KR20010001813A - Continuous Process for the Production of Biosurfactant using a Technology of Immobilized Enzyme - Google Patents
Continuous Process for the Production of Biosurfactant using a Technology of Immobilized Enzyme Download PDFInfo
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- KR20010001813A KR20010001813A KR1019990021267A KR19990021267A KR20010001813A KR 20010001813 A KR20010001813 A KR 20010001813A KR 1019990021267 A KR1019990021267 A KR 1019990021267A KR 19990021267 A KR19990021267 A KR 19990021267A KR 20010001813 A KR20010001813 A KR 20010001813A
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- Prior art keywords
- enzyme
- reactor
- production
- surfactant
- membrane
- Prior art date
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 16
- 239000003876 biosurfactant Substances 0.000 title claims abstract description 13
- 238000010924 continuous production Methods 0.000 title abstract description 5
- 108010093096 Immobilized Enzymes Proteins 0.000 title description 2
- 238000005516 engineering process Methods 0.000 title description 2
- 239000012528 membrane Substances 0.000 claims abstract description 20
- 108090000790 Enzymes Proteins 0.000 claims abstract description 18
- 102000004190 Enzymes Human genes 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 12
- 238000003980 solgel method Methods 0.000 claims abstract description 4
- FYGDTMLNYKFZSV-DZOUCCHMSA-N alpha-D-Glcp-(1->4)-alpha-D-Glcp-(1->4)-D-Glcp Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)O[C@H](O[C@@H]2[C@H](OC(O)[C@H](O)[C@H]2O)CO)[C@H](O)[C@H]1O FYGDTMLNYKFZSV-DZOUCCHMSA-N 0.000 claims abstract 3
- 238000002360 preparation method Methods 0.000 claims description 4
- 239000011496 polyurethane foam Substances 0.000 abstract description 11
- 238000000926 separation method Methods 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 5
- 229920002472 Starch Polymers 0.000 abstract description 4
- 235000019698 starch Nutrition 0.000 abstract description 4
- 239000008107 starch Substances 0.000 abstract description 4
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 230000003100 immobilizing effect Effects 0.000 abstract 3
- 229920001730 Moisture cure polyurethane Polymers 0.000 abstract 1
- 238000012856 packing Methods 0.000 abstract 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 9
- 230000000694 effects Effects 0.000 description 5
- 235000000346 sugar Nutrition 0.000 description 5
- 230000000704 physical effect Effects 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 150000008163 sugars Chemical class 0.000 description 3
- 239000004094 surface-active agent Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000560 biocompatible material Substances 0.000 description 2
- 238000004128 high performance liquid chromatography Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000000108 ultra-filtration Methods 0.000 description 1
Classifications
-
- G06Q50/40—
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B60—VEHICLES IN GENERAL
- B60Q—ARRANGEMENT OF SIGNALLING OR LIGHTING DEVICES, THE MOUNTING OR SUPPORTING THEREOF OR CIRCUITS THEREFOR, FOR VEHICLES IN GENERAL
- B60Q5/00—Arrangement or adaptation of acoustic signal devices
Abstract
Description
생물계면활성제는 환원당을 주원료로 하여 회분식 반응기에의하여 생산되고 있다. 또한 연속식 생산 반응기로는 원료를 공급하여 반응기에서 발효를 한 뒤 이 생산물들을 ultrafiltration에 의하여 효모를 재순환 하는 공정을 연구중에 있다. 그러나 이러한 모든 공정들은 부가적인 분리공정들을 함유하고 있어 생산원가 상승의 원인이 되고 있다. 본 발명은 다른 분리기능이 없이 고정화된 효소에 의하여 생물계면활성제를 생산하는 동시에 분리 기능을 수행하는 공정의 발명이다.Biosurfactants are produced in batch reactors using reducing sugars as the main raw material. In addition, we are studying a process to recycle yeast by ultrafiltration after supplying raw materials to a continuous production reactor and fermenting the reactor. All of these processes, however, contain additional separation processes, which contribute to an increase in production costs. The present invention is an invention of a process for producing a biosurfactant by an immobilized enzyme without any other separation function and at the same time performing the separation function.
본 발명은 생물계면활성제의 주원료인 환원당을 생산하는 공정에서부터 생물계면활성제를 생산하는 공정에 이르기까지 모두 환경친화적인 물질을 사용하여 2차적인 환경오염이 없으며 부가적인 분리공정을 함유하지 않은 생산공정을 이루고자 한다.The present invention is a production process that does not contain secondary environmental pollution and does not contain an additional separation process from the production of reducing sugars, the main raw material of the biosurfactant to the process of producing the biosurfactant. To achieve this.
첫 번째로 전분으로부터 환원당을 생산하는 공정에서는 반응기 기능과 분리기능을 동시에 수행할 수 있는 막 반응기의 제조와 이 막 반응기에 사용되는 막을 제조하는 것이다. 막의 제조는 저온에서 유리나 세라믹을 제조하는 졸-겔 방법을 이용하여 효소가 고정화된 유기/무기 혼성막을 제조하고, 이막을 막 반응기에 적용하여 전분으로부터 환원당을 생산하는 공정을 제조하였다.First, in the process of producing reducing sugars from starch, the production of a membrane reactor capable of performing the reactor function and the separation function at the same time and the production of the membrane used in the membrane reactor. In the preparation of the membrane, an organic / inorganic hybrid membrane in which an enzyme is immobilized was prepared by using a sol-gel method of preparing glass or ceramic at low temperature, and the membrane was applied to a membrane reactor to prepare a process of producing reducing sugar from starch.
두 번째로는 기계적 물성과 안정성을 갖고 산소 운반도 용이하며 분리공정이 쉽고 재사용이 가능하여 연속식 공정에 응용이 가능한 폴리우레탄폼에 물리적으로 효소를 고정화하고, 효소가 고정화된 폴리우레탄폼을 튜브 반응기에 충진하여 PFR 반응기에 적용하였다. 또한 전체적으로 사용되어지는 물질이 모두 환경 친화적인 물질들을 사용하여 환경오염이 없는 생물계면활성제 생산 반응공정을 확립하였다.Second, it has mechanical properties and stability, it is easy to transport oxygen, easy to separate process and reusable, so that the enzyme is physically immobilized on the polyurethane foam that can be applied to the continuous process, and the polyurethane foam on which the enzyme is immobilized is tubed. The reactor was charged and applied to the PFR reactor. In addition, all of the materials used are environmentally friendly materials to establish a biosurfactant production reaction process without pollution.
효소고정화기술을 이용하여 아래의 그림에서 보여지고 있는 것처럼 환경 친화적인 생물계면활성제 생산공정을 제조하고자 한다.Using enzyme fixation technology, we will manufacture environmentally friendly biosurfactant production process as shown in the figure below.
[실시예 1]Example 1
효소가 고정화된 유기/무기 혼성막 제조 및 막 반응기의 응용.Preparation of Organic / Inorganic Hybrid Membranes with Enzyme Immobilization and Application of Membrane Reactor.
졸-겔 공정에 의하여 제조되어진 효소 고정화된 막을 1 ㎠로 자른 뒤 효소의 활성을 측정하여 그림 2에 보였다. 그림 2에서 보여지고 있듯이 장시간 동안 효소가 안정하게 활성을 유지하는 것을 확인 할 수가 있었다. 이 막을 이용하여 막 반응기를 만들고 (그림 2), 그 후 전분을 막 반응기에 공급하고 생산되어진 생성물은 HPLC에 의하여 분석하였다. HPLC에 의하여 분석한 결과를 그림 4에 나타내었으며, 한성분만의 환원당이 전체 생성물의 96% 이상 생산되어지는 것을 확인할 수 있었다.The enzyme-immobilized membrane prepared by the sol-gel process was cut into 1 cm 2, and the enzyme activity was measured. As shown in Figure 2, it was confirmed that the enzyme remained stable for a long time. The membrane was used to make a membrane reactor (Figure 2), then starch was fed to the membrane reactor and the product produced was analyzed by HPLC. The analysis results by HPLC are shown in Figure 4, it can be seen that only one component of reducing sugar is produced more than 96% of the total product.
[실시예 2]Example 2
효소가 고정화된 폴리우레탄 폼 제조 및 반응기 제작Enzyme-immobilized Polyurethane Foam Production and Reactor Production
폴리우레탄 폼은 다양한 폴리올을 이용하여 폴리우레탄 폼의 전구체인 프리폴리머를 합성하였다. 합성되어진 프리폴리머를 사용하여 다양한 물성을 갖는 폴리우레탄 폼을 제조하였으며, 그림 4에 폴리우레탄 폼의 수분 흡수력을 시간별로 나타내었다.Polyurethane foams were synthesized using various polyols as prepolymers that are precursors of polyurethane foams. Polyurethane foams having various physical properties were prepared using the synthesized prepolymer, and FIG. 4 shows the water absorption of polyurethane foam over time.
그림 5에서 보여지고 있듯이 수분흡수력과 물성이 우수한 최적의 조건을 선택하여 물리적으로 효소를 고정화하고, 효소의 활성을 측정하여 그림 6에서 나타내었다. 그림에 나타나듯이 효소활성이 장시간 동안 안정하게 유지되어지고 있는 것을 확인할 수가 있다.As shown in Fig. 5, the enzyme was physically immobilized by selecting an optimal condition having excellent water absorption and physical properties, and the enzyme activity was measured. As shown in the figure, it can be seen that the enzyme activity is maintained for a long time.
최적의 물성을 갖는 폴리우레탄 폼에 효소를 고정화하고, 효소가 고정화된 폴리우레탄 폼을 PFR 반응기에 충진하고 1차 막 반응기에서 생산되어진 단 성분만의 말토올리고당을 공급하여 생체 적합적인 생물계면활성제를 생산하였다.The enzyme is immobilized on the polyurethane foam having the optimal physical properties, and the enzyme-immobilized polyurethane foam is filled in the PFR reactor, and only the maltooligosaccharides produced in the primary membrane reactor are supplied to provide biocompatible biosurfactants. Produced.
생성된 계면활성제의 표면 특성과 생체 적합성능을 측정하였다. 농도와 표면장력을 그림 7에 나타내었으며, 14 mmol에서 33 dyne/cm의 결과를 얻었다. 생체 적합성은 생성된 계면활성제를 팔에 도포하여 부작용의 유무를 확인하였으며, 24 시간이상 다른 부작용이 없었고, 양질의 생체적합성물질을 합성할 수가 있었다.The surface properties and biocompatibility of the resulting surfactants were measured. The concentration and surface tension are shown in Fig. 7, and 33 dyne / cm at 14 mmol was obtained. Biocompatibility was confirmed by applying the generated surfactant to the arm for the presence of side effects, no other side effects for more than 24 hours, was able to synthesize a high quality biocompatible material.
일차적으로 막 반응기의 사용되는 효소를 조절함으로서 저 부가가치의 물질로부터 고 부가가치의 물질의 생산을 저가로 생산 할 수가 있으며 모두 생체적합적인 물질을 사용함으로서 환경오염을 줄일 수가 있어 앞으로 환경규제에 대하여 쉽게 대처할 수가 있다. 또한 생산된 생물계면활성제는 생체 적합성을 지니고 있어 고 부가가치가 있으며, 또한 합성 계면활성제에 의하여 야기되는 2차 오염에 대한 문제를 해결할 수가 있다.By controlling the enzymes used in the membrane reactor, the production of high value-added materials from low value-added materials can be produced at low cost, and all biocompatible materials can be used to reduce environmental pollution. There is a number. In addition, the produced biosurfactants are biocompatible and have high added value, and can solve the problem of secondary contamination caused by synthetic surfactants.
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KR1019990021267A KR20010001813A (en) | 1999-06-08 | 1999-06-08 | Continuous Process for the Production of Biosurfactant using a Technology of Immobilized Enzyme |
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Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4628030A (en) * | 1983-08-09 | 1986-12-09 | Petrotec Forschungs Ag | Process for the production of rhamnolipids |
JPS63258484A (en) * | 1987-04-15 | 1988-10-25 | Ensuikou Seito Kk | Production of maltooligosaccharide |
JPS63304984A (en) * | 1987-06-08 | 1988-12-13 | Sakai Eng Kk | Use and technology of ester type urethane foam as bioreactor carrier |
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1999
- 1999-06-08 KR KR1019990021267A patent/KR20010001813A/en not_active Application Discontinuation
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4628030A (en) * | 1983-08-09 | 1986-12-09 | Petrotec Forschungs Ag | Process for the production of rhamnolipids |
JPS63258484A (en) * | 1987-04-15 | 1988-10-25 | Ensuikou Seito Kk | Production of maltooligosaccharide |
JPS63304984A (en) * | 1987-06-08 | 1988-12-13 | Sakai Eng Kk | Use and technology of ester type urethane foam as bioreactor carrier |
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