CN203333554U - Multi-throat carbon black reaction furnace - Google Patents
Multi-throat carbon black reaction furnace Download PDFInfo
- Publication number
- CN203333554U CN203333554U CN2013200693044U CN201320069304U CN203333554U CN 203333554 U CN203333554 U CN 203333554U CN 2013200693044 U CN2013200693044 U CN 2013200693044U CN 201320069304 U CN201320069304 U CN 201320069304U CN 203333554 U CN203333554 U CN 203333554U
- Authority
- CN
- China
- Prior art keywords
- section
- trunnion
- carbon black
- throat
- trunnions
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Landscapes
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Abstract
The utility model discloses a multi-throat carbon black reaction furnace which consists of a combustion section (3), a reducing guide section (4), a throat section (6), a reaction section (8), a quenching section (9) and a retention section (10) and is characterized in that two or more throats (14) are arranged at the throat section (6). The multi-throat carbon black reaction furnace disclosed by the utility model has the advantages that the process (combustion-supporting) air enters from the end part of the combustion section of the reaction furnace; the throat section of the carbon black reaction furnace is changed from a one-hole section into a multi-hole section; the multi-hole reaction section corresponds to the multi-throat section; and raw material oil enters each throat. The traditional reaction furnace mode of one throat for one carbon black reaction furnace is changed; the problem of imperfect product quality caused by non-uniform atomization mixing of the raw material oil of the large-diameter throat is improved; top-grade carbon black can be produced by use of a lower-quality oil material to realize the effects of effectively utilizing the resources, lowering the cost and increasing the economic benefits; and the multi-throat carbon black reaction furnace disclosed by the utility model is particularly applicable to the technical field of tread carbon black production.
Description
Technical field
The utility model belongs to the rubber grade carbon black technical field, is tire tread carbon black plant technical field furtherly, relates in particular to the Reaktionsofen of producing N100, N200, N300 series carbon black.
Background technology
The black reactor be applied in all devices in the carbon black manufacturing processed, particularly production of carbon black is the nucleus equipment of carbon black production device.
Black reactor, in the chemical industry technical field, is that a kind of temperature of reaction is high, heat load intensity is large, one of the reactor of severe reaction conditions.Almost the major progress each time of carbon black production technology all relates to the improvement of carbon black reactor directly or indirectly.
The experimental study of carbon black reactor and to design and develop be to improve carbon black list furnace output and efficiency, raising reactor hot strength, the reaction of strengthening soot formation is ultimate aim.
Common carbon black is the carbon black that adopts oven process to manufacture, and is divided into tyre surface carbon black and carcass carbon black, in the industry the inside, is called again: hard (carbon) black and soft carbon, and oven process tyre surface carbon black manufacture method generally has two kinds.
A kind of is regardless of oil fuel and stock oil, by black reactor, is axially entered.Oil plant part fuel combustion under the effect of process (combustion-supporting) air provides the hot kinetic energy of remainder oil-cracking, generates the mixture of carbon black and flue gas.
Another kind be oil fuel (gas) in the perfect combustion of black reactor burning zone, the hot kinetic energy of the oil breaking of supplying raw materials, radially inject the stock oil atomization in the trunnion section and mix, and generates the mixture of carbon black and flue gas in the conversion zone cracking.
Above-mentioned two kinds of methods, the mixture of carbon black and flue gas is all stopped carbon black at quench zone by quenched water and reacts.
Furnace treated black production so far, has been experienced double teacher: first-generation carbon black reactor: single chamber/bis-chamber black reactor; S-generation carbon black reactor: new process carbon black Reaktionsofen; Third generation carbon black reactor: the black reactor of low hysteresis carbon black; The 4th generation carbon black reactor: maximization new process carbon black Reaktionsofen; The 5th generation carbon black reactor: nano carbon black/heterogeneous black reactor.
The main flow of the black reactor used at present be the 4th generation carbon black reactor: maximization new process carbon black Reaktionsofen.It is the improvement scale-up version Reaktionsofen on s-generation black reactor-new process carbon black reactor basis.
Along with the development of off-colour industry, single furnace output is improving gradually.Single furnace output is developed into the maximization black reactor of producing 60kt per year by the black reactor of producing 5kt per year.
Along with the increase of single furnace output, the way of usually enhancing production capacities is augmenting response stove size.Reaktionsofen burning zone size increases, and brings the uniformity coefficient of thermal load to improve, and has improved the hot kinetic energy that is conducive to the stock oil cracking; The increase of trunnion section size, enlarge in the lower concentration mist of oil district at trunnion central axis position, is unfavorable for raw material oil throwing and mixing; The increase of conversion zone size, cause that the high temperature field of soot formation and the unevenness of aerodynamic field increase, and have affected the identity of the form of carbon black; The increase of quench zone size, the quenched water that makes usually to adopt hydraulic giant radially to spray can not whole shutoff quench zone cross section, causes the termination reaction time difference, has influence on form and the quality of carbon black.
When particularly producing according to the N100, the N200 that stipulate in new national standard 3778-2011 standard, N300 series carbon black, problem due to technology and equipment, can not reach the intermediate value requirement of stipulating in standard always, the main quality index of its product all the lower limit of standard-required even below, it is up to standard reluctantly before this standard is not implemented, new standard substantially all is judged to substandard product after implementing.In order to produce qualified carbon black products, be all generally to adopt high-quality carbolineum as stock oil, cost rises like this, and quality is also extremely unstable because carbon black products can not reach the intermediate value of standard code.Now domestic general method of producing black pigment is that oil mixes the formation carbon black oil at the bottom of the tower adopted after carbolineum and coal tar distillation, manufacture rubber tyre surface carbon black, but quality is difficult to the requirement of the standard that reaches, after particularly having adopted new GB, original technique does not reach the qualified product output of intermediate value substantially.
And, because the Reaktionsofen size increases, the problem that the quality product of bringing descends can't overcome, therefore, for the general many stoves parallel connection that adopts of enhancing production capacities.Be that a plurality of black reactors are in parallel after Reaktionsofen or after air preheater, what also have is in parallel before entering main bag filter.So both the increasing device floor space, increased again plant investment, reduced economic benefit.No matter be the production technique that increases the size of black reactor or adopt black reactor in parallel, up to now, the structure of black reactor is the single throat tubular construction form of a trunnion of a Reaktionsofen always.
In order to change this state, contriver of the present utility model has done a large amount of research and test, has proposed goal of the invention of the present utility model.
The utility model content
Goal of the invention of the present utility model is just must increase the size of black reactor or the industry idea of black reactor in parallel in order to overcome above-mentioned increase carbon black output, and the structure that changes black reactor is the traditional concept of the single throat tubular construction form of a trunnion of a Reaktionsofen always.A kind of many trunnions black reactor is provided.
Technical solution of the present utility model is to realize like this, this many trunnions black reactor, there is burning zone (3), convergent diversion section (4), trunnion section (6), conversion zone (8), quench zone (9), remaining portion (10) forms, and it is characterized in that the quantity of the trunnion (14) of trunnion section (6) is more than 2 or 2.Such structure can produce hard (carbon) black smoothly, and does not need to change other devices.
Useful technique effect of the present utility model is: black reactor trunnion Duan Youyi hole changes over porous, and the porous reaction section is corresponding with many trunnions section, and stock oil enters respectively each trunnion.Changed the Reaktionsofen pattern that a traditional black reactor can only a trunnion; Improve the atomization of major diameter trunnion stock oil and mixed the quality product shortcoming problem of being not good at causing; Can use low-qualityer carbon black feed stock oil plant to produce high-grade carbon black, reach efficent use of resources, reduce costs, promote the effect of economic benefit, patent of the present invention is particularly suitable for tyre surface carbon black production technology field.
The accompanying drawing explanation
Embodiment
Below in conjunction with the embodiment provided in accompanying drawing, structure of the present utility model and use are elaborated.With reference to accompanying drawing, accompanying drawing 1 and accompanying drawing 2 form the embodiment that 4 trunnions form; Accompanying drawing 1 and accompanying drawing 3 form the embodiment of 3 trunnions, and accompanying drawing 1 and accompanying drawing 2 trunnions of 4 compositions and trunnion section contour structures are oval-shaped embodiment; Accompanying drawing 1 and accompanying drawing 5 form the embodiment of the another kind of trunnion segment structure form of 2 trunnions.As for the embodiment more than 4 trunnions, from above-mentioned 4 kinds of structures can the order inference out.From accompanying drawing, can clearly be seen that, the black reactor of trunnion more than this kind, there is burning zone (3), convergent diversion section (4) trunnion section (6), conversion zone (8), quench zone (9), remaining portion (10) forms, and it is characterized in that the quantity of the trunnion (14) of trunnion section (6) is more than 2 or 2.
In order to improve the efficiency of hot kinetic energy, between the convergent diversion section (4) at the front portion of said trunnion section (6) and burning zone (3) rear portion, there is the porous trunnion diversion section (5) corresponding with trunnion (14) quantity.
In order to increase the reaction efficiency of carbon black, there is the reaction tubes (15) corresponding with the trunnion quantity of trunnion section (6) in said conversion zone (8) inside.
In order to improve the efficiency of carbon black reaction, control the reaction fine degree of trunnion, the quantity of said trunnion is controlled as 2-12.
In order to adapt to the characteristics of current software control procedure, through optimizing, the quantity of said trunnion is 2-6.
In order to adapt to the actual production requirement of many trunnions black reactor, in many trunnions outside of said trunnion section (6), there is a coolant jacket with cooling fluid entrance (11) and cooling liquid outlet (7).In the trunnion section, to adopt liquid cooling, liquid is the fluent meterial that water, thermal oil or other specific heat are large, boiling point is higher.Therefore, the trunnion section can adopt steel to make, thereby can realize easily from 2 trunnions until 12 structural requirements of the even or inhomogeneous arrangement of 20 trunnions even.
Chilling hydraulic giant (13) in said quench zone (9) is by the radial spray hydraulic giant and axially sprays the chilling hydraulic giant combination that hydraulic giant forms.Form radially hydraulic giant and axially the protected type cooling surface of hydraulic giant composition at quench zone, stop the reaction of carbon black in the time of can waiting, the aggregate that makes carbon black need this section formation and the shape of other requirements.
The Fuel lance (21) of said burning zone (3) is perpendicular to the axis of burning zone, at the circumferential direction of burning zone, is radial array.This spread pattern, can take full advantage of the heat energy of preheated air and fully mix with the air of preheating.More independent axial oil atomizer gun or jet gun have better combustion efficacy and provide larger hot kinetic energy intensity for carbon black reacts.Also can adopt axial spray gun (2) and the structure formation of spray gun (21) combination radially.
Said raw material spray gun (12) is the raw material spray gun group around trunnion circumference radial arrangement.The raw material spray gun is generally the carbon black oil spray gun, can produce by different array modes the emitted dose of varying strength.
The device of this patent, can be applied to, in the construction of Reaktionsofen of the current various structure formations such as vertical, horizontal, structure, can replace fully.Further, on the basis of former black reactor, the finite structure transformation through partial combustion section, trunnion section, conversion zone, can realize producing the product that meets specified requirement in the GB3778-2011 standard.
The carbon black of being produced by this Reaktionsofen, be generally the tyre surface carbon black in rubber grade carbon black, namely so-called hard (carbon) black in common industry.According to the specified standards in GB 3778-2011, belong to the carbon black of N100, N200, N300 series.
Device of the present utility model, adopt carbon black oil fully, both can produce the N200 that meets national Specification and the rubber tread carbon black of N300 series.From the angle of energy utilization, replace expensive carbolineum fully and produced hard (carbon) black, and can stablize the requirement be up to state standards, produced beyond thought effect.The fact of this patent, overcome the technology prejudice that black reactor all the time can only stove one trunnion, and overcome the industry prejudice that the low-quality carbon black oil that always exists in the carbon black industry can not be produced separately high-quality hard (carbon) black.
In a word, by the enforcement of this patent, can use the high-grade carbon black of low-qualityer oil seed production, reach efficent use of resources, reduce costs, promote the economic benefit of enterprise.For entire society, produced the social benefit of great saving and reusing of energy source, there is great application value.
Below provide the technical parameter of producing 40000 tons of different sorts carbon blacks per year, the effect produced with the device to this patent provides concrete technical indicator reference.
In table:
FIC103 Nm
3/ h--------process (combustion-supporting) air rate;
FIC102 (oil) kg/h-----oil fuel flow rate;
FIC101 (oil) kg/h-----stock oil flow rate.
From also can find out the production effect of equipment of the present utility model in table, be difficult to reach tinctorial strength, the CTAB specific surface area of the intermediate value of GB regulation in the past, the technical parameter index of outer surface area now all can reach, the quality and performance of product approaches and has reached the standard-required of U.S.'s carbon black products.
Claims (9)
1. trunnion black reactor more than a kind, there is burning zone (3), convergent diversion section (4), porous trunnion diversion section (5), trunnion section (6), conversion zone (8), quench zone (9) and remaining portion (10) form, burning zone disposes air distributor and Fuel lance, the burning zone rear portion is convergent diversion section (4), this convergent diversion section is communicated with trunnion section (6) by porous trunnion diversion section (5), trunnion section rear portion is conversion zone (8), the rear portion of conversion zone is quench zone (9), the rear portion of quench zone is remaining portion (10), the quantity that it is characterized in that the trunnion (14) of trunnion section (6) is more than 2 or 2.
2. according to a kind of many trunnions black reactor claimed in claim 1, between the front portion that it is characterized in that said trunnion section (6) and the convergent diversion section (4) at burning zone (3) rear portion, there is the porous trunnion diversion section (5) corresponding with trunnion (14) quantity.
3. according to the described a kind of many trunnions black reactor of claim 1 or 2, it is characterized in that said conversion zone (8) inside has the reaction tubes (15) corresponding with the trunnion quantity of trunnion section (6).
4. according to a kind of many trunnions black reactor claimed in claim 3, the quantity that it is characterized in that said trunnion is 2-12.
5. according to a kind of many trunnions black reactor claimed in claim 4, the quantity that it is characterized in that said trunnion is 2-6.
6. according to a kind of many trunnions black reactor claimed in claim 3, it is characterized in that many trunnions outside of said trunnion section (6) has a coolant jacket with cooling fluid entrance (11) and cooling liquid outlet (7).
7. according to a kind of many trunnions black reactor claimed in claim 3, it is characterized in that chilling hydraulic giant (13) in said quench zone (9) is by the radial spray hydraulic giant and axially spray that hydraulic giant is formed in that same cross section or different cross section arrange the combination of chilling hydraulic giant.
8. according to a kind of many trunnions black reactor claimed in claim 1, it is characterized in that the axis of the Fuel lance (21) of said burning zone (3) perpendicular to burning zone, at the circumferential direction of burning zone, be radial array or be parallel to one or more than one Fuel lance (2) of the axis of burning zone.
9. according to a kind of many trunnions black reactor claimed in claim 3, it is characterized in that said raw material spray gun (12) is for the raw material spray gun group around trunnion circumference radial arrangement.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200693044U CN203333554U (en) | 2013-02-06 | 2013-02-06 | Multi-throat carbon black reaction furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013200693044U CN203333554U (en) | 2013-02-06 | 2013-02-06 | Multi-throat carbon black reaction furnace |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203333554U true CN203333554U (en) | 2013-12-11 |
Family
ID=49702244
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013200693044U Expired - Fee Related CN203333554U (en) | 2013-02-06 | 2013-02-06 | Multi-throat carbon black reaction furnace |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203333554U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103980741A (en) * | 2014-04-11 | 2014-08-13 | 嘉峪关大友嘉能化工有限公司 | Method and reacting furnace for production of rubber-grade carbon black from coal tar |
| CN113502070A (en) * | 2021-08-04 | 2021-10-15 | 烁元新材料(东营)股份有限公司 | Low-rolling-resistance carbon black discharging forming device for tire and forming processing method |
| CN113667327A (en) * | 2021-09-17 | 2021-11-19 | 山西焦化股份有限公司 | Production method of carbon black |
-
2013
- 2013-02-06 CN CN2013200693044U patent/CN203333554U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103980741A (en) * | 2014-04-11 | 2014-08-13 | 嘉峪关大友嘉能化工有限公司 | Method and reacting furnace for production of rubber-grade carbon black from coal tar |
| CN103980741B (en) * | 2014-04-11 | 2016-01-20 | 嘉峪关大友嘉能化工有限公司 | A kind of method and Reaktionsofen producing rubber grade carbon black with coal tar |
| CN113502070A (en) * | 2021-08-04 | 2021-10-15 | 烁元新材料(东营)股份有限公司 | Low-rolling-resistance carbon black discharging forming device for tire and forming processing method |
| CN113667327A (en) * | 2021-09-17 | 2021-11-19 | 山西焦化股份有限公司 | Production method of carbon black |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103980741B (en) | A kind of method and Reaktionsofen producing rubber grade carbon black with coal tar | |
| CN109054460B (en) | Novel hard carbon black reacting furnace | |
| CN105647242B (en) | A kind of reacting furnace for preparing ultra-wide aggregation distribution carbon black and preparation method thereof | |
| CN203333554U (en) | Multi-throat carbon black reaction furnace | |
| CN101891976A (en) | Novel soft carbon black reaction furnace | |
| CN103113764A (en) | Multi-choke carbon black reacting furnace | |
| CN202148276U (en) | Hard carbon black reaction furnace | |
| CN102286221B (en) | Hard carbon black reaction furnace | |
| EP2563864B1 (en) | Carbon black reactor | |
| CN110511599A (en) | Hard (carbon) black reacting furnace | |
| CN101920186B (en) | High treatment capacity feed atomizing nozzle | |
| CN109135350B (en) | 5 ten thousand tons/year natural gas hard carbon black reacting furnace | |
| CN210711361U (en) | Hard carbon black reaction furnace | |
| CN102964883A (en) | Hot-cracking-method carbon black production process assisted by hydrogen-enriched gas | |
| CN102850826B (en) | Preparation process of pigment carbon black, and combustion furnace thereof | |
| CN203704727U (en) | Novel high-temperature carbon black raw oil preheating device | |
| CN111393878A (en) | Method for producing carbon black by mixing raw oil | |
| CN215924826U (en) | Carbon black reaction furnace for preparing conductive carbon black | |
| CN202359057U (en) | Hard carbon black reaction furnace applicable to coal tar material | |
| CN203373306U (en) | Pipework of carbon black reacting furnace | |
| CN106675113A (en) | U-shaped carbon black reaction furnace device for producing carbon black | |
| RU2394054C2 (en) | Method of producing semi-active technical carbon and reactor for realising said method | |
| CN204661597U (en) | A kind of black reactor trunnion device | |
| CN105950206B (en) | It is a kind of to simulate the device and method that the quick coking of carbonaceous macromolecular delayed coking prepares coking | |
| CN203833862U (en) | Carbon black reacting furnace throat pipe device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131211 Termination date: 20160206 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |