CA1250296A - Perfluorobicyclo compounds - Google Patents
Perfluorobicyclo compoundsInfo
- Publication number
- CA1250296A CA1250296A CA000418692A CA418692A CA1250296A CA 1250296 A CA1250296 A CA 1250296A CA 000418692 A CA000418692 A CA 000418692A CA 418692 A CA418692 A CA 418692A CA 1250296 A CA1250296 A CA 1250296A
- Authority
- CA
- Canada
- Prior art keywords
- ring
- perfluoro
- process according
- methyloctahydroquinolidine
- hydrogen fluoride
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
Abstract
ABSTRACT OF THE DISCLOSURE
A perfluorobicyclo compound of the general formula:
A perfluorobicyclo compound of the general formula:
Description
~ 25711-348 This invention relates to novel perfluorobicyclo compounds useful as oxygen-carrying components for blood substitutes, oxygen-carrying transfusions, and the like.
More specifically, this invention relates to per-fluorobicyclo compound of the general formula /~ /
CF
(CF2)m ~ N B (CF2)n (I) ~ \~
wherein either or both of Ring A and Ring B may optionally be substituted with one or more lower perfluoroalkyl groups and m and n represent 3 or 4.
In the general formula (I), m and n each represent 3 or 4, and thus Ring A and Ring B each represents a five-membered ring or a six-membered ring, and thus a condensed ring is formed from these two.
Examples of the condensed ring formed by Ring A and Ring B include perfluoroderivatives of quinolidine, indolidine, pyrrolidine, etc.
Either or both of Ring A and Ring`B may optionally be substituted with one or more, preferably 1 - 3, lower perfluoroalkyl groups at any position. The perfluoroalkyl group as the substituent is either linear or branched, and ex-amples of these groups include those having 1 - 4 carbon atoms, such as perfluoromethyl group, perfluoroethyl group, perfluoro-:;' $
` . ~ ., n-propyl group, perfluoro-iso-propyl group, perfluoro-n-butyl group, perfluoro-iso-butyl group, perfluoro-sec-bu-tyl group and perfluoro-tert-butyl group, among which those having 1 - 3 carbon atoms are preferred. When two or more such substituents are present, they may be different from each other.
The total carbon number in the compound of the general formula (I) is generally 8 - 12, preferably 9 - 11, more preferably 10.
The present invention also relates to a process for producing the compound of the general formula (I), which pro-cess comprises fluorinating a corresponding perhydrocompound of the general formula:
~ CH ~
(CH2)m A I B (CH2) (II) \~ /
wherein Ring A and Ring B may optionally be substituted by one or more alkyl groups, and m and n each represent 3 or 4.
As the fluorination method, there may be mentioned, for example, known fluorination methods such as direct fluori-nation method, cobalt fluorination method, electrolytic fluori-nation method, etc.
For the production of the compound (I) of this in-vention, the electrolytic fluorination method is preferred, and this may be effected by, ~or example, mixing and dissolving anhydrous hydrogen fluoride and a perhydro compound, as a starting material in an electrolytic cell, and thereafter effecting electrolysis. In said electrolysis, the voltage is generally 3 - 9 V, the anode current density is generally 1 - 300 A~dm2, and the bath temperature is generally 4 - 10C.
~ l~ - 2a -
More specifically, this invention relates to per-fluorobicyclo compound of the general formula /~ /
CF
(CF2)m ~ N B (CF2)n (I) ~ \~
wherein either or both of Ring A and Ring B may optionally be substituted with one or more lower perfluoroalkyl groups and m and n represent 3 or 4.
In the general formula (I), m and n each represent 3 or 4, and thus Ring A and Ring B each represents a five-membered ring or a six-membered ring, and thus a condensed ring is formed from these two.
Examples of the condensed ring formed by Ring A and Ring B include perfluoroderivatives of quinolidine, indolidine, pyrrolidine, etc.
Either or both of Ring A and Ring`B may optionally be substituted with one or more, preferably 1 - 3, lower perfluoroalkyl groups at any position. The perfluoroalkyl group as the substituent is either linear or branched, and ex-amples of these groups include those having 1 - 4 carbon atoms, such as perfluoromethyl group, perfluoroethyl group, perfluoro-:;' $
` . ~ ., n-propyl group, perfluoro-iso-propyl group, perfluoro-n-butyl group, perfluoro-iso-butyl group, perfluoro-sec-bu-tyl group and perfluoro-tert-butyl group, among which those having 1 - 3 carbon atoms are preferred. When two or more such substituents are present, they may be different from each other.
The total carbon number in the compound of the general formula (I) is generally 8 - 12, preferably 9 - 11, more preferably 10.
The present invention also relates to a process for producing the compound of the general formula (I), which pro-cess comprises fluorinating a corresponding perhydrocompound of the general formula:
~ CH ~
(CH2)m A I B (CH2) (II) \~ /
wherein Ring A and Ring B may optionally be substituted by one or more alkyl groups, and m and n each represent 3 or 4.
As the fluorination method, there may be mentioned, for example, known fluorination methods such as direct fluori-nation method, cobalt fluorination method, electrolytic fluori-nation method, etc.
For the production of the compound (I) of this in-vention, the electrolytic fluorination method is preferred, and this may be effected by, ~or example, mixing and dissolving anhydrous hydrogen fluoride and a perhydro compound, as a starting material in an electrolytic cell, and thereafter effecting electrolysis. In said electrolysis, the voltage is generally 3 - 9 V, the anode current density is generally 1 - 300 A~dm2, and the bath temperature is generally 4 - 10C.
~ l~ - 2a -
2~6 1 Since the thus formed compound of the general formula (I) is insoluble in anhydrous hydrofluoric acid, it precipitates in the lower layer of the electrolytic cell.
Separation and purification of the compound (I) from said precipitates may be effected by, for example, adding a liquid mi~ture of an equal volume of an aqueous alkali solution and an amine compound to the recovered precipitates, separating the lowest layer containing the compound (I) (at that time, partially fluorinated compounds are separated into the amine layer), washing it with an appropriate amount of aqueous acetone containing potassium iodide to remove compounds having fluorine atoms bound to nitrogen atoms, and further subjecting to fractional distillation to separate the compound (I).
Since, in addition to the capability of dissolving large quantities of oxygen, the compound of the general formula (I) of this invention is metabilically inert and also is rapidly eliminated from the body, for example, an aqueous emulsion containing 5 - 50% ~w/v), preferably 10 - 40~ (w/v), of the compound (I) may be prepared and advantageously employed as oxygen-carrying components ror blood substitutes, oxygen-carrying transfusions, etc. for warm-blooded animals including humans (e.g. dogs, cats, cows, horses, rats, mice, guinea pigs, etc.).
On preparing the aforesaid emulsion, an ~2~Z96 1 emulsifier such as polymeric nonionic surfactants, phospholipids, etc., are employed in an amount of 1 - 5%
~w~v) each alone or in combination.
As the medium, a physiologically acceptable aqueous solution is employed, and, if necessary, an iso-tonizing amount of an isotonizing agent such as glycerol may be added to isotonize the emuls~Lon, and a plasma extender such as hydroxyethylstarch, dextran etc., may be added to adjust the colloid osmotic pressure of the emulsion.
Thus, an aqueous emulsion may be prepared by homogenizing the various components as those described above to a particle size of 0.05 - 0.3 ~, preferably to 0.2 ~ or less, using e.g. a high-pressure jet-type homogenizer.
The perhydro compounds corresponding to the compound of the general formula (I), as starting materials are substantially known compounds.
The present invention is further illustrated in more detail below with reference to Examples and Reference Examples, but the invention is not limited thereto.
Example 1 As an electrolytic cell, a tank (made of Monel metal) having a capacity of 1.5 Q, containing electrodes made of nickel (purity of 99.6~ or higher) (6 anodes and 7 cathodes) alternately arranged with an electrode gap of 1.7 - 2,0 ~m with an effective anode surface area of 1 10~5 dm2 and ~urther equipped wi-th reflex condenser made of copper above the cell~ was employed.
Into this electrolytic cell was introduced 1.2 Q of anhydrQns hdyrofluoric acid, and impurities (water and sulfuric acid) present in very small amounts were removed by the preliminary electrolysis. Thereafter, 0.85 mole (130 g) of 4-methyloctahydroquinolidine was dissolved in the hydrofluoric acid, and while passing helium gas at a flow rate of 100 ml/min from the lower part of the cell, the electrolysis was effected with an anode current density of 1.0 - 2.0 A/dm2, a voltage of 4.0 6.2 V and a bath temperature of 4 - 10C. The electrolysis was continued for 1051 A-hr until the electro-lytic voltage reached 9.0 V. Anhydrous hydrofluoric acid was additionally introduced 200 ml per 24 hours. The gas generated during the electrolysis was passed through an iron tube packed with sodium fluoride pellets to remove the entrained anhydrous hydrofluoric acid, an then led into a trap coolecl with dry ice-acetone to liquefy and trap the product. On the other hand, the bath liquid in the electrolytic cell separated into two layers, the upper layer containing hydrogen fluoride and the lower layer fluorobicyclo compounds. The lower layer was separated.
The liquid collected by cooling the above generated gas and the lower layer liquid of the electro-lytic cell were combined, 70% KOH aqueous solution and diisobutylamine were added in equal volumes, and refluxing was conducted for 7 days. The perfluoro product was 9~
1 separated uslng a separatory funnel, washed with 70~ (w/v) acetone aqueous solution containing 10~ (w/v) of potassium iodide, then subjected to fractional distil-lation using an apparatus for fractional distillation equipped with a spinning band column to obtain perfluoro-4-methyloctahydroquinolidine (b.p. 145 - 155C/760 mm Hg).
Said compound was confirmed to be the desired compound perfluoro-4-methyloctahydroquinolidine also by the infrared absorption spectrum, F nuclear magnetic resonance 10- spectrum, and mass spectrum.
Examples 2 - 101 Perfluorobicyclo compounds corresponding to perhydro compounds used as starting materials were obtained:by the procedures similar to those in Example 1.
These are sammarized in Table 1.
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Separation and purification of the compound (I) from said precipitates may be effected by, for example, adding a liquid mi~ture of an equal volume of an aqueous alkali solution and an amine compound to the recovered precipitates, separating the lowest layer containing the compound (I) (at that time, partially fluorinated compounds are separated into the amine layer), washing it with an appropriate amount of aqueous acetone containing potassium iodide to remove compounds having fluorine atoms bound to nitrogen atoms, and further subjecting to fractional distillation to separate the compound (I).
Since, in addition to the capability of dissolving large quantities of oxygen, the compound of the general formula (I) of this invention is metabilically inert and also is rapidly eliminated from the body, for example, an aqueous emulsion containing 5 - 50% ~w/v), preferably 10 - 40~ (w/v), of the compound (I) may be prepared and advantageously employed as oxygen-carrying components ror blood substitutes, oxygen-carrying transfusions, etc. for warm-blooded animals including humans (e.g. dogs, cats, cows, horses, rats, mice, guinea pigs, etc.).
On preparing the aforesaid emulsion, an ~2~Z96 1 emulsifier such as polymeric nonionic surfactants, phospholipids, etc., are employed in an amount of 1 - 5%
~w~v) each alone or in combination.
As the medium, a physiologically acceptable aqueous solution is employed, and, if necessary, an iso-tonizing amount of an isotonizing agent such as glycerol may be added to isotonize the emuls~Lon, and a plasma extender such as hydroxyethylstarch, dextran etc., may be added to adjust the colloid osmotic pressure of the emulsion.
Thus, an aqueous emulsion may be prepared by homogenizing the various components as those described above to a particle size of 0.05 - 0.3 ~, preferably to 0.2 ~ or less, using e.g. a high-pressure jet-type homogenizer.
The perhydro compounds corresponding to the compound of the general formula (I), as starting materials are substantially known compounds.
The present invention is further illustrated in more detail below with reference to Examples and Reference Examples, but the invention is not limited thereto.
Example 1 As an electrolytic cell, a tank (made of Monel metal) having a capacity of 1.5 Q, containing electrodes made of nickel (purity of 99.6~ or higher) (6 anodes and 7 cathodes) alternately arranged with an electrode gap of 1.7 - 2,0 ~m with an effective anode surface area of 1 10~5 dm2 and ~urther equipped wi-th reflex condenser made of copper above the cell~ was employed.
Into this electrolytic cell was introduced 1.2 Q of anhydrQns hdyrofluoric acid, and impurities (water and sulfuric acid) present in very small amounts were removed by the preliminary electrolysis. Thereafter, 0.85 mole (130 g) of 4-methyloctahydroquinolidine was dissolved in the hydrofluoric acid, and while passing helium gas at a flow rate of 100 ml/min from the lower part of the cell, the electrolysis was effected with an anode current density of 1.0 - 2.0 A/dm2, a voltage of 4.0 6.2 V and a bath temperature of 4 - 10C. The electrolysis was continued for 1051 A-hr until the electro-lytic voltage reached 9.0 V. Anhydrous hydrofluoric acid was additionally introduced 200 ml per 24 hours. The gas generated during the electrolysis was passed through an iron tube packed with sodium fluoride pellets to remove the entrained anhydrous hydrofluoric acid, an then led into a trap coolecl with dry ice-acetone to liquefy and trap the product. On the other hand, the bath liquid in the electrolytic cell separated into two layers, the upper layer containing hydrogen fluoride and the lower layer fluorobicyclo compounds. The lower layer was separated.
The liquid collected by cooling the above generated gas and the lower layer liquid of the electro-lytic cell were combined, 70% KOH aqueous solution and diisobutylamine were added in equal volumes, and refluxing was conducted for 7 days. The perfluoro product was 9~
1 separated uslng a separatory funnel, washed with 70~ (w/v) acetone aqueous solution containing 10~ (w/v) of potassium iodide, then subjected to fractional distil-lation using an apparatus for fractional distillation equipped with a spinning band column to obtain perfluoro-4-methyloctahydroquinolidine (b.p. 145 - 155C/760 mm Hg).
Said compound was confirmed to be the desired compound perfluoro-4-methyloctahydroquinolidine also by the infrared absorption spectrum, F nuclear magnetic resonance 10- spectrum, and mass spectrum.
Examples 2 - 101 Perfluorobicyclo compounds corresponding to perhydro compounds used as starting materials were obtained:by the procedures similar to those in Example 1.
These are sammarized in Table 1.
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)29~i 1 Reference Example 1 400 g of Vitelline phospholipid was added to 8.5 Q of lactic acid added Ringer's solution, and stirred by a mixer to prepare a coarse emulsion, then 2.5 kg of perfluoro-4-methyloctahydroquinolidine was added thereto and stirred vigorously again by the mixer to prepare a coarse emulsion. This coarse emulsion was placed in a liquid tank of a jet emulsifier (manufactured by Manton-Gaulin Co.) and circulated while maintaining the liquidtemperature at 50~ 5C to effect emulsification.
The concentration of perfluoro-4-methyloctahydro-quinolidine in the obtained emulsion was 27.3% (w/v).
The particle diameter as measured by the centrifugal sedimentation method was 0.05 - 0.25 ~. This emulsion was allotted into vials for injection, stoppered and thermally sterilized in a rotary sterilizer, but there was no significant increase in the particle diameter observed.
Reference Example 2 An emulsion was obtained by procedures similar to those in Reference Example 1 except that perfluoro-4-methyloctahydroquinolidine was replaced by perpluoro-
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)29~i 1 Reference Example 1 400 g of Vitelline phospholipid was added to 8.5 Q of lactic acid added Ringer's solution, and stirred by a mixer to prepare a coarse emulsion, then 2.5 kg of perfluoro-4-methyloctahydroquinolidine was added thereto and stirred vigorously again by the mixer to prepare a coarse emulsion. This coarse emulsion was placed in a liquid tank of a jet emulsifier (manufactured by Manton-Gaulin Co.) and circulated while maintaining the liquidtemperature at 50~ 5C to effect emulsification.
The concentration of perfluoro-4-methyloctahydro-quinolidine in the obtained emulsion was 27.3% (w/v).
The particle diameter as measured by the centrifugal sedimentation method was 0.05 - 0.25 ~. This emulsion was allotted into vials for injection, stoppered and thermally sterilized in a rotary sterilizer, but there was no significant increase in the particle diameter observed.
Reference Example 2 An emulsion was obtained by procedures similar to those in Reference Example 1 except that perfluoro-4-methyloctahydroquinolidine was replaced by perpluoro-
4-ethyloctahydroquinolidine. The particle diameter of the thus obtained emulsion was 0Ø5 - 0.25 ~.
~2~i~)296 1 Experimental Example 1 Stability of Emulsions.
Water was added to 20 g of each perfluoro-bicyclo compound selected in the present invention and 4 g of vitelline phospholipid to make the total volume 200 ml, and emulsification was effected using a Manton- Gaulin emulsifier as used above under nitrogen stream at 200 - 600 kg/cm2 while maintaining the liquid temperature at 40 - 45C. Each obtained emulsion was filtered through a 0.65 ~ membrane filter, allotted into 20 ml-capacity vials, and, after replacing the atmosphereby nitrogen gas, thermally treated at 100C for 30 minutes, followed by storing at 4C of room temperature to examine the stability. The particle diameter of the emulsion was measured by the centrifugal sedimentation method by Yokoyama et al. [Chem. Pharm. Bull. 22 (12) 2966 (1974)], and from the obtained data, the average particle diameter distribution was calculated using a microcomputer.
Thus, the particle diameter distributions of each perfluoro-carbon emulsion before and after heating, and after heating and storing at 4C and room temperature (15 - 28C) are ~hown in Tables 2 and 3. As is evident from the results, the emulsions according to the present invention are very stable against heating and the influence on the average particle diameter due to heating was not observed at all. Further, when stored at 4C after heating, there was no increase in the average particle diameter observed even after-5 months.
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1 ExperimentalExample 2 Acute Toxicity Test.
The acute toxicity test on the preparations of the present invention was carried out using the preparations of the present invention shown in Table 4 which had been physiologically isotonized. The test animals used were Wister-strain male rats (weighing 100 - 120 g). The emulsion was intravenously admini-stered and the animals were observed for one week after the administration.
The results are such that with either emulsion containing perfluoro-4-methyloctahydroquinolidine or perfluoro-4-ethyloctahydroquinolidine, there was no death case at 100 ml/kg-body weight and thus their toxicity are very small.
~Z~2~36 Table 4 Composition % t'w~v) _ Oil Perfluorobicyclo Compound 30 Component . _ (9 vol) Emulsify-ing Agent Vitelline Phospholipid 4.0 - -~ ..
~aCl 6.00 NaHCO3 2.1 ~Cl 0.336 Electro- MgC12 6~2O 0.427 lyte CaC12~2H2O 0.356 D-Glucose 1.802 , . I
pH 8.0 1 Experimental Example 3 Distribution of Perfluoro-compound in Organs.
Using Wister-strain male rats weighing 120 -130 g, the emulsion prepared in Reference ExamplP 1 was adminis~ered into the tail vein [at 4 g/kg as perfluoro-4-methyloctahydroquinolidine], and for a period of 3 months after the administration, the content of said compound in the liver, spleen and fat tissues due to uptake were measured by means of gas chromatography.
The content of perfluoro-4-methyloctahydro-~Z~g~Z96 1 quinolidine uptake in each organ 1, 2 and 4 weeks and 3 months after the administration are shown in Table
~2~i~)296 1 Experimental Example 1 Stability of Emulsions.
Water was added to 20 g of each perfluoro-bicyclo compound selected in the present invention and 4 g of vitelline phospholipid to make the total volume 200 ml, and emulsification was effected using a Manton- Gaulin emulsifier as used above under nitrogen stream at 200 - 600 kg/cm2 while maintaining the liquid temperature at 40 - 45C. Each obtained emulsion was filtered through a 0.65 ~ membrane filter, allotted into 20 ml-capacity vials, and, after replacing the atmosphereby nitrogen gas, thermally treated at 100C for 30 minutes, followed by storing at 4C of room temperature to examine the stability. The particle diameter of the emulsion was measured by the centrifugal sedimentation method by Yokoyama et al. [Chem. Pharm. Bull. 22 (12) 2966 (1974)], and from the obtained data, the average particle diameter distribution was calculated using a microcomputer.
Thus, the particle diameter distributions of each perfluoro-carbon emulsion before and after heating, and after heating and storing at 4C and room temperature (15 - 28C) are ~hown in Tables 2 and 3. As is evident from the results, the emulsions according to the present invention are very stable against heating and the influence on the average particle diameter due to heating was not observed at all. Further, when stored at 4C after heating, there was no increase in the average particle diameter observed even after-5 months.
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1 ExperimentalExample 2 Acute Toxicity Test.
The acute toxicity test on the preparations of the present invention was carried out using the preparations of the present invention shown in Table 4 which had been physiologically isotonized. The test animals used were Wister-strain male rats (weighing 100 - 120 g). The emulsion was intravenously admini-stered and the animals were observed for one week after the administration.
The results are such that with either emulsion containing perfluoro-4-methyloctahydroquinolidine or perfluoro-4-ethyloctahydroquinolidine, there was no death case at 100 ml/kg-body weight and thus their toxicity are very small.
~Z~2~36 Table 4 Composition % t'w~v) _ Oil Perfluorobicyclo Compound 30 Component . _ (9 vol) Emulsify-ing Agent Vitelline Phospholipid 4.0 - -~ ..
~aCl 6.00 NaHCO3 2.1 ~Cl 0.336 Electro- MgC12 6~2O 0.427 lyte CaC12~2H2O 0.356 D-Glucose 1.802 , . I
pH 8.0 1 Experimental Example 3 Distribution of Perfluoro-compound in Organs.
Using Wister-strain male rats weighing 120 -130 g, the emulsion prepared in Reference ExamplP 1 was adminis~ered into the tail vein [at 4 g/kg as perfluoro-4-methyloctahydroquinolidine], and for a period of 3 months after the administration, the content of said compound in the liver, spleen and fat tissues due to uptake were measured by means of gas chromatography.
The content of perfluoro-4-methyloctahydro-~Z~g~Z96 1 quinolidine uptake in each organ 1, 2 and 4 weeks and 3 months after the administration are shown in Table
5. The compound was taken up in greater amounts by the reticulo-endothelial organs shortly after the admini stration, but soon disappeared rapidly. There was no evidence o~ adverse influence on the liver or spleen organ.
As a result, the half-life of perfluoro-4-methyloc~ahydroquinolidine was calculated to be 7.33 days.
Table 5 . .__ _ . . . ._ Time after the Residual Rate of Organ administration perfluorobicyclo compound, ~
_ 1 Week 19.~2 2 Weeks 8.66 Liver 4 Weeks 1.88 3 Months 0.30 . .... _ 1 Week 11.61 2 Weeks 9.33 Spleen Weeks 2.45 3 Months 0.09 1 Experimental Example 4 Anatominal Remarks.
Wister-strain male rats weighing 120 - 130 g were administered with 4 g/kg of the perfluorobicyclo-compound emulsion prepared in Reference Example 1 or 2, and the dissected organs were observed for a period of 3 montAs after the administration, and further the organs (liver and sple~n~ were weighed, to determine the weight relatige to the body weight.
One, 2 and 4 weeks and 3 months after the administration of the emulsion~ the important organs, i.e. the lung, liver and spleen were observed, to find no evidence of the influence on the organs by either said compound because of their rapid elimination.
As a result, the half-life of perfluoro-4-methyloc~ahydroquinolidine was calculated to be 7.33 days.
Table 5 . .__ _ . . . ._ Time after the Residual Rate of Organ administration perfluorobicyclo compound, ~
_ 1 Week 19.~2 2 Weeks 8.66 Liver 4 Weeks 1.88 3 Months 0.30 . .... _ 1 Week 11.61 2 Weeks 9.33 Spleen Weeks 2.45 3 Months 0.09 1 Experimental Example 4 Anatominal Remarks.
Wister-strain male rats weighing 120 - 130 g were administered with 4 g/kg of the perfluorobicyclo-compound emulsion prepared in Reference Example 1 or 2, and the dissected organs were observed for a period of 3 montAs after the administration, and further the organs (liver and sple~n~ were weighed, to determine the weight relatige to the body weight.
One, 2 and 4 weeks and 3 months after the administration of the emulsion~ the important organs, i.e. the lung, liver and spleen were observed, to find no evidence of the influence on the organs by either said compound because of their rapid elimination.
Claims (25)
PROPERTY OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:
1. A perfluorobicyclo compound of the general formula:
(I) wherein either or both of Ring A and Ring B may optionally be substituted with one or more lower perfluoroalkyl groups and m and n each represent 3 or 4.
(I) wherein either or both of Ring A and Ring B may optionally be substituted with one or more lower perfluoroalkyl groups and m and n each represent 3 or 4.
2. Perfluoro-4-methyloctahydroquinolidine.
3. Perfluoro-2-methyloctahydroquinolidine.
4. Perfluoro-1-methyloctahydroquinolidine.
5. Perfluoro-9a-methyloctahydroquinolidine.
6. Perfluoro-4-ethyloctahydroquinolidine.
7. A process for producing the perfluorobicyclo com-pound of formula as defined in claim 1, which process com-prises:
fluorinating a corresponding perhydrocompound of the general formula:
(II) wherein Ring A and Ring B may optionally be substituted by one or more alkyl groups, and m and n each represent 3 or 4.
fluorinating a corresponding perhydrocompound of the general formula:
(II) wherein Ring A and Ring B may optionally be substituted by one or more alkyl groups, and m and n each represent 3 or 4.
8. A process according to claim 7, wherein the total carbon number of the starting material in 8 to 12.
9. A process according to claim 7, wherein the total carbon number of the starting material is 9 to 11.
10. A process according to claim 7, wherein the total carbon number of the starting material is 10.
11. A process according to claim 7, wherein in the starting material each of Ring A and Ring B is unsubstituted or sub-stituted by 1 to 3 alkyl groups having 1 to 3 carbon atoms.
12. A process according to claim 8, wherein in the starting material each of Ring A and Ring B is unsubstituted or substituted by 1 to 2 alkyl groups having 1 to 2 carbon atoms.
13. A process according to claim 7, 8 or 9 wherein the fluorination is carried out by an electrolytic fluori-nation method using anhydrous hydrogen fluoride.
14. A process according to claim 10, 11 or 12 wherein the fluorination is carried out by an electrolytic fluori-nation method using anhydrous hydrogen fluoride.
15. A process according to claim 7, wherein in the starting material both m and n are 4 and either Ring A or Ring B is substituted by a methyl or ethyl group.
16. A process for producing perfluoro-4-methylocta-hydroquinolidine, which process comprises fluorinating 4-methyloctahydroquinolidine.
17. A process according to claim 16, wherein the fluori-nation is carried out by an electrolytic fluorination method using anhydrous hydrogen fluoride.
18. A process for producing perfluoro-2-methylocta-hydroquinolidine, which process comprises fluorinating 2-methyloctahydroquinolidine.
19. A process according to claim 18, wherein the fluori-nation is carried out by an electrolytic fluorination method using anhydrous hydrogen fluoride.
20. A process for producing perfluoro-1-methylocta-hydroquinolidine, which process comprises fluorinating 1-methyloctahydroquinolidine.
21. A process according to claim 20, wherein the fluori-nation is carried out by an electrolytic fluorination method using anhydrous hydrogen fluoride.
22. A process for producing perfluoro-9a-methylocta-hydroquinolidine, which process comprises fluorinating 9a-methyloctahydroquinolidine.
23. A process according to claim 22, wherein the fluorination is carried out by an electrolytic fluorination method using anhydrous hydrogen fluoride.
24. A process for producing perfluoro-4-ethylocta-hydroquinolidine, which process comprises fluorinating 4-ethyloctahydroquinolidine.
25. A process according to claim 24, wherein the fluorination is carried out by an electrolytic fluorination method using anhydrous hydrogen fluoride.
Priority Applications (1)
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CA000418692A CA1250296A (en) | 1982-12-29 | 1982-12-29 | Perfluorobicyclo compounds |
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CA000418692A CA1250296A (en) | 1982-12-29 | 1982-12-29 | Perfluorobicyclo compounds |
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CA1250296A true CA1250296A (en) | 1989-02-21 |
Family
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US5236469A (en) * | 1990-10-26 | 1993-08-17 | Weyerhaeuser Company | Oxygenated analogs of botanic seed |
US5427593A (en) * | 1990-10-26 | 1995-06-27 | Weyerhaeuser Company | Analogs of botanic seed |
US6119395A (en) * | 1997-02-03 | 2000-09-19 | Weyerhaeuser Company | End seals for manufacturing seed |
US7131234B2 (en) | 2003-11-25 | 2006-11-07 | Weyerhaeuser Co. | Combination end seal and restraint |
US7168205B2 (en) | 2001-12-05 | 2007-01-30 | Weyerhaeuser Co. | Seed coat for manufactured seeds |
US7228658B2 (en) | 2003-08-27 | 2007-06-12 | Weyerhaeuser Company | Method of attaching an end seal to manufactured seeds |
US7356965B2 (en) | 2003-12-11 | 2008-04-15 | Weyerhaeuser Co. | Multi-embryo manufactured seed |
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US7555865B2 (en) | 2003-11-25 | 2009-07-07 | Weyerhaeuser Nr Company | Method and system of manufacturing artificial seed coats |
US7568309B2 (en) | 2004-06-30 | 2009-08-04 | Weyerhaeuser Nr Company | Method and system for producing manufactured seeds |
US7591287B2 (en) | 2003-12-18 | 2009-09-22 | Weyerhaeuser Nr Company | System and method for filling a seedcoat with a liquid to a selected level |
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US5427593A (en) * | 1990-10-26 | 1995-06-27 | Weyerhaeuser Company | Analogs of botanic seed |
US5451241A (en) * | 1990-10-26 | 1995-09-19 | Weyerhaeuser Company | Oxygenated analogs of botanic seed |
US5486218A (en) * | 1990-10-26 | 1996-01-23 | Weyerhaeuser Company | Oxygenated analogs of botanic seed |
US5564224A (en) * | 1990-10-26 | 1996-10-15 | Weyerhaeuser Company | Plant germinants produced from analogs of botanic seed |
US5666762A (en) * | 1990-10-26 | 1997-09-16 | Weyerhaeuser Company | Respiration-limited manufactured seed |
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US5236469A (en) * | 1990-10-26 | 1993-08-17 | Weyerhaeuser Company | Oxygenated analogs of botanic seed |
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US7603807B2 (en) | 2003-11-26 | 2009-10-20 | Weyerhaeuser Nr Company | Vacuum pick-up device with mechanically assisted release |
US7356965B2 (en) | 2003-12-11 | 2008-04-15 | Weyerhaeuser Co. | Multi-embryo manufactured seed |
US7591287B2 (en) | 2003-12-18 | 2009-09-22 | Weyerhaeuser Nr Company | System and method for filling a seedcoat with a liquid to a selected level |
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