WO2018004314A1 - Membrane de séparation de gaz sélective d'oxyde nitreux et procédé de purification d'oxyde nitreux l'utilisant - Google Patents
Membrane de séparation de gaz sélective d'oxyde nitreux et procédé de purification d'oxyde nitreux l'utilisant Download PDFInfo
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- WO2018004314A1 WO2018004314A1 PCT/KR2017/007000 KR2017007000W WO2018004314A1 WO 2018004314 A1 WO2018004314 A1 WO 2018004314A1 KR 2017007000 W KR2017007000 W KR 2017007000W WO 2018004314 A1 WO2018004314 A1 WO 2018004314A1
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- WIPO (PCT)
- Prior art keywords
- nitrous oxide
- polymer
- gas separation
- membrane
- separation membrane
- Prior art date
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- GQPLMRYTRLFLPF-UHFFFAOYSA-N Nitrous Oxide Chemical compound [O-][N+]#N GQPLMRYTRLFLPF-UHFFFAOYSA-N 0.000 title claims abstract description 282
- 238000000926 separation method Methods 0.000 title claims abstract description 146
- 239000001272 nitrous oxide Substances 0.000 title claims abstract description 138
- 239000012528 membrane Substances 0.000 title claims abstract description 134
- 238000000034 method Methods 0.000 title claims abstract description 32
- 239000007789 gas Substances 0.000 claims abstract description 174
- 229920000642 polymer Polymers 0.000 claims abstract description 50
- 229920001721 polyimide Polymers 0.000 claims abstract description 45
- 239000000203 mixture Substances 0.000 claims abstract description 41
- 238000004519 manufacturing process Methods 0.000 claims abstract description 27
- 229920002492 poly(sulfone) Polymers 0.000 claims abstract description 22
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 claims abstract description 18
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000002861 polymer material Substances 0.000 claims abstract description 13
- 235000011037 adipic acid Nutrition 0.000 claims abstract description 9
- 239000001361 adipic acid Substances 0.000 claims abstract description 9
- 238000000197 pyrolysis Methods 0.000 claims abstract description 9
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims abstract description 8
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 8
- 239000004642 Polyimide Substances 0.000 claims description 39
- 239000002808 molecular sieve Substances 0.000 claims description 16
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 229910021536 Zeolite Inorganic materials 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 8
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 8
- 229910010272 inorganic material Inorganic materials 0.000 claims description 8
- 239000011147 inorganic material Substances 0.000 claims description 8
- 239000004417 polycarbonate Substances 0.000 claims description 8
- 239000010457 zeolite Substances 0.000 claims description 8
- 229920002301 cellulose acetate Polymers 0.000 claims description 7
- 229920000515 polycarbonate Polymers 0.000 claims description 7
- 239000012510 hollow fiber Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 5
- 239000004693 Polybenzimidazole Substances 0.000 claims description 4
- 229920002647 polyamide Polymers 0.000 claims description 4
- 229920002480 polybenzimidazole Polymers 0.000 claims description 4
- 238000000746 purification Methods 0.000 claims description 4
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 2
- 239000004952 Polyamide Substances 0.000 claims 2
- 229920013637 polyphenylene oxide polymer Polymers 0.000 claims 2
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 claims 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 40
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 20
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 12
- 239000001301 oxygen Substances 0.000 abstract description 12
- 229910052760 oxygen Inorganic materials 0.000 abstract description 12
- 230000001747 exhibiting effect Effects 0.000 abstract description 5
- GNEVIACKFGQMHB-UHFFFAOYSA-N carbon suboxide Chemical compound O=C=C=C=O GNEVIACKFGQMHB-UHFFFAOYSA-N 0.000 abstract 1
- 239000002075 main ingredient Substances 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 33
- 239000010409 thin film Substances 0.000 description 24
- 239000000463 material Substances 0.000 description 16
- 238000009501 film coating Methods 0.000 description 12
- 230000035699 permeability Effects 0.000 description 11
- 238000005516 engineering process Methods 0.000 description 7
- -1 poly (dimethylsiloxane) Polymers 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 238000000576 coating method Methods 0.000 description 6
- 239000004721 Polyphenylene oxide Substances 0.000 description 5
- 239000012535 impurity Substances 0.000 description 5
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 5
- 229920006380 polyphenylene oxide Polymers 0.000 description 5
- 239000001856 Ethyl cellulose Substances 0.000 description 4
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 4
- 239000004205 dimethyl polysiloxane Substances 0.000 description 4
- 235000013870 dimethyl polysiloxane Nutrition 0.000 description 4
- 229920001249 ethyl cellulose Polymers 0.000 description 4
- 235000019325 ethyl cellulose Nutrition 0.000 description 4
- 229920006260 polyaryletherketone Polymers 0.000 description 4
- 229920002857 polybutadiene Polymers 0.000 description 4
- 229920000306 polymethylpentene Polymers 0.000 description 4
- 239000005062 Polybutadiene Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 229920001577 copolymer Polymers 0.000 description 3
- 229920001971 elastomer Polymers 0.000 description 3
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 3
- 239000004926 polymethyl methacrylate Substances 0.000 description 3
- 239000005033 polyvinylidene chloride Substances 0.000 description 3
- 239000005060 rubber Substances 0.000 description 3
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 244000043261 Hevea brasiliensis Species 0.000 description 2
- 229920001328 Polyvinylidene chloride Polymers 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 229920005549 butyl rubber Polymers 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000002131 composite material Substances 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000002474 experimental method Methods 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 2
- 229920003052 natural elastomer Polymers 0.000 description 2
- 229920001194 natural rubber Polymers 0.000 description 2
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 2
- 238000005371 permeation separation Methods 0.000 description 2
- 229920000573 polyethylene Polymers 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004065 semiconductor Substances 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- JOLYFVJXLWUTBQ-UHFFFAOYSA-N 4-methyl-2-methylidenecyclopentane-1,3-dione Chemical compound C=C1C(CC(C1=O)C)=O JOLYFVJXLWUTBQ-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- AGSHZHCXQFVBNG-UHFFFAOYSA-N O=O.N Chemical compound O=O.N AGSHZHCXQFVBNG-UHFFFAOYSA-N 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 229920001646 UPILEX Polymers 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 239000010408 film Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 239000004973 liquid crystal related substance Substances 0.000 description 1
- 238000004377 microelectronic Methods 0.000 description 1
- 230000008450 motivation Effects 0.000 description 1
- 238000005121 nitriding Methods 0.000 description 1
- CXQXSVUQTKDNFP-UHFFFAOYSA-N octamethyltrisiloxane Chemical compound C[Si](C)(C)O[Si](C)(C)O[Si](C)(C)C CXQXSVUQTKDNFP-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 238000004987 plasma desorption mass spectroscopy Methods 0.000 description 1
- 229920003205 poly(diphenylsiloxane) Polymers 0.000 description 1
- 229920005597 polymer membrane Polymers 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 239000004945 silicone rubber Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/66—Polymers having sulfur in the main chain, with or without nitrogen, oxygen or carbon only
- B01D71/68—Polysulfones; Polyethersulfones
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/107—Organic support material
- B01D69/1071—Woven, non-woven or net mesh
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/22—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion
- B01D53/228—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by diffusion characterised by specific membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/02—Hollow fibre modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/06—Tubular membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D63/00—Apparatus in general for separation processes using semi-permeable membranes
- B01D63/10—Spiral-wound membrane modules
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D67/00—Processes specially adapted for manufacturing semi-permeable membranes for separation processes or apparatus
- B01D67/0079—Manufacture of membranes comprising organic and inorganic components
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/04—Tubular membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/08—Hollow fibre membranes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D69/00—Semi-permeable membranes for separation processes or apparatus characterised by their form, structure or properties; Manufacturing processes specially adapted therefor
- B01D69/10—Supported membranes; Membrane supports
- B01D69/108—Inorganic support material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D71/00—Semi-permeable membranes for separation processes or apparatus characterised by the material; Manufacturing processes specially adapted therefor
- B01D71/06—Organic material
- B01D71/58—Other polymers having nitrogen in the main chain, with or without oxygen or carbon only
- B01D71/62—Polycondensates having nitrogen-containing heterocyclic rings in the main chain
- B01D71/64—Polyimides; Polyamide-imides; Polyester-imides; Polyamide acids or similar polyimide precursors
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/10—Capture or disposal of greenhouse gases of nitrous oxide (N2O)
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/30—Improvements relating to adipic acid or caprolactam production
Definitions
- the present invention relates to a nitrous oxide selective gas separation membrane, and in particular, to separate high-purity nitrous oxide from a nitrous oxide-containing gas mixture produced during the production of nitrous oxide by pyrolysis of ammonium nitrate, or to prepare adipic acid, nitric acid and caprolactam
- the present invention relates to a nitrous oxide selective gas separation membrane that can be used industrially to separate high-purity nitrous oxide from nitrous oxide-containing exhaust gas mixture discharged from industrial processes such as processes.
- Nitrous oxide has been in great demand in the microelectronic process of the semiconductor, liquid crystal display (LCD) and organic light emitting diode (OLED) fields.
- Nitrous oxide is used for the production of silicon oxide layers formed from a gas mixture of silane and nitrous oxide chemically or by plasma deposition under low pressure. Nitrous oxide is also used for nitriding thin film silicon films.
- Oxygen and nitrogen are the major impurities containing nitrous oxide that have a significant impact on quality in the silicon oxidation process.
- nitrous oxide is prepared by pyrolyzing ammonium nitrate, which must be purified by removing impurities such as nitrogen and oxygen contained in the pyrolysis product.
- Nitrous oxide is contained in the exhaust gas emitted from the adipic acid production process, the nitric acid production process, and the caprolactam production process.
- the main impurities of the exhaust gas are oxygen and nitrogen. It is desired to recover nitrous oxide from nitrous oxide-containing exhaust gas and reuse it. This is because the recovery and reuse of nitrous oxide can not only reduce greenhouse gas emissions but also provide economic benefits.
- Membrane separation technology is the most promising technique for separating and concentrating nitrous oxide discharged from industrial processes from mixed oxygen and nitrogen.
- Membrane separation technology has advantages in that impurities can be efficiently separated from existing separation technologies such as adsorption and distillation, as well as a small device, low energy consumption, and continuous operation.
- separator materials presented in the documents cited in the above papers are silicone rubber, polydimethylsiloxane, perpulouro (2-methylene-4-methyl-1,3-dioxocyclopentane) and poly [bis (tripulolu).
- Roethoxy) phosphazenene] and the like also have low selectivity and permeability and are not effective for the separation of nitrous oxide.
- the present inventors have effectively utilized nitrous oxide from nitrous oxide-containing gas mixture produced by pyrolysis of ammonium nitrate and nitrous oxide-containing exhaust gas emitted from industrial processes such as adipic acid manufacturing process, nitric acid manufacturing process and caprolactam manufacturing process. While studying a gas separation membrane that can be economically separated, a nitrous oxide selective gas separation membrane was found to have excellent separation performance of nitrous oxide, and the present invention was completed.
- An object of the present invention is to efficiently treat nitrous oxide from nitrous oxide-containing gas mixtures produced by pyrolysis of ammonium oxyoxide and nitrous oxide-containing exhaust gases emitted in industrial processes such as adipic acid, nitric acid, and caprolactam. And economic separation.
- a gas separation layer comprising a polymer material which is a polysulfone polymer or a polyimide polymer.
- nitrous oxide selective gas separation membrane characterized by exhibiting nitrous oxide separation characteristics.
- separator module comprising at least one nitrous oxide selective gas separator comprising a; and a gas separation layer comprising a polymer material which is a polysulfone polymer or a polyimide polymer.
- It provides a method for purifying nitrous oxide comprising the step (step 2) of separating the nitrous oxide in the gas mixture supplied in step 1.
- the nitrous oxide selective gas separation membrane according to the present invention can efficiently and economically separate or concentrate nitrous oxide from a gas mixture containing nitrous oxide, nitrogen, oxygen or other gas as a main component.
- the present invention is a.
- a gas separation layer comprising a polymer material which is a polysulfone polymer or a polyimide polymer.
- nitrous oxide selective gas separation membrane characterized by exhibiting nitrous oxide separation characteristics.
- the nitrous oxide selective gas separation membrane according to the present invention is characterized by exhibiting nitrous oxide separation characteristics, in particular, characterized in that it comprises a gas separation layer comprising a polymer material which is a polysulfone-based polymer or a polyimide-based polymer.
- the gas separation layer including the polymer material of the polysulfone-based polymer or the polyimide-based polymer proposed in the present invention has not only a high nitrous oxide / nitrogen selectivity but also a high nitrous oxide permeation rate.
- the gas separation layer has a separation coefficient of nitrous oxide / nitrogen at a permeation temperature of 0 ° C. to 100 ° C. and a permeation pressure of 0 bar to 100 bar ( ⁇ , P N 2 O / P N 2). ) May be 30 or more, 35 or more are preferred, more preferably 40 or more, even more preferably more than 40, most preferably 40-50.
- the gas permeation separation performance of the gas separation membrane depends on the permeation selectivity and the permeation rate relative to the relative ratio of permeability between the gas mixture components to be separated and the gas mixture components to be separated.
- ⁇ the permeability coefficient
- ⁇ the ratio
- P N 2 O / PN 2 the ratio
- the membrane material is coated in the form of a composite membrane or processed into an asymmetric structure having a thin film layer to increase the permeation rate of gases per unit time.
- the gas separation layer preferably has a permeation rate of nitrous oxide of 100 GPU or more, more preferably 150 GPU or more, and more preferably 200 GPU to 1,000 GPU, in a range of a permeation temperature of 0 ° C. to 100 ° C. and a permeation pressure of 0 bar to 100 bar. Most preferred.
- the gas separation layer may be in the form of a mixture of at least one inorganic material selected from the group consisting of zeolite, carbon molecular sieve, metal organic structure (MOF) and aluminophosphate molecular sieve.
- the gas separation membrane further includes a porous support layer.
- the gas separation membrane including the porous support layer and the gas separation layer may have a form in which the gas separation layer is present in a thin film form on the surface of the porous support layer.
- the porous support layer may mean a support made of a membrane having perforated fine pores connecting the front and back of the membrane, and its shape and material are not specified.
- the porous support layer may be, for example, a hollow fiber porous support layer, a spiral porous support layer, a flat porous support layer, a nonwoven support layer, and the material may be a polysulfone polymer, a polyimide polymer, a cellulose acetate polymer, or a polycarbonate It may be one kind of polymer selected from the group consisting of a polymer, a polyamide-based polymer, a polyphenylene oxide-based polymer, and a polybenzimidazole-based polymer, a copolymer, a blend combination thereof, zeolite, carbon molecular sieve, metal organic structure (MOF) and an inorganic substance selected from the group consisting of aluminophosphate molecular sieves, mixtures thereof and the like.
- a polysulfone polymer a polyimide polymer
- a cellulose acetate polymer or a polycarbonate
- It may be one kind of polymer selected from the group consisting
- the porous support layer is preferably made of a polymer material, but a support made of an inorganic material or a metal component such as ceramic or metal powder may be used alone or together with a polymer in order to increase mechanical strength or heat resistance.
- the gas separation membrane may be one type selected from the group consisting of hollow fiber membranes, spiral wound membranes, and tubular membranes.
- separator module comprising at least one nitrous oxide selective gas separator comprising a; and a gas separation layer comprising a polymer material which is a polysulfone polymer or a polyimide polymer.
- the membrane module according to the present invention is characterized in that it comprises at least one nitrous oxide selective gas separation membrane.
- the nitrous oxide selective gas separation membrane including the polymer material of the polysulfone-based polymer or the polyimide-based polymer proposed in the present invention has not only a high nitrous oxide / nitrogen selectivity but also a high nitrous oxide permeation rate.
- the membrane module has a separation coefficient ( ⁇ , P N2O / P N2 ) of nitrous oxide / nitrogen in a range of 0 ° C. to 100 ° C. and a permeation pressure of 0 bar to 100 bar of 30 or more. It is preferable that it is 35 or more, It is more preferable that it is 40 or more, It is still more preferable that it is more than 40, It is most preferable that it is 40-50.
- the gas permeation separation performance of the gas separation membrane depends on the permeation selectivity and the permeation rate relative to the relative ratio of permeability between the gas mixture components to be separated and the gas mixture components to be separated.
- ⁇ the permeability coefficient
- ⁇ the ratio
- P N 2 O / PN 2 the ratio
- the membrane material is coated in the form of a composite membrane or processed into an asymmetric structure having a thin film layer to increase the permeation rate of gases per unit time.
- the separator module preferably has a permeation rate of nitrous oxide in the range of 0 ° C. to 100 ° C. and a permeation pressure of 0 bar to 100 bar, preferably 100 GPU or more, more preferably 150 GPU or more, and 200 GPU to 1,000 GPU. Most preferred.
- the gas separation layer may be in the form of a mixture of at least one inorganic material selected from the group consisting of zeolite, carbon molecular sieve, metal organic structure (MOF) and aluminophosphate molecular sieve.
- the gas separation membrane preferably further comprises a porous support layer.
- the gas separation membrane including the porous support layer and the gas separation layer may have a form in which the gas separation layer is present in a thin film form on the surface of the porous support layer.
- the porous support layer may mean a support made of a membrane having perforated fine pores connecting the front and back of the membrane, and its shape and material are not specified.
- the porous support layer may be, for example, a hollow fiber porous support layer, a spiral porous support layer, a flat porous support layer, a nonwoven support layer, and the material may be a polysulfone polymer, a polyimide polymer, a cellulose acetate polymer, or a polycarbonate It may be one kind of polymer selected from the group consisting of a polymer, a polyamide-based polymer, a polyphenylene oxide-based polymer, and a polybenzimidazole-based polymer, a copolymer, a blend combination thereof, zeolite, carbon molecular sieve, metal organic structure (MOF) and an inorganic substance selected from the group consisting of aluminophosphate molecular sieves, mixtures thereof and the like.
- a polysulfone polymer a polyimide polymer
- a cellulose acetate polymer or a polycarbonate
- It may be one kind of polymer selected from the group consisting
- the porous support layer is preferably made of a polymer material, but a support made of an inorganic material or a metal component such as ceramic or metal powder may be used alone or together with a polymer in order to increase mechanical strength or heat resistance.
- the gas separation membrane may be one type selected from the group consisting of hollow fiber membranes, spiral wound membranes, and tubular membranes.
- It provides a method for purifying nitrous oxide comprising the step (step 2) of separating the nitrous oxide in the gas mixture supplied in step 1.
- step 1 is a step of supplying a gas mixture containing nitrous oxide to the separator module.
- the method for purifying nitrous oxide is obtained from exhaust gas generated in a nitrogen-containing material production process such as nitrous oxide (N 2 O) production process, adipic acid production process, nitric acid production process, caprolactam production process by pyrolysis of ammonium nitrate.
- a nitrogen-containing material production process such as nitrous oxide (N 2 O) production process, adipic acid production process, nitric acid production process, caprolactam production process by pyrolysis of ammonium nitrate.
- a gas mixture containing nitrous oxide of step 1 is supplied to the membrane module.
- the membrane module of step 1 comprises a gas separation layer comprising a polymer material which is a polysulfone-based polymer or a polyimide-based polymer as described in the present invention as described above, and nitrous oxide characterized in that it exhibits nitrous oxide separation characteristics
- a separator module comprising at least one nitrogen selective gas separator.
- the membrane module has a separation coefficient (?, P N2O / P N2 ) of 40 to 50 in the range of the permeation temperature of 0 °C to 100 °C and the permeation pressure of 0 bar to 100 bar, the nitrous oxide Since the transmission rate of 100 to 1,000 GPU, it can exhibit excellent nitrous oxide separation performance.
- step 2 is a step of separating nitrous oxide from the gas mixture supplied in step 1 above.
- Step 2 is a step of selectively separating the nitrous oxide contained in the gas mixture including the nitrous oxide supplied in step 1 through the membrane module.
- the gas mixture contains about 0.3% by volume to 60% by volume of nitrous oxide, and the most impurities may contain 5% by volume to 60% by volume of nitrogen and 0% by volume to 40% by volume of oxygen.
- nitrous oxide may be separated from nitrogen and oxygen, and concentrated to a concentration of 80% by volume or more.
- Polysulphone PSF; Polysulfone (BASF) was manufactured on a self-made porous polyimide support with a thin film coating having a thickness of 1 to 5 ⁇ m to prepare a gas separation membrane, and the prepared gas separation membrane had an area of 330 cm 2 . It was prepared.
- Polyimide (PI; Polyimide, Hunstman, USA) was produced by coating a thin film with a thickness of 1 to 5 ⁇ m on a self-made porous polyimide support to prepare a gas separation membrane, and the prepared gas separation membrane had an area of 330 cm 2 . Prepared to size.
- PSF polysulfone
- Polyimide (PI; Polyimide, P84 from Evonik, Germany) was coated with a thin film having a thickness of 1 to 5 ⁇ m to a porous polyimide support, and a gas separation membrane was prepared. Prepared to the size of 2 .
- Polyimide (PI; Polyimide, Upilex, Ube, Japan) was applied to the self-made porous polyimide support to prepare a gas separation membrane by thin-film coating, and the prepared gas separation membrane was an area of 330 cm 2. Prepared to the size of.
- a cellulose acetate polymer membrane (Cellulose Acetate, Kodak Film Co., Ltd.) was prepared in a size of 330 cm 2 .
- Polycarbonate (PC; Polycarbonate, LG Chemical Co., Ltd.) on the self-made porous polyimide support was a thin film coating to a thickness of 1 to 5 ⁇ m to prepare a gas separation membrane, the prepared gas separation membrane having an area of 330 cm 2 Prepared to size.
- Polydimethylsiloxane (PDMS; Dow Corning, USA) was manufactured by coating a thin film with a thickness of 1 to 5 ⁇ m on a self-made porous polyimide support to prepare a gas separation membrane, and the prepared gas separation membrane had an area of 330 cm. Prepared to the size of 2 .
- the self-made porous polyimide support was coated with a natural rubber (NR, Korea LG Chemical Co., Ltd.) to a thickness of 1 to 5 ⁇ m thickness to prepare a gas separation membrane, the prepared gas separation membrane area 330 cm 2 Prepared to the size of.
- a natural rubber NR, Korea LG Chemical Co., Ltd.
- Polybutadiene (Polybutadiene; PBD, Korea Daelim Industrial Co., Ltd.) on a self-made porous polyimide support was a thin film coating to a thickness of 1 to 5 ⁇ m to prepare a gas separation membrane, the prepared gas separation membrane having an area of 330 cm 2 Prepared to size.
- a gas separation membrane was prepared by coating a self-made porous polyimide support with a thin film of polyethylene (PE; LG Chemical Co., Ltd.) to a thickness of 1 to 5 ⁇ m.
- the prepared gas separation membrane was an area of 330 cm 2 . It was prepared.
- a gas separation membrane was prepared by coating a thin film of methyl rubber (LG Chem. Korea) with a thickness of 1 to 5 ⁇ m on a porous polyimide support fabricated by itself, and preparing the gas separation membrane with an area of 330 cm 2 . It was prepared.
- Butyl rubber (Buthyl rubber, LG Chem Co., Ltd.) on the self-made porous polyimide support to perform a thin film coating to a thickness of 1 to 5 ⁇ m thickness to prepare a gas separation membrane, the prepared gas separation membrane having a size of 330 cm 2 area It was prepared.
- a gas separation membrane was formed by coating a thin film of poly (4-methylpentene-1) (PMP, Korea Daelim Industrial Co., Ltd.) with a thickness of 1 to 5 ⁇ m on a self-made porous polyimide support.
- the prepared gas separation membrane was prepared in an area of 330 cm 2 .
- a gas separation membrane was prepared by performing a thin film coating of ethyl cellulose (EC, East membrane Kodak, USA) on a self-made porous polyimide support with a thickness of 1 to 5 ⁇ m, and the prepared gas separation membrane having an area of 330 cm. Prepared to the size of 2 .
- EC ethyl cellulose
- Polyaryletherketone (PEK, BASF Co., Ltd., USA) thin film coating was performed on a self-made porous polyimide support to prepare a gas separation membrane, and the prepared gas separation membrane had an area of 330 cm 2. Prepared to the size of.
- a gas separation membrane was prepared by performing a thin film coating of polyphenylene oxide (PEO, LG Chem, Korea) with a thickness of 1 to 5 ⁇ m on a self-made porous polyimide support, and preparing the gas separation membrane with an area of 330 cm. Prepared to the size of 2 .
- PEO polyphenylene oxide
- Polybenzimidizole (PBI, PBI advanced materials, Inc.) was produced by coating a thin film with a thickness of 1 to 5 ⁇ m on a porous polyimide support fabricated by itself to prepare a gas separation membrane, and the prepared gas separation membrane had an area of 330 cm. Prepared to the size of 2 .
- Poly (methyl methacrylate; PMMA, LG Chem Co., Ltd., Korea) was a thin film coating to a thickness of 1 to 5 ⁇ m on the porous polyimide support itself prepared to prepare a gas separation membrane, the prepared gas separation membrane It was prepared to a size of area 330 cm 2 .
- PVDC Polyvinylidene chloride
- the nitrous oxide permeation rate is excellent from 49.2 GPU to 643.3 GPU per company,
- the calculated separation coefficient ⁇ (P N 2 O / P N 2 ) is 40.5 to 45.2, that is, it can be confirmed that exhibiting excellent separation characteristics to 40 or more.
- the gas separation membrane according to the present invention can be used to separate or concentrate nitrous oxide from a nitrous oxide-containing gas mixture generated in the chemical industry at a high concentration.
- it can be used to separate high-purity nitrous oxide from the gas mixture produced during the production of nitrous oxide by pyrolysis of ammonium nitrate, and also contains nitrous oxide-containing exhaust gases from adipic acid, nitric acid and caprolactam manufacturing processes. It is expected to be useful for the membrane separation process for recovering nitrous oxide for medical and semiconductor, LCD, and OLED.
- the nitrous oxide selective gas separation membrane according to the present invention is useful for efficiently and economically separating or concentrating nitrous oxide from a gas mixture containing nitrous oxide, nitrogen or oxygen or other gas as a main component.
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Abstract
La présente invention concerne une membrane de séparation de gaz sélective d'oxyde nitreux qui comprend une couche de séparation de gaz contenant un matériau polymère qui est un polymère à base de polysulfone ou un polymère à base de polyimide. La membrane de séparation de gaz sélective d'oxyde nitreux présente une propriété de séparation d'oxyde nitreux. La membrane de séparation de gaz sélective d'oxyde nitreux selon la présente invention est efficace dans la séparation d'oxyde nitreux de haute pureté à partir d'un mélange gazeux contenant du suboxyde de carbone produit dans un procédé de fabrication d'oxyde nitreux par pyrolyse de nitrate d'ammonium contenant de l'oxyde nitreux, de l'azote ou de l'oxygène ou d'autres gaz comme ingrédients principaux. La membrane peut aussi à partir d'un mélange de gaz d'échappement contenant de l'oxyde nitreux déchargé de procédés industriels tels que des procédés de fabrication de l'acide adipique, l'acide nitrique et le caprolactame, effectuer une séparation efficace de l'oxyde nitreux. Cette présente invention permet d'effectuer de manière économique une séparation et une concentration.
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KR1020160082598A KR101748609B1 (ko) | 2016-06-30 | 2016-06-30 | 아산화질소 선택성 기체 분리막 및 이를 이용한 아산화질소 정제방법 |
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
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CN108704493A (zh) * | 2018-06-26 | 2018-10-26 | 黑龙江大学 | 一种免冲洗pvdf管式微孔膜的制备方法 |
CN112320941A (zh) * | 2020-10-21 | 2021-02-05 | 西安建筑科技大学 | 一种利用分离膜填料驯化产n2o反硝化菌的装置及方法 |
EP3858786A4 (fr) * | 2018-09-28 | 2022-06-22 | Showa Denko K.K. | Procédé de purification d'oxyde nitreux |
Families Citing this family (3)
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KR101951780B1 (ko) * | 2017-08-31 | 2019-02-25 | 한국화학연구원 | 가변운전이 가능한 아산화질소 회수 방법 및 장치 |
KR101952945B1 (ko) * | 2017-08-31 | 2019-02-27 | 한국화학연구원 | 아산화질소 회수 방법 |
KR101951773B1 (ko) * | 2017-08-31 | 2019-02-25 | 한국화학연구원 | 가변운전이 가능한 하이브리드 아산화질소 회수 방법 및 장치 |
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CN112320941A (zh) * | 2020-10-21 | 2021-02-05 | 西安建筑科技大学 | 一种利用分离膜填料驯化产n2o反硝化菌的装置及方法 |
CN112320941B (zh) * | 2020-10-21 | 2022-10-11 | 西安建筑科技大学 | 一种利用分离膜填料驯化产n2o反硝化菌的装置及方法 |
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