CN104907100A - Method for preparing catalyst composition for producing isolongifolene - Google Patents
Method for preparing catalyst composition for producing isolongifolene Download PDFInfo
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- CN104907100A CN104907100A CN201510286180.9A CN201510286180A CN104907100A CN 104907100 A CN104907100 A CN 104907100A CN 201510286180 A CN201510286180 A CN 201510286180A CN 104907100 A CN104907100 A CN 104907100A
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- isolonglifolene
- concentrated sulfuric
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Abstract
The invention discloses a method for preparing a catalyst composition for producing isolongifolene and belongs to the technical field of preparation of forestry chemical products. The method comprises the steps: firstly, putting zirconia and silica into 98% concentrated sulfuric acid for acidifying for 1 hour; then, drying at the temperature of 50-55 DEG C, and then, calcining for 4 hours at the temperature of 550-600 DEG C; and finally, uniformly mixing the calcined material with cation exchange resin while the calcined material is hot, thereby preparing the catalyst composition. By applying the catalyst composition prepared by the method to the production of isolongifolene, the yield of isolongifolene can be effectively increased, and thus the production cost of isolongifolene is reduced.
Description
Technical field
The invention belongs to silvichemical preparing technical field, particularly relate to a kind of preparation method of isolonglifolene production carbon monoxide-olefin polymeric.
Background technology
Isolonglifolene is through catalytic isomerization products therefrom by the longifolene in heavy turpentine, the same with longifolene is also a kind of sesquiterpene, be a kind of novel raw material in synthetic perfume industry, the spices such as isolongitolanone, Isolongifolenone, isolonglifolene alcohol, isolongifolenyl acetate, amborol can be synthesized; Itself there is banksia rose fragrance, with being widely used in modern synthetic perfume industry.
At present, the yield of the isolonglifolene obtained according to conventional synthetic method is not very high always, and this makes the production cost of isolonglifolene remain high always.
Summary of the invention
The technical problem that the present invention solves is to provide a kind of preparation method of isolonglifolene production carbon monoxide-olefin polymeric, by carbon monoxide-olefin polymeric obtained for the method for the production of isolonglifolene, can effectively improve its yield, thus reduce its production cost.
In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
Raw material is made up of the component of following weight portion:
30 parts ~ 45 parts cationic ion-exchange resins, 30 parts ~ 35 parts zirconias, 10 parts ~ 15 parts silica and 50 parts ~ 60 part 98% concentrated sulfuric acids;
Its preparation method comprises the following steps:
A, by above-mentioned parts by weight, zirconia, silica are put into 98% concentrated sulfuric acid acidifying 1 hour;
B, at 50 DEG C ~ 55 DEG C, carry out drying by under the zirconia after step A acidification, silica, and then carry out calcining 4 hours at 550 DEG C ~ 600 DEG C;
C, the zirconia after step B calcination processing, silica are mixed with cationic ion-exchange resin while hot obtained.
In technique scheme, technical scheme is more specifically: 30 parts of cationic ion-exchange resins, 35 parts of zirconias, 12 parts of silica and 50 part of 98% concentrated sulfuric acid;
Further, 45 parts of cationic ion-exchange resins, 32 parts of zirconias, 10 parts of silica and 55 part of 98% concentrated sulfuric acid.
Further, 40 parts of cationic ion-exchange resins, 30 parts of zirconias, 15 parts of silica and 60 part of 98% concentrated sulfuric acid.
Owing to adopting technique scheme, the beneficial effect that the present invention obtains is:
By inventive catalyst composition for the production of isolonglifolene, can effectively improve its yield, thus reduce its production cost.
Detailed description of the invention
Below in conjunction with specific embodiment, the invention will be further described, and protection scope of the present invention is not only confined to following examples.
Embodiment 1
The raw material of this isolonglifolene production carbon monoxide-olefin polymeric is composed of the following components:
3000g cationic ion-exchange resin, 3500g zirconia, 1200g silica and the 5000g98% concentrated sulfuric acid;
Its preparation method comprises the following steps:
A, zirconia, silica are put into 98% concentrated sulfuric acid acidifying 1 hour;
B, at 50 DEG C ~ 55 DEG C, carry out drying by under the zirconia after step A acidification, silica, and then carry out calcining 4 hours at 550 DEG C ~ 600 DEG C;
C, the zirconia after step B calcination processing, silica are mixed with cationic ion-exchange resin while hot obtained.
By carbon monoxide-olefin polymeric obtained for the present embodiment for the production of isolonglifolene, the yield of its isolonglifolene is up to 92%.
Embodiment 2
The raw material of this isolonglifolene production carbon monoxide-olefin polymeric is composed of the following components:
4500g cationic ion-exchange resin, 3200g zirconia, 1000g silica and the 5500g98% concentrated sulfuric acid;
Its preparation method comprises the following steps:
A, zirconia, silica are put into 98% concentrated sulfuric acid acidifying 1 hour;
B, at 50 DEG C ~ 55 DEG C, carry out drying by under the zirconia after step A acidification, silica, and then carry out calcining 4 hours at 550 DEG C ~ 600 DEG C;
C, the zirconia after step B calcination processing, silica are mixed with cationic ion-exchange resin while hot obtained.
By carbon monoxide-olefin polymeric obtained for the present embodiment for the production of isolonglifolene, the yield of its isolonglifolene is up to 91%.
Embodiment 3
The raw material of this isolonglifolene production carbon monoxide-olefin polymeric is composed of the following components:
4000g cationic ion-exchange resin, 3000g zirconia, 1500g silica and the 6000g98% concentrated sulfuric acid;
Its preparation method comprises the following steps:
A, zirconia, silica are put into 98% concentrated sulfuric acid acidifying 1 hour;
B, at 50 DEG C ~ 55 DEG C, carry out drying by under the zirconia after step A acidification, silica, and then carry out calcining 4 hours at 550 DEG C ~ 600 DEG C;
C, the zirconia after step B calcination processing, silica are mixed with cationic ion-exchange resin while hot obtained.
By carbon monoxide-olefin polymeric obtained for the present embodiment for the production of isolonglifolene, the yield of its isolonglifolene is up to 91.5%.
Claims (4)
1. a preparation method for isolonglifolene production carbon monoxide-olefin polymeric, is characterized in that:
Raw material is made up of the component of following weight portion:
30 parts ~ 45 parts cationic ion-exchange resins, 30 parts ~ 35 parts zirconias, 10 parts ~ 15 parts silica and 50 parts ~ 60 part 98% concentrated sulfuric acids;
Its preparation method comprises the following steps:
A, by above-mentioned parts by weight, zirconia, silica are put into 98% concentrated sulfuric acid acidifying 1 hour;
B, at 50 DEG C ~ 55 DEG C, carry out drying by under the zirconia after step A acidification, silica, and then carry out calcining 4 hours at 550 DEG C ~ 600 DEG C;
C, the zirconia after step B calcination processing, silica are mixed with cationic ion-exchange resin while hot obtained.
2. the preparation method of isolonglifolene production carbon monoxide-olefin polymeric according to claim 1, is characterized in that: 30 parts of cationic ion-exchange resins, 35 parts of zirconias, 12 parts of silica and 50 part of 98% concentrated sulfuric acid.
3. the preparation method of isolonglifolene production carbon monoxide-olefin polymeric according to claim 1, is characterized in that: 45 parts of cationic ion-exchange resins, 32 parts of zirconias, 10 parts of silica and 55 part of 98% concentrated sulfuric acid.
4. the preparation method of isolonglifolene production carbon monoxide-olefin polymeric according to claim 1, is characterized in that: 40 parts of cationic ion-exchange resins, 30 parts of zirconias, 15 parts of silica and 60 part of 98% concentrated sulfuric acid.
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CN201510286180.9A CN104907100A (en) | 2015-05-29 | 2015-05-29 | Method for preparing catalyst composition for producing isolongifolene |
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CN201510286180.9A CN104907100A (en) | 2015-05-29 | 2015-05-29 | Method for preparing catalyst composition for producing isolongifolene |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109749017A (en) * | 2017-11-03 | 2019-05-14 | 宁波激智科技股份有限公司 | A kind of composition and a kind of brightness enhancement film |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1849280A (en) * | 2003-05-30 | 2006-10-18 | 科学与工业研究委员会 | Catalytic process for the preparation of isolongifolene |
CN104151128A (en) * | 2014-08-21 | 2014-11-19 | 梧州市嘉盈树胶有限公司 | Preparation method of isolongifolene |
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2015
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Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1849280A (en) * | 2003-05-30 | 2006-10-18 | 科学与工业研究委员会 | Catalytic process for the preparation of isolongifolene |
CN104151128A (en) * | 2014-08-21 | 2014-11-19 | 梧州市嘉盈树胶有限公司 | Preparation method of isolongifolene |
Non-Patent Citations (1)
Title |
---|
周国斌: "固体超强酸催化萜烯化合物异构化反应的研究", 《中国优秀博硕士学位论文全文数据库(硕士),工程科技I辑》 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109749017A (en) * | 2017-11-03 | 2019-05-14 | 宁波激智科技股份有限公司 | A kind of composition and a kind of brightness enhancement film |
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Application publication date: 20150916 |
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