plate 4 can ensure the Y zeolite roasting quality treating roasting in described middle cylinder 20 are further set.

According to the present invention, the quantity arranging described flight 3 in described middle cylinder 20 can have multiple, can select in relative broad range, specifically can determine according to the requirement of roasting.In the present invention, the quantity of described flight 3 is on the arbitrary section axially vertical with described middle cylinder 20, along the quantity of the flight 3 that cross section circumference occurs for a week.Under preferable case, the quantity of described flight 3 is the circumferential 1-6/week along described middle cylinder 20, is preferably 2-4/week.

According to the present invention, described flight 3 arranges distribution in described middle cylinder 20 can be had multiple, and under preferable case, multiple described flight 3 distributes along the circumference of described middle cylinder 20; Described circumference is distributed as equal distribution or unequal distribution, and preferred described flight 3 is distributed as equal distribution along the circumference of described middle cylinder 20.

According to the present invention, under preferable case, each described flight 3 along from feed end 24 to the directional spreding of discharge end 25 on whole described middle cylinder 20.Namely axially extend to from the position that described middle cylinder 20 is connected with described feed end 24 always along described middle cylinder 20 position that described middle cylinder 20 is connected with described discharge end 25.

According to the present invention, described flight 3 has certain length, and to realize the object stirring and promote the Y zeolite treating roasting, under preferable case, the length of each described flight 3 is 1-4:1 with the ratio of the internal diameter of described middle cylinder 20.

According to the present invention, described flight 3 can arrange multiple along the axis of described middle cylinder 20, during the layout of multiple described flight 3 on described middle cylinder 20 inwall, each described flight 3 is all independent to be arranged, mutually do not connect between multiple described flight 3, between adjacent two flights 3, have certain distance, under preferable case, adjacent two described flights 3 be arranged in parallel, and minor increment is apart 0.1-0.5 times of described flight 3 length.

According to the present invention, described middle cylinder 20 distributes multiple described flight 3, and forms certain spatial distribution in middle cylinder 20, and under preferable case, multiple described flight 3 distributes on the whole in the shape of a spiral.

According to the present invention, described flight 3 is that the object realizing stirring and promote the Y zeolite treating roasting can have various shape, and as long strip shape, waviness, volution etc., under preferable case, described flight 3 is long strip shape.

According to the present invention, described weir plate 4 along the axial distribution of described middle cylinder 20, namely along directional spreding from the opening for feed 21 of described cylindrical shell 2 to discharge port 22.Described weir plate 4 can be annular plate, the periphery of described weir plate 4 and the contact internal walls of described middle cylinder 20.

According to the present invention, described weir plate 4 can be multiple, and multiple weir plate 4 is along the axial distribution of described middle cylinder 20, forms one or more partition in the axis of described middle cylinder 20.Arranging of described weir plate 4 can be equalization also can be unequal distribution, is preferably equal distribution.

According to the present invention, the quantity that described weir plate 4 is arranged is preferably 0.1-3/rice, is more preferably 0.1-2/rice.

According to the present invention, when arranging described weir plate 4 in described middle cylinder 20, described middle cylinder 20 is divided into multistage, described flight 3 can eachly integrally be arranged in described middle cylinder 20, extends to the position that described middle cylinder 20 is connected with described discharge end 25 from the position that described middle cylinder 20 is connected with described feed end 24; Described flight 3 also can be divided into multistage by described weir plate 4, arranges respectively in every section, and the described flight 3 in different section does not connect mutually; Preferred described flight 3 is divided into multistage.Described flight 3 does not contact with described weir plate 4.

According to the present invention, described stoving oven is when carrying out baking operation, and described middle cylinder 20 is set as rotating, and described middle cylinder 20 is with certain rotational speed, and the velocity of rotation of setting middle cylinder 20, namely determines corresponding roasting time.Under preferable case, velocity of rotation is 0.1-10rpm; Be more preferably 1-5rpm.

Treat the Y zeolite of roasting from opening for feed 21 to the movement of discharge port 22 for increasing, when mounted, become the pitch angle of 1-5 ° to install with the axis of cylindrical shell 2 with sea line, during installation, opening for feed 21 is higher than discharge port 22 for described stoving oven.The discharge of the Y zeolite after can being conducive to roasting is so set.

According to the present invention, described body of heater 1 can be the various bodies of heater of existing stoving oven, and under preferable case, described body of heater 1 comprises thermostat 10, thermal insulation layer 11, zone of heating 12 and burner hearth 13, and described middle cylinder 20 is arranged in the described burner hearth 13 in described body of heater 1.Zone of heating 12 is for the middle cylinder 20 in heating furnace 13, and thermal insulation layer 11 is positioned at the skin of zone of heating 12, surrounds the burner hearth 13 of zone of heating 12 and zone of heating 12 internal layer, for preventing and reduce the heat loss of whole body of heater 1.

According to the present invention, described zone of heating 12 can heat in different ways, such as fuel oil, combustion gas or Electric heating; Be preferably Electric heating.

In described stoving oven, described thermostat 10 connects described zone of heating 12 and maturing temperature measuring sensor (not shown), ensures the stable of maturing temperature.

Fig. 4 is the structural representation of the cylindrical shell of existing a kind of stoving oven.Cylindrical shell 2 comprises feed end 24, middle cylinder 20 and discharge end 25.Described feed end 24 and described discharge end 25 offer opening for feed 21 and discharge port 22 respectively.The inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4.The axis that described flight 3 is parallel to described middle cylinder 20 is arranged, and described weir plate 4 is arranged perpendicular to the axis of described middle cylinder 20.The quantity that described flight 3 and described weir plate 4 are arranged is 1.Described middle cylinder 20 is for rotating, and described feed end 24 and described discharge end 25 are fixing.During operation, described middle cylinder 20 rotates, and adds the Y zeolite treating roasting from opening for feed 21, then the Y zeolite after discharge port 22 collects roasting.

Fig. 5 is the structural representation of the cylindrical shell of existing another kind of stoving oven.One end of cylindrical shell 2 is unlimited, as opening for feed 21; At the homonymy of described opening for feed 21, discharge port 22 is offered in the below of described cylindrical shell 2.The inside of described cylindrical shell 2 arranges multiple flight 3, and each flight 3 forming V-shape is arranged, and the inside of erectting the described cylindrical shell 2 of welding is given prominence to.The V-arrangement summit of described flight 3 is pointed to identical with the turning direction of cylindrical shell 2, and axial vertical with described cylindrical shell 2.Described flight 3 extends along described tubular axis and is arranged on the inwall of whole described cylindrical shell, and described flight 3 is arranged in two rows altogether, and wherein space between adjacent two the described flights 3 of described flight 3 is arranged facing to another in the V-arrangement summit of the described flight 3 of a row.During baking operation, first clockwise direction rotates described cylindrical shell 2 and is delivered into from described opening for feed 21 Y zeolite treating roasting, after roasting enough scheduled times, is rotated backward counterclockwise by described cylindrical shell 2, is released by the Y zeolite after roasting from discharge port 22.

This shows, from the key distinction of above-mentioned existing stoving oven, the present invention is that flight 3 is different arranging of middle cylinder 20.And other structure unit and the annexation between them can be identical or different with above-mentioned existing stoving oven.

According to the present invention, the improvement of stoving oven improves the roasting quality of Y zeolite, the second time of the Y zeolite after roasting exchanges no longer to be needed to use ammonium salt, make to wash with water or acid solution washs, described second time exchanges can carry out in making beating tank, and the water of use is preferably deionized water, and the temperature that described second time exchanges also reduces than prior art, under preferable case, the temperature that described second time exchanges is 20-70 DEG C, and the temperature that preferred described second time exchanges is 30-60 DEG C.

According to the present invention, under preferable case, the weight ratio for the water in the water that washs or acid solution and the Y zeolite after roasting is 3-15:1, preferred 5-8:1.

According to the present invention, it can also be acid solution washing that described second time exchanges, and the pH value of described acid solution is not less than 3, and under preferable case, described pH value is for being more than or equal to 3 and being less than 7.

According to the present invention, described acid solution can be the solution of arbitrary acid, can be the solution of organic acid or mineral acid, and under preferable case, described acid solution is one or more in oxalic acid aqueous solution, aqueous sulfuric acid, aqueous nitric acid and hydrochloric acid; Preferred described acid solution is hydrochloric acid or oxalic acid aqueous solution.

According to the present invention, described second time exchange time chien shih roasting after Y zeolite fully wash, to remove the sodium ion on it, under preferable case, the time that described second time exchanges is 0.5-1.5 hour.

According to the present invention, the filtration of the described Y zeolite after second time exchanges can adopt the method for this area routine to implement, described filtration can be carried out in flame filter press, obtains the Y zeolite of modification, and measures the Na in Y zeolite by fluorometry ₂o content.

The present invention also provides a kind of preparation method of catalytic cracking catalyst, the method comprises: Y zeolite is carried out modification, obtain the Y zeolite of modification, and with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of the modification of 5-50 % by weight, 0.5-50 % by weight carries out plastic with the clay mixture of the binding agent of oxide basis and 5-90 % by weight, and the plastic product obtained is carried out drying successively, roasting, washing, obtain product of roasting, the temperature of the roasting of dried described plastic product is 350-400 DEG C, described product of roasting washs successively, filter and drying, the washing of described product of roasting is washing, the temperature of the washing of described product of roasting is 20-45 DEG C, be 5-20:1 for the water of the washing of described product of roasting and the weight ratio of described product of roasting, the method of modifying of the Y zeolite that described method of Y zeolite being carried out modification provides for the invention described above.

According to the present invention, under preferable case, the time of the roasting of dried described plastic product is 0.5-5 hour, and the time of preferred roasting is 1-4 hour.

According to the present invention, the washing that described product of roasting carries out can be carried out in making beating tank, can use deionized water.Y zeolite due to modification is that the method for modifying of the Y zeolite provided by the invention described above is obtained, sodium ions content is low, therefore the washing that described product of roasting carries out also can have the condition of improvement, and the weight ratio of the water and described product of roasting that are preferred for the washing of described product of roasting is 5-15:1; The time of the washing of described product of roasting is 0.5-1.5 hour.

A preferred embodiment of the invention, the schema of the preparation method of catalytic cracking catalyst of the present invention as shown in Figure 7, comprise and the aqueous solution of Y zeolite and ammonium salt carried out first time and exchange, then drying, roasting is carried out, product of roasting and water or acid solution are carried out second time exchange, then filter second time and exchange product, obtain the Y zeolite of modification.The Y zeolite of modification, binding agent and clay are added plastic cans and carries out plastic, then drying, roasting, washing, filtration and drying obtain catalytic cracking catalyst.

In catalytic cracking catalyst preparation method of the present invention, Y zeolite is carried out the method for modifying that method that modification adopts is the Y zeolite that the invention described above provides, as mentioned above, do not repeat them here.The Y zeolite (sodium ions content meets industrial requirements after measured) of the modification obtained does the raw material preparing catalytic cracking catalyst.Conventional catalytic cracking catalyst preparation method can be adopted to implement the preparation of catalytic cracking catalyst.

According to the present invention, the method for the routine that described plastic can adopt catalytic cracking catalyst to prepare is implemented.Be specially described plastic to carry out in plastic cans, the mixture comprising the Y zeolite of modification, binding agent and clay is carried out plastic.The Y zeolite of described modification is the Y zeolite of the modification obtained with the method for modifying of above-mentioned Y zeolite provided by the invention; Described binding agent is one or more in aluminum oxide, hydrated aluminum oxide, Alumina gel, silicon sol, silica-alumina gel, silicon-aluminum sol and their precursor, is preferably pseudo-boehmite or Alumina gel; Described clay is one or more in kaolin, halloysite, polynite, diatomite, halloysite, saponite, rectorite, sepiolite, attapulgite, hydrotalcite, wilkinite, preferred kaolin or rectorite.The condition of described plastic comprises: can by deionized water, hydrochloric acid and binding agent, be that 1.5-4:0.2-0.3:1 adds plastic cans stirring to pulp by the weight ratio of raw material, simultaneously wherein the add-on of binding agent with the 0.5-50 % by weight for catalytic cracking catalyst gross weight during oxide basis, hydrochloric acid is the concentrated hydrochloric acid of concentration 36 % by weight, beating time is 0.5-1.5 hour, and the temperature of pulper slurry is 20-50 DEG C; Again the Modified Zeolite Y of the 5-50 % by weight of catalytic cracking catalyst gross weight is added stirring to pulp in plastic cans, beating time is 2-4 hour, and the temperature of pulper slurry is 20-50 DEG C; Again the clay of the 5-90 % by weight of catalytic cracking catalyst gross weight and 0.5-50 % by weight binding agent are added plastic cans stirring to pulp plastic, gelation time is 2-8 hour, and gelling temperature is 20-50 DEG C, obtains plastic product.

According to the present invention, the drying of described plastic product, drying means conventional during catalytic cracking catalyst can be adopted to prepare.The drying of described plastic product can be carried out in spray-dryer, and described spray-dired condition comprises: spray inlet temperature 400-550 DEG C, temperature out 120-200 DEG C, spray pressure 8-14MPa.

According to the present invention, the roasting of dried described plastic product be using described plastic product after drying as treating the roasting that calcining matter carries out, carry out in stoving oven as Figure 1-3.The cylindrical shell 2 that the stoving oven that the present invention uses comprises body of heater 1 and is arranged in described body of heater 1, described cylindrical shell 2 comprises feed end 24, middle cylinder 20 and discharge end 25 successively; The inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4; Angle between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, and does not contact between adjacent two flights 3.

The present invention by arranging flight 3 and weir plate 4 on the inwall of middle cylinder 20, and flight 3 forms angle with the axis of middle cylinder, the roasting process treating calcining matter is controlled, with batch treat that calcining matter has sufficient and identical roasting time, obtain same roasting effect.Described stoving oven is as previously described, does not repeat them here.Obtain product of roasting.

According to the present invention, the filtration of the product of roasting after washing can adopt is preparation method enforcement conventional in catalytic cracking catalyst.Described filtration can be carried out in flame filter press.

According to the present invention, the drying of the product of roasting after washing, filtration, can adopt the drying means of the routine preparing catalytic cracking catalyst to implement.Described drying can be carried out in pneumatic dryer, and the drying conditions of described plastic product comprises: dry temperature is 120-200 DEG C, and the dry time is 1-2 hour.

Present invention also offers a kind of preparation method of catalytic cracking catalyst, the method comprises: with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of 5-50 % by weight, 0.5-50 % by weight carries out plastic successively with the mixture of the clay of the binding agent of oxide basis and 5-90 % by weight, dry, roasting, obtain calcining matter, carry out plastic successively, the temperature of the roasting of dried described mixture is 350-400 DEG C, described calcining matter washs successively, filter and drying, the washing of described calcining matter is washing, the temperature of the washing of described calcining matter is 20-45 DEG C, be 5-20:1 for the water of the washing of described calcining matter and the weight ratio of described calcining matter, carry out successively plastic, dried described mixture roasting use stoving oven comprise body of heater 1 and be arranged on the cylindrical shell 2 in described body of heater 1, described cylindrical shell 2 comprises feed end 4, middle cylinder 20 and discharge end 25 successively, the inwall of described middle cylinder 20 is provided with flight 3 and weir plate 4, angle between the bearing of trend of described flight 3 and the axial direction of described middle cylinder 20 is acute angle or obtuse angle, and does not contact between adjacent two flights 3, carry out plastic successively, the roasting of dried described mixture comprises carrying out plastic successively, dried described mixture is sent in the described cylindrical shell 2 that is in maturing temperature from the opening for feed 21 of described cylindrical shell 2, and discharge from discharge port 22.

According to the present invention, under preferable case, carry out plastic successively, time of roasting of dried described mixture is 0.5-5 hour, the time of preferred roasting is 1-4 hour.

According to the present invention, the washing that described calcining matter carries out can be carried out in making beating tank, can use deionized water.Y zeolite due to modification is that the method for modifying of the Y zeolite provided by the invention described above is obtained, sodium ions content is low, therefore the washing that described product of roasting carries out also can have the condition of improvement, and the weight ratio of the water and described calcining matter that are preferred for the washing of described calcining matter is 5-15:1; The time of the washing of described calcining matter is 0.5-1.5 hour.

A preferred embodiment of the invention, the preparation of catalytic cracking catalyst is carried out according to the flow process shown in Fig. 8, comprise Modified Zeolite Y, binding agent and clay to be mixed together and carry out plastic, drying, roasting, washing, filtration and drying, obtain catalytic cracking catalyst.Described Y zeolite can be through the Y zeolite of the modification that various method of modifying obtains, as the REY obtained with RE ion-exchange, the REHY obtained is exchanged with RE and ammonium salt, with the USY that hydrothermal method, EDTA complexometry, gas phase SiCl4 dealumination complement silicon method, ammonium silicofluoride aluminium-eliminating and silicon-replenishing method obtain, in the present invention, under preferable case, described Y zeolite is the Y zeolite of the modification obtained with the method for modifying of above-mentioned Y zeolite provided by the invention.Described binding agent is one or more in aluminum oxide, hydrated aluminum oxide, Alumina gel, silicon sol, silica-alumina gel, silicon-aluminum sol and their precursor, is preferably pseudo-boehmite or Alumina gel; Described clay is one or more in kaolin, halloysite, polynite, diatomite, halloysite, saponite, rectorite, sepiolite, attapulgite, hydrotalcite, wilkinite, preferred kaolin or rectorite.

According to the present invention, the method for the routine that the plastic of described mixture can adopt catalytic cracking catalyst to prepare is implemented.The plastic being specially described mixture can be carried out in plastic cans, and the mixture comprising the Y zeolite of modification, binding agent and clay is carried out plastic.The Gelation Conditions of described mixture comprises: can by deionized water, hydrochloric acid and binding agent, be that 1.5-4:0.2-0.3:1 adds plastic cans stirring to pulp by the weight ratio of raw material, simultaneously wherein the add-on of binding agent with the 0.5-50 % by weight for catalytic cracking catalyst gross weight during oxide basis, hydrochloric acid is the concentrated hydrochloric acid of concentration 36 % by weight, beating time is 0.5-1.5 hour, and the temperature of pulper slurry is 20-50 DEG C; Again the Modified Zeolite Y of the 5-50 % by weight of catalytic cracking catalyst gross weight is added stirring to pulp in plastic cans, beating time is 2-4 hour, and the temperature of pulper slurry is 20-50 DEG C; Again the clay of the 5-90 % by weight of catalytic cracking catalyst gross weight and 0.5-50 % by weight binding agent are added plastic cans stirring to pulp plastic, gelation time is 2-8 hour, and gelling temperature is 20-50 DEG C, obtains the plastic product of described mixture.

According to the present invention, the drying of the described mixture after plastic, the drying means of the middle routine that catalytic cracking catalyst can be adopted to prepare.Described drying can be carried out in spray-dryer, and described spray-dired condition comprises: spray inlet temperature 400-550 DEG C, temperature out 120-200 DEG C, spray pressure 8-14MPa.

According to the present invention, carry out plastic successively, the roasting of dried described mixture be using through plastic and dried described mixture as treating the roasting that calcining matter carries out, carry out in stoving oven as Figure 1-3.The present invention by arranging flight 3 and weir plate 4 on the inwall of middle cylinder 20, and flight 3 forms angle with the axis of middle cylinder, the roasting process treating calcining matter is controlled, with batch treat that calcining matter has sufficient and identical roasting time, obtain same roasting effect.Described stoving oven is as previously described, does not repeat them here.Obtain calcining matter.

According to the present invention, the filtration of the calcining matter after washing can adopt is preparing filter method enforcement conventional in catalytic cracking catalyst.Described filtration can be carried out in flame filter press.

According to the present invention, the drying of the calcining matter after washing, filtration can adopt the drying means of the routine preparing catalytic cracking catalyst to implement.Such as described drying can be carried out in pneumatic dryer, and described drying conditions comprises: dry temperature is 120-200 DEG C, and the dry time is 1-2 hour.

The preparation of catalytic cracking catalyst in the present invention, because the sodium ions content of the Y zeolite of the modification of use is qualified, in calcination steps prepared by catalytic cracking catalyst, adopt again the stoving oven that the present invention improves, thus can maturing temperature be reduced, reduce energy consumption, and the requirement of washing step is also reduced, not only water temperature is lower than prior art, and washing water consumption also obviously reduces.

Below will be described the present invention by embodiment.In following examples, the Na of Y zeolite ₂o content passes through fluorescence analysis method: and RIPP117-90 standard method (see volumes such as " Petrochemical Engineering Analysis method " (RIPP test method) Yang Cuiding, Science Press, nineteen ninety publishes).

Embodiment 1

The present embodiment is for illustration of the method for modifying of Y zeolite of the present invention.

50kgNaY type molecular sieve (Shandong catalyst plant) is added in the making beating tank that 400kg deionized water is housed, add ammonium sulfate 150kg, the weight ratio of water and NaY type molecular sieve is 8:1, the weight ratio of ammonium sulfate and NaY type molecular sieve is 3:1, first time exchange is carried out in making beating tank, exchange temperature is 80 DEG C, and swap time is 2 hours.NaY type molecular sieve after exchange enters in flash distillation dryer and carries out drying, and dry temperature is 180 DEG C, and the dry time is 1.5 hours.

Using dried NaY type molecular sieve as treating that the Y zeolite of roasting is put into stoving oven and carried out roasting.As shown in Figure 1, stoving oven arranges flight 3 and weir plate 4 on the inwall of middle cylinder 20.The internal diameter of whole cylindrical shell 2 is 1m, and the length of whole cylindrical shell 2 is 7m, and wherein feed end 24 and the respective length of discharge end 25 are 0.5m, and the length of middle cylinder 20 is 6m.Weir plate 4 is annular plate, be straightened be welded on middle cylinder 20 inwall on, the height of weir plate 4 is 10cm, thickness is 5mm, weir plate 4 totally two pieces, by middle cylinder 20 trisection long for 6m, first piece in the position axially extending 2m along middle cylinder 20 from middle cylinder 20 and feed end 24 junction to discharge end 25 direction, the position continuing to extend to 4m is second piece; By on the inwall of three sections of middle cylinder 20 of weir plate 4 decile, at every section, flight 3 is set, flight 3 is long strip shape, the length direction of flight 3 becomes 30 ° of angles with the axis of middle cylinder 20, flight 3 be straightened be welded on middle cylinder 20 inwall on, be highly 10cm, thickness is 5mm, by on the inwall of three sections of middle cylinder 20 of weir plate 4 decile, be 3 in the quantity of the flight 3 of every section of equalization of the circumference along middle cylinder 20 setting.Middle cylinder 20 is set to rotate under the drive of connecting steering mechanism 23, and turning direction makes material acted on by flight 3 realizes back-mixing as far as possible.

Whole stoving oven tilts 1 ° to place relative to sea line with the axial of cylindrical shell 2, and opening for feed 21 is high, and discharge port 22 is low.

Stoving oven heating is reached maturing temperature 490 DEG C, rotate middle cylinder 20,50kg is treated the Y zeolite of roasting all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that the Y zeolite of roasting is forced to push in middle cylinder 20 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Y zeolite after roasting is collected at discharge port 22 place of stoving oven cylindrical shell 2.Under setting middle cylinder 20 rotating speed 1.8rpm condition, roasting time is 1 hour.Record the weight of the time being fed to continuous discharge and the Y zeolite received continuously, the Y zeolite received when getting continuous discharge analyzes lattice constant and degree of crystallinity.The results are shown in Table 1,2.Table 1 is discharging time, the continuous discharge time is the time period of Y zeolite after discharge port 22 place collects roasting first time continuously first, and the weight calculating the Y zeolite after the roasting of collecting accounts for the percentage ratio of the gross weight of the Y zeolite after whole roastings of finally collecting; Other column data gauge outfit implications the like.Table 2 is the lattice constant of Y zeolite collected and degree of crystallinity, the discharging time of the corresponding table 1 of the Y zeolite collected.

Y zeolite after roasting carries out second time and exchanges.In the making beating tank filling 384kg deionized water, add the Y zeolite after the roasting of 48kg, obtain the slurries containing Y zeolite, then add hydrochloric acid, regulate the pH=3.5 of slurries, the weight ratio of water and Y zeolite is 8:1, and second time exchange temperature is 50 DEG C, and swap time is 1.5 hours.The Y zeolite exchanged is filtered, obtains the Y zeolite exchanged, be numbered Z1.The Na in the Y zeolite Z1 of modification is measured by fluorometry ₂o content.The results are shown in Table 3.

Comparative example 1

According to the method Modified Zeolite Y of embodiment 1, unlike, stoving oven is the stoving oven cylindrical shell shown in the stoving oven cylindrical shell alternate figures 1 shown in Fig. 4.Wherein, as shown in Figure 4, in middle cylinder 20, flight 3 quantity is 1, and flight 3 extends to the junction of middle cylinder 20 and discharge end 25, with the axis being parallel of middle cylinder 20 on the length direction of flight 3 from middle cylinder 20 and the junction of feed end 24.Weir plate 4 quantity is 1, is arranged in the position extending 3m along middle cylinder 20 axis from middle cylinder 20 with feed end 24 junction to discharge end 25.Weir plate 4 is annular plate, is divided into two sections by flight 3.Flight 3 does not contact with weir plate 4.The Y zeolite production code member of modification is D1.The results are shown in Table 1-3.

Comparative example 2

According to the method Modified Zeolite Y of embodiment 1, unlike, stoving oven is the stoving oven cylindrical shell shown in the stoving oven cylindrical shell alternate figures 1 shown in Fig. 5.Wherein, as shown in Figure 5, middle cylinder 20 is provided with multiple flight 3, and each flight 3 forming V-shape is arranged on middle cylinder 20, and the V-arrangement summit of flight 3 is pointed to identical with the turning direction of middle cylinder 20, and axial vertical with middle cylinder 20.The opening the other end that the open at one end that flight 3 is connected from middle cylinder 20 with feed end 24 is connected along the axial array of middle cylinder 20 to middle cylinder 20 with discharge end 25, V-arrangement flight 3 is arranged in two rows altogether, and wherein the V-arrangement summit of row's flight 3 is facing to the space between adjacent two flights 3 of another row's flight 3.The slant range 20cm be spaced apart between respective V-arrangement summit often in row between flight 3 and flight 3.Two limits of the v-shaped structure of composition flight 3 are length is respectively 20cm, and be highly 10cm, thickness is the length bar shaped of 5mm, and the angle that two limits of composition flight 3V shape structure are formed is 30 °.V-arrangement flight 3 is erect and is welded on the inwall of middle cylinder 2, inner outstanding to middle cylinder.The Y zeolite production code member of modification is D2.The results are shown in Table 1-3.

Embodiment 2

50kgNaY type molecular sieve (Shandong catalyst plant) is added in the making beating tank that 250kg deionized water is housed, add ammonium sulfate 35kg, the weight ratio of water and NaY type molecular sieve is 5:1, the weight ratio of ammonium sulfate and NaY type molecular sieve is 0.7:1, first time exchange is carried out in making beating tank, exchange temperature is 100 DEG C, and swap time is 1.5 hours.NaY type molecular sieve after exchange enters in flash distillation dryer and carries out drying, and dry temperature is 200 DEG C, and the dry time is 1 hour.

Using dried NaY type molecular sieve as treating that the Y zeolite of roasting is put into stoving oven and carried out roasting.As shown in Figure 2, with the stoving oven used in embodiment 1 unlike, weir plate 4 totally three pieces, middle cylinder 20 quartern long by 6m, in distance middle cylinder 20 and 1.5 meters, feed end 24 junction, the position of 3 meters and 4.5 meters erects first, second, and third piece of weir plate respectively, and these weir plates are arranged by from middle cylinder 20 and feed end 24 junction to the direction of middle cylinder 20 with discharge end 25 junction; The length direction of flight 3 becomes 10 ° of angles with the axis of middle cylinder 20, the open at one end that flight 3 is connected with feed end 24 from middle cylinder 20 extends to the opening the other end that middle cylinder 20 is connected with discharge end 25, and the quantity of the flight 3 that the circumference equalization along middle cylinder 20 is arranged is 2.Weir plate 4 has opening, and flight 3 extends there through, and flight 3 does not contact with weir plate 4.

Whole stoving oven tilts 5 ° to place relative to sea line with the axial of cylindrical shell 2, and opening for feed 21 is high, and discharge port 22 is low.

Stoving oven heating is reached maturing temperature 400 DEG C, rotate middle cylinder 20,50kg is treated the Y zeolite of roasting all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that the Y zeolite of roasting is forced to push in middle cylinder 20 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Y zeolite after roasting is collected at discharge port 22 place of stoving oven cylindrical shell 2.Under setting middle cylinder 20 rotating speed 1rpm condition, roasting time is 4 hours.Record the weight of the time being fed to continuous discharge and the molecular sieve received continuously, degree of crystallinity analyzed by the molecular sieve received when getting continuous discharge.The results are shown in Table 1,2.

Y zeolite after roasting carries out second time and exchanges.Y zeolite add the roasting of 48kg in the making beating tank filling 240kg deionized water after, obtain the slurries containing Y zeolite, add oxalic acid aqueous solution again, regulate the pH=3.6 of slurries, the weight ratio of water and Y zeolite is 5:1, second time exchange temperature is 30 DEG C, and swap time is 1.5 hours.The Y zeolite exchanged is filtered, obtains the Y zeolite exchanged, be numbered Z2.The Na in the Y zeolite Z2 of modification is measured by fluorometry ₂o content.The results are shown in Table 3.

Embodiment 3

50kgNaY type molecular sieve (Shandong catalyst plant) is added in the making beating tank that 150kg deionized water is housed, add ammonium sulfate 100kg, the weight ratio of water and NaY type molecular sieve is 3:1, the weight ratio of ammonium sulfate and NaY type molecular sieve is 2:1, first time exchange is carried out in making beating tank, exchange temperature is 60 DEG C, and swap time is 1 hour.NaY type molecular sieve after exchange enters in flash distillation dryer and carries out drying, and dry temperature is 120 DEG C, and the dry time is 2 hours.

Using dried NaY type molecular sieve as treating that the Y zeolite of roasting is put into stoving oven and carried out roasting.As shown in Figure 3, the stoving oven used with embodiment 1 is unlike, weir plate 4 totally a piece, and the middle cylinder 20 that 6m is long is halved, and is arranged on the position axially extending 3m along middle cylinder 20 from middle cylinder 20 and feed end 24 junction to discharge end 25.The length direction of flight 3 becomes 20 ° of angles with the axis of middle cylinder 20, the open at one end that flight 3 is connected with feed end 24 from middle cylinder 20 extends to the opening the other end that middle cylinder 20 is connected with discharge end 25, and the quantity of the flight 3 that the circumference equalization along middle cylinder 20 is arranged is 4; Weir plate 4 is divided into 4 sections by flight 3, and flight 3 does not contact with weir plate 4.

Whole stoving oven tilts 3 ° to place relative to sea line with the axial of cylindrical shell 2, and opening for feed 21 is high, and discharge port 22 is low.

Stoving oven heating reaches maturing temperature 450 DEG C, rotate middle cylinder 20,50kg is treated the Y zeolite of roasting all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that the Y zeolite of roasting is forced to push in middle cylinder 20 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Y zeolite after roasting is collected at discharge port 22 place of stoving oven cylindrical shell 2.Under setting middle cylinder 20 rotating speed 1.5rpm condition, roasting time is 2.5 hours.Record the weight of the time being fed to continuous discharge and the molecular sieve received continuously, degree of crystallinity analyzed by the molecular sieve received when getting continuous discharge.The results are shown in Table 1,2.

Y zeolite after roasting carries out second time and exchanges.Y zeolite add the roasting of 48kg in the making beating tank filling 288kg deionized water after, the weight ratio of water and Y zeolite is 6:1, and second time exchange temperature is 60 DEG C, and swap time is 1.5 hours.Filtered by the Y zeolite exchanged, the Y zeolite obtaining having exchanged is numbered Z3.The Na in the Y zeolite Z3 of modification is measured by fluorometry ₂o content.The results are shown in Table 3.

Embodiment 4

According to the method for embodiment 1, unlike, under setting middle cylinder 20 rotating speed 3.6rpm condition, roasting time is 0.5 hour.The Y zeolite obtaining modification is numbered Z4.The results are shown in Table 1-3.

Table 1

Table 2

Table 3

Y zeolite is numbered	Z1	Z2	Z3	Z4	D1	D2
							Na ₂O content/% by weight	1.2	1.35	1.2	1.4	1.5	1.6

Embodiment 5

The present embodiment is for illustration of the preparation method of catalytic cracking catalyst of the present invention.

By 29kg pseudo-boehmite (Al ₂o ₃content is 75 % by weight, Shandong Aluminum Plant), 43.5kg deionized water and 5.8kg hydrochloric acid (36 % by weight) adds plastic cans stirring to pulp, beating time is 1 hour, and pulper slurry temperature is 20 DEG C; Again the Y zeolite Z1 of 38kg embodiment 1 modification is added stirring to pulp in plastic cans, beating time is 3 hours, and pulper slurry temperature is 20 DEG C; Again by 30kg kaolin (Law Firm Suzhou Jiangsu) and 41kg Alumina gel (Al ₂o ₃content is 24 % by weight, Shandong Aluminum Plant) add in plastic cans plastic of pulling an oar, gelation time is 8 hours, and gelling temperature is 20 DEG C, obtains plastic product.Then plastic product is delivered into spray-drying tower, spraying dry at spray inlet temperature is 550 DEG C, temperature out is 200 DEG C, and spray pressure is 8MPa.Obtain dried plastic product.

Using dried plastic product as treating that calcining matter is put into stoving oven and carried out roasting.Use the stoving oven in embodiment 1, as shown in Figure 1.

Stoving oven heating is reached maturing temperature 350 DEG C, rotate middle cylinder 20,50kg is treated calcining matter all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that calcining matter is forced to push in middle cylinder 20 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Roasting product of roasting is collected at discharge port 22 place of stoving oven cylindrical shell 2.The speed setting of middle cylinder 20 is 1rpm, and roasting time is 4 hours.

Product of roasting washs.In the making beating tank filling 750kg deionized water, add the product of roasting of 50kg, obtain the slurries containing product of roasting, the weight ratio of water and product of roasting is 15:1, and wash temperature is 20 DEG C, and washing time is 1.2 hours.

The product of roasting washed is carried out filter, dry, Filter slurry in flame filter press, then dry in pneumatic dryer, drying temperature is 120 DEG C, and time of drying is 2 hours, obtains catalytic cracking catalyst products C 1.The physical property of product parametric measurement the results are shown in Table 4.

Embodiment 6

By 29kg pseudo-boehmite (Al ₂o ₃content is 75 % by weight, Shandong Aluminum Plant), 116kg deionized water and 8.7kg hydrochloric acid (36 % by weight) adds plastic cans stirring to pulp, beating time is 0.5 hour, and pulper slurry temperature is 50 DEG C; Again the Y zeolite Z2 of 36kg embodiment 2 modification is added stirring to pulp in plastic cans, beating time is 2 hours, and pulper slurry temperature is 50 DEG C; Again by 32kg rectorite (Law Firm Suzhou Jiangsu) and 41kg Alumina gel (Al ₂o ₃content is 24 % by weight, Shandong Aluminum Plant) add plastic cans making beating plastic, gelation time is 2 hours, and gelling temperature is 50 DEG C, obtains plastic product.Then plastic product is delivered into spray-drying tower, spraying dry at spray inlet temperature is 400 DEG C, temperature out is 120 DEG C, and spray pressure is 14MPa.Obtain dried plastic product.

Using dried plastic product as treating that calcining matter is put into stoving oven and carried out roasting.Use the stoving oven in embodiment 2, as shown in Figure 2.

Stoving oven heating is reached maturing temperature 375 DEG C, rotate middle cylinder 20,50kg is treated the catalytic cracking catalyst of roasting all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that calcining matter is forced to push in cylindrical shell 2 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Collect product of roasting at discharge port 22 place of stoving oven cylindrical shell 2, the speed setting of middle cylinder 20 is 1.5rpm, and roasting time is 2.5 hours.

Product of roasting washs.In the making beating tank filling 250kg deionized water, add the product of roasting of 50kg, obtain the slurries containing product of roasting, the weight ratio of water and product of roasting is 5:1, and wash temperature is 30 DEG C, and washing time is 1 hour.

The product of roasting washed is carried out filter, dry, Filter slurry in flame filter press, then dry in pneumatic dryer, drying temperature is 200 DEG C, and time of drying is 1 hour, obtains catalytic cracking catalyst products C 2.The physical property of product parametric measurement the results are shown in Table 4.

Embodiment 7

By 30kg pseudo-boehmite (Al ₂o ₃content is 75 % by weight, Shandong Aluminum Plant), 90kg deionized water and 7.5kg hydrochloric acid (36 % by weight) adds plastic cans stirring to pulp, beating time is 1.5 hours, and pulper slurry temperature is 30 DEG C; Again the Y zeolite Z3 of 40kg embodiment 3 modification is added stirring to pulp in plastic cans, beating time is 4 hours, and pulper slurry temperature is 30 DEG C; Again by 27kg kaolin (Law Firm Suzhou Jiangsu) and 41kg Alumina gel (Al ₂o ₃content is 24 % by weight, Shandong Aluminum Plant) add plastic cans making beating plastic, gelation time is 6 hours, and gelling temperature is 30 DEG C, obtains plastic product.Then plastic product is delivered into spray-drying tower, spraying dry at spray inlet temperature is 480 DEG C, temperature out is 160 DEG C, and spray pressure is 12MPa.Obtain dried plastic product.

Using dried plastic product as treating that calcining matter is put into stoving oven and carried out roasting.Stoving oven in use embodiment 3 as shown in Figure 3.

Stoving oven heating is reached maturing temperature 400 DEG C, rotate middle cylinder 20,50kg is treated calcining matter all joins cylindrical shell 2 continuously from the opening for feed 21 of cylindrical shell 2, treat that calcining matter is forced to push in cylindrical shell 2 to carry out roasting by flight 3 under the rotary action of middle cylinder 20.Collect product of roasting at discharge port 22 place of stoving oven cylindrical shell 2, the speed setting of middle cylinder 20 is 1.8rpm, and roasting time is 1 hour.

Product of roasting washs.In the making beating tank filling 500kg deionized water, add the product of roasting of 50kg, obtain the slurries containing product of roasting, the weight ratio of water and product of roasting is 10:1, and wash temperature is 45 DEG C, and washing time is 1.5 hours.

The product of roasting washed is carried out filter, dry, Filter slurry in flame filter press, then dry in pneumatic dryer, drying temperature is 180 DEG C, and time of drying is 1.5 hours, obtains catalytic cracking catalyst products C 3.The physical property of product parametric measurement the results are shown in Table 4.

Comparative example 3

Catalytic cracking catalyst is prepared according to the method for embodiment 5, unlike, stoving oven is the stoving oven cylindrical shell shown in the stoving oven cylindrical shell alternate figures 1 shown in Fig. 4.Catalytic cracking catalyst production code member is D3.Measurement result is in table 4.

Test case

The Catalytic Cracking Performance of catalytic cracking catalyst C1-C3 and D3 that embodiment 5-7 and comparative example 3 prepare is described.

Catalytic cracking catalyst composition assay: fluorometry, oxide content measures.The results are shown in Table 4.

Catalytic cracking catalyst Determination of Physical Property Parameters: pore volume and specific area measuring, method is RIPP151-90 standard method (see " Petrochemical Engineering Analysis method " (RIPP test method), Yang Cui delimits the organizational structure, Science Press, and nineteen ninety publishes); Abrasion index and apparent bulk density measure, and method is RIPP29-90 standard method (see " Petrochemical Engineering Analysis method " (RIPP test method), Yang Cui delimits the organizational structure, Science Press, and nineteen ninety publishes).The results are shown in Table 4.

Light oil microactivity is evaluated: adopt the standard method of RIPP92-90 (see volumes such as " Petrochemical Engineering Analysis method " (RIPP test method) Yang Cuiding, Science Press, nineteen ninety publishes) light oil microactivity of assess sample, catalyzer loading amount is 5.0g, temperature of reaction is 460 DEG C, and stock oil is the huge port solar oil of boiling range 235-337 DEG C, and product composition is by gas chromatographic analysis, calculate light oil microactivity according to product composition, result in table 4.

Light oil microactivity (MA)=(lower than the gasoline production+gas yield+coke output of 216 DEG C in product)/charging total amount × 100%

Heavy oil cracking performance evaluation condition: catalyzer is first at 800 DEG C, 100% steam aging 12 hours, then fixed fluidized bed at ACE() device to be evaluated, stock oil is military mixed three heavy oil (physico-chemical parameter is in table 5), and temperature of reaction 500 DEG C, agent weight of oil ratio is 4.

Wherein, transformation efficiency=yield of gasoline+yield of liquefied gas+dry gas yield+coking yield

Yield of light oil=yield of gasoline+diesel yield

Liquid yield=yield of liquefied gas+yield of gasoline+diesel yield

Coke selectivity=coking yield/transformation efficiency

Evaluate the cracking performance of catalytic cracking catalyst C1-C3 and D3 according to the method described above respectively, the results are shown in table 6.

Table 4

Catalyzer is numbered	C1	C2	C3	D3
					Al ₂O ₃Content/% by weight	48.2	48.6	49.1	52.1
Na ₂O content/% by weight	0.07	0.07	0.07	0.19
					Pore volume/(mLg ^-1)	0.40	0.39	0.40	0.35
Specific surface area/(m ²·g ^-1)	283	280	285	245
					Abrasion index/(%h ^-1)	1.5	1.7	1.4	1.9
Apparent bulk density/(gmL ^-1)	0.73	0.74	0.74	0.75
					Micro-activity (800,4h)/%	82	81	82	74

Table 5

Table 6

Catalyzer	C1	C2	C3	D3
					Product slates, % by weight
Dry gas	1.2	1.15	1.18	1.23
					Liquefied gas	12.45	12.69	13.01	13.01
Coke	6.16	6.41	5.59	5.75
					Gasoline	55.25	54.05	55.08	47.17
Diesel oil	16.78	17.28	16.99	19.91
					Heavy oil	8.16	8.42	8.15	12.93
Add up to	100	100	100	100
					Transformation efficiency, % by weight	75.06	74.3	74.86	67.16
Coke selectivity, % by weight	8.21	8.63	7.47	8.56
					Yield of light oil, % by weight	72.03	71.33	72.07	67.08
Liquid yield, % by weight	84.48	84.02	85.08	80.09

Note: yield of light oil is the total recovery of gasoline and diesel oil, liquid yield is yield of light oil and yield of liquefied gas sum.

As can be seen from the test-results data of table 1, in embodiment 1-4, adopt the stoving oven that the present invention improves, in the Y zeolite discharging continuum after roasting, just can complete the discharging of whole Y zeolite when discharging first.And when adopting the embodiment in comparative example 1, Y zeolite discharging after roasting is discontinuous, need the discharging that just can complete whole Y zeolite in three batches, it is stable that the stoving oven of visible use prior art can not ensure to treat that the Y zeolite of roasting stops in stoving oven, therefore causes in a collection of Y zeolite the product having and experience different roasting time.

The Y zeolite of modifications different for above-mentioned discharging time is carried out roasting effect compare, measure lattice constant or the degree of crystallinity of the Y zeolite after roasting respectively, data results as can be seen from table 2, when adopting embodiment provided by the invention, the consistence of the lattice constant data of the Y zeolite of modification is better, under the embodiment of comparative example 1, the Y zeolite roasting product of the modification obtained, because roasting time is inconsistent, the Y zeolite lattice constant consistence after the roasting that different batches receives is poor.And, roasting is carried out with the roasting time (0.5 hour) suitable with the second time continuous discharge time in comparative example 1 in embodiment 4, the lattice constant showing the Y zeolite after the roasting that embodiment 4 obtains in table 2, not as the result of embodiment 1-3, illustrates that roasting time can obtain better roasting effect at present preferred 1-4 is little.The Na of the Y zeolite of modification from table 3 further ₂o assay result can be found out, the Y zeolite of the modification obtained with embodiment roasting provided by the invention, the roasting product Na collected ₂o is low, can have good quality product.

In addition, embodiment provided by the invention improve efficiently the effect of the continuous roasting of Y zeolite, improves the consistence of roasting process, stoving oven space and roasting heat amount are fully utilized, improve the roasting quality of product, maturing temperature reduces, and decreases energy consumption.

From the results shown in Table 4, in the preparation of catalytic cracking catalyst, the Y zeolite of the modification adopting Y zeolite method of modifying of the present invention to obtain is as raw material, calcination steps uses the stoving oven improved, the sodium oxide content of gained catalytic cracking catalyst significantly reduces, pore volume and specific surface area obviously increase, and micro-activity significantly improves.

From the results shown in Table 6, compared with comparative example 3, catalytic cracking catalyst prepared by the present invention has higher transformation efficiency, liquid yield, yield of light oil and lower coke selectivity.

The preparation method of Y zeolite method of modifying provided by the invention and catalytic cracking catalyst can not only obtain the qualified product of sodium ion, the catalytic cracking catalyst prepared has better Catalytic Cracking Performance, and energy consumption in preparation process, the discharge of ammonia nitrogen waste water and the consumption of catalytic cracking catalyst bath water are all lowered.

Claims

1. the preparation method of a catalytic cracking catalyst, the method comprises: Y zeolite is carried out modification, obtain the Y zeolite of modification, and with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of the modification of 5-50 % by weight, 0.5-50 % by weight carries out plastic with the clay mixture of the binding agent of oxide basis and 5-90 % by weight, and the plastic product obtained is carried out drying successively, roasting, obtain product of roasting, the temperature of the roasting of dried described plastic product is 350-400 DEG C, described product of roasting washs successively, filter and drying, the washing of described product of roasting is washing, the temperature of the washing of described product of roasting is 20-45 DEG C, be 5-20:1 for the water of the washing of described product of roasting and the weight ratio of described product of roasting, described method of Y zeolite being carried out modification comprises: Y zeolite carried out successively first time exchange, drying, roasting, second time exchange and filter, carry out the stoving oven that first time exchanges, the roasting of dried described Y zeolite uses successively to comprise body of heater (1) and be arranged on the cylindrical shell (2) in described body of heater (1), described cylindrical shell (2) comprises feed end (24), middle cylinder (20) and discharge end (25) successively, the inwall of described middle cylinder (20) is provided with flight (3) and weir plate (4), angle between the bearing of trend of described flight (3) and the axial direction of described middle cylinder (20) is acute angle or obtuse angle, and does not contact between adjacent two flights (3), carry out that first time exchanges, the roasting of dried described Y zeolite comprises carrying out successively that first time exchanges, dried described Y zeolite sends in the described cylindrical shell (2) that is in maturing temperature from the opening for feed (21) of described cylindrical shell (2), and discharge from discharge port (22) successively, carry out the temperature of the roasting of exchange, dried described Y zeolite for the first time successively for being more than or equal to 400 DEG C and being less than 500 DEG C, described second time is exchanged for and washes with water or acid solution washing, and the temperature that described second time exchanges is 20-70 DEG C.

2. method according to claim 1, wherein, the maturing temperature carrying out exchange, dried described Y zeolite for the first time is successively 400-490 DEG C, and roasting time is 0.5-5 hour.

3. method according to claim 1, wherein, the temperature that described second time exchanges is 30-60 DEG C.

4. method according to claim 1, wherein, in described second time exchanges, the weight ratio for the water in the water that washs or acid solution and Y zeolite is 3-15:1.

5. the method according to claim 1 or 4, wherein, the pH value of described acid solution is for being more than or equal to 3 and being less than 7.

6. method according to claim 5, wherein, described acid solution is one or more in oxalic acid aqueous solution, aqueous sulfuric acid, aqueous nitric acid and hydrochloric acid.

7. method according to claim 1, wherein, the stoving oven that the roasting of dried described plastic product uses comprises body of heater (1) and is arranged on the cylindrical shell (2) in described body of heater (1), and described cylindrical shell (2) comprises feed end (24), middle cylinder (20) and discharge end (25) successively; The inwall of described middle cylinder (20) is provided with flight (3) and weir plate (4); Angle between the bearing of trend of described flight (3) and the axial direction of described middle cylinder (20) is acute angle or obtuse angle, and does not contact between adjacent two flights (3).

8. the preparation method of a catalytic cracking catalyst, the method comprises: with catalytic cracking catalyst gross weight for benchmark, by the Y zeolite of 5-50 % by weight, 0.5-50 % by weight carries out plastic successively with the clay mixture of the binding agent of oxide basis and 5-90 % by weight, dry, roasting, obtain calcining matter, carry out plastic successively, the temperature of the roasting of dried described mixture is 350-400 DEG C, described calcining matter washs successively, filter and drying, the washing of described calcining matter is washing, the temperature of the washing of described calcining matter is 20-45 DEG C, be 5-20:1 for the water of the washing of described calcining matter and the weight ratio of described calcining matter, carry out successively plastic, dried described mixture roasting use stoving oven comprise body of heater (1) and be arranged on the cylindrical shell (2) in described body of heater (1), described cylindrical shell (2) comprises feed end (24), middle cylinder (20) and discharge end (25) successively, the inwall of described middle cylinder (20) is provided with flight (3) and weir plate (4), angle between the bearing of trend of described flight (3) and the axial direction of described middle cylinder (20) is acute angle or obtuse angle, and does not contact between adjacent two flights (3), carry out plastic successively, the roasting of dried described mixture comprises carrying out plastic successively, dried described mixture is sent in the described cylindrical shell (2) that is in maturing temperature from the opening for feed (21) of described cylindrical shell (2), and discharge from discharge port (22).

9. the method according to claim 1,7 or 8, wherein, the angle between the bearing of trend of described flight (3) and the axial direction of described middle cylinder (20) is for being greater than 0 ° and being less than or equal to 45 °.

10. the method according to claim 1,7 or 8, wherein, described flight (3) is for multiple, and multiple described flight (3) distributes along the circumference of described middle cylinder (20).

11. methods according to claim 1,7 or 8, wherein, the quantity that described flight (3) distributes along the circumference of described middle cylinder (20) is 1-6/week.

12. methods according to claim 1,7 or 8, wherein, each described flight (3) along from feed end (24) to the directional spreding of discharge end (25) on whole described middle cylinder (20).

13. methods according to claim 1,7 or 8, wherein, the ratio of the length of each described flight (3) and the internal diameter of described middle cylinder (20) is 1-4:1.

14. methods according to claim 1,7 or 8, wherein, adjacent two described flights (3) be arranged in parallel, and minor increment be apart the 0.1-0.5 of described flight (3) length doubly.

15. methods according to claim 1,7 or 8, wherein, multiple described flight (3) distributes on the whole in the shape of a spiral.

16. methods according to claim 1 or 8, wherein, described weir plate (4) is annular plate, the periphery of annular plate and the contact internal walls of described middle cylinder (20).

17. methods according to claim 1,7 or 8, wherein, described weir plate (4) is for multiple, and multiple described weir plate (4) is along the axial distribution of described middle cylinder (20).

18. methods according to claim 1,7 or 8, wherein, the quantity of described weir plate (4) is 0.1-3/rice.

19. methods according to claim 1,7 or 8, wherein, described flight (3) does not contact with described weir plate (4).