CN102674371B - Method for preparing white carbon black by utilizing silicon resin industrial waste acid - Google Patents

Method for preparing white carbon black by utilizing silicon resin industrial waste acid Download PDF

Info

Publication number
CN102674371B
CN102674371B CN 201210116359 CN201210116359A CN102674371B CN 102674371 B CN102674371 B CN 102674371B CN 201210116359 CN201210116359 CN 201210116359 CN 201210116359 A CN201210116359 A CN 201210116359A CN 102674371 B CN102674371 B CN 102674371B
Authority
CN
China
Prior art keywords
industrial waste
waste acid
carbon black
silicone resin
white carbon
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
Application number
CN 201210116359
Other languages
Chinese (zh)
Other versions
CN102674371A (en
Inventor
陈利民
倪勇
吴连斌
蒋剑雄
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HANGZHOU SILICONE WAY TECHNOLOGY Co Ltd
Original Assignee
HANGZHOU SILICONE WAY TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by HANGZHOU SILICONE WAY TECHNOLOGY Co Ltd filed Critical HANGZHOU SILICONE WAY TECHNOLOGY Co Ltd
Priority to CN 201210116359 priority Critical patent/CN102674371B/en
Publication of CN102674371A publication Critical patent/CN102674371A/en
Application granted granted Critical
Publication of CN102674371B publication Critical patent/CN102674371B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Processing Of Solid Wastes (AREA)
  • Silicon Compounds (AREA)

Abstract

The invention relates to a technology for preparing white carbon black. In order to solve the problem that a large quantity of waste hydrochloric acid generated in the preparation process of organic silicon resin pollutes the environment, the invention provides a method for preparing white carbon black by utilizing silicon resin industrial waste acid, which comprises the following steps: adding the silicon resin industrial waste acid into a reaction kettle, and agitating, heating and raising the temperature to 50-60 DEG C; dropwise adding water glass with a mass percent concentration of 10-30 percent into the reaction kettle within 1-1.5 hours, adjusting the pH value of the industrial waste acid to 6.5-8 after dropwise adding and uniformly agitating; and raising the temperature of reaction liquid to 75-90 DEG C, aging for 2-4 hours, carrying out centrifugal filtering or plate and frame type filtering, pulping and washing for more times, and drying and crushing to obtain the white carbon black. The method has the advantages of environment friendliness, simple process and low production cost, and moreover, the environment pollution brought by waste acid can be better solved.

Description

A kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black
Technical field
The present invention relates to a kind of technology for preparing white carbon black, relate to specifically a kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black.
Background technology
White carbon black has another name called and is that hydrated SiO 2, molecular formula are SiO 2NH 2O, relative density is 2.319~2.653,1750 ℃ of fusing points are a kind of white, nontoxic, amorphous micro mist, have porous, light weight, high dispersive, high temperature resistant, do not burn, chemically stable and the excellent properties such as electrical insulating property is good.White carbon black is a kind of multifunction additive, is widely used in the industries such as silicon rubber, coating, printing ink, medicine, papermaking, food, makeup, chemically machinery polished, can play the effects such as reinforcement, thickening, thixotroping, delustring.At present the main production method of white carbon black has two kinds: vapor phase process and the precipitator method, and the former mainly adopts the raw materials such as silicoorganic compound, chlorosilane and silicon chlorides to produce, and product is of fine quality and valency is high; The latter utilizes silicate and inorganic acid reaction to produce, and product price is cheap, thereby the huge market demand.Along with the demand growth in fields such as tire production, Rubber Industry, toothpaste industry, coatings industries, the white carbon black that adopts the precipitator method to produce will be with 10% speed increment within the coming years at present.
Silicone resin is mainly from chlorosilane, makes through several operations such as hydrolysis, washing, concentrated and polycondensations.And this process of preparation silicone resin can produce a large amount of waste hydrochloric acids.Along with China's silicone resin output increases year by year, the amount of spent acid is also increasing, and contains organic solvent, organosilicon small molecules and other auxiliary agent in these spent acid, be difficult to process, and be a great potential safety hazard, if directly discharging is also very large source of pollution.Therefore, need to find a kind ofly can take full advantage of spent acid, not only technique is simple, and facility investment is few, can transform the method for the high product of production added value, and can fully utilize spent acid again, to satisfy the Sustainable development of organosilicon industry, solves simultaneously problem of environmental pollution.
The Chinese patent of CN1031821A discloses a kind of sulfuric acid alkylation acid sludge that utilizes and has made the white carbon black technology, this invention utilizes in acid sludge isolated sulfuric acid to replace in the past the precipitator method to make the required market of white carbon black pure sulfuric acid or hydrochloric acid in short supply, greatly reduce production costs, eliminate simultaneously spent acid to the pollution of environment.At first acid sludge is mixed with water, obtain dilute sulphuric acid and oil after standing demix, oil can be made oil fuel.Then make method for white carbon black by the precipitator method, carry out neutralization reaction with the dilute sulphuric acid and the water glass that are separated to, more aging, filter, washing, dry, pulverizing namely get transparent white carbon black products.But the method can only be used for the acid sludge of sulfuric acid alkylation to be processed, and can contain Na in the product that it obtains 2S and Na 2SR is difficult to clean out fully, and acid discharges hydrogen sulfide and stench appears in mercaptan when use procedure is met, and use is restricted.
Summary of the invention
For solving the problem that produces a large amount of waste hydrochloric acid contaminate environment in the silicone resin preparation process, the invention provides a kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black, the method is environmentally friendly, technique is simple, and production cost is low, and can well solve the environmental pollution that spent acid brings.
The present invention is achieved by the following technical solutions: a kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black, described preparation method are following steps:
(1), add silicone resin industrial waste acid, stirring heating to be warming up to 50~60 ℃ in reactor;
(2), to add mass percent concentration in 1~1.5 hour in the reactor be 15~30% water glass, dropwise to stir after with the silicone resin industrial waste acid, the pH value of reaction solution being adjusted to 6.5~8 afterwards; Under regular situation, churning time was to the maximum about 0.5 hour.
(3), reaction solution is warming up to 75~90 ℃, ageing 2~4 hours is adopted centrifugal or plate and frame filters, and carries out drying after making beating washing several times, pulverizes and obtains white carbon black;
Wherein, the mass ratio of silicone resin industrial waste acid and water glass is 1:1.075~3.15.
Silicone resin industrial waste acid described in step (1) is selected from the chlorosilane monomer or organosilicon high-boiling product is produced the spent acid that silicone resin produces, as preferably, the silicone resin industrial waste acid is selected from and produces organic group and Siliciumatom mol ratio (R/Si) is the spent acid that 0.95~1.3 chlorosilane monomer or organosilicon high-boiling product production silicone resin produce, the mass percent concentration of silicone resin industrial waste acid is 8~20%, as being preferably 10~20%.
Can contain organic solvent in silicone resin Industry Waste hydrochloric acid, the machine solvent that contains in silicone resin Industry Waste hydrochloric acid is the mixture of one or more arbitrary proportions in methyl alcohol, ethanol, propyl carbinol or Virahol.
The modulus of the water glass described in step (2) is 2.0~3.2, and as preferably, modulus is 2.5~3.0.
The present invention adopts and produces by chlorosilane monomer or organosilicon high-boiling product the spent acid that silicone resin produces, owing to having a small amount of organosilicon performed polymer and strong solvent in spent acid, need not separately to add relevant auxiliary agent and namely can overcome because gel produces the problem that strong aggregation produces bad dispersibility, thereby obtain the better white carbon black of performance.Whole technique is simple, and the environmental pollution that can fine minimizing spent acid brings.Product can be used for the fields such as rubber item, jointing compound and coating.
Compared with prior art, the invention has the beneficial effects as follows:
(1) preparation method of the present invention is environmentally friendly, technique is simple, and production cost is low, and facility investment is few, can transform the high product of production added value.
(2) can fully utilize spent acid, to satisfy the Sustainable development of organosilicon industry, solve simultaneously problem of environmental pollution.
Specific implementation method
Below in conjunction with embodiment, the present invention is described in further detail, desired raw material is all commercially available.
Embodiment 1:
Add in the reactor of 5L that to use R/Si be the industrial waste acid 2000g that 0.95 silicone resin produces, it is mixed with mass percent concentration is 20%, be heated with stirring to 50 ℃, 1.5 in individual hour with modulus be 3 and mass percent concentration be that 30% water glass 2150g drops in reactor, after dropwising, stir again after with pH regulator to 7.5 with 20% industrial waste acid.Reaction solution is warming up to 75 ℃, ageing 2 hours.Obtain white carbon black after centrifuging, making beating washing 2 times, drying, pulverizing.
The dioxide-containing silica 96.4% of this white carbon black, specific surface area 125m 2/ g, particle diameter 195nm.
Embodiment 2:
Add in the reactor of 5L that to use R/Si be the industrial waste acid 1000g that 1.3 silicone resin produces, it is mixed with mass percent concentration is 10%, be heated with stirring to 60 ℃, in 1 hour with modulus be 2 and concentration be that 15% water glass 3150g drops in reactor, after dropwising, the industrial waste acid with 10% stirs after with pH regulator to 8 again.Be warming up to 90 ℃, ageing 4 hours.Obtain white carbon black after centrifuging, making beating washing 2 times, drying, pulverizing.
The dioxide-containing silica 97.6% of this white carbon black, specific surface area 185m 2/ g, particle diameter 135nm.
Embodiment 3:
Add in the reactor of 5L that to use R/Si be the industrial waste acid 1300g that 1.1 silicone resin produces, it is mixed with mass percent concentration is 15%, be heated with stirring to 55 ℃, in 1 hour with modulus be 2.6 and concentration be that 20% water glass 2950g drops in reactor, after dropwising, the industrial waste acid with 15% stirs after with pH regulator to 6.5 again.Be warming up to 90 ℃, ageing 4 hours.Obtain white carbon black after centrifuging, making beating washing 2 times, drying, pulverizing.
The dioxide-containing silica 97.3% of this white carbon black, specific surface area 225m 2/ g, particle diameter 85nm.
Embodiment 4:
Add in the reactor of 100L that to use R/Si be the industrial waste acid 26Kg that 1.2 silicone resin produces, it is mixed with mass percent concentration is 8%, be heated with stirring to 55 ℃, 1.5 in individual hour with modulus be 2.5 and concentration be that 10% water glass 60.4Kg drops in reactor, after dropwising, the industrial waste acid with 8% continues to stir after pH is controlled at 7.Be warming up to 85 ℃, ageing 3 hours.After filtering, pull an oar washing 3 times, drying, pulverizing, plate and frame obtains white carbon black.
The dioxide-containing silica 97.7% of this white carbon black, specific surface area 245m 2/ g, particle diameter 80nm.

Claims (3)

1. a method of utilizing the silicone resin industrial waste acid to prepare white carbon black, is characterized in that, described method is following steps:
(1), add the silicone resin industrial waste acid in reactor, be heated to 50~60 ℃ under agitation condition, described silicone resin industrial waste acid is selected from the chlorosilane monomer or organosilicon high-boiling product is produced the spent acid that silicone resin produces, and wherein in the chlorosilane monomer, organic group and Siliciumatom mol ratio are 0.95~1.3;
(2), to drip mass percent concentration in 1~1.5 hour in the reactor be 10~30% water glass, dropwise to stir after with the silicone resin industrial waste acid, the pH value of reaction solution being adjusted to 6.5~8 afterwards;
(3), reaction solution is warming up to 75~90 ℃, ageing 2~4 hours is adopted centrifugal or plate and frame filters, and carries out drying after making beating washing several times, pulverizes and obtain white carbon black;
Wherein, the mass ratio of silicone resin industrial waste acid and water glass is 1:1.075~3.15.
2. a kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black according to claim 1, it is characterized in that: the mass percent concentration of silicone resin industrial waste acid is 8~20%.
3. a kind of method of utilizing the silicone resin industrial waste acid to prepare white carbon black according to claim 1 and 2, it is characterized in that: the modulus of the water glass described in step (2) is 2.0~3.2.
CN 201210116359 2012-04-20 2012-04-20 Method for preparing white carbon black by utilizing silicon resin industrial waste acid Expired - Fee Related CN102674371B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201210116359 CN102674371B (en) 2012-04-20 2012-04-20 Method for preparing white carbon black by utilizing silicon resin industrial waste acid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201210116359 CN102674371B (en) 2012-04-20 2012-04-20 Method for preparing white carbon black by utilizing silicon resin industrial waste acid

Publications (2)

Publication Number Publication Date
CN102674371A CN102674371A (en) 2012-09-19
CN102674371B true CN102674371B (en) 2013-11-06

Family

ID=46807016

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201210116359 Expired - Fee Related CN102674371B (en) 2012-04-20 2012-04-20 Method for preparing white carbon black by utilizing silicon resin industrial waste acid

Country Status (1)

Country Link
CN (1) CN102674371B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105585032B (en) * 2015-09-09 2017-10-20 洛阳国兴矿业科技有限公司 The method that fluorine resource is reclaimed from low product bauxite waste gas decomposition
CN105540926B (en) * 2016-01-07 2018-02-16 江苏盛吉化工有限公司 A kind of method using acid waste water co-producing white carbon black and inorganic salts

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102219224B (en) * 2011-03-30 2012-12-12 廖险峰 Method for preparing high-dispersion white carbon black by using acetic acid-contained industrial waste water

Also Published As

Publication number Publication date
CN102674371A (en) 2012-09-19

Similar Documents

Publication Publication Date Title
CN101979443B (en) Method for producing modified white carbon black
CN100484873C (en) Method for preparing white carbon black by using oil shale ash
CN106311199B (en) A kind of stable dispersion and the controllable SiO of photocatalytic activity2@TiO2Core-shell structure, preparation method and its application
CN101214963B (en) Method for preparing high pure nano silicon dioxide from oil shale slag
CN102583403B (en) Preparation method of super-hydrophobic nanoscale white carbon black membrane and super-hydrophobic nanoscale white carbon black powder
CN1693194A (en) Technology for producing white carbon black, sodium sulfite, sodium bisulfite by sodium sulfate method
CN109824903A (en) A kind of high refractive index boracic organic silicon rigidity-increasing stick and preparation method thereof
CN105016343B (en) A kind of method that utilization aluminous fly-ash prepares hydrophabic silica
CN102674371B (en) Method for preparing white carbon black by utilizing silicon resin industrial waste acid
CN102198942A (en) Preparation method of silicon dioxide
CN101746763A (en) Method for preparing nano silicon dioxide by vapor phase process
CN104512896A (en) Method for preparing white carbon black by using high aluminum fly ash, and white carbon black
CN102616791B (en) Method for preparing white carbon black from diatomite in situ
CN104418332B (en) A kind of preparation method of silicon dioxide
CN101209842A (en) Method for producing white carbon black and simultaneously recycling product from by-product of organosilicon reaction
CN105858676A (en) Production method for coproducing sodium silicate and sodium fluoride
CN103466643A (en) Method for preparing white carbon black by circularly using mother liquor
CN110817892B (en) Preparation method of superfine white carbon black for coating paint
CN103359747A (en) Method for in situ modification of nano silica in batches
CN104211072A (en) Nano silicon dioxide production process technology
CN109319793B (en) Preparation method of high-specific-surface high-oil-absorption white carbon black
CN110040740A (en) The method that crystal seed is oriented to method synthesis total silicon SOD zeolite
CN105504980A (en) Formula and manufacturing method for manufacturing aqueous ink
CN108864801A (en) A kind of preparation method of salt tolerant higher suspension thickener for coating
CN108910947B (en) Thin-sheet micro-nano (K, Na) NbO3Crystal and method for producing same

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
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: 20131106

Termination date: 20210420

CF01 Termination of patent right due to non-payment of annual fee