SU104224A1 - The method of producing polychloride terpenes - Google Patents
The method of producing polychloride terpenesInfo
- Publication number
- SU104224A1 SU104224A1 SU453234A SU453234A SU104224A1 SU 104224 A1 SU104224 A1 SU 104224A1 SU 453234 A SU453234 A SU 453234A SU 453234 A SU453234 A SU 453234A SU 104224 A1 SU104224 A1 SU 104224A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- polychloride
- producing
- terpenes
- chlorination
- chlorine
- Prior art date
Links
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
Дл иодучеии высоких инсСктпц; щых свойств полихлоридов терпено необходимо , чтобы содержание хлора в этих продуктах было выше . Такое глубокое хлорирование териенов св зало со значительной нродолжительиостыо процесса, так как нкертиость хлортериенов возрастает по мере их охла;кдени .For high-school education; The properties of polychloride should be terpented so that the chlorine content of these products is higher. Such deep chlorination of the terienes is due to a significant inhibition of the process, since the inersency of the chloroterienes increases as they cool down;
Дл ускормш нроирсса используют фотохимический способ хлорировани , который требует лрлмепенид растворител и исключает возмолаюсть иримеиени Koxi.H i4c-c.i;i)ro иеремевшвани .For accelerators, a photochemical chlorination method is used, which requires a solvent solvent and eliminates the possibility of Koxi.H i4c-c.i; i) ro and iremote.
Согласно изобретению ускорение ироцесса хлорировани териенов достигаетс иримеиением небольших количеств ииициатора-азодинитрила аиизо масл иой кислоты. Хлориро-вание проводитс в темноте с получением иолихлортерпеиов любой степсии хлорировани .According to the invention, the acceleration of the chlorination process of the terienes is achieved by irimetion of small amounts of the initiator, azodinitrile and iso-butyric acid. Chlorination is carried out in the dark to produce iolichlorterpei of any steppe of chlorination.
11 р и м ) 1. а-упи:енов;Я фракци сккпида.ра, содержап1;а Э. п-пинрна, хлорируетс при 50-110° до содержани хлора в продукте 35-40 /о газообразным хлором в течеиИе 5-10 часов.11 p and m) 1. a-upi: enov; I skkpida.ra fraction, content 1; and E. n-pinrna, is chlorinated at 50-110 ° to the chlorine content in the product 35-40 / o with chlorine gas in leaks 10 hours.
Затем 11 реакционную массу добавл ют ид-О. ; ;;;и ь-изо5утирош1трила от веса готового продукта и хлорируют до содержани хлора . Общее врем хлорировани GO чагов.Then 11 the reaction mass is added id-O. ; ;;; and ь-iso-thuish-triple based on the weight of the finished product and is chlorinated to contain chlorine. The total chlorination time of the GO chagov.
Ирин.ер 2. ..и.ииеиова фракци скипидара гид)):)хл)рируетс газообразным хлористым иодородом и далее хлорируетс ТПК л:с, как s примере 1 до содержани хлора п течение 60 часов.Irin.er 2. ..and. Iiei fraction of turpentine guide)) :) chl) is radiated with gaseous iodine chloride and further chlorinated by TLC l: s, as in example 1, up to a chlorine content for 60 hours.
Пример ,. ЕамфСИ хлорируетс таккг , .;;м- (вп (пример 1) до содержани 08о/о хлора в течеийе 60 часов.Example EAMPSI is chlorinated with a Ccg,. ;; m- (BN (Example 1) to a chlorine content of 08 ° / o for 60 hours.
1 р е дм е т j ;i обре т е н и 1 remitt; j
Способ получени нолихлоридов тердеUiii livn-si :i iniii;;; ; : rsiviieHiii или их гидрохлпридов в темиоте. в пр ;1;сутствии к,ата:аи:1т()ра, о т л и ч а ю щ и И с тем, что, с целые ускорени процесса хлори1 1 )-;,:мг iii::.::Mi: T провод т в присутствии катализатора - азадииитрила динзимасл иой кислоты, вз том в количестве не 0. от нес готового продукта.The method of producing tertiary nolichlorides is Uiii livn-si: i iniii ;;; ; : rsiviieHiii or their hydrochloride hydrochloride in the Theme. in pr; 1; in the absence of, ata: ai: 1t () pa, o tl and h a y i and so that, with the whole acceleration of the chlorine process 1) -,: mg iii ::. :: Mi: T is carried out in the presence of a catalyst — azadiiitrile dinisoilic acid, taken in an amount of not 0. from the finished product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU453234A SU104224A1 (en) | 1955-04-04 | 1955-04-04 | The method of producing polychloride terpenes |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU453234A SU104224A1 (en) | 1955-04-04 | 1955-04-04 | The method of producing polychloride terpenes |
Publications (1)
Publication Number | Publication Date |
---|---|
SU104224A1 true SU104224A1 (en) | 1955-11-30 |
Family
ID=48377760
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU453234A SU104224A1 (en) | 1955-04-04 | 1955-04-04 | The method of producing polychloride terpenes |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU104224A1 (en) |
-
1955
- 1955-04-04 SU SU453234A patent/SU104224A1/en active
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