CN206721081U - A kind of carbon black reaction system and carbon black process system - Google Patents
A kind of carbon black reaction system and carbon black process system Download PDFInfo
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- CN206721081U CN206721081U CN201720104218.0U CN201720104218U CN206721081U CN 206721081 U CN206721081 U CN 206721081U CN 201720104218 U CN201720104218 U CN 201720104218U CN 206721081 U CN206721081 U CN 206721081U
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- tail gas
- carbon black
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Abstract
A kind of carbon black reaction system and carbon black process system, are related to production of carbon black field.Carbon black reaction system includes reactor, the first feedstock oil transmission system, the second feedstock oil transmission system, tank field system, air delivery system and two level tail gas transmission system, reactor includes combustion chamber, trunnion, reative cell, air preheater and tail gas pre-heater, combustion chamber, trunnion and reative cell are sequentially communicated, air preheater and tail gas pre-heater connect with reative cell respectively, first feedstock oil transmission system and combustion chamber, second feedstock oil transmission system connects with trunnion, and tank field system connects with the first feedstock oil transmission system, the second feedstock oil transmission system.A kind of carbon black process system, it includes above-mentioned carbon black reaction system.Above-mentioned carbon black reaction system and carbon black process system, air and two level tail gas are heated using tail gas by the air preheater and tail gas pre-heater of parallel connection, improve the organic efficiency of tail gas heat quantity.
Description
Technical field
Production of carbon black field is the utility model is related to, in particular to a kind of carbon black reaction system and carbon black process system
System.
Background technology
The main production raw material of carbon black is coal tar, ethylene bottom oil, carbolineum, natural gas, blast furnace gas etc..Carbon black
Production technology has oven process, spray-on process, lamp black method, channel process, drum process, mixed gas method, cracking process, acetylene method and plasma method, its
Middle oven process, spray-on process, lamp black method, channel process, drum process, mixed gas method are imperfect combustion method, pyrolysismethod, acetylene method and plasma method
For pyrolysis method.Lamp black method carbon black is mainly used as colouring agent for paint at present, drum process and mixed gas method carbon black be mainly used in paint and
Ink colour carbon black, acetylene method carbon black are mainly used in dry cell production, and other manufacturing technique methods are in production rubber charcoal
Black middle application.
Oven process is in reative cell, and raw material hydrocarbon (liquid hydrocarbon, gaseous hydrocarbon or its mixture) forms closed with appropriate air
Turbulent systems, producing high temperature with air burning by the original hydrocarbon in part makes another part raw material hydrocarbon be cracked to form carbon black, then will
The method that the carbon black being suspended in flue gas is cooled down, filtered, collecting, being granulated into finished product carbon black.Wherein, with gaseous hydrocarbon (natural gas or
Coal bed gas) for the manufacture method of primary raw material it is referred to as steam stove method, with liquid hydrocarbon (aromatic hydrocarbons heavy oil, including catalytic cracking clarified oil, second
Alkene tar, coal tar distillate etc.) for the manufacture method of primary raw material it is referred to as Audit For Process.
Audit For Process is due to just there is the features such as process adjustments method is more, heat utilization rate is high, energy consumption is small and cost is low,
As main carbon black manufacture method.In existing technology, the tail gas of the high temperature obtained after cracking reaction is directly carried out down
The charcoal collection processing of one system so that the high temperature energy that tail gas carries can not utilize.
Utility model content
The purpose of this utility model is to provide a kind of carbon black reaction system, and it can pass through the air preheater of reactor
Air and two level tail gas are heated with tail gas pre-heater tail gas using high temperature in parallel with reactor, improve tail gas heat quantity
Organic efficiency.
Another object of the present utility model is to provide a kind of carbon black process system, and it can utilize the tail gas of high temperature to sky
Gas and two level tail gas are heated.
What embodiment of the present utility model was realized in：
A kind of carbon black reaction system, including reactor, the first feedstock oil transmission system, the second feedstock oil transmission system, tank
Sound zone system, air delivery system and two level tail gas transmission system, reactor include combustion chamber, trunnion, reative cell, air preheat
Device and tail gas pre-heater, combustion chamber, trunnion and reative cell are sequentially communicated, the outlet of reative cell respectively with air preheater and tail gas
So that the tail gas in reative cell is fed directly into air preheater and tail gas pre-heater, the transmission of the first feedstock oil is for preheater connection
System and combustion chamber, the second feedstock oil transmission system connect with trunnion；Tank field system is multiple storage tanks, is set on storage tank base
There are multiple grooves, connecting rod and universal wheel are provided with groove, one end of connecting rod is connected with universal wheel, and the other end passes through butterfly hinge
It is connected with groove；Tank field system connects with the first feedstock oil transmission system, and tank field system also connects with the second feedstock oil transmission system
It is logical；Air delivery system connects with air preheater, and two level tail gas transmission system is respectively communicated to tail gas pre-heater and reactor
Entrance with by two level tail gas transmission system heat after two level tail gas be delivered to combustion chamber.
In the utility model preferred embodiment, above-mentioned air preheater is connected by pipeline with tail gas pre-heater.
In the utility model preferred embodiment, above-mentioned tail gas pre-heater is multiple, and the outlet of reative cell passes through pipeline
Connected with multiple tail gas pre-heaters.
In the utility model preferred embodiment, the tube-side inlet of above-mentioned air preheater connects with reative cell, air
The tube side outlet of preheater connects with collection system；Air from air delivery system passes through air preheater shell side and air
Heat exchange occurs for the tail gas in the tube side of preheater.
In the utility model preferred embodiment, the tube-side inlet of above-mentioned tail gas pre-heater is connected by pipeline and reative cell
Logical, the tube side outlet of tail gas pre-heater connects with collection system；Two level tail gas from two level tail gas transmission system passes through tail gas
With the tail gas in tail gas pre-heater tube side heat exchange occurs for preheater shell side.
In the utility model preferred embodiment, above-mentioned carbon black reaction system also includes circulation, circulating water
System is connected by spray head with the outer wall of reative cell, cold to cracking reacted tail gas progress by the water in circulation
But.
In the utility model preferred embodiment, above-mentioned air preheater and tail gas pre-heater connect with the second heat exchanger
It is logical, enter after air preheater and the mixing of the tail gas of tail gas pre-heater in the second heat exchanger and the recirculated water in circulation
Row heat exchange.
In the utility model preferred embodiment, above-mentioned storage tank is divided into petroleum tank, carbolic oil oil-washing tank, petroleum tank and first
Feedstock oil transmission system connects with the second feedstock oil transmission system, carbolic oil oil-washing tank and granulating and drying system connectivity.
In the utility model preferred embodiment, the outlet of above-mentioned storage tank is provided with for filtering Tank corrosion product
Screen pack.
A kind of carbon black process system, it includes above-mentioned carbon black reaction system, collection system, granulating and drying system, storage
Packaging system, exhaust gas purification system, carbon black reaction system are connected with collection system, and tail gas caused by carbon black reaction system is passed
Collection system is delivered to, collection system, granulating and drying system and storage package system are sequentially communicated, pelletizing of carbon black packed, and receive
Collecting system also connects with exhaust gas purification system, and exhaust gas purification system connects with two level tail gas transmission system, by two after purification
Level tail gas is passed through combustion chamber as fuel.
The beneficial effect of the utility model embodiment is：Carbon black reaction system of the present utility model, by air preheater and
Tail gas pre-heater is in parallel, and is communicated to the outlet of reative cell so that the tail gas for the high temperature discharged in reative cell can be pre- in air
Hot device and tail gas pre-heater carry out heat exchange, improve the organic efficiency of tail gas heat quantity, are advantageous to cost-effective.Include above-mentioned charcoal
The carbon black reaction system of black reaction system can also improve the organic efficiency of tail gas heat quantity.
Brief description of the drawings
, below will be to required use in embodiment in order to illustrate more clearly of the technical scheme of the utility model embodiment
Accompanying drawing be briefly described, it will be appreciated that the following drawings illustrate only some embodiments of the present utility model, therefore should not be by
Regard the restriction to scope as, for those of ordinary skill in the art, on the premise of not paying creative work, may be used also
To obtain other related accompanying drawings according to these accompanying drawings.
Fig. 1 is the schematic flow sheet of the utility model embodiment carbon black reaction system；
Fig. 2 is the schematic diagram of the utility model embodiment reactor；
Fig. 3 is another schematic diagram of the utility model embodiment reactor；
Fig. 4 is the schematic diagram of the utility model embodiment petroleum tank；
Fig. 5 is another schematic diagram of the utility model embodiment petroleum tank；
Fig. 6 is the schematic flow sheet of the utility model embodiment carbon black process system.
Icon：100- carbon black reaction systems；110- reactors；150- the first feedstock oil transmission systems；The raw materials of 160- second
Oily transmission system；170- air delivery systems；180- two level tail gas transmission systems；190- tank fields system；171- air reservoirs；
172- air compressor machines；151- First Heat Exchangers；The heat exchangers of 152- second；111- combustion chambers；112- trunnions；120- reative cells；130-
Air preheater；140- tail gas pre-heaters；121- spray heads；131- tube-side inlets；141- tube-side inlets；132- tube sides export；
142- tube sides export；133- shell side inlets；143- shell side inlets；134- shell-side outlets；144- shell-side outlets；191- petroleum tanks；
192- carbolic oil oil-washing tanks；193- screen packs；194- bases；195- sides；196- grooves；197- connecting rods；198- universal wheels；199-
Butterfly hinge；200- carbon black process systems；210- collection systems；220- granulating and drying systems；230- storage package systems；240-
Exhaust gas purification system；260- circulations.
Embodiment
It is new below in conjunction with this practicality to make the purpose, technical scheme and advantage of the utility model embodiment clearer
Accompanying drawing in type embodiment, the technical scheme in the embodiment of the utility model is clearly and completely described, it is clear that is retouched
The embodiment stated is the utility model part of the embodiment, rather than whole embodiments.Generally here described in accompanying drawing and
The component of the utility model embodiment shown can be configured to arrange and design with a variety of.
Therefore, the detailed description of the embodiment of the present utility model to providing in the accompanying drawings is not intended to limit requirement below
The scope of the utility model of protection, but it is merely representative of selected embodiment of the present utility model.Based in the utility model
Embodiment, the every other embodiment that those of ordinary skill in the art are obtained under the premise of creative work is not made, all
Belong to the scope of the utility model protection.
It should be noted that：Similar label and letter represents similar terms in following accompanying drawing, therefore, once a certain Xiang Yi
It is defined, then it further need not be defined and explained in subsequent accompanying drawing in individual accompanying drawing.
In addition, term " first ", " second " etc. are only used for distinguishing description, and it is not intended that indicating or implying relatively important
Property.
In description of the present utility model, it is also necessary to which explanation, unless otherwise clearly defined and limited, term is " even
It is logical " it should be interpreted broadly, for example, it may be fixed connection or detachable connection, or integratedly connect；It can be machine
Tool connects or is electrically connected；Can be joined directly together, can also be indirectly connected by intermediary, can be two members
Connection inside part.For the ordinary skill in the art, it can understand that above-mentioned term is new in this practicality with concrete condition
Concrete meaning in type.
Embodiment
Fig. 1 is refer to, the present embodiment provides a kind of carbon black reaction system 100, and it includes reactor 110, the first feedstock oil
Transmission system 150, the second feedstock oil transmission system 160, air delivery system 170, two level tail gas transmission system 180 and tank field system
System 190.Reactor 110, the first feedstock oil transmission system 150, the second feedstock oil transmission system 160, air delivery system 170 with
And the section connections different from reactor 110 respectively of two level tail gas transmission system 180.
Fig. 2 and Fig. 3 are refer to, reactor 110 includes combustion chamber 111, trunnion 112, reative cell 120, air preheater 130
With tail gas pre-heater 140, the outlet of combustion chamber 111 connects with trunnion 112, and the outlet of trunnion 112 connects with the entrance of reative cell 120
Logical, the outlet of air preheater 130 and reactor 110, tail gas pre-heater 140 connects with by pipeline with reactor 110.
Air preheater 130 is arranged in parallel with reactor 110, it is possible to provide the passage of the tail gas of high temperature circulation in parallel, the tail gas of high temperature
Collection system 210 is delivered to after air preheater 130 and tail gas pre-heater 140.The tail gas of high temperature is in air preheater 130
Heat exchange is carried out with air, heat exchange is carried out in tail gas pre-heater 140 and the low temperature two level tail gas after purification.It should be understood that air
Preheater 130 and tail gas pre-heater 140 can respectively with reative cell 120 outlet, without by pipeline communication, this
Sample can also reach the effect in parallel of air preheater 130 and tail gas pre-heater 140, can also realize that the tail gas of high temperature carries heat
The technique effect of high efficiente callback, and the scope of the present embodiment protection.
Referring to Fig.1 and 2, combustion chamber 111 is arranged on the front end of reactor 110, carry out burning instead in combustion chamber 111
Should, the heat for reacting release provides heat for the pyrolytic reaction in reative cell 120, by the second fuel oil preheating.Two level tail gas passes
System 180, the entrance of the first feedstock oil transmission system 150 and air delivery system 170 all respectively with combustion chamber 111 is sent to connect,
The combustion reaction into combustion chamber 111 provides combustion adjuvant and fuel respectively.
Trunnion 112 is elongated pipeline, and its diameter is less than the diameter of combustion chamber 111 and reative cell 120, and trunnion 112 is set
Fluid can be caused in trunnion 112 less by diameter by putting, flow velocity increase, to reach cracking reaction in reative cell 120
Technological requirement.
Fig. 1 and Fig. 6 are refer to, reative cell 120 is tube furnace, and its inwall is insulation material.Reative cell 120 includes reaction
Section, quench zone and stay segment, conversion zone, quench zone and stay segment are followed successively by from the entrance of reative cell 120 to outlet.Enter in conversion zone
Row cracking reaction, multiple spray heads 121, spray head 121 and circulation for cooling are provided with the tube wall of quench zone
260 connections.The buffering circulation of stay segment inner exhaust gas, carbon dust float in stay segment.
Refer to Fig. 3, air preheater 130 is tube-sheet heat exchanger, the tube-side inlet 131 of air preheater 130 with it is anti-
The outlet of room 120 is answered, tube side outlet 132 connects with the collection system 210 of reative cell 120, anti-by cracking in reative cell 120
The tail gas for the obtained high temperature answered is transported to collection system 210 by the tube side of air preheater 130.The shell of air preheater 130
Journey connects with air delivery system 170, and the air in air delivery system 170 flows from the shell side inlet 133 of air preheater 130
Enter, flowed out after the progress heat exchange of the tail gas of air preheater 130 and high temperature from shell-side outlet 134.It should be appreciated that air preheat
Device 130 can be tube-sheet type or shell-and-tube, and no matter which kind of heat exchanger is attained by the technique effect of heat exchange, all
In the protection domain of the present embodiment.
Continue referring to Fig. 3, tail gas pre-heater 140 is shell-and-tube heat exchanger, the tube-side inlet 141 of tail gas pre-heater 140 with
The outlet of reative cell 120 is connected by pipeline communication, tube side outlet 142 with collection system 210；The shell side of tail gas pre-heater 140 with
Two level tail gas transmission system 180 connects.The shell side of two level tail gas in two level tail gas transmission system 180 from air preheater 130
Entrance 143 flows into, and is flowed out after the progress heat exchange of the tail gas of tail gas pre-heater 140 and high temperature from shell-side outlet 144.It should manage
Solution, the type of tail gas pre-heater 140 can be tube-sheet type or shell-and-tube, and no matter which kind of preheater is attained by
The technique effect of heat exchange, all in the protection domain of the present embodiment.
Fig. 4 and Fig. 5 are refer to, tank field system 190 includes multiple storage tanks, and storage tank is divided into petroleum tank 191 and carbolic oil oil-washing tank
192.The shape and structure of petroleum tank 191 is identical with carbolic oil oil-washing tank 192.Illustrated with the structure example of petroleum tank 191, petroleum tank
191 and the outlet of carbolic oil oil-washing tank 192 be provided with screen pack 193, screen pack 193 is used for filtering corrosive product iron sulfide and sulphur list
Matter.For storage tank, substantial amounts of corrosion product iron sulfide and sulphur simple substance can be especially generated in petroleum tank 191.Corrosion product
Generation have very big potential safety hazard.If make these corrosion products as oil flows into reactor 110 together or other set
It is standby, no small potential safety hazard may be brought.Corrosion product can be blocked in the outlet of storage tank by the setting of screen pack 193,
During maintenance clean afterwards, corrosion product is washed, the setting of screen pack 193 effectively reduces potential safety hazard.
Fluted 196 are set on the surface that the base 194 of petroleum tank 191 contacts with ground, the both ends of groove 196 connect
Two relative sides 195 of base 194.One end of connecting rod 197 is flexibly connected by butterfly hinge 199 with side 195, connecting rod
197 other end is connected with universal wheel 198.Under a kind of state, connecting rod 197 is in contact with side 195, and petroleum tank 191 is placed
On the ground；When needing to move another state of petroleum tank 191, butterfly hinge 199 is pulled, connecting rod 197 is in same with side 195
In one plane, universal wheel 198 contacts ground, and ground is left in the bottom of base 194, and the movement of petroleum tank 191 can be achieved.
Fig. 2 and Fig. 6 are refer to, the first feedstock oil of tank field system 190 is sent to combustion by the first feedstock oil transmission system 150
Room 111 is burnt, air delivery system 170 will pass through the sky of heat exchange heating by pump in the tail gas of air preheater 130 and high temperature
Gas is sent to the entrance of combustion chamber 111.
First Heat Exchanger 151 is provided with second feedstock oil transmission system 160, the second raw material from tank field system 190
Oil is transferred into the entrance of trunnion 112 after the heat exchange heating of First Heat Exchanger 151.
Two level tail gas transmission system 180 connects with combustion chamber 111, and the two level tail gas from exhaust gas purification system 240 is in tail
In air preheater 140 after heat exchange heats up, it is transferred into combustion chamber 111 and is burnt.
Air compressor machine 172 is connected with air reservoir 171, and air reservoir 171 is connected by pipeline and pump with combustion chamber 111.
The tail gas for the high temperature discharged from air preheater 130 and tail gas pre-heater 140 is after the cooling of the second heat exchanger 152
It is transported to the second heat exchanger 152.
Fig. 1 and Fig. 6 are refer to, tank field system 190 includes petroleum tank 191 and carbolic oil oil-washing tank 192, petroleum tank 191 and
One feedstock oil transmission system 150 connects with the second feedstock oil transmission system 160, to send feedstock oil to carbon black reaction system
100.Carbolic oil oil-washing tank 192 is connected with granulating and drying system 220, and thermal source is provided for granulating and drying system 220.
The operation principle of carbon black reaction system 100：First feedstock oil transmission system 150 is former by the first of tank field system 190
Material oil is sent to the entrance of combustion chamber 111；Air is stored in air reservoir 171 by air compressor machine 172, the air in air reservoir 171
Also it is sent to the entrance of combustion chamber 111；Air in air delivery system 170 is after air preheater 130 carries out heat exchange
It is sent to the entrance of combustion chamber 111；Second feedstock oil of tank field is sent to the entrance of trunnion 112 by the second feedstock oil transmission system 160,
In the transmit process of the second feedstock oil, the first feedstock oil carries out heat exchange heating in First Heat Exchanger 151, it is preheated after second
Feedstock oil is easier to make for cracking reaction, and has saved energy.In combustion chamber 111, the first feedstock oil with air burn instead
Heat should be discharged, the heat of release is by the second fuel oil preheating.Gas caused by second feedstock oil and the combustion reaction of combustion chamber 111
Flowing velocity is accelerated after trunnion 112, rear into reative cell 120 that pyrolytic reaction occurs.Height of the carbolineum in 120 thousands of degree of reative cell
Temperature lower cracking reaction production hydrogen, vapor, carbon monoxide, carbon dioxide and carbon dust.It should be understood that in the present embodiment, reaction
Raw material be carbolineum but it is also possible to be other aromatic hydrocarbons heavy oil.Carbon black pellet is smaller, by hydrogen, vapor, carbon monoxide, dioxy
Change four kinds of gas purging discharges of carbon, form the tail gas of high temperature.It is provided with the tube wall of the quench zone of reative cell 120 for cooling down drop
The spray head 121 of temperature, spray head 121 connect with circulation 260.
Air preheater 130 is flowed into from a tail gas part for the high temperature of the outlet of reative cell 120 discharge, another part flows into tail
Air preheater 140.The tail gas of high temperature carries out heat exchange in air preheater 130 and tail gas pre-heater 140, and temperature reduces heel row
Go out, be delivered to the removing carbon black of collection system 210 after then flowing through the 152 further heat exchange cooling of the second heat exchanger, be delivered to
Exhaust gas purification system 240 obtains two level tail gas after removing vapor.Due to there is temperature-fall period during removing vapor, obtain
Two level exhaust temperature be less than 100 DEG C.Now the main component in two level tail gas is hydrogen, carbon monoxide and carbon dioxide, two
Level tail gas tail gas pre-heater 140 after heat exchange heats up by two level tail gas transmission system 180, deliver to combustion chamber 111 and enter
Mouthful.Due to containing imflammable gas hydrogen and carbon monoxide in two level tail gas, combustion chamber 111 is sent back to after two level tail gas is heated up,
Hydrogen and carbon monoxide can be used as fuel to carry out combustion reaction first, and reducing the dosage of the first feedstock oil reduces cost.
Meanwhile the two level exhaust temperature after heat exchange raises, the input of energy is decreased during burning.This implementation
The process route of example is set, and corresponding equipment setting realizes energy regenerating, has saved cost.
Simultaneously in the air preheater 130 of reactor 110, tail gas and the air in air delivery system 170 of high temperature enter
Row heat exchange, the heat that the tail gas of high temperature carries is transmitted to the air of low temperature, and the air by heating is carried out into combustion chamber 111
Combustion reaction, because air has carried out heat exchange in air preheater 130 in advance, temperature is raised, thus anti-in burning
Burned, release heat is easier in answering.
Fig. 6 is refer to, the present embodiment also provides a kind of carbon black process system 200 for including above-mentioned carbon black reaction system 100,
Above-mentioned carbon black process system 200 also includes circulation 260, collection system 210, granulating and drying system 220, storage package system
System 230, exhaust gas purification system 240, tank field system 190 and circulation 260.Second heat exchanger of carbon black reaction system 100
152 are connected with collection system 210, and the tail gas of carbon black reaction system 100 is sent into collection system 210.Collection system 210 is successively
Connected with granulating and drying system 220 and storage package system 230.Collection system 210 also connects with exhaust gas purification system 240, tail
Gas cleaning system 240 connects with two level tail gas transmission system 180.
In the tail gas of air preheater 130, tail gas pre-heater 140 Jing Guo heat exchange, carbon black is carried out in collection system 210
Collect, carbon black and gas are separated.Tail gas by the heat exchange of tail gas pre-heater 140 removes water by exhaust gas purification system 240
Two level tail gas is obtained after steam, two level tail gas is sent to the entrance of combustion chamber 111 through two level tail gas transmission system 180.Tank field system
190 be that the first feedstock oil transmission system 150 and the second feedstock oil transmission system 160 provide the first feedstock oil and the second feedstock oil,
In the present embodiment, the first feedstock oil and the second feedstock oil are carbolineum, in other embodiments or other raw materials.
The carbon black of collection becomes spheroid product after granulating and drying system 220, and spheroid product is packed through storage package system 230
Product.
In summary, a kind of carbon black reaction system 100, the reaction of above-mentioned carbon black reaction system 100 be the utility model is related to
The outlet of device 110 has been arranged in parallel air preheater 130 and tail gas pre-heater 140.The high temperature obtained by the reaction of Pintsch process
Tail gas carry out heat exchange in air preheater 130 and air, while the tail gas of high temperature is in tail gas pre-heater 140 and two level tail gas
Carry out heat exchange.The heat of carrying has been transmitted to two level tail gas and air by the tail gas of high temperature, realizes the recycling to energy,
Cost is saved.The utility model also provides a kind of carbon black process system 200 for including above-mentioned carbon black reaction system 100, above-mentioned
The heat of carrying has been transmitted to two level tail gas and air by the tail gas of high temperature by carbon black process system 200, realizes and energy is returned
Receive and utilize, saved cost.
Preferred embodiment of the present utility model is the foregoing is only, is not limited to the utility model, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all in the spirit and principles of the utility model
Within, any modification, equivalent substitution and improvements made etc., it should be included within the scope of protection of the utility model.
Claims (10)
1. a kind of carbon black reaction system, it is characterised in that it includes reactor, the first feedstock oil transmission system, the second feedstock oil
Transmission system, tank field system, air delivery system and two level tail gas transmission system, the reactor include combustion chamber, trunnion,
Reative cell, air preheater and tail gas pre-heater, the combustion chamber, the trunnion and the reative cell are sequentially communicated, described anti-
The outlet of room is answered to be connected respectively with the air preheater and the tail gas pre-heater so that the tail gas in the reative cell is direct
The air preheater and the tail gas pre-heater, the first feedstock oil transmission system and the combustion chamber are delivered to,
The second feedstock oil transmission system connects with the trunnion；The tank field system is multiple storage tanks, is set on the storage tank base
Multiple grooves are equipped with, connecting rod and universal wheel are provided with the groove, one end of the connecting rod is connected with the universal wheel, another
End is connected by butterfly hinge with the groove；The tank field system connects with the first feedstock oil transmission system, the tank
Sound zone system also connects with the second feedstock oil transmission system；The air delivery system connects with the air preheater, institute
State two level tail gas transmission system and be respectively communicated to the entrance of the tail gas pre-heater and the reactor with by the two level tail gas
Two level tail gas after being heated in transmission system is delivered to the combustion chamber.
2. carbon black reaction system according to claim 1, it is characterised in that the air preheater by pipeline with it is described
Tail gas pre-heater connects.
3. carbon black reaction system according to claim 2, it is characterised in that the tail gas pre-heater is described anti-to be multiple
The outlet of room is answered to be connected by pipeline with multiple tail gas pre-heaters.
4. carbon black reaction system according to claim 3, it is characterised in that the tube-side inlet of the air preheater and institute
Reative cell connection is stated, the tube side outlet of the air preheater connects with collection system；Sky from the air delivery system
By the air preheater shell side and the tail gas in the tube side of the air preheater heat exchange occurs for gas.
5. carbon black reaction system according to claim 3, it is characterised in that the tube-side inlet of the tail gas pre-heater passes through
Pipeline connects with the reative cell, and the tube side outlet of the tail gas pre-heater connects with collection system；From the two level tail gas
The two level tail gas of transmission system occurs heat with the tail gas in the tail gas pre-heater tube side by the tail gas pre-heater shell side and handed over
Change.
6. carbon black reaction system according to claim 1, it is characterised in that the carbon black reaction system also includes recirculated water
System, the circulation are connected by spray head with the outer wall of the reative cell, pass through the water in the circulation
Cooled down to cracking reacted tail gas.
7. carbon black reaction system according to claim 6, it is characterised in that the air preheater and tail gas preheating
Device connects with the second heat exchanger, described the after the air preheater and the mixing of the tail gas of the tail gas pre-heater
Two heat exchangers carry out heat exchange with the recirculated water in the circulation.
8. carbon black reaction system according to claim 1, it is characterised in that the storage tank is divided into petroleum tank, carbolic oil washing oil
Tank, the petroleum tank are connected with the first feedstock oil transmission system and the second feedstock oil transmission system, and the carbolic oil is washed
Oil tank and granulating and drying system connectivity.
9. carbon black reaction system according to claim 8, it is characterised in that the outlet of the storage tank is provided with for filtering
The screen pack of Tank corrosion product.
10. a kind of carbon black process system, it is characterised in that it includes the carbon black reaction system as described in claim any one of 1-9
System, collection system, granulating and drying system, storage package system, exhaust gas purification system, the carbon black reaction system and the collection
System connectivity, tail gas caused by the carbon black reaction system is sent to the collection system, the collection system, described made
Grain drying system and the storage package system be sequentially communicated, pelletizing of carbon black is packed, the collection system also with the tail
Gas cleaning system connects, and the exhaust gas purification system connects with the two level tail gas transmission system, by the two level tail after purification
Gas is passed through the combustion chamber as fuel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104218.0U CN206721081U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black reaction system and carbon black process system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720104218.0U CN206721081U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black reaction system and carbon black process system |
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| CN206721081U true CN206721081U (en) | 2017-12-08 |
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| CN201720104218.0U Expired - Fee Related CN206721081U (en) | 2017-01-23 | 2017-01-23 | A kind of carbon black reaction system and carbon black process system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108610661A (en) * | 2018-04-18 | 2018-10-02 | 句容市盛达环保净化材料有限公司 | The method of producing black pigment of cooling water recycling |
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2017
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108610661A (en) * | 2018-04-18 | 2018-10-02 | 句容市盛达环保净化材料有限公司 | The method of producing black pigment of cooling water recycling |
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