CN108862208A - A kind of processing method of the Waste Sulfuric Acid of alkylation production process discharge - Google Patents
A kind of processing method of the Waste Sulfuric Acid of alkylation production process discharge Download PDFInfo
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- CN108862208A CN108862208A CN201810977333.8A CN201810977333A CN108862208A CN 108862208 A CN108862208 A CN 108862208A CN 201810977333 A CN201810977333 A CN 201810977333A CN 108862208 A CN108862208 A CN 108862208A
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- sulfuric acid
- waste sulfuric
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- alkylation
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/69—Sulfur trioxide; Sulfuric acid
- C01B17/74—Preparation
Abstract
Disclosed in this invention is a kind of processing method of the Waste Sulfuric Acid of alkylation production process discharge, the status that the Waste Sulfuric Acid environmental hazard discharged mainly for sulfuric acid process alkylation process is significant, processing difficulty is big, cost of disposal is high, it proposes a kind of first by Waste Sulfuric Acid and oxidation reactive aluminum, generate solid product, then by solid product successively in roasting temperature from low to high, after substep removing moisture and organic impurities, it decomposes again and releases sulfur trioxide, by this part, fresh sulfuric acid is made in sulfur trioxide absorption, to realize the regeneration of waste sulfuric acid from alkylation.Technology of the present invention removes moisture and organic impurities by the method for substep Roasting Decomposition, then at a lower temperature, the regeneration of sulfuric acid is realized using the decomposition release sulfur trioxide of aluminum sulfate, avoids the spent acid high temperature incineration treatment process of high energy consumption.The technique can utilize original device, in the case where investment is little, significantly reduces the processing cost of Waste Sulfuric Acid, obtain preferable economic benefit and environmental benefit.
Description
Technical field
The present invention relates to the process fields of Waste Sulfuric Acid, and in particular to a kind of place of the Waste Sulfuric Acid of alkylation production process discharge
Reason method.
Background technique
Sulfuric acid is widely used in many industrial processes as important basic chemical industry raw material, including：Alkane
The processes such as base, nitrification, esterification, sulfonation, catalysis and gas dry, or result from the gentle soma of titanium white production, pickling iron and steel
The processes such as dry.Sulfuric acid Many times in these industrial process are to come as catalyst or medium using not entering most
In whole product, therefore a large amount of Waste Sulfuric Acid is produced during these.Alkyl is more typically include in these Waste Sulfuric Acids
Change spent acid and titanium pigment waste acid.
By taking waste sulfuric acid from alkylation as an example, wherein acid concentration is 90% or so, containing a large amount of organic impurities, has irritation gas
Taste and strong corrosive belong to dangerous liquid waste, and processing difficulty is big, become the biggest obstacle for restricting alkylation process.Currently, than
The processing mode of more mature waste sulfuric acid from alkylation is high temperature pyrolytic cracking (HTP), can thoroughly solve the sulphur such as spent acid and sour gas and ask
Topic, technique mainly have 2 kinds：1. E.I.Du Pont Company's SAR technology (double conversion double absorption acid-making process, the country are commonly called as dry method), 2. Top's rope
Company's WSA technology (country is commonly called as wet process).But high temperature pyrolysis processing load is big, equipment corrosion is strong, operating cost is high, seriously
Influence the treating capacity of waste sulfuric acid from alkylation.
In terms of the processing about waste sulfuric acid from alkylation, relevant patent has very much, is broadly divided into three aspects：(1) sharp
Prepare different sulfate products with alkylation spent acid, as Chinese patent CN201611258083.X, CN201710345627.4,
CN201710010923.9, CN201510951508.4, CN201510951949.4, CN201510946136.6 etc.；(2) it adopts
With different mode Pintsch process, as Chinese patent CN201611093229.X, CN201510346801.8,
CN201610041456.1,CN201710468949.8；(3) pass through having in different oxidizing removal waste sulfuric acid from alkylation
Machine object, such as Chinese patent CN201611093369.7, CN201611092684.8, CN201510946095.0.
This patent proposes that a kind of processing method of the Waste Sulfuric Acid of novel alkylation production process discharge, this method are creative
Propose " recycle chemistry chain " using aluminium oxide to realize the processing of Waste Sulfuric Acid：It is carried out first with aluminium oxide and Waste Sulfuric Acid anti-
It answers, obtains the aluminum sulfate containing impurity, impurity therein mainly includes organic matter and part moisture content in Waste Sulfuric Acid, then one
By the method heated the crystallization water and organic impurities in aluminum sulfate are escaped at a temperature of fixed from aluminum sulfate, finally rises again
High-temperature aluminum sulfate decompose to generate aluminium oxide and sulfur trioxide, and will decompose that obtained sulfur trioxide absorb can be with
Oleum is prepared, obtains fresh sulfuric acid after final dilution.Fresh sulfuric acid can reach alkyl plant application requirement and
Applied to other chemical industries, the recycling of waste sulfuric acid from alkylation is realized.This method avoid the spent acid of high energy consumption to burn
Treatment process is burnt, the processing cost of Waste Sulfuric Acid can be significantly reduced, obtain preferable economic benefit and environmental benefit, is had very wide
Wealthy application prospect.
Specific embodiment
1) waste sulfuric acid from alkylation is reacted in small-sized stirred tank with aluminium oxide according to certain mass ratio, reaction process
Middle control certain temperature is simultaneously stirred continuously, and is stopped stirring when reaction system is in thick, is made its solidification；2) by the solidification in 1)
Object is placed at 250 DEG C~350 DEG C and is roasted；3) 2) sample in is continued to roast at 650 DEG C~850 DEG C, and adopted
The tail gas after roasting is absorbed with 98% or more the concentrated sulfuric acid.After reaction according to national standard using acid base titration
Method analysis absorbs the acid concentration in after-fume sulfuric acid, using the chemistry of remaining solid after Xray fluorescence spectrometer analysis roasting
Composition.
Embodiment 1
50g aluminium oxide is added in 50g Waste Sulfuric Acid to be stirred to react, control reaction temperature is 60 DEG C, reaction mass
It is transferred into 250 DEG C of Muffle kiln roasting after solidification, is continuously heating to 650 DEG C after 2h, keeps this temperature 3h, while will roasting
It burns tail gas and is passed through in the concentrated sulfuric acid of 20g98.3% and absorbed.
Embodiment 2
35g aluminium oxide is added in 50g Waste Sulfuric Acid to be stirred to react, control reaction temperature is 70 DEG C, reaction mass
It is transferred into 280 DEG C of Muffle kiln roasting after solidification, is continuously heating to 700 DEG C after 2h, keeps this temperature 3h, while will roasting
It burns tail gas and is passed through in the concentrated sulfuric acid of 20g98.3% and absorbed.
Embodiment 3
20g aluminium oxide is added in 30g Waste Sulfuric Acid to be stirred to react, control reaction temperature is 80 DEG C, reaction mass
It is transferred into 300 DEG C of Muffle kiln roasting after solidification, is continuously heating to 750 DEG C after 2h, keeps this temperature 3h, while will roasting
It burns tail gas and is passed through in the concentrated sulfuric acid of 20g98.3% and absorbed.
Embodiment 4
15g aluminium oxide is added in 30g Waste Sulfuric Acid to be stirred to react, control reaction temperature is 90 DEG C, reaction mass
It is transferred into 330 DEG C of Muffle kiln roasting after solidification, is continuously heating to 800 DEG C after 2h, keeps this temperature 3h, while will roasting
It burns tail gas and is passed through in the concentrated sulfuric acid of 20g98.3% and absorbed.
It is as shown in the table for the analysis data statistics in embodiment：
| Project | Sulfuric acid concentration/% in absorbing liquid | Al in remaining solid2O3Content/% | S content/% in remaining solid |
| Embodiment 1 | 125 | 91 | 2.8 |
| Embodiment 2 | 123 | 91.7 | 2.3 |
| Embodiment 3 | 105 | 92.5 | 2.1 |
| Embodiment 4 | 106 | 93.2 | 1.9 |
As can be seen from the table, alkyl can be realized by the method for aluminium oxide " recycle chemistry chain " at a lower temperature
The regeneration treatment for changing Waste Sulfuric Acid, obtains the fresh concentrated sulfuric acid.
Claims (6)
1. a kind of processing method of the Waste Sulfuric Acid of alkylation production process discharge, including following sequence of step：
1) it is reacted in Waste Sulfuric Acid to be added to excessive oxidation aluminium solid, obtains solid intermediate product (I)；
2) solid intermediate product (I) obtained to step 1) processing carries out low-temperature bake processing, obtains solid-phase intermediate (II)；
3) solid intermediate product (II) obtained to step 2) processing carries out high-temperature roasting processing, obtains gaseous sulfur trioxide product
And alumina solid；
4) it absorbs gaseous sulfur trioxide product obtained in step 3) to obtain fresh sulfuric acid；
5) alumina solid obtained in step 3) is returned in step 1), realizes and is recycled.
2. a kind of processing method of waste sulfuric acid from alkylation according to claim 1, it is characterised in that：By Waste Sulfuric Acid and oxygen
Change aluminium to be reacted, aluminium oxide and sulfuric acid mass ratio are between 0.1 to 10, wherein it is preferred that between 0.5 to 1, at reaction temperature
Between -5 DEG C to 250 DEG C, preferred temperature be 50 DEG C to 200 DEG C, react with stirring or moving component equipment in into
Row, finally obtains solid product.
3. a kind of processing method of waste sulfuric acid from alkylation according to claim 1, it is characterised in that：To step 1) processing
Obtained solid product carries out calcination process, and maturing temperature is between 100 DEG C to 500 DEG C, wherein it is preferred that 250 DEG C to 350 DEG C
Between, contained humidity and organic impurities are in this stage roasting process with gas phase in the obtained intermediate products (II) of step 1) processing
Form is removed from solid material.
4. a kind of processing method of waste sulfuric acid from alkylation according to claim 1, it is characterised in that：By step 2) place
Solid material after reason carries out calcination process at higher temperatures, and maturing temperature is between 350 DEG C to 1000 DEG C, wherein excellent
Select between 650 DEG C to 850 DEG C, element sulphur contained in the obtained solid product of step 2) processing in this stage roasting process with
The form loss of sulfur trioxide comes out, and the main component of remaining solid substance is aluminum oxide, in remaining solid substance, sulphur member
Mass percentage shared by element is not higher than 10%, and in the case where more preferred, mass percentage shared by element sulphur is not higher than
3%.
5. a kind of processing method of waste sulfuric acid from alkylation according to claim 1, it is characterised in that：Make in step 3)
With 85% or more the concentrated sulfuric acid, more preferably 98% or more the concentrated sulfuric acid absorbs sulfur trioxide, obtains oleum, then right
Oleum is diluted, to obtain fresh sulfuric acid.
6. a kind of processing method of waste sulfuric acid from alkylation according to claim 1, it is characterised in that：From step 1) to step
It is rapid 5), aluminium oxide sulfuric acid conversion, decomposition, it is regenerated during be recycled, constitute recycle chemistry chain (chemical
loop)。
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110255507A (en) * | 2019-08-02 | 2019-09-20 | 青岛惠城信德新材料研究院有限公司 | A kind of Waste Sulfuric Acid regeneration method |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101139660A (en) * | 2007-10-08 | 2008-03-12 | 郑满秀 | Method for extracting iron-lead and gold-silver from gold concentrate acidifying baking residue |
| CN103771353A (en) * | 2012-10-24 | 2014-05-07 | 中国石油化工股份有限公司 | Regeneration method for alkylated waste sulfuric acid |
| CN104944384A (en) * | 2014-03-25 | 2015-09-30 | 山东鲁北企业集团总公司 | Combined process and combined device for comprehensive utilization for chemical decomposition waste sulphuric acid and gypsum |
| CN105480998A (en) * | 2015-12-17 | 2016-04-13 | 广西大学 | Method for preparing aluminum sulfate by catalyzing alkylated waste sulfuric acid with lignocellulose ester |
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2018
- 2018-08-27 CN CN201810977333.8A patent/CN108862208B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101139660A (en) * | 2007-10-08 | 2008-03-12 | 郑满秀 | Method for extracting iron-lead and gold-silver from gold concentrate acidifying baking residue |
| CN103771353A (en) * | 2012-10-24 | 2014-05-07 | 中国石油化工股份有限公司 | Regeneration method for alkylated waste sulfuric acid |
| CN104944384A (en) * | 2014-03-25 | 2015-09-30 | 山东鲁北企业集团总公司 | Combined process and combined device for comprehensive utilization for chemical decomposition waste sulphuric acid and gypsum |
| CN105480998A (en) * | 2015-12-17 | 2016-04-13 | 广西大学 | Method for preparing aluminum sulfate by catalyzing alkylated waste sulfuric acid with lignocellulose ester |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110255507A (en) * | 2019-08-02 | 2019-09-20 | 青岛惠城信德新材料研究院有限公司 | A kind of Waste Sulfuric Acid regeneration method |
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