CN111018757B - Method for synthesizing 3-mercaptopropionic acid from acidic waste gas - Google Patents
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- DKIDEFUBRARXTE-UHFFFAOYSA-N 3-mercaptopropanoic acid Chemical compound OC(=O)CCS DKIDEFUBRARXTE-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 238000000034 method Methods 0.000 title claims abstract description 35
- 239000002912 waste gas Substances 0.000 title claims abstract description 29
- 230000002194 synthesizing effect Effects 0.000 title claims abstract description 25
- 230000002378 acidificating effect Effects 0.000 title claims abstract description 18
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims abstract description 97
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims abstract description 97
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 claims abstract description 78
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract description 39
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims abstract description 39
- 238000006243 chemical reaction Methods 0.000 claims abstract description 35
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims abstract description 28
- 239000002253 acid Substances 0.000 claims abstract description 19
- 238000001179 sorption measurement Methods 0.000 claims abstract description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 32
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 28
- 239000007789 gas Substances 0.000 claims description 23
- QGJOPFRUJISHPQ-UHFFFAOYSA-N Carbon disulfide Chemical compound S=C=S QGJOPFRUJISHPQ-UHFFFAOYSA-N 0.000 claims description 21
- 229910052757 nitrogen Inorganic materials 0.000 claims description 16
- 238000001704 evaporation Methods 0.000 claims description 14
- 230000008020 evaporation Effects 0.000 claims description 14
- 238000000926 separation method Methods 0.000 claims description 14
- 239000000203 mixture Substances 0.000 claims description 9
- 238000001816 cooling Methods 0.000 claims description 8
- QGJOPFRUJISHPQ-NJFSPNSNSA-N carbon disulfide-14c Chemical compound S=[14C]=S QGJOPFRUJISHPQ-NJFSPNSNSA-N 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 7
- 239000007791 liquid phase Substances 0.000 claims description 7
- 238000003756 stirring Methods 0.000 claims description 3
- 239000003513 alkali Substances 0.000 claims description 2
- 239000012295 chemical reaction liquid Substances 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims description 2
- 239000000047 product Substances 0.000 abstract description 48
- 239000002699 waste material Substances 0.000 abstract description 10
- 239000002994 raw material Substances 0.000 abstract description 9
- 239000003054 catalyst Substances 0.000 abstract description 8
- 239000002904 solvent Substances 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 7
- 238000003786 synthesis reaction Methods 0.000 abstract description 7
- 230000015572 biosynthetic process Effects 0.000 abstract description 6
- 238000000605 extraction Methods 0.000 abstract description 4
- 230000020477 pH reduction Effects 0.000 abstract description 4
- -1 mercapto compounds Chemical class 0.000 abstract description 3
- 239000006227 byproduct Substances 0.000 abstract description 2
- 208000012839 conversion disease Diseases 0.000 abstract description 2
- 239000011261 inert gas Substances 0.000 description 7
- 239000011259 mixed solution Substances 0.000 description 7
- 230000001276 controlling effect Effects 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 4
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- HYHCSLBZRBJJCH-UHFFFAOYSA-M sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- ODJQKYXPKWQWNK-UHFFFAOYSA-N 3,3'-Thiobispropanoic acid Chemical group OC(=O)CCSCCC(O)=O ODJQKYXPKWQWNK-UHFFFAOYSA-N 0.000 description 1
- 239000003490 Thiodipropionic acid Substances 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- JOBBTVPTPXRUBP-UHFFFAOYSA-N [3-(3-sulfanylpropanoyloxy)-2,2-bis(3-sulfanylpropanoyloxymethyl)propyl] 3-sulfanylpropanoate Chemical compound SCCC(=O)OCC(COC(=O)CCS)(COC(=O)CCS)COC(=O)CCS JOBBTVPTPXRUBP-UHFFFAOYSA-N 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- WATWJIUSRGPENY-UHFFFAOYSA-N antimony atom Chemical compound [Sb] WATWJIUSRGPENY-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000013064 chemical raw material Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000012760 heat stabilizer Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000019303 thiodipropionic acid Nutrition 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C319/00—Preparation of thiols, sulfides, hydropolysulfides or polysulfides
- C07C319/02—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of thiols
- C07C319/04—Preparation of thiols, sulfides, hydropolysulfides or polysulfides of thiols by addition of hydrogen sulfide or its salts to unsaturated compounds
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The invention relates to the technical field of synthesis of mercapto compounds, and particularly relates to a method for synthesizing 3-mercaptopropionic acid from acidic waste gas. The method comprises the first step of purifying hydrogen sulfide in the acid waste gas by a pressure swing adsorption method; secondly, synthesizing 3-mercaptopropionic acid: step one, selecting materials; step two, the first step reaction; step three, the second step reaction; step four, the third step reaction. The method for synthesizing 3-mercaptopropionic acid from acidic waste gas adopts a method of changing hydrogen sulfide in acidic waste gas discharged by an oil refinery into valuable, taking reasonable utilization of resources as guidance, and synthesizing 3-mercaptopropionic acid with low cost and less three wastes. The invention takes acrylic acid and hydrogen sulfide products obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent, so that the reaction conversion rate is high, the yield is high, byproducts are reduced, the traditional process route is broken through, and the problem of three wastes caused by acidification and extraction is avoided, therefore, the invention is an excellent synthesis and post-treatment route.
Description
Technical Field
The invention relates to the technical field of synthesis of mercapto compounds, and particularly relates to a method for synthesizing 3-mercaptopropionic acid from acidic waste gas.
Background
The 3-mercaptopropionic acid is an important chemical raw material, and the main application fields are medicines, auxiliaries, water reducing agents and the like. Can be used for preparing medicine Finalou (clomezazone), which has effects of improving sleep and tranquilization; can be used for preparing pentaerythritol tetra (3-mercaptopropionate), which is an intermediate for organic synthesis and can be used in the field of paint as a curing agent; can be used for preparing polycarboxylic acid high-efficiency water reducing agent and synthesizing heat stabilizers such as organic tin, organic antimony and the like. At present, acrylonitrile and sodium hydrosulfide are used as raw materials to produce the acrylonitrile and the sodium hydrosulfide at home and abroad, the process can be carried out under normal pressure, but the acrylonitrile is a highly toxic product and is regulated by public security departments, the process flow is long, the reaction temperature and the reaction time are strictly required, the operation flexibility is low, the three wastes are more, the environmental pollution is large, and the process tends to be gradually eliminated.
In the prior art, although a method for effectively synthesizing 3-mercaptopropionic acid by using hydrogen sulfide and acrylic acid is disclosed, the traditional process route is to directly use pure hydrogen sulfide for preparation, so that the production cost is higher, acidification is easy to generate, and the three wastes are caused during extraction.
In addition, a large amount of acid waste gas is discharged in the production process of the oil refinery, and the acid waste gas contains hydrogen sulfide, so that if the acid waste gas is utilized, the waste can be changed into valuable.
Disclosure of Invention
The invention aims to provide a method for synthesizing 3-mercaptopropionic acid from acidic waste gas, which can change waste into valuable and avoid the 'three wastes' problem caused by acidification and extraction.
In order to achieve the purpose, the invention adopts the following technical scheme:
the method for synthesizing the 3-mercaptopropionic acid by using the acidic waste gas comprises the following steps:
first, the pressure swing adsorption process purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then carrying out flash evaporation on the liquid phase, carrying out first separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesizing 3-mercaptopropionic acid
Step one, selecting materials: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent;
step two, the first step reaction: under the protection of inert gas and with controlled temperature, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for a certain time;
step three, reaction in the second step: heating to a certain temperature, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding the acrylic acid;
step four, reaction in the third step: then the rest hydrogen sulfide product is added, stirred and reacted for a certain time, and then the 3-mercaptopropionic acid is obtained through reduced pressure rectification.
In the above technical solution, in the first step of the second step, the molar ratio of the acrylic acid to the hydrogen sulfide in the hydrogen sulfide product is 1: 1 to 4.
In the above technical solution, in the first step of the second step, the molar ratio of the acrylic acid to the hydrogen sulfide in the hydrogen sulfide product is 1: 3.
in the above technical solution, in the step one of the second step, the molar ratio of the acrylic acid to the triethylamine to the dimethylacetamide is 1: 0.1-0.4: 2 to 5.
In the above technical scheme, in the step one of the second step, the molar ratio of the acrylic acid to the triethylamine to the dimethylacetamide is 1:0.2: 3.5.
In the technical scheme, in the second step, under the protection of inert gas and at the temperature of 5-15 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 2-3 hours.
In the technical scheme, in the third step of the second step, the temperature is raised to 75-85 ℃, then acrylic acid is dripped for reaction, and the time for dripping acrylic acid is controlled to be 1.5-2.5 h.
In the technical scheme, in the fourth step of the second step, the rest hydrogen sulfide product is introduced, stirred and reacted for 4-6 h, and then the 3-mercaptopropionic acid is obtained through reduced pressure rectification.
In the technical scheme, the molar ratio of hydrogen sulfide of part of hydrogen sulfide products in the second step to hydrogen sulfide of the rest hydrogen sulfide products in the fourth step is 2-3: 1.
Compared with the prior art, the invention has the beneficial effects that:
(1) the method for synthesizing 3-mercaptopropionic acid from acidic waste gas provided by the invention adopts hydrogen sulfide in acidic waste gas discharged from an oil refinery, changes waste into valuable, takes reasonable utilization of resources as guidance, and synthesizes 3-mercaptopropionic acid with low cost and less three wastes. The invention takes acrylic acid and hydrogen sulfide products obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent, so that the reaction conversion rate is high, the yield is high, byproducts are reduced, the traditional process route is broken through, and the problem of three wastes caused by acidification and extraction is avoided, therefore, the invention is an excellent synthesis and post-treatment route.
(2) The method for synthesizing the 3-mercaptopropionic acid by using the acidic waste gas has the characteristics of simple method, low production cost and suitability for industrial large-scale application.
Detailed Description
In order to make the technical problems, technical solutions and advantageous effects solved by the present invention more apparent, the present invention is further described in detail below with reference to the following embodiments. It should be understood that the specific embodiments described herein are merely illustrative of the invention and are not intended to limit the invention.
Example 1.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps:
first, the pressure swing adsorption process purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then carrying out flash evaporation on the liquid phase, carrying out first separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesis of 3-mercaptopropionic acid
Step one, selecting materials: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent; in this example, the molar ratio of acrylic acid to hydrogen sulfide in the hydrogen sulfide product was 1: 3; in this example, the molar ratio of acrylic acid to triethylamine to dimethylacetamide is 1:0.2: 3.5;
step two, the first step reaction: under the protection of inert gas and at the temperature of 10 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 2.5 hours;
step three, reaction in the second step: heating to 80 ℃, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding acrylic acid to be 2 h;
step four, reaction in the third step: and then introducing the rest hydrogen sulfide product, stirring for reaction for 5 hours, and then carrying out reduced pressure rectification to obtain the 3-mercaptopropionic acid.
In this example, the molar ratio of hydrogen sulfide from a portion of the hydrogen sulfide product in step two of the second step to the remainder of the hydrogen sulfide product in step four was 2.5: 1.
Example 2.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps:
first, the pressure swing adsorption method purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then, carrying out flash evaporation on the liquid phase, carrying out primary separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesizing 3-mercaptopropionic acid
Step one, selecting materials: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent; in this example, the molar ratio of acrylic acid to hydrogen sulfide in the hydrogen sulfide product was 1: 1; in this example, the molar ratio of acrylic acid to triethylamine to dimethylacetamide was 1: 0.1: 2;
step two, the first step reaction: under the protection of inert gas and at the temperature of 5 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 3 hours;
step three, reaction in the second step: heating to 75 ℃, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding acrylic acid to be 2.5 h;
step four, reaction in the third step: and then introducing the rest hydrogen sulfide product, stirring for reaction for 4 hours, and then carrying out reduced pressure rectification to obtain the 3-mercaptopropionic acid.
In this example, the molar ratio of hydrogen sulfide from a portion of the hydrogen sulfide product in step two of the second step to the remainder of the hydrogen sulfide product in step four was 2: 1.
Example 3.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps:
first, the pressure swing adsorption method purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then carrying out flash evaporation on the liquid phase, carrying out first separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesizing 3-mercaptopropionic acid
Step one, material selection: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent; in this example, the molar ratio of acrylic acid to hydrogen sulfide in the hydrogen sulfide product was 1: 4; in this example, the molar ratio of acrylic acid to triethylamine and dimethylacetamide was 1: 0.4: 5;
step two, the first step reaction: under the protection of inert gas and at the temperature of 15 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 2 hours;
step three, reaction in the second step: heating to 85 ℃, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding acrylic acid to be 1.5 h;
step four, reaction in the third step: then the rest hydrogen sulfide product is added, stirred and reacted for 6 hours, and then the 3-mercaptopropionic acid is obtained after reduced pressure rectification.
In this example, the molar ratio of hydrogen sulfide from a portion of the hydrogen sulfide product in step two of the second step to the remainder of the hydrogen sulfide product in step four was 3: 1.
Example 4.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps:
first, the pressure swing adsorption method purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then, carrying out flash evaporation on the liquid phase, carrying out primary separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesizing 3-mercaptopropionic acid
Step one, selecting materials: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent; in this example, the molar ratio of acrylic acid to hydrogen sulfide in the hydrogen sulfide product was 1: 2; in this example, the molar ratio of acrylic acid to triethylamine to dimethylacetamide was 1: 0.0.3: 2.5;
step two, the first step reaction: under the protection of inert gas and at the temperature of 8 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 2.8 hours;
step three, reaction in the second step: heating to 78 ℃, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding the acrylic acid to be 2.3 h;
step four, reaction in the third step: and then the rest hydrogen sulfide product is introduced, stirred and reacted for 4.5 hours, and then the 3-mercaptopropionic acid is obtained through reduced pressure rectification.
In this example, the molar ratio of hydrogen sulfide from the portion of the hydrogen sulfide product in step two of the second step to the hydrogen sulfide from the remainder of the hydrogen sulfide product in step four was 2.2: 1.
Example 5.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps:
first, the pressure swing adsorption process purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then carrying out flash evaporation on the liquid phase, carrying out first separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesis of 3-mercaptopropionic acid
Step one, selecting materials: taking acrylic acid and a hydrogen sulfide product obtained in the first step as raw materials, triethylamine as a catalyst and dimethylacetamide as a solvent; in this example, the molar ratio of acrylic acid to hydrogen sulfide in the hydrogen sulfide product was 1: 2.5; in this example, the molar ratio of acrylic acid to triethylamine and dimethylacetamide was 1: 0.3: 4;
step two, the first step reaction: under the protection of inert gas and at the temperature of 12 ℃, the mixed solution of triethylamine and dimethylacetamide and part of hydrogen sulfide products are stirred and react for 2.2 hours;
step three, reaction in the second step: heating to 82 ℃, then dropwise adding acrylic acid for reaction, and controlling the time for dropwise adding acrylic acid to be 1.8 h;
step four, reaction in the third step: and then the rest hydrogen sulfide product is introduced, stirred and reacted for 5.5 hours, and then the 3-mercaptopropionic acid is obtained through reduced pressure rectification.
In this example, the molar ratio of hydrogen sulfide from the portion of the hydrogen sulfide product in step two of the second step to the hydrogen sulfide from the remainder of the hydrogen sulfide product in step four was 2.8: 1.
Practical application examples.
A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas comprises the following steps: after the air in a 1000ml high-pressure reaction kettle is replaced by nitrogen for three times, 20.2g of triethylamine and 304.5g of dimethylacetamide are added, stirred and cooled to 10 ℃, and the temperature is controlled to be 10 +/-5 ℃. Introducing 34g of purified hydrogen sulfide, reacting for 2h, discharging excessive hydrogen sulfide gas, absorbing with alkali, raising the temperature to 80 ℃, adding 72g of acrylic acid into the reaction kettle within 2h, continuously introducing 68g of hydrogen sulfide, and reacting for 5 h. The obtained reaction liquid is directly stripped to obtain 68g of a mixture of triethylamine and dimethylacetamide under normal pressure, then high vacuum rectification is carried out to collect 228.9g of dimethylacetamide at the temperature of 80-110 ℃, and distillation is carried out to collect 69g of 3-mercaptopropionic acid at the temperature of 110-130 ℃, wherein the content is more than or equal to 99.0%, the yield is 65.09%, and the high-boiling residue is thiodipropionic acid.
Although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention.
Claims (1)
1. A method for synthesizing 3-mercaptopropionic acid by using acidic waste gas is characterized by comprising the following steps: the method comprises the following steps:
first, the pressure swing adsorption process purifies the hydrogen sulfide in the acid waste gas
Cooling and pressurizing the acid gas to liquefy part of the gas, wherein methane and nitrogen are still gas, and removing the methane and nitrogen after gas-liquid separation; then carrying out flash evaporation on the liquid phase, carrying out first separation on the hydrogen sulfide and the carbon disulfide, and introducing the mixture of the hydrogen sulfide and the carbon disulfide subjected to flash evaporation into a rectifying tower for rectification to obtain a hydrogen sulfide product with the content of more than 99.5%;
second step, synthesizing 3-mercaptopropionic acid
Replacing air in a 1000ml high-pressure reaction kettle with nitrogen for three times, adding 20.2g of triethylamine and 304.5g of dimethylacetamide, stirring and cooling to 10 ℃, controlling the temperature to be 10 +/-5 ℃, introducing 34g of hydrogen sulfide purified in the first step, reacting for 2 hours, discharging excessive hydrogen sulfide gas, absorbing with alkali, raising the temperature to 80 ℃, introducing 72g of acrylic acid into the reaction kettle within 2 hours, continuously introducing 68g of hydrogen sulfide, reacting for 5 hours, directly stripping the obtained reaction liquid, obtaining a mixture of triethylamine and dimethylacetamide under normal pressure, rectifying under high vacuum to collect 80-110 ℃ fraction as dimethylacetamide, and fractionating to collect 110-130 ℃ fraction as 3-mercaptopropionic acid.
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| CN101965330A (en) * | 2008-03-12 | 2011-02-02 | 昭和电工株式会社 | Method for producing beta-mercapto carboxylic acids |
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