CN1865202A - Piperyene cis and trans isomer separating method - Google Patents
Piperyene cis and trans isomer separating method Download PDFInfo
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- CN1865202A CN1865202A CN 200510025920 CN200510025920A CN1865202A CN 1865202 A CN1865202 A CN 1865202A CN 200510025920 CN200510025920 CN 200510025920 CN 200510025920 A CN200510025920 A CN 200510025920A CN 1865202 A CN1865202 A CN 1865202A
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Abstract
This invention discloses a chicken gel food and the method for making the same. The procedures comprise: mix the minced chicken breast with salt solution, and send to the colloidal mill, after degassing, add in compound microcosmic salt, extract at 0-6Deg C for 24-58 hours, filtrate and separate the supernatant by centrifuging, add kara gel and calcium chloride to the supernatant, adjust the pH between 6.0 and 7.5, then heat in the 60-90Deg C water bath for 15-45min, cool to the room temperature and obtain the chicken gel food. This invention enriches the cryogenic chicken food, fills the blank of the market, and is innovative. This invention can promote the finely processing of the chicken product, provide a new way for the finely processing of chicken food, improve the added value, solve the social problem of 'hard chicken sale', and accelerate the domestic animal industry development.
Description
Technical field
The present invention relates to the separation method of a kind of piperyene cis, trans-isomer(ide), particularly the method that adopts extracting rectifying to separate piperyene cis, trans-isomer(ide).
Background technology
M-pentadiene is one of conjugated diene main in the five fractions of petroleum cracked carbon, at industrial polymerization single polymerization monomer and the fine chemical material of being used as usually.It has cis and trans two kinds of isomer, and cis and trans two kinds of isomer ratios between two are generally 1 in the m-pentadiene that is obtained by five fractions of petroleum cracked carbon: between (1.5～3).
Polyreaction for the differential responses condition, two kinds of isomer of m-pentadiene can present different chemical property, can only make the trans-isomer(ide) polymerization as anionic catalyst, Ziegler-Natta catalyst or transition-metal catalyst, cis-isomeride does not participate in reaction; And alfin sodium catalyst and free-radical emulsion polymerization all help the cis-isomeride polymerization.In addition, in fine chemistry industry is synthetic, also there is the situation of having only m-pentadiene list kind isomer to participate in reaction, as when producing methyl tetrahydro phthalic anhydride by m-pentadiene and cis-butenedioic anhydride reaction, generally the process enrichment m-pentadiene of producing with carbon five tripping devices (1,3-pentadiene) is a raw material, in two kinds of isomer of m-pentadiene, have only trans m-pentadiene and cis-butenedioic anhydride to react.When having only single kind m-pentadiene isomer to participate in reaction, another kind of isomer just exists as inert media, this obvious negative influence that brought of giving reaction, as make yield, catalyst efficiency and product purity reduce, and the energy consumption increase etc.Sometimes, the sort of isomer of m-pentadiene of not participating in reaction also is used as refuse and is handled, and this not only causes the waste of resource, returns environmental protection and brings pressure.So, piperyene cis, trans-isomer(ide) to be separated in industrial be of great value.
Yet, can't realize with general rectifying separation owing to piperyene cis, both boiling-point differences of trans-isomer(ide) have only 1.9 ℃.In preparation during reagent, adopt methods such as gel permeation chromatography and liquid chromatography to separate usually, this separation method costs dearly.Also have the report to handle the cis m-pentadiene isomer that m-pentadiene obtains higher degree, yet it is a cost to sacrifice trans m-pentadiene but with maleic anhydride.Patent US3, the isomer of 403,196 report available ammonium chlorides cuprous fractionation by adsorption purification cis transconfigurations, can be the ratio of trans in the m-pentadiene raw material and cis by 2 less than bringing up to 6 to 7.But this method is not to be a kind of separation truly yet, and is because absorption and parsing belong to a kind of astable material exchange process, difficult to realize stable operation in addition.As seen, the separation method of all existing piperyene cis, trans-isomer(ide) does not all have industrial application value.
Summary of the invention
The invention provides the separation method of a kind of piperyene cis, trans-isomer(ide), it adopts industrial extraction and distillation technology commonly used, has solved existing similar separation method and has been difficult for realizing this technical problem of industrial applications.
Below be the technical scheme that the present invention solves the problems of the technologies described above:
The separation method of a kind of piperyene cis, trans-isomer(ide), this method comprises following process:
1) the m-pentadiene raw material enters extractive distillation column and carries out extracting rectifying, and extraction agent is that dimethyl formamide, N-Methyl pyrrolidone, acetonitrile or water-content are any in the acetonitrile solution of 5～15wt%.The extractant feed temperature is 20～80 ℃, and the m-pentadiene raw material is 1 with the feed weight ratio of extraction agent: (6～20).Working pressure is 0～0.2MPa, and tower still temperature is 70～250 ℃, and tower top temperature is 40～60 ℃.The cat head material rate of distillating is 40～70%, and reflux ratio is 2～20.Cat head gets trans m-pentadiene, and the tower still gets the material of cis m-pentadiene and extraction agent;
2) above-mentioned tower still material enters rectifying tower and carries out rectifying.Working pressure is 0～0.2MPa, and tower still temperature is 70～180 ℃, and tower top temperature is 38～60 ℃, and reflux ratio is 0.5～5.Cat head gets the cis m-pentadiene, and the tower still gets extraction agent and recycled.
Said process 1 described extractant feed temperature is preferably 30～50 ℃; The m-pentadiene raw material is preferably 1 with the feed weight ratio of extraction agent: (8～16); Working pressure is preferably normal pressure; Tower still temperature is preferably 75～125 ℃, and tower top temperature is preferably 43～48 ℃; It is best with the percentage ratio that is less than or equal to trans m-pentadiene content in the raw material that cat head distillates rate, is generally 50～60%; Reflux ratio is preferably 4～8; Extraction agent is preferably dimethyl formamide.
Said process 2 described working pressures are preferably normal pressure; Tower still temperature is preferably 80～110 ℃, and tower top temperature is preferably 40～44 ℃.
Technical scheme provided by the invention has mainly comprised two steps, wherein step 1 is the most key, the present invention has increased relative volatility between cis and the trans m-pentadiene by having selected the ideal extraction agent, and searched out suitable extracting rectifying operational condition, realized the separation of piperyene cis, trans-isomer(ide) well, the rectifying of the 2nd step is separated cis m-pentadiene product with extraction agent, obtain cis m-pentadiene product, and realize the recycled of extraction agent.Adopt method provided by the invention can obtain higher cis of purity or trans m-pentadiene product at last.
The extractive distillation column that step 1 adopts can be packing tower or sieve-tray tower, and the theoretical plate number of extractive distillation column generally should be advisable with 40～60 theoretical stages more than 30.Certainly higher theoretical plate number can make separating effect desirable more.The rectifying of step 2 is comparatively simple, because the boiling point of the extraction agent that the present invention selects is all apparently higher than the boiling point of m-pentadiene, the theoretical plate number of rectifying tower can select 10～20.
Positive effect of the present invention has been to provide the separation method of a kind of ideal piperyene cis, trans-isomer(ide), and it adopts extraction and distillation technology commonly used, is easy to realize industrial applications, has overcome the defective that prior art exists preferably.
Below will the invention will be further described by specific embodiment.Effect of the present invention is not limited to the data that embodiment shows, extractive distillation column adopts higher theoretical plate number and adopts bigger extraction agent and m-pentadiene material feeding ratio, obviously can obtain better effect.
In an embodiment, cat head distillates rate D/F and is defined as:
Embodiment
The m-pentadiene raw material that each embodiment uses is that its composition is listed as table 1 through the purified five fractions of petroleum cracked carbon:
Table 1.
| Component | Content (wt%) |
| Trans-m-pentadiene | 60.0 |
| Cis-m-pentadiene | 34.5 |
| The above hydro carbons of other C5 and C6 | Surplus |
[embodiment 1～5]
Form as entering an extractive distillation column behind m-pentadiene raw material preheating to 40～50 of table 1 ℃ and carry out extracting rectifying, extractive distillation column is a packing tower, and theoretical plate number is 45.The m-pentadiene raw material enters extractive distillation column with the speed of 400g/h from the 32nd block of column plate, and extraction agent is from the 4th column plate charging.Each embodiment extractive distillation column is operated under normal pressure, and other main extracting rectifying operational condition sees Table 2.
The extracting rectifying column overhead obtains trans m-pentadiene, and product purity sees Table 4.Extracting rectifying Tata still material enters subsequently and carries out rectifying in the rectifying tower, and rectifying tower is a packing tower, and theoretical plate number is 7, and opening for feed is positioned at the 5th block of plate, and each embodiment rectifying tower is operated under normal pressure, and other main distillation operation condition sees Table 3.Rectifying Tata still obtains extraction agent, and extraction agent is sent the extractive distillation column recycled back to, and cat head obtains the cis m-pentadiene, and product purity sees Table 4.
Table 2
| Extraction agent | The extractant feed temperature (℃) | Raw material/extraction agent (weight ratio) | Tower still/tower top temperature (℃) | Reflux ratio | D/F (％) | |
| Embodiment 1 | DMF | 30 | 1/16 | 125/48 | 20 | 60 |
| Embodiment 2 | DMF | 50 | 1/12 | 116/47 | 6 | 45 |
| Embodiment 3 | DMF | 55 | 1/8 | 114/46 | 6 | 50 |
| Embodiment 4 | DMF | 50 | 1/16 | 125/46 | 8 | 40 |
| Embodiment 5 | Acetonitrile solution | 45 | 1/12 | 75/43 | 6 | 49 |
Annotate: DMF is a dimethyl formamide; The water-content of acetonitrile solution is 10wt%.
Table 3.
| Tower still temperature (℃) | Tower top temperature (℃) | Reflux ratio | |
| Embodiment 1 | 100 | 44 | 0.5 |
| Embodiment 2 | 110 | 44 | 2 |
| Embodiment 3 | 100 | 44 | 3 |
| Embodiment 4 | 100 | 44 | 5 |
| Embodiment 5 | 80 | 40 | 4 |
Table 4.
| Trans m-pentadiene product purity (%) | Cis m-pentadiene product purity (%) | |
| Embodiment 1 | 83.5 | 59.7 |
| Embodiment 2 | 87.8 | 65.3 |
| Embodiment 3 | 81.3 | 61.8 |
| Embodiment 4 | 93.9 | 74.3 |
| Embodiment 5 | 80.5 | 60.0 |
Claims (10)
1, the separation method of a kind of piperyene cis, trans-isomer(ide), this method comprises following process:
1) the m-pentadiene raw material enters extractive distillation column and carries out extracting rectifying, extraction agent is a dimethyl formamide, N-Methyl pyrrolidone, acetonitrile or water-content are any in the acetonitrile solution of 5～15wt%, the extractant feed temperature is 20～80 ℃, the m-pentadiene raw material is 1 with the feed weight ratio of extraction agent: (6～20), working pressure is 0～0.2MPa, tower still temperature is 70～250 ℃, tower top temperature is 40～60 ℃, the cat head material rate of distillating is 40～70%, reflux ratio is 2～20, cat head gets trans m-pentadiene, and the tower still gets the material of cis m-pentadiene and extraction agent;
2) above-mentioned tower still material enters rectifying tower and carries out rectifying, and working pressure is 0～0.2MPa, and tower still temperature is 70～180 ℃, and tower top temperature is 38～60 ℃, and reflux ratio is 0.5～5, and cat head gets the cis m-pentadiene, and the tower still gets extraction agent and recycled.
2, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 1 described extractant feed temperature is 30～50 ℃.
3, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that the process 1 described m-pentadiene raw material and the feed weight ratio of extraction agent are 1: (8～16).
4, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 1 described working pressure is a normal pressure.
5, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 1 described tower still temperature is 75～125 ℃, and tower top temperature is 43～48 ℃.
6, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that the process 1 described cat head rate of distillating is 50～60%.
7, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 1 described reflux ratio is 4～8.
8, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 1 described extraction agent is a dimethyl formamide.
9, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 2 described working pressures are normal pressure.
10, the separation method of piperyene cis according to claim 1, trans-isomer(ide) is characterized in that process 2 described tower still temperature are 80～110 ℃, and tower top temperature is 40～44 ℃.
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145523A (en) * | 2013-03-12 | 2013-06-12 | 上海派尔科化工材料有限公司 | Production method of high-purity trans-m-pentadiene |
| CN103204759A (en) * | 2013-03-12 | 2013-07-17 | 上海派尔科化工材料有限公司 | Comprehensive pentadiene utilization method |
| CN115572274A (en) * | 2022-11-11 | 2023-01-06 | 淄博鲁华泓锦新材料集团股份有限公司 | Method for continuously co-producing nadic anhydride and methyl tetrahydrophthalic anhydride by using cracking carbon five as raw material |
-
2005
- 2005-05-18 CN CNB200510025920XA patent/CN100503528C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103145523A (en) * | 2013-03-12 | 2013-06-12 | 上海派尔科化工材料有限公司 | Production method of high-purity trans-m-pentadiene |
| CN103204759A (en) * | 2013-03-12 | 2013-07-17 | 上海派尔科化工材料有限公司 | Comprehensive pentadiene utilization method |
| CN103204759B (en) * | 2013-03-12 | 2015-01-14 | 上海派尔科化工材料有限公司 | Comprehensive pentadiene utilization method |
| CN103145523B (en) * | 2013-03-12 | 2015-03-04 | 上海派尔科化工材料有限公司 | Production method of high-purity trans-m-pentadiene |
| CN115572274A (en) * | 2022-11-11 | 2023-01-06 | 淄博鲁华泓锦新材料集团股份有限公司 | Method for continuously co-producing nadic anhydride and methyl tetrahydrophthalic anhydride by using cracking carbon five as raw material |
| CN115572274B (en) * | 2022-11-11 | 2023-03-17 | 淄博鲁华泓锦新材料集团股份有限公司 | Method for continuously co-producing nadic anhydride and methyl tetrahydrophthalic anhydride by using cracking carbon five as raw material |
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| CN100503528C (en) | 2009-06-24 |
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