CN112679998A - Preparation facilities of high pigment carbon black - Google Patents
Preparation facilities of high pigment carbon black Download PDFInfo
- Publication number
- CN112679998A CN112679998A CN202110028920.4A CN202110028920A CN112679998A CN 112679998 A CN112679998 A CN 112679998A CN 202110028920 A CN202110028920 A CN 202110028920A CN 112679998 A CN112679998 A CN 112679998A
- Authority
- CN
- China
- Prior art keywords
- gas
- carbon black
- tail gas
- equipment
- ozone
- 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.)
- Pending
Links
Images
Landscapes
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Abstract
The invention discloses a preparation device of high-pigment carbon black, which comprises an ozone generating device, a material mixing device, a gas-solid separation device and a tail gas decomposition device, and is characterized in that the material mixing device comprises a cylinder, a material inlet, a material outlet, a gas inlet and a tail gas outlet; the material outlet is connected with the material tank through a valve body; the gas inlet is connected with the ozone generating equipment; the tail gas outlet is connected with the gas-solid separation equipment; the gas-solid separation equipment can be connected with the tail gas decomposition equipment; the barrel can rotate.
Description
Technical Field
The present invention relates to a method and an apparatus for producing high-color carbon black, and more particularly, to a method and an apparatus for oxidizing carbon black with a mixed gas containing ozone and other gases.
Background
In ancient times, people burned animal and vegetable oils, pine branches, and collected the black ash (the earliest carbon black) that was used in the formulation of inks and black pigments. In 1872, the first commercial production of Carbon Black on a large scale occurred in the world, with the formation of the term "Carbon Black".
The pigment carbon black is carbon black used for production of products such as printing ink, paint, plastics and the like, and accounts for about 90% of non-rubber carbon black. The classification of pigment carbon blacks is internationally generally classified into three types, i.e., high-pigment carbon blacks, medium-pigment carbon blacks, and low-pigment carbon blacks, according to the coloring power of the carbon blacks.
The binders for coatings, paints and printing inks are generally polar, whereas conventional carbon black has few surface functional groups and no polarity per se, and thus is difficult to disperse uniformly in a solvent. Therefore, it is necessary to perform oxidation treatment on carbon black to increase oxygen-containing functional groups on the surface of the carbon black, thereby increasing the polarity of the surface of the carbon black and facilitating dispersion in a solvent.
The oxidation modification technology used at home and abroad at present is divided into liquid phase oxidation, gas phase oxidation, plasma oxidation and the like. The liquid phase oxidation uses nitric acid, potassium permanganate, sodium hypochlorite and the like as oxidants, the technology is mature, and generally, the processes of oxidation, water washing, drying and the like are carried out, so that more waste acid and waste water are generated, and the pollution is serious. Plasma oxidation and catalyst oxidation have high requirements on experimental conditions and high required cost. The oxidant used in the gas phase oxidation mainly comprises ozone, oxygen, air, carbon dioxide and the like, wherein the technology for oxidizing carbon black by ozone has the advantages of high oxidation efficiency, mild reaction conditions, environmental protection, low cost and the like.
Xu Chen et al use air and ozone oxidation Carbon black, XPS results show that air oxidation makes the surface oxygen content 7.3 times the original, ozone treatment surface oxygen content 10 times the former (Xu Chen, Mark Farber, et al. mechanisms of surfactant adsorption on non-polar, air-oxidized and ozone-treated Carbon surfaces [ J ] Carbon 2003, 41 (8): 1489-1500). After ozone oxidation treatment, the volatile content of common carbon black is increased, and the pH value is changed from 8.25 to 3-4 (study on surface modification of Yidonating forest, Wanghaixing, ozone oxidation carbon black [ J ], Hebei chemical industry, 2006, 29 (7): 17-19). Experiments show that the pH value of the carbon black is reduced, the volatile content is increased, and the fluidity is increased along with the increase of the ozone oxidation time (Wuhaihua, the oxidation process of the carbon black and the research on preparing water-based color paste by oxidizing the carbon black [ D ]. the university of eastern China & 2017: 31-45).
The ozone oxidation device in US2682448 oxidizes carbon black by using a drum device and an exhaust gas recycling device, so that the pH value of the oxidized carbon black is reduced from 9-10 to 2.9-7. The ozone oxidation unit of US3353980 and CN202509026 uses a fluidized bed unit to oxidize carbon black. US3245820 uses a stirred bed to mix low structure furnace black (E.M. surface area at 120-150 m)2Between/g, BET specific surface area of 100-170m2G, oil absorption value of 7-14gal/100 lbs) with an ozone-containing gas stream to obtain a high flow, high pigment ink. US3333979 uses equipment to grind carbon black, destroys the agglomerate structure of the carbon black, and simultaneously introduces gas (air, oxygen, ozone, etc.) to increase the chemical activity of the carbon black, and the prepared carbon black is applied to butyl rubber, so that the tensile strength, elongation, modulus and wear resistance can be improved. CN201842796 and CN1958145 are both independent material mixing and oxidizing equipment. US9388300 is a liquid phase oxidation apparatus, requiring subsequent drying of the carbon black.
In order to realize industrialization conveniently, the invention designs a set of high-efficiency and energy-saving gas-phase carbon black oxidation method and equipment, and the equipment comprises an ozone carbon black oxidation device with a built-in shoveling plate, so that the material mixing can be accelerated, and the reaction time can be reduced; contain the tail gas and recycle the device, can not only reuse unreacted ozone, can also separate material and tail gas, do not harm equipment.
Disclosure of Invention
The invention relates to a preparation method of high-pigment carbon black, which is characterized by comprising the following steps: comprises a step of subjecting the mixed gas and carbon black to an oxidation reaction; the mixed gas comprises ozone and other gases; the volume ratio of the ozone to other gases is 1:100-100: 1; the flow rate of the mixed gas is 0.01L/min-50L/min; the reaction temperature of the oxidation reaction is 0-100 ℃; the reaction time of the oxidation reaction is 10min-20 h.
The carbon black used in the present invention is not particularly limited, and may be a pellet or a powder.
Preferably, the volume ratio of the ozone to the other gas is 1:100-100:1, preferably 1:50-90: 1.
The other gas is one or a mixture of air, oxygen and circulating tail gas.
The circulating tail gas is obtained by treating the tail gas by a gas-solid separation device and filtering the tail gas by a tail gas refiltering device.
Preferably, the flow rate of the mixed gas is 0.01L/min to 50L/min, preferably 0.1L/min to 30L/min.
Preferably, the reaction temperature is 0 ℃ to 100 ℃, preferably 10 ℃ to 80 ℃.
Preferably, the reaction time is 10min to 20h, preferably 30min to 10 h.
The invention also discloses a preparation device of the high-pigment carbon black, which comprises ozone generation equipment, material mixing equipment, gas-solid separation equipment and tail gas decomposition equipment, and is characterized in that the material mixing equipment comprises a cylinder, a material inlet, a material outlet, a gas inlet and a tail gas outlet; the material outlet is connected with the material tank through a valve body; the gas inlet is connected with the ozone generating equipment; the tail gas outlet is connected with the gas-solid separation equipment; the gas-solid separation equipment can be connected with the tail gas decomposition equipment; the barrel can rotate.
Preferably, the rotating speed of the cylinder is 0-10r/min, preferably 1-8r/min, and the speed can be regulated by variable frequency.
Preferably, the system further comprises an exhaust gas refiltering device, wherein the exhaust gas refiltering device comprises an air filter and a precision filter which are connected in sequence.
The air inlet of the ozone generating equipment can be filled with air, and the air outlet of the ozone generating equipment is connected with the material mixing equipment.
The air inlet of the ozone generating equipment can also be connected with the tail gas refiltering equipment, and circulating tail gas is introduced.
The material mixing equipment is made of stainless steel materials, a plurality of shoveling plates are arranged in the material mixing equipment, and the included angle between each shoveling plate and the cylinder wall is 30-120 degrees; preferably 50 to 100.
The gas-solid separation equipment is one or more cyclone separators, and the gas-solid separation equipment is connected with the tail gas decomposition equipment and/or the tail gas refiltering equipment.
The exhaust gas decomposition device may destroy ozone in the exhaust gas using high temperature or a catalyst.
The tail gas refilter equipment comprises an air filter and a precision filter which are sequentially connected, and dust is further removed from the tail gas through the tail gas refilter equipment, so that the dust is prevented from entering the ozone generator through a tail gas recycling pipeline.
The carbon black obtained by the method of the present invention has a fluidity of greater than 20mm, a pH value of less than 6 and a reflectance of less than 30.
The invention also discloses application of the carbon black in printing ink, coating, batteries, plastics and papermaking.
The invention aims to provide a method and a device for preparing high-pigment carbon black, wherein the method is simple, convenient and feasible, has low cost, is beneficial to preparing the high-pigment carbon black, has a simple device structure, is easy to operate, and can recycle tail gas.
The carbon black selected by the invention can be granules or powder, the indexes of pH value, fluidity, blackness and the like of the carbon black are changed by controlling the process conditions of ozone concentration, airflow, pressure, reaction temperature, rotating speed of a roller and the like, and the prepared carbon black has the characteristics of high fluidity, low pH value, low blackness reflectivity and the like.
The terms "comprising", "including", "containing", "having" and the like in the present invention mean that other components or steps which are not listed in the present invention are not excluded.
Drawings
FIG. 1 is a schematic view showing the structure of a high-color carbon black producing apparatus according to the present invention.
Description of reference numerals: 1-an ozone generator; 2-a cylinder body; 3-material inlet; 4-material outlet; 5-material tank 1; 6, a motor; 7-material tank 2; 8-a cyclone separator 1; 9-material tank 3; 10-a cyclone 2; 11-tail gas decomposition equipment; 12-an air filter; 13-precision filter.
Detailed Description
Example 1
The apparatus of the invention is described below with reference to figure 1:
carbon black enters the cylinder body from the material inlet, the motor drives the cylinder body to rotate at a constant speed through the bearing, mixed gas of ozone and air prepared by the ozone generator enters the cylinder body through the gas inlet, a plurality of shoveling plates are arranged in the cylinder body, so that the carbon black can fully contact with the mixed gas for oxidation reaction, the fully oxidized carbon black enters the material tank 1 through the material outlet for collection, the tail gas enters the cyclone separator 1 through the gas outlet of the cylinder body, gas-solid separation is carried out in a cyclone separator 1, the separated carbon black enters a material tank 2, tail gas from the cyclone separator 1 is introduced into the cyclone separator 2 for gas-solid separation again, the separated carbon black enters a material tank 3, the tail gas passes through a three-way pipe, the waste gas can directly enter a waste gas decomposer device for waste gas treatment, and can also enter an ozone generator through an air filter and a precision filter as a gas source.
Example 2
Ozone is generated by an air source ozone generator, the volume ratio of ozone to air is 10:1, the gas flow rate is 5L/min, the rotating speed of a roller is 1r/min, the reaction temperature is 40 ℃, and when carbon black is oxidized for 1h, the main technical indexes of the produced carbon black are shown in a table I:
table carbon black Performance indices before and after Oxidation
| Before treatment | After treatment | Reference national standard | |
| pH | 8.9 | 3.0 | GB/T7045 |
| Fluidity/mm | 16.5 | 28.5 | GB/T7052 |
| Blackness (reflectivity) | 37.8 | 25.1 | GB/T7048 |
Example 3
Ozone is generated by an air source ozone generator, the volume ratio of ozone to oxygen is 1:1, the gas flow rate is 10L/min, the rotating speed of a roller is 6r/min, the reaction temperature is 20 ℃, and when carbon black is oxidized for 0.5h, the main technical indexes of the produced carbon black are shown in the following table II:
carbon black performance index before and after surface oxidation
| Before treatment | After treatment | Reference national standard | |
| pH | 8.9 | 2.3 | GB/T7045 |
| Fluidity/mm | 16.5 | 30.6 | GB/T7052 |
| Blackness (reflectivity) | 37.8 | 22.1 | GB/T7048 |
Example 4
Ozone is generated by an air source ozone generator, the volume ratio of the ozone to the circulating tail gas is 1:5, the gas flow rate is 2L/min, the rotating speed of a roller is 3r/min, the reaction temperature is 30 ℃, and when carbon black is oxidized for 2 hours, the main technical indexes of the produced carbon black are shown in the third table:
carbon black performance index before and after table tri-oxidation
| Before treatment | After treatment | Reference national standard | |
| pH | 8.9 | 3.1 | GB/T7045 |
| Fluidity/mm | 16.5 | 27.9 | GB/T7052 |
| Blackness (reflectivity) | 37.8 | 25.6 | GB/T7048 |
Claims (5)
1. A preparation device of high-pigment carbon black comprises an ozone generation device, a material mixing device, a gas-solid separation device and a tail gas decomposition device, and is characterized in that the material mixing device comprises a cylinder, a material inlet, a material outlet, a gas inlet and a tail gas outlet; the material outlet is connected with the material tank through a valve body; the gas inlet is connected with the ozone generating equipment; the tail gas outlet is connected with the gas-solid separation equipment; the gas-solid separation equipment can be connected with the tail gas decomposition equipment; the barrel can rotate.
2. The apparatus of claim 1, further comprising a tail gas refiltering device, wherein the gas-solid separation device is connected with the tail gas refiltering device; the tail gas refiltering device comprises an air filter and a precision filter which are sequentially connected.
3. The apparatus as claimed in claim 1, wherein the air inlet of the ozone generating device is accessible to air.
4. The apparatus of claim 2, wherein the air inlet of the ozone generating means is also connectable to the exhaust gas refiltering means.
5. The apparatus of claim 1, wherein the gas-solid separation device is one or more cyclones.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110028920.4A CN112679998A (en) | 2021-01-11 | 2021-01-11 | Preparation facilities of high pigment carbon black |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202110028920.4A CN112679998A (en) | 2021-01-11 | 2021-01-11 | Preparation facilities of high pigment carbon black |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN112679998A true CN112679998A (en) | 2021-04-20 |
Family
ID=75457065
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202110028920.4A Pending CN112679998A (en) | 2021-01-11 | 2021-01-11 | Preparation facilities of high pigment carbon black |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN112679998A (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2341708Y (en) * | 1998-09-01 | 1999-10-06 | 中国科学院山西煤炭化学研究所 | Reactor for carbon black surface oxidation and fluidizing bed by furnace method producing particles |
| CN102585565A (en) * | 2012-03-19 | 2012-07-18 | 苏州宝化炭黑有限公司 | Method and device for manufacturing carbon black pigment |
| CN108342100A (en) * | 2017-01-23 | 2018-07-31 | Oci有限公司 | Carbon black method for oxidation |
-
2021
- 2021-01-11 CN CN202110028920.4A patent/CN112679998A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2341708Y (en) * | 1998-09-01 | 1999-10-06 | 中国科学院山西煤炭化学研究所 | Reactor for carbon black surface oxidation and fluidizing bed by furnace method producing particles |
| CN102585565A (en) * | 2012-03-19 | 2012-07-18 | 苏州宝化炭黑有限公司 | Method and device for manufacturing carbon black pigment |
| CN108342100A (en) * | 2017-01-23 | 2018-07-31 | Oci有限公司 | Carbon black method for oxidation |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN106179262B (en) | Composite material and preparation method and purposes with absorption-visible light photocatalytic degradation synergistic effect | |
| JP3778956B2 (en) | Carbon black | |
| CN108439570A (en) | Charcoal loads nano zero valence iron activation sodium peroxydisulfate system and its preparation and application | |
| CA1037208A (en) | Black colouring agent | |
| CN113058659A (en) | Nano TiO (titanium dioxide)2Preparation method and application of/UiO-66 composite material | |
| CN104804479B (en) | Two-phase pyrolysis carbon black/white carbon black composite filler and preparation method thereof | |
| CN112724711A (en) | Preparation method of high-pigment carbon black | |
| CN107737594A (en) | A kind of catalyst for degradation of formaldehyde waste water and preparation method and application | |
| CN104672955A (en) | Oxidizing and granulating device for pigment carbon black and pigment carbon black prepared by same | |
| CN104693845A (en) | High-toluene-light transmittance pigment carbon black subjected to oxidation treatment and production technique thereof | |
| CN110449162B (en) | Modified manganese slag-iron vitriol slag mixed slag catalyst and preparation method and application thereof | |
| CN111974404A (en) | Photo-assisted BiFe1-xCuxO3Method for treating residual ciprofloxacin in water body by activated peroxymonosulfate | |
| CN214528800U (en) | Preparation facilities of high pigment carbon black | |
| CN106732332B (en) | A method of by coal ash for manufacturing for titanium doped mesopore silicon dioxide nano material | |
| CN112679998A (en) | Preparation facilities of high pigment carbon black | |
| CN110964349B (en) | Oxidation modified carbon black and preparation method thereof | |
| AU2021104818A4 (en) | Desulfurization Method of Oxidized Coal by Electr-Fenton-iron Reduction Method | |
| CN204689931U (en) | A kind of colour carbon black oxidation-prilling granulator | |
| CN204803259U (en) | Furnace black oxidation unit | |
| EP0719731B1 (en) | Process for the thermal treatment of iron oxides in a circulating fluid bed | |
| CN108970641A (en) | A kind of pulping wastewater treatment catalyst and preparation method thereof based on aluminium base quantum dot | |
| CN106731571A (en) | The purifier and its method of a kind of vehicle spray painting VOCs | |
| CN114272895A (en) | Nitrogen-sulfur-phosphorus co-doped ordered porous biochar and preparation method and application thereof | |
| CN109289862B (en) | Manganese oxide MnOxLoaded nano zero-valent iron composite material and preparation method and application thereof | |
| CN201684589U (en) | Conical fluidized bed reactor for granulation carbon black ozone oxidation |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210420 |
|
| RJ01 | Rejection of invention patent application after publication |