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CN103044274B - Method for synthesizing tolterodine tartrate without solvent - Google Patents

Method for synthesizing tolterodine tartrate without solvent Download PDF

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CN103044274B
CN103044274B CN201210527645.1A CN201210527645A CN103044274B CN 103044274 B CN103044274 B CN 103044274B CN 201210527645 A CN201210527645 A CN 201210527645A CN 103044274 B CN103044274 B CN 103044274B
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tolterodine
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organic phase
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CN103044274A (en
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王建军
杨如
肖鸿
江晓漫
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Zhuzhou Bonded Zone Lizhu Synthetic Pharmaceutical Co Ltd
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Zhuzhou Bonded Zone Lizhu Synthetic Pharmaceutical Co Ltd
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Abstract

The invention relates to a novel preparation method for synthesizing tolterodine tartrate. The method does not need to use the solvent and overcomes the defects of complicated aftertreatment, expensive cost and low product purity of a conventional technology, the reaction time is shortened, and industrial mass production requirements are met.

Description

A kind of method of solvent-free synthetic Tolterodine tartrate
Technical field
The present invention relates to pharmacy field, be specifically related to a kind of method of solvent-free synthetic Tolterodine tartrate.
Background technology
Tolterodine tartrate (Tolterodine Tartrate, structural formula 1), chemistry (R)-N by name, N-di-isopropyl-3-(2-hydroxy-5-methyl base phenyl)-3 phenylpropylamine L-(+) tartrates
Structural formula 1 (Tolterodine tartrate)
Tolterodine tartrate is the novel muscarinic receptor antagonist of Pharmacia & Upjohn company of U.S. research and development, can emulatively be combined with m receptor, thereby the combination of block nerves mediator vagusstoff and m receptor, can effectively suppress the contraction of detrusor, thereby alleviate the symptoms such as frequent micturition, urgent urination and urge incontinence, its meta-bolites is stronger to the selectivity of m receptor.1998 first in Switzerland listing, and the symptoms such as the clinical frequent micturition that is mainly used in being caused by overactive bladder, urgent urination and urge incontinence, due to its good curative effect be subject to widespread use compared with little toxic side effect.
In existing technology mainly with the initial reaction such as styracin, phenylacrolein raw material, for example: patent EP0960109A1, US5922914 etc. has reported, utilize identical starting raw material (p-cresol and styracin) first to prepare 3 under sulfuric acid catalysis condition, 4-dihydro-6-4-phenyl-2H-chromen-2-one, rear with reductive agent (LiAlH 4, DIBAL etc.) and 6-methyl 4-phenyl chroman-2-alcohol of reduction, then obtain the tolterodine free alkali of racemization with Diisopropylamine reduction amination under Pd/C exists, split and obtain target product finally by L-(+) tartrate.But the synthesising method reacting condition in above-mentioned report is all very harsh, and reactivity hazard is high, operation easier is large, makes tolterodine be difficult to realize large-scale industrial production.
Patent documentation EP2364966, EP2281801 disclose respectively the synthetic method taking cinnamyl chloride as raw material, but owing to all having used organic solvent toluene, methyl alcohol, ethanol etc. as reaction solvent in two technical schemes, easily there is etherificate and produce byproduct in reaction solvent, makes subsequent disposal very difficult.
Patent documentation WO2007147547 has reported the synthetic method taking cinnamyl chloride as raw material, it first replaces and obtains N with Diisopropylamine, N-diisopropyl benzene allylamine, obtaining the tolterodine of racemization with p-cresol effect, finally split and obtain target compound, the raw materials used cinnamyl chloride price of this technique is higher, and methylsulfonic acid is easy to enter in product in last handling process, cause product purity lower, therefore application is restricted.
Summary of the invention
The technical problem to be solved in the present invention is: overcome the synthetic technique shortcoming of prior art unresolvable tartaric acid tolterodine, provide a kind of route simple, operate simple and easy, product yield is high, meet the new Tolterodine tartrate synthetic route of the large production requirement of industry.
We have proposed a kind of method of novel synthetic Tolterodine tartrate, and concrete scheme route is as follows:
The present invention is synthetic to be comprised:
Step 1: styryl carbinol, thionyl chloride reaction, obtain product cinnamyl chloride;
Step 2: cinnamyl chloride, Diisopropylamine, alkali, iodide reaction, obtain product N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine;
Step 3:N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine, p-cresol, tosic acid reaction, obtain racemize tolterodine;
Step 4: racemize tolterodine, tartrate, dehydrated alcohol reaction, obtain tolterodine L-(+) tartrate.
In above-mentioned steps 1, described styryl carbinol and the feed ratio of chlorinating agent are 1: 1.
In above-mentioned steps 1, styryl carbinol solution is cooled to after 5-25 DEG C, drips chlorinating agent and react, temperature of reaction is 10-75 DEG C; React complete after, add dichloromethane extraction product.
In above-mentioned steps 2, described iodide are the one in potassiumiodide, sodium iodide.
In above-mentioned steps 2, described alkali is organic bases or mineral alkali, is specially the one in Anhydrous potassium carbonate, anhydrous sodium carbonate, sodium bicarbonate, saleratus, triethylamine, Diisopropylamine; Selecting excellent is Carbon Dioxide hydrogen potassium.
In above-mentioned steps 2, described cinnamyl chloride and the molar ratio of iodide are 1: 0.1; Temperature of reaction is 80-130 DEG C.After completion of the reaction, in reaction solution, add equivalent methylene dichloride and water to extract 2-6 time, separate, get organic layer, further use toluene and pure water washed product.
In above-mentioned steps 3, described N, the molar ratio of N-di-isopropyl-3-phenyl-2-propenyl-1-amine and tosic acid is 1: 1~1: 2, preferably 1: 1.1; Reaction times is 4-8 hour, and temperature of reaction is 80-130 DEG C.After completion of the reaction, in reaction solution, add ethyl acetate and pure water, after stirring, leave standstill separatory, organic phase solution regulates pH to 9-10, and organic layer is got in layering, and washing concentrating obtains product.
In above-mentioned steps 4, racemize tolterodine and tartaric molar ratio are 1: 1.1.Reaction is carried out in dehydrated alcohol, first racemize tolterodine is dissolved in dehydrated alcohol, and heating, as reaction solution; Again tartaric ethanol solution is dripped in reaction solution, slow cooling to 0 DEG C, growing the grain 18-36 hour, suction filtration is dry, obtains crude product product, continues to obtain Tolterodine tartrate fine work with dehydrated alcohol recrystallization.
That contriver gropes, independently creates and obtain through long-term, a large amount of experiments in technical scheme of the present invention.Compared with the technology of this technical scheme and existing synthetic Tolterodine tartrate, there is following advantage:
The first, in step 1, adopt and utilize styryl carbinol and chlorinating agent to synthesize cinnamyl chloride under condition of no solvent, obtained the high-quality product of high yield, first chlorinating agent thionyl chloride is used for to this experiment.
The second, in step 2, adopt cinnamyl chloride and Diisopropylamine, utilize alkali, iodide are made catalyzer and under solvent-free condition, are reacted and synthesized the high-quality product of high yield.In reaction process, adopt solvent-free synthetic technology, solved and on conventional art, formed a difficult problem for etherificate by product because of the use of alcoholic solvent, and shortened the reaction times.
Three, in step 3, adopted tosic acid to replace the methylsulphonic acid that in conventional art, corrodibility is strong, price is relatively expensive, the relative methylsulphonic acid of aftertreatment is easy: methylsulphonic acid is easy to enter in product in last handling process, causes product purity lower; And, because methylsulphonic acid is corrosive thick liquid, be difficult to transport, the inconvenience that feeds intake, tosic acid is solid, has overcome disadvantageous factor in above industrial production.This reaction is simultaneously also to carry out under condition of no solvent.
Specific embodiment
Referring to specific embodiment, the present invention is described.It will be appreciated by those skilled in the art that these embodiment are only for the present invention is described, the scope that it does not limit the present invention in any way.
Experimental technique in following embodiment, if no special instructions, is ordinary method.Chemical feedstocks, reagent material etc. used in following embodiment, if no special instructions, is commercially available purchase product.
Wherein, the cinnamyl chloride relating in this specification sheets embodiment, the purity detecting of two kinds of materials of Tolterodine tartrate, condition is as follows:
(1) detection of cinnamyl chloride
Gas chromatographic detection (GC) condition: chromatographic column: Agilent DB-wax 30.0m length × 0.32mm internal diameter and film thickness 0.25um; Sampler temperature: 200 DEG C; Detector temperature: 250 DEG C; Post flow: 2.0ml/min; Post case: 60 DEG C of 40 DEG C/min are warming up to 220 DEG C; Solvent: CH 2cl 2; Sample size: 1ul.
(2) detection of Tolterodine tartrate
High performance liquid phase detects (HPLC) condition: chromatographic column: Yi Lite C18 (HyPersil ODSZ) 250mm length × 4.6mm internal diameter and 5um particle diameter; Column temperature: 40 DEG C; Flow velocity: 1.0ml/min; Moving phase: NH 4cl is dissolved in 500ml water and 500ml acetonitrile, regulates pH value to 3.01; Detect wavelength: 282nm; Sample size: 10um
Embodiment 1
At 250ml there-necked flask, add styryl carbinol (20.1g, 0.15mol), reactant solution is cooled to 5-10 DEG C with ice-water bath, slowly drip thionyl chloride (18g, 0.15mol).Dropwise the water-bath of recession deicing, 60 DEG C are refluxed 3 hours.TLC monitoring has been reacted, and is cooled to and under room temperature condition, adds 50ml purified water, and then add methylene dichloride 50ml to extract once, and dichloromethane layer washs once with 6% sodium hydrogen carbonate solution 50ml, separatory.Wash at twice dichloromethane layer by 100ml purified water, collect dichloromethane layer, then use anhydrous sodium sulfate drying 1h, filter, concentrate to obtain cinnamyl chloride 22.7g, productive rate: 99%, GC purity 97%.
Embodiment 2
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), Anhydrous potassium carbonate (45g, 0.325mol), potassiumiodide (2.7g, 0.01625mol) join successively 500ml there-necked flask, be heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 500ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 67.1g, productive rate: 95%, GC purity 98%.
Embodiment 3
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), anhydrous sodium carbonate (34.45g, 0.325mol), potassiumiodide (2.7g, 0.01625mol) join successively 500ml there-necked flask, be heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 1000ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 65.4g, productive rate: 93%, GC purity 97%.
Embodiment 4
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), sodium bicarbonate (27.30g, 0.325mol), sodium iodide (2.454g, 0.01625mol) join successively 500ml there-necked flask, be heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 1000ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 64.2g, productive rate: 91%, GC purity 98%.
Embodiment 5
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), triethylamine (32.83g, 0.325mol), potassiumiodide (2.7g, 0.01625mol) joins 500ml there-necked flask successively, is heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 1000ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 58.6g, productive rate: 83%, GC purity 95%.
Embodiment 6
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), triethylamine (32.83g, 0.325mol), potassiumiodide (2.7g, 0.01625mol) joins 500ml there-necked flask successively, is heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 1000ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 58g, productive rate: 82%, GC purity 97%.
Embodiment 7
By cinnamyl chloride (49.6g, 0.325mol), Diisopropylamine (65.8g, 0.65mol), Anhydrous potassium carbonate (22.42g, 0.163mol), potassiumiodide (2.7g, 0.01625mol), join successively 500ml there-necked flask, be heated to 100 DEG C of back flow reaction 8h.TLC monitoring has been reacted, and reaction solution is transferred to 2L there-necked flask, adds successively purified water 1000ml, methylene dichloride 260ml, extracting and demixing.Water layer adds respectively methylene dichloride 130ml extracting twice again.Merge organic phase, with the washing of 200ml purified water, layering, organic phase anhydrous sodium sulfate drying 1h, filters, concentrated organic phase.Concentrated product is transferred in 1L there-necked flask, adds 500ml purified water, and 260ml toluene, with 36.5%HCl adjusting pH to 2, layering.Use respectively toluene 130ml washed twice water layer, stratified pumping phase.Water regulates pH to 12 with NaOH solution, adds normal hexane 260ml extraction, and organic phase is got in layering, again add normal hexane 130ml aqueous phase extracted, merge organic layer twice, wash at twice organic phase with purified water 400ml, organic phase is got in layering, add anhydrous sodium sulfate drying 1h, filter, concentrate to obtain N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine 61.4g, productive rate 87%, product purity 97%.
Embodiment 8
In 250ml there-necked flask, add successively N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine (10g, 0.046mol), p-cresol (25.5g, 0.235mol), tosic acid (15.9g, 0.092mol), is heated to 80 DEG C of reaction 4h.TLC monitoring has been reacted, and is cooled to room temperature, in reaction flask, adds respectively ethyl acetate 100ml and purified water 100ml, stirs 10min, leaves standstill separatory, and organic phase regulates pH to 9, layering with aqueous sodium hydroxide solution.Ethyl acetate layer washs once by 100ml purified water, and separatory is collected ethyl acetate layer, uses anhydrous sodium sulfate drying 1h, filters, and concentrates to obtain oily product 12.1g, productive rate: 84.5%.HPLC purity 95%.
Embodiment 9
In 250ml there-necked flask, add successively N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine (10g, 0.046mol), p-cresol (25.5g, 0.235mol), tosic acid (15.9g, 0.092mol), is heated to 120 DEG C of reaction 4h.TLC monitoring has been reacted, and is cooled to room temperature, in reaction flask, adds respectively ethyl acetate l00ml and purified water 100ml, stirs 10min, leaves standstill separatory, and organic phase regulates pH to 9, layering with aqueous sodium hydroxide solution.Ethyl acetate layer washs once by l00ml purified water, and separatory is collected ethyl acetate layer, uses anhydrous sodium sulfate drying 1h, filters, and concentrates to obtain oily product 12.5g, productive rate: 87.3%.HPLC purity 95%.
Embodiment 10
In 250ml there-necked flask, add successively N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine (10g, 0.046mol), p-cresol (25.5g, 0.235mol), tosic acid (15.9g, 0.092mol), is heated to 130 DEG C of reaction 4h.TLC monitoring has been reacted, and is cooled to room temperature, in reaction flask, adds respectively ethyl acetate l00ml and purified water l00ml, stirs l0min, leaves standstill separatory, and organic phase regulates pH to 9.5, layering with aqueous sodium hydroxide solution.Ethyl acetate layer washs once by l00ml purified water, and separatory is collected ethyl acetate layer, uses anhydrous sodium sulfate drying lh, filters, and concentrates to obtain oily product 13.6g, productive rate: 95%.HPLC purity 96%.
Embodiment 11
In 250ml there-necked flask, add successively N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine (10g, 0.046mol), p-cresol (25.5g, 0.235mol), tosic acid (15.9g, 0.092mol), is heated to 130 DEG C of reaction 4h.TLC monitoring has been reacted, and is cooled to room temperature, in reaction flask, adds respectively ethyl acetate 100ml and purified water 100ml, stirs 10min, leaves standstill separatory, and organic phase regulates pH to 10, layering with aqueous sodium hydroxide solution.Ethyl acetate layer washs once by 100ml purified water, and separatory is collected ethyl acetate layer, uses anhydrous sodium sulfate drying 1h, filters, and concentrates to obtain oily product 12.6g, productive rate: 88%.HPLC purity 96%.
Embodiment 12
In 250ml there-necked flask, take racemize tolterodine (20g, 61.4mmol) and be dissolved in 200ml dehydrated alcohol, be heated to 60 DEG C.Tartrate (10.2g, 67.5mmol) be dissolved in hot dehydrated alcohol 200ml, slowly be added dropwise to above-mentioned solution, add rear backflow 1h, then slow cooling to 0 DEG C, growing the grain 24h, suction filtration, washs solid product, 40 DEG C of condition drying under reduced pressure at twice with 80ml ice ethanol, obtain product 12.2g, productive rate: 46%.
Among 250ml there-necked flask, add Tolterodine tartrate crude product (12.2g, 28.2mmol), then adding 600ml dehydrated alcohol backflow 0.5h, then slow cooling room temperature, leaves standstill growing the grain 24h, suction filtration, with 40ml ice washing with alcohol solid product, 40 DEG C of condition drying under reduced pressure, obtain Tolterodine tartrate fine work 9g, productive rate: 73.8%.HPLC purity: 99.9%, ee value 99.5%, [a] 25(1%, methanol)=28.2 °.
Embodiment 13
By N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine (10g, 0.046mol), p-cresol (25.5g, 0.235mol), A acid (0.165mol) adds 250ml there-necked flask, is heated to 130 DEG C of reactions 4 hours.TLC monitoring has been reacted, and is cooled to room temperature, and reaction solution is transferred to 500ml there-necked flask, adds toluene 200ml, and purified water 200ml, with the aqueous solution adjusting pH to 9.5 of alkali, stratification.Purify and wash toluene layer with 100ml, separatory, collects toluene layer, uses anhydrous sodium sulfate drying 1h, filters, the concentrated oily product that to obtain.
The impact of table a different catalysts on step 3
By table, a can find out, while selecting tosic acid, productive rate is higher, and product purity is better, reaches industrial pharmaceutical production requirement.
Embodiment 14
At 250ml there-necked flask, add styryl carbinol (20.1g, 0.15mol), reactant solution is cooled to 5 to 10 DEG C with ice-water bath, slowly drip chlorinating agent B.Dropwise the water-bath of recession deicing, 60 DEG C are refluxed 3 hours.TLC monitoring has been reacted, and is cooled to and under room temperature condition, adds 50ml purified water, and then add methylene dichloride 50ml to extract once, and dichloromethane layer washs once with 6% sodium hydrogen carbonate solution 50ml, separatory.Wash at twice dichloromethane layer by 100ml purified water, collect dichloromethane layer, then use anhydrous sodium sulfate drying 1h, filter, concentrate to obtain cinnamyl chloride.
The impact of table b differential responses raw material on step 1
From the experimental result of table b, can find out, select the raw material of thionyl chloride as reaction, experimental implementation process is simple, and productive rate is the highest, and product purity reaches 97%.

Claims (9)

1. a method for synthetic Tolterodine tartrate, comprising:
Step 1: styryl carbinol, thionyl chloride reaction, obtain product cinnamyl chloride;
Step 2: cinnamyl chloride, Diisopropylamine, iodide and alkali reaction, obtain product N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine, the reaction of described step 2 is carried out under condition of no solvent;
Step 3:N, N-di-isopropyl-3-phenyl-2-propenyl-1-amine, p-cresol, tosic acid reaction, obtain racemize tolterodine;
Step 4: racemize tolterodine, tartrate, dehydrated alcohol reaction, obtain tolterodine L-(+) tartrate.
2. the method for synthetic Tolterodine tartrate according to claim 1, is characterized in that: in described step 2, iodide are the one in potassiumiodide, sodium iodide.
3. the method for synthetic Tolterodine tartrate according to claim 2, is characterized in that: in described step 2, iodide are potassiumiodide.
4. the method for synthetic Tolterodine tartrate according to claim 1, is characterized in that: in described step 2, alkali is the one in Anhydrous potassium carbonate, anhydrous sodium carbonate, sodium bicarbonate, saleratus, triethylamine, Diisopropylamine.
5. the method for synthetic Tolterodine tartrate according to claim 4, is characterized in that: in described step 2, alkali is Anhydrous potassium carbonate.
6. the method for synthetic Tolterodine tartrate according to claim 1, is characterized in that: in described step 2, the mol ratio of cinnamyl chloride and iodide is 1:0.1.
7. the method for synthetic Tolterodine tartrate according to claim 1, is characterized in that: in described step 3, and N, the mol ratio of N-di-isopropyl-3-phenyl-2-propenyl-1-amine and tosic acid is 1.1~1:2.
8. the method for synthetic Tolterodine tartrate according to claim 7, is characterized in that: in described step 3, and N, the mol ratio of N-di-isopropyl-3-phenyl-2-propenyl-1-amine and tosic acid is 1:1.1.
9. the method for synthetic Tolterodine tartrate according to claim 1, is characterized in that: in described step 4, racemize tolterodine and tartaric mol ratio are 1:1.1.
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