CN201762287U - Rotary continuous catalytic cracking equipment - Google Patents
Rotary continuous catalytic cracking equipment Download PDFInfo
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- CN201762287U CN201762287U CN2010202689872U CN201020268987U CN201762287U CN 201762287 U CN201762287 U CN 201762287U CN 2010202689872 U CN2010202689872 U CN 2010202689872U CN 201020268987 U CN201020268987 U CN 201020268987U CN 201762287 U CN201762287 U CN 201762287U
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Abstract
The utility model discloses rotary continuous catalytic cracking equipment which comprises an automatic charging and dreg removing device, a rotary catalytic cracking kettle, a wax removing distribution device, a vertical multi-segment condensing device, and a gas purification and storage cabinet. With waste rubber and waste plastics as raw materials, the automatic charging and dreg removing device, the rotary catalytic cracking kettle, a cracked gas catalytic bed and a multi-segment circulating water condenser are adopted to obtain an excellent fuel oil product. After being purified, absorbed and stored, non-condensed gas is used as a heat source of a combustion chamber of the cracking kettle; and water spraying type tail gas purification and emission is carried out at a multi-point warming combustion fire hole. A carbon black obtained through cracking is discharged from an automatic dreg removing opening, and an excellent carbon black is obtained through magnetic separating, winnowing, powder refining, activation classifying and packaging treatments. The complete set of equipment carries out catalytic cracking under the full-airtight normal-pressure anaerobic state; the process is safe and reliable, and no secondary pollution is caused; moreover, the rotary continuous catalytic cracking equipment can obtain such new products as the carbon black, fuel oil, fuel gas and the like, so as to achieve the purposes of automatic charging and dreg removing, continuous production, low energy consumption, high product qualification rate and high yield.
Description
Technical field:
The utility model relates to a kind of chemical industry catalytic pyrolysis equipment, relates in particular to a kind of rotary continuous catalytic pyrolysis equipment.
Background technology:
Along with the process industry expanding economy, with rubber, plastics are that raw-material product usage quantity is increasing, consequent waste rubber, the environmental pollution that plastics cause is on the rise, paid close attention to by common people, become the countries in the world research topic, how to handle the waste rubber-plastic pollutent, become the big research topic of present pendulum in face of scientific and technical personnel, reasonably handle development and use, advanced technical equipment must be arranged, with science, efficiently, environmental protection, the developing goal of comprehensive utilization makes the waste rubber plastics that pollute the human living space, turn waste into wealth, obtain a large amount of renewable resource products, recycling economy and sustainable development are achieved in that rotary continuous catalytic pyrolysis equipment is technical.
The utility model content:
In view of this, the purpose of this utility model provides a kind ofly can carry out the normal pressure continuous catalysis cracking to the waste rubber plastics, obtains the rotary continuous catalytic pyrolysis equipment of new energy product.
The technical solution of the utility model realizes in the following manner:
A kind of rotary continuous catalytic pyrolysis equipment, wherein, mainly comprise automatic charging, deslagging device, automatic charging, the other rotary-catalytic cracking still that is connected with of deslagging device, the other paraffin removal distribution device that is connected with of rotary-catalytic cracking still, the paraffin removal distribution device is other to be connected with the vertical multi-sectional condensing works and to be arranged on the other gas sweetening cabinet that is connected with of vertical multi-sectional condensing works.
Automatic charging, deslagging device are by material conveyor, be arranged on the feed screw of material conveyor below, the other hopper that is connected with of feed screw, material baffle and carbon black dw, the carbon black locker room that is arranged on automatic charging, deslagging device below constitutes, and below, carbon black locker room also is provided with carbon black lift and carbon black e Foerderanlage.
The rotary-catalytic cracking still is by rotation cracking kettle, be arranged on the burning and gas-exhausting heat energy utilization device of rotation cracking kettle top, be arranged on the thermal insulation layer of rotation cracking still external surface, the cracking still internal catalyst bed, be arranged on the combustion chamber porthole of rotation cracking kettle below, the multiple spot burning crater of heating, cracking still power set and cracked gas sealing export mixes also are provided with the carbon black outlet on the rotation cracking kettle.
The paraffin removal distribution device is arranged on the connection loop expansion pipe on the Wax remover by Wax remover, and the lightweight cracked gas that is arranged on Wax remover top promotes catalytic bed, and cracked gas separates catalytic bed and the paraffin removal holder constitutes.
The vertical multi-sectional condensing works mainly is made of the condenser lifting catalyst converter other with being arranged on condenser, condenser is provided with condenser feed water inlet and condenser oil fuel products export, promoting catalyst converter is provided with lifting catalyst converter feed water inlet and promotes catalyst converter oil fuel products export, condensation cycle water out.
The gas sweetening cabinet is mainly by synthetic scavenging solution container, constitute with the gas storage cabinet that is connected with synthetic scavenging solution container, synthetic scavenging solution container is provided with the incondensable gas collector, the incondensable gas dispersion hole, synthetic scavenging solution container top is provided with solid absorption chamber and synthetic scavenging solution inlet, the bottom is provided with synthetic scavenging solution outlet, top, solid absorption chamber is connected with the gas holder conduit, the tank body of synthetic scavenging solution container is provided with limited mouth, gas storage is cashier's office in a shop held and is provided with the gas holder air guide port, and the gas storage cabinet is connected by the gas holder conduit with synthetic scavenging solution container.
The lightweight cracked gas promotes catalytic bed, cracked gas separates catalytic bed, condenser, lifting catalyst converter and gas storage cabinet and is equipped with digital temperature pressure monitor instrument.
The condenser lower end is provided with the condenser hold-up vessel, promotes the catalyst converter lower end and is provided with lifting catalyst converter hold-up vessel.
Positively effect of the present utility model is:
The utility model is at the disposable innoxious technical equipment of waste rubber-plastic, adopt automatic feed, rotary-catalytic cracking still, cracked gas catalytic bed, multistage recirculated water cooling condenser, obtain fine oil fuel product, incondensable gas is through purifying, adsorb, store the back for cracking still combustion chamber thermal source, the multiple spot burning crater of heating, the discharging of water spray tail gas clean-up.Cracking obtains carbon black product and is discharged by the self-skimming mouth, obtains the fine carbon black products through magnetic separation, selection by winnowing, segmentation, activation after dividing grade packaged processing.A complete set of equipment is catalytic pyrolysis under fully-closed normal pressure anaerobic state, and is safe and reliable, non-secondary pollution.Can carry out disposable harmless treatment to the waste rubber plastics, obtain new energy product such as carbon black, oil fuel, combustion gas simultaneously, reach automatic feed, slagging-off serialization production, it is low to consume energy, the qualification rate of product and the purpose that goes out the rate raising.
Description of drawings:
Fig. 1 is the utility model structural representation.
Embodiment:
As seen from Figure 1: this rotary continuous catalytic pyrolysis equipment mainly divides five parts: mainly comprise automatic charging, deslagging device 40, automatic charging, the deslagging device 40 other rotary-catalytic cracking stills 41 that are provided with, the rotary-catalytic cracking still 41 other paraffin removal distribution devices 42 that are provided with, paraffin removal distribution device 42 other gas sweetening cabinets 44 compositions that are provided with vertical multi-sectional condensing works 43 and are arranged on vertical multi-sectional condensing works 43 sides.
Automatic charging, deslagging device 40 are by material conveyor 1, be arranged on the feed screw 2 of material conveyor 1 below, be arranged on the hopper 3 on feed screw 2 sides, material baffle 4 and carbon black dw 5, the carbon black locker room 7 that is arranged on automatic charging, deslagging device 40 belows constitutes, and 7 belows, carbon black locker room also are provided with carbon black lift and carbon black e Foerderanlage 45.
Rotary-catalytic cracking still 41 is by rotation cracking kettle 8, be arranged on the burning and gas-exhausting heat energy utilization device 9 of rotation cracking kettle 8 tops, be arranged on the thermal insulation layer 10 of rotation cracking kettle 8 outside surfaces, cracking still catalyst bed 11, be arranged on the combustion chamber porthole 12 of rotation cracking kettle 8 belows, the multiple spot burning crater 13 of heating, cracking still power set 14 and cracked gas sealing outlet 15 constitute, and also are provided with carbon black outlet 6 on the rotation cracking kettle 8.
Paraffin removal distribution device 42 is arranged on the connection loop expansion pipe 16 on the Wax remover 17 by Wax remover 17, and the lightweight cracked gas that is arranged on Wax remover 17 tops promotes catalytic bed 18, and cracked gas separates catalytic bed 19 and paraffin removal holder 39 constitutes.
Vertical multi-sectional condensing works 43 mainly is made of condenser 20 and the lifting catalyst converters 21 that are arranged on condenser 20 sides, condenser 20 is provided with condenser feed water inlet 22 and condenser oil fuel products export 25, promoting catalyst converter 21 is provided with lifting catalyst converter feed water inlet 23 and promotes catalyst converter oil fuel products export 24, condensation cycle water out 26.
The lightweight cracked gas promotes catalytic bed 18, cracked gas separates catalytic bed 19, condenser 20, lifting catalyst converter 21 and gas storage cabinet 35 and is equipped with digital temperature pressure monitor instrument 46.
Condenser 20 lower ends are provided with condenser hold-up vessel 38.
Promote catalyst converter 21 lower ends and be provided with lifting catalyst converter hold-up vessel 37.
Claims (9)
1. rotary continuous catalytic pyrolysis equipment, it is characterized in that: mainly by automatic charging, deslagging device (40), be arranged on automatic charging, deslagging device (40) connection rotary-catalytic cracking still (41), be arranged on rotary-catalytic cracking still (41) and connect paraffin removal distribution device (42), be arranged on paraffin removal distribution device (42) and connect vertical multi-sectional condensing works (43) and be arranged on vertical multi-sectional condensing works (43) and be connected gas sweetening cabinet (44) composition.
2. rotary continuous catalytic pyrolysis equipment according to claim 1, it is characterized in that: automatic charging, deslagging device (40) are by material conveyor (1), be arranged on the feed screw (2) of material conveyor (1) below, be arranged on the other hopper (3) that is provided with of feed screw (2), material baffle (4) and carbon black dw (5), the carbon black locker room (7) that is arranged on automatic charging, deslagging device (40) below constitutes, and carbon black locker room (7) below also is provided with carbon black lift and carbon black e Foerderanlage (45).
3. rotary continuous catalytic pyrolysis equipment according to claim 1 and 2, it is characterized in that: rotary-catalytic cracking still (41) is by rotation cracking kettle (8), be arranged on the burning and gas-exhausting heat energy utilization device (9) of rotation cracking kettle (8) top, be arranged on the thermal insulation layer (10) of rotation cracking kettle (8) outside surface, cracking still internal catalyst bed (11), be arranged on the combustion chamber porthole (12) of rotation cracking kettle (8) below, the multiple spot burning crater (13) of heating, cracking still power set (14) and cracked gas sealing outlet (15) constitute, and also are provided with carbon black outlet (6) on the rotation cracking kettle (8).
4. rotary continuous catalytic pyrolysis equipment according to claim 3, it is characterized in that: paraffin removal distribution device (42) is by Wax remover (17), be arranged on the connection loop expansion pipe (16) on the Wax remover (17), the lightweight cracked gas that is arranged on Wax remover (17) top promotes catalytic bed (18), and cracked gas separates catalytic bed (19) and paraffin removal holder (39) constitutes.
5. rotary continuous catalytic pyrolysis equipment according to claim 4, it is characterized in that: vertical multi-sectional condensing works (43) mainly by condenser (20) be arranged on condenser (20) and be connected and promote catalyst converter (21) and constitute, condenser (20) is provided with condenser feed water inlet (22) and condenser oil fuel products export (25), promoting catalyst converter (21) is provided with lifting catalyst converter feed water inlet (23) and promotes catalyst converter oil fuel products export (24), condensation cycle water out (26).
6. rotary continuous catalytic pyrolysis equipment according to claim 5, it is characterized in that: gas sweetening cabinet (44) mainly constitutes by synthesizing scavenging solution container (29) and being arranged on the other gas storage cabinet (35) of synthetic scavenging solution container (29), synthetic scavenging solution container (29) is provided with incondensable gas collector (27), incondensable gas dispersion hole (28), synthetic scavenging solution container (29) top is provided with solid absorption chamber (30) and synthetic scavenging solution inlet (31), the bottom is provided with synthetic scavenging solution outlet (36), top, solid absorption chamber (30) is provided with gas holder conduit (33), also be provided with limited mouth (32) on the tank body of synthetic scavenging solution container (29), gas storage cabinet (35) upper end is provided with gas holder air guide port (34), and gas storage cabinet (35) is connected by gas holder conduit (33) with synthetic scavenging solution container (29).
7. rotary continuous catalytic pyrolysis equipment according to claim 5 is characterized in that: the lightweight cracked gas promotes catalytic bed (18), cracked gas separates catalytic bed (19), condenser (20), lifting catalyst converter (21) and gas storage cabinet (35) and is equipped with digital temperature pressure monitor instrument (46).
8. rotary continuous catalytic pyrolysis equipment according to claim 5 is characterized in that: condenser (20) lower end is provided with condenser hold-up vessel (38).
9. rotary continuous catalytic pyrolysis equipment according to claim 5 is characterized in that: promote catalyst converter (21) lower end and be provided with lifting catalyst converter hold-up vessel (37).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202689872U CN201762287U (en) | 2010-07-23 | 2010-07-23 | Rotary continuous catalytic cracking equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202689872U CN201762287U (en) | 2010-07-23 | 2010-07-23 | Rotary continuous catalytic cracking equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201762287U true CN201762287U (en) | 2011-03-16 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202689872U Expired - Fee Related CN201762287U (en) | 2010-07-23 | 2010-07-23 | Rotary continuous catalytic cracking equipment |
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| CN (1) | CN201762287U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102504857A (en) * | 2011-11-07 | 2012-06-20 | 李昊民 | Intermittent type waste rubber cracking device |
| CN102703106A (en) * | 2012-06-25 | 2012-10-03 | 徐效奇 | Instant cracking reaction device adopting high-frequency heating and converting oil into membrane |
| TWI494352B (en) * | 2013-08-19 | 2015-08-01 | Chien Hsiung Chang | A scrap tire pyrolysis equipment and method thereof |
| CN104962308A (en) * | 2015-07-17 | 2015-10-07 | 刘云 | Production method of direct-fired waste plastic oil refining device |
-
2010
- 2010-07-23 CN CN2010202689872U patent/CN201762287U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102504857A (en) * | 2011-11-07 | 2012-06-20 | 李昊民 | Intermittent type waste rubber cracking device |
| CN102504857B (en) * | 2011-11-07 | 2013-11-06 | 李昊民 | Intermittent type waste rubber cracking device |
| CN102703106A (en) * | 2012-06-25 | 2012-10-03 | 徐效奇 | Instant cracking reaction device adopting high-frequency heating and converting oil into membrane |
| TWI494352B (en) * | 2013-08-19 | 2015-08-01 | Chien Hsiung Chang | A scrap tire pyrolysis equipment and method thereof |
| CN104962308A (en) * | 2015-07-17 | 2015-10-07 | 刘云 | Production method of direct-fired waste plastic oil refining device |
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| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110316 Termination date: 20120723 |