Process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone)

Abstract

The present invention relates to an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone). The present invention more particularly relates to an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and poor quality tert-Butyl isocyanate (TBIC) with purity less than or equal to 98%, preferably less than or equal to 85%.

Description

FIELD OF THE INVENTION

The present invention relates to an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone). The present invention more particularly relates to an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and poor quality tert-Butyl isocyanate (TBIC) with purity less than or equal to 85%, preferably less than or equal to 80%.

BACKGROUND OF THE INVENTION

Amicarbazone, 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide is a member of the class of triazoles that is 4,5-dihydro-1H-1,2,4-triazol-5-one which is substituted at position 1 by a tert-butylaminocarbonyl group and at position 3 by an isopropyl group. Amicarbazone, is a triazolinone-based herbicidal active compound represented by Formula I.

4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) is represented by Formula II

Tert-Butyl isocyanate (TBIC) is represented by Formula III

The process for preparation of Amicarbazone by coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and tert-Butyl isocyanate (TBIC) is disclosed in U.S. Pat. No. 9,332,762(B2) (Indian equivalent 2071/KOLNP/2015).

U.S. Pat. No. 9,332,762(B2) (Indian equivalent 2071/KOLNP/2015) teaches process for preparation of Amicarbazone in example 10, 11 and 12 using amino-triazolinone (TAZ) and t-butyl isocyanate (TBIC). Further the process also involve the use of toluene and KOH.

Project pre-feasibility report for Proposed Expansion Project For Manufacturing of Agrochemical Active Ingredients & Intermediates and Fine Chemicals at Ankleshwar Project Proponent M/s. Deccan Fine Chemicals (India) Pvt. Ltd. (http://environmentclearance.nic.in/writereaddata/Online/TOR/03_May_2017_1900586535FXM3T5NAnnexure-Prefeasibilityreport.pdf)

This report teaches method Amicarbazone Preparation as follows,

Amicarbazone Preparation: TBIC and Triazolinone are charged into the reactor and heated less than 60° C. Tert-butylisocyanate is charged at a controlled rate at more than 65° C. After the completion of the reaction, mixture is neutralized and cooled.

Amicrabazone is isolated by filtration and then dried.

CN107162993A discloses synthesis of Amicarbazone by adding Triazolinones, potassium hydroxide, catalyst and the solvent into the reactor. Then the tertiary butyl isocyanates prepared is added dropwise, and a heating reaction is performed to obtain the amicarbazone.

Need of the Present Invention

The present inventors have observed that the production sites of Amicarbazone and site of origin of tert-Butyl isocyanate (TBIC) are generally different. At times, production sites may received poor quality (TBIC) which needs to be discarded. Tert-Butyl isocyanate may get decomposed either in transit to the production site or at the origin. Therefore, there is a need for development of a process capable of preparing Amicarbazone employing 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and poor quality tert-Butyl isocyanate (TBIC).

Solution Provided by the Present Invention

The present inventors have surprisingly developed a robust process to produce high quality active ingredient Amicarbazone with various grades of tertiary butyl isocyanate (TBIC).

The present inventors have found that with good quality tertiary butyl isocyanate (TBIC) it is routinely possible to produce high quality of active ingredient Amicarbazone. However, with tertiary butyl isocyanate (TBIC) of poor quality, only under modified conditions of the present invention it is possible to generate active ingredient meeting the approved specifications.

The present inventors found that tertiary butyl isocyanate (TBIC) of a lower grade can be utilized, via subtle process modifications, to generate Amicarbazone technical grade active ingredient meeting quality specifications.

The present invention provide a robust approach to generate acceptable quality (per manufacturing specifications.) Amicarbazone technical grade active ingredient via the use of poorer grade of TBIC which is hitherto unknown.

Advantages of the Present Invention

1. The present invention provide a versatile process that can utilize tertiary butyl isocyanate (TBIC) of poorer quality (low purity) to generate active ingredient Amicarbazone of high purity.

2. The present invention utilize tertiary butyl isocyanate (TBIC) of poorer quality (low purity) which would be generally discarded in case the same is decomposed for example TBIC, which is a highly reactive Isocyanate, needs to maintained/transported pure via exclusion of air/moisture and if not maintained it may decomposed during transit to production site. This would lower the cost of production of Amicarbazone.

OBJECTS OF THE INVENTION

It is an object of the present invention to provide a robust process to produce high quality active ingredient Amicarbazone with various grades of tertiary butyl isocyanate (TBIC) having low purity.

It is another object of the present invention to provide a process to produce high quality active ingredient, Amicarbazone with poor quality tert-Butyl isocyanate (TBIC) with purity equal to or less than 98%, preferably less than or equal to 85%.

SUMMARY OF THE INVENTION

According to an aspect of the present invention there is provided a process for the preparation of Amicarbazone comprising the step of:

• • i. Preparing a solution of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ), Potassium hydroxide and toluene;
  • ii. Raising the temperature of the solution obtained in step (i) to the range of 50° C. to 70° C.;
  • iii. Adding tert-Butyl isocyanate (TBIC) without distillation to the solution of step (ii)
  • iv. Heating the solution obtained at temperature in the range of 60° C. to 75° C.;
  • v. Cooling the solution obtained in step (iv) to form Amicarbazone.

BRIEF DESCRIPTION OF FIGURES

FIG. 1 show Amicarbazone purity (HPLC) achieved by the process of the present invention (Exp #21).

FIG. 2 show impurities (HPLC) detected in the Amicarbazone prepared by the process of the present invention (Exp #21).

FIG. 3 show Amicarbazone purity (HPLC) achieved by the process of the present invention (Exp #23).

FIG. 4 show impurities (HPLC) detected in the Amicarbazone prepared by the process of the present invention (Exp #23).

FIG. 5 show Amicarbazone purity (HPLC) achieved by the process of the present invention (Exp #25).

FIG. 6 show impurities (HPLC) detected in the Amicarbazone prepared by the process of the present invention (Exp #25).

DETAILED DESCRIPTION OF THE INVENTION

The present invention relates to an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone).

In an embodiment the present invention provide an improved process for the preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and poor quality tert-Butyl isocyanate (TBIC) with purity less than or equal to 88%, preferably less than or equal to 80%.

In another embodiment the present invention provide a process for the preparation of Amicarbazone comprising the step of:

• • i. Preparing a solution of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ), Potassium hydroxide and toluene;
  • ii. Raising the temperature of the solution obtained in step (i) to the range of 50° C. to 70° C.;
  • iii. Adding tert-Butyl isocyanate (TBIC) without distillation to the solution of step (ii)
  • iv. Heating the solution obtained at temperature in the range of 60° C. to 75° C.;
  • v. Cooling the solution obtained in step (iv) to form Amicarbazone.

In the process of the present invention step (iii) comprises at least 18% molar excess of TBIC with respect to TAZ;

In the process of the present invention the solution is cooled to the temperature in the range of 40° C. to 50° C.;

In the process of the present invention the cooled solution is optionally seeded with Amicarbazone.

Poor quality tert-Butyl isocyanate (TBIC) is defined as a compound with purity less than or equal to 98%.

In an embodiment of the present invention the tert-Butyl isocyanate (TBIC) used in the process of the present invention have purity in the range of 80% to 98%.

In another embodiment of the present invention the tert ert-Butyl isocyanate (TBIC) used in the process of the present invention have purity less than 85%.

In yet another embodiment the present invention the Amicarbazone obtained as a final product have purity more than 97%.

In yet another embodiment the Heating, Cooling and Filtration may be carried out using conventional processes.

FIG. 1, FIG. 3 and FIG. 5 show Amicarbazone purity (HPLC) achieved according to coupling process of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and poor quality tert-Butyl isocyanate (TBIC) with purity less than or equal to 80%, in order to get good quality of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone).

FIG. 2, FIG. 4 and FIG. 6 show impurities (HPLC) detected in Amicarbazone when prepared by the process of the present invention.

The Results Achieved by Experiment 21 (FIGS. 1 and 2) are Tabulated in Table 1

TABLE 1
Component	Specification	Result
Amicarbazone purity, % w/w	Minimum 96.5%	97.3%
Bis-Acyl compound, % w/w	Maximum 1.30%	1.16%
Di-tert-butil-urea, % w/w	Maximum 0.60%	0.15%
3H-1,2,4-triazol-3-one,	Maximum 0.40%	0.48%
4 amino-2,4-dihydro-5-(1-
methylethul), % w/w (Common name:
Aminotriazolinone)
Toluene, % w/w	Maximum 0.50%	0.11%
Karl Fischer, % ww	Maximum 0.30%	0.14%

The Results Achieved by Experiment 23 (FIGS. 3 and 4) are Tabulated in Table 2

TABLE 2
Component	Specification	Result
Amicarbazone purity, % w/w	Minimum 96.5%	97.4%
Bis-Acyl compound, % w/w	Maximum 1.30%	0.97
Di-tert-butil-urea, % w/w	Maximum 0.60%	0.12
3H-1,2,4-triazol-3-one,	Maximum 0.40%	0.18
4 amino-2,4-dihydro-5-(1-
methylethul), % w/w (Common name:
Aminotriazolinone)
Toluene, % w/w	Maximum 0.50%	0.11
Karl Fischer, % ww	Maximum 0.30%	0.20

The Results Achieved by Experiment 25 (FIGS. 5 and 6) are Tabulated in Table 3

TABLE 3
Component	Specification	Result
Amicarbazone purity, % w/w	Minimum 96.5%	98.2%
Bis-Acyl compound, % w/w	Maximum 1.30%	0.93
Di-tert-butil-urea, % w/w	Maximum 0.60%	0.08
3H-1,2,4-triazol-3-one,	Maximum 0.40%	0.02
4 amino-2,4-dihydro-5-(1-
methylethul), % w/w (Common name:
Aminotriazolinone)
Toluene, % w/w	Maximum 0.50%	0.17
Karl Fischer, % ww	Maximum 0.30%	0.08%

Experiment 21, 23 and 25 are conducted in a manner as described in Example 1.

EXAMPLES

The present invention will now be explained in detail by reference to the following formulation examples and a test example, which should not be construed as limiting the scope of the present invention.

Example 1

Process for Preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by Coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Poor Quality tert-Butyl isocyanate (TBIC) with Purity Less than or Equal to 80%.

• • i. Weight the required amount of Toluene, TAZ and Potassium hydroxide and put it under stirring into the 4-Neck Flask;
  • ii. Drying (azeotropic drying (through the distillation column)) of TAZ under vacuum of 167 mmHg under controlled temperature between 61 to 67° C. until get the moisture level of 0.04% in the toluene;
  • iii. Raise the temperature inside the flask and keep at 60° C. (±1° C.);
  • iv. Increase agitation and add slowly and in constant flow in 30 minutes the required amount of TBIC undistilled in order to have 18% molar excess in relation to TAZ amount;
  • v. Raise the temperature inside the flask slowly and in constantly heating to 70° C. (1° C.) in 10 min and keep it for 5 minutes;
  • vi. Cool down the temperature slowly and in constantly inside the flask until 50° C. (1° C.) in 10 minutes and keep it;
  • vii. Adding seed of Amicarbazone and keep stirring for 10 min;
  • viii. Stop stirring and cool down the temperature inside the flask until 10° C. in 2 hours;
  • ix. Filter the product formed and wash the crystals with the required amount of water;
  • x. Dry the crystals under vacuum (200-400 mmHg) at 35-40° C. until get maximum 0.30% of moisture;
  • xi. Assay the crystals using the specific method.

Example 2

Process for Preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by Coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Poor Quality tert-Butyl isocyanate (TBIC) with Purity Less than or Equal to 80%.

• • i. 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Potassium hydroxide solution drying under vacuum at 176 mmHg at 67° C.
  • ii. Poor quality of tert-Butyl isocyanate (TBIC) without distillation adding under nitrogen atmosphere and controlled temperature of 60° C.;
  • iii. Temperature raising until 70° C.;
  • iv. Temperature cooling down until 50° C.;
  • v. Add 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) seed;
  • vi. Cooling down until 10° C. in 2 hours;
  • vii. Filtration;
  • viii. Drying under vacuum at 35-40° C.

The 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) purity and tert-Butyl isocyanate (TBIC) molar excess compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) are tabulated in Table 4.

TABLE 4
		tert-Butyl
		isocyanate	4-amino-N-tert-butyl-4,5-dihydro-3-
Sr.	Experiment	(TBIC) molar	isopropyl-5-oxo-1H-1,2,4-triazole-1-
No	No.	excess	carboxamide (Amicarbazone) purity
1	Exp#25	18.00%	98.20%
2	Exp#28	20.00%	98.70%
3	Exp#29	22.00%	98.40%

Conclusion: The molar excess equal to or greater than 18.00% of Poor quality of tert-Butyl isocyanate (TBIC) compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) achieve high purity of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone).

Comparative Example 1

Process for Preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by Coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Poor Quality tert-Butyl isocyanate (TBIC) with Purity Less than or Equal to 80%.

• • i. 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Potassium hydroxide solution drying under vacuum at 176 mmHg at 67° C.
  • ii. Poor quality of tert-Butyl isocyanate (TBIC) without distillation adding under nitrogen atmosphere and controlled temperature of 60° C.;
  • iii. Temperature raising until 70° C.;
  • iv. Temperature cooling down until 50° C.;
  • v. Add 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) seed;
  • vi. Cooling down until 10° C. in 2 hours;
  • vii. Filtration;
  • viii. Drying under vacuum at 35-40° C.

The 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) purity and tert-Butyl isocyanate (TBIC) molar excess compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) are tabulated in Table 5.

TABLE 5
		tert-Butyl
		isocyanate	4-amino-N-tert-butyl-4,5-dihydro-3-
Sr.	Experiment	(TBIC) molar	isopropyl-5-oxo-1H-1,2,4-triazole-1-
No	No.	excess	carboxamide (Amicarbazone) purity
1	Exp#4	4.00%	73.20%
2	Exp#6	9.50%	83.50%
3	Exp#27	10.00%	88.50%

Conclusion: The molar excess less than 18.00% of poor quality of tert-Butyl isocyanate (TBIC) compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) achieve low purity of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone).

Comparative Example 2

Process for Preparation of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) by Coupling of 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Pure tert-Butyl isocyanate (TBIC) with Purity Higher than or Equal to 98%.

• • i. 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) and Potassium hydroxide solution drying under vacuum at 176 mmHg at 67° C.
  • ii. Pure tert-Butyl isocyanate (TBIC) without distillation adding under nitrogen atmosphere and controlled temperature of 60° C.;
  • iii. Temperature raising until 70° C.;
  • iv. Temperature cooling down until 50° C.;
  • v. Add 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) seed;
  • vi. Cooling down until 10° C. in 2 hours;
  • vii. Filtration;
  • viii. Drying under vacuum at 35-40° C.

The 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone) purity and tert-Butyl isocyanate (TBIC) molar excess compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) are tabulated in Table 6.

TABLE 6
		tert-Butyl
		isocyanate	4-amino-N-tert-butyl-4,5-dihydro-3-
Sr.	Experiment	(TBIC) molar	isopropyl-5-oxo-1H-1,2,4-triazole-1-
No	No.	excess	carboxamide (Amicarbazone) purity
1	Exp#54	4.00%	97.25%
2	Exp#60	3.00%	98.27%
3	Exp#61	5.00%	98.27%

Conclusion: The molar excess less than 18.00% of Good quality of tert-Butyl isocyanate (TBIC) (i.e. 4-5% of TBIC molar excess) as compared to 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) achieve high purity of 4-amino-N-tert-butyl-4,5-dihydro-3-isopropyl-5-oxo-1H-1,2,4-triazole-1-carboxamide (Amicarbazone).

Experimental Data

		Reagents
Reactants	Purity (%)	B1	B2	B3	B4	B5
TBIC	81.20%	21.2923	21.2923	51.5728	51.5728	21.2936
(Poor quality)
TBIC	98.50%	--	--	--	---	--
(Good quality)
TAZ	97.71%	30	30	72.664	72.664	30
Toluene	99.27%	103.6276	103.6276	300	251.8384	123.8577
KOH (51.81%)	51.81%	0.4471	0.4471	1.0829	1.2995	0.6706
Washing Water	--	not measured	not	not	not	not
			measured	measured	measured	measured
moles TBIC		0.215	0.215	0.520	0.520	0.215
moles TAZ		0.206	0.206	0.500	0.500	0.206
Moles Ratio		4.0%	4.0%	4.0%	4.0%	4.0%
TBIZ/TAZ
TAZ	Azeotropic	No	No	No	No	No
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	15	15	15	15	21
	min
Molar excess of		4.00%	4.00%	4.00%	4.00%	4.01%
TBIC compared
to TAZ
Time kept at		10	10	10	10	22.5
70° C., min
Time for cooling
down until 50° C.,		not measured	not	not	not	not
min			measured	measured	measured	measured
Time for cooling		---	---	---	---	---
down at 10° C.,
min
Amicarbazone		17.0%	62.0%	49.8%	73.0%	55.2%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = No
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = 4.00%
Amicarbazone purity, % w/w = Low purity

		Reagents
Reactants	Purity (%)	B6	B7	B8	B9	B10
TBIC	81.20%	38.68	34.105	22.33	22.977	22.4077
(Poor quality)
TBIC	98.50%	--	--	--	---	--
(Good quality)
TAZ	97.71%	51.7769	47.1471	29.8909	28.0572	29.9949
Toluene	99.27%	137.3479	121 1027	79.2911	79.2911	79.567
KOH (51.81%)	51.81%	0.9823	0.8661	0.5671	0.5835	0.5691
Washing Water	--	not measured	41.3448	27.0702	27.0702	not
						measured
moles TBIC		0.390	0.344	0.225	0.232	0.226
moles TAZ		0.356	0.324	0.206	0.193	0.206
Moles Ratio		9.5%	6.0%	9.5%	20.0%	9.5%
TBBI/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	Yes	Yes	Yes	Yes	Yes
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		9.47%	6.00%	9.47%	20.00%	9.47%
TBIC compared
to TAZ
Time kept at		30	5	5	5	5
70° C., min
Time for cooling		not measured	30	15	10	10
down until 50° C.,
min
Time for cooling		---	150	30	60	10
down at 10° C.,
min
Amicarbazone		83.5%	63.3%	58.3%	101.9%	56.7%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying under vacuum = Yes
Was used TBIC distilled = Yes
Molar excess of TBIC compared to TAZ = Less than 18%
Amicarbazone purity, % w/w = Low purity

		Reagents
Reactants	Purity (%)	B11	B12	B13	B14	B15
TBIC	81.20%	40.5817	47.7384	52.6735	55.4773	54.2132
(Poor
quality)
TBIC	98.50%	--	--	--	---	--
(Good
quality)
TAZ	97.71%	49.5542	58.2933	61.7467	65.0335	56.7425
Toluene	99.27%	144.1006	169.5132	187.0371	196.9931	192.5044
KOH
(51.81%)	51.81%	1.0306	1.2124	1.3377	1.4089	1.3768
Washing	--	27.0702	57.8723	63.8551	67.2541	65.7216
Water
moles TBIC		0.409	0.481	0.531	0.559	0.547
moles TAZ		0.341	0.401	0.425	0.447	0.390
Moles Ratio		20.0%	20.0%	25.0%	25.0%	40.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	Yes	Yes	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	mm
Molar excess		20.00%	20.00%	25.00%	25.00%	40.00%
of TBIC
compared to
TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for		10	10	10	10	10
cooling down
until 50° C.,
min
Time for		60	60	60	60	60
cooling down
at 10° C., min
Amicarbazone		90.0%	82.2%	97.5%	92.7%	92.2%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

		Reagents
Reactants	Purity (%)	B16	B17	B18	B19	B20
TBIC	81.20%	55.7794	55.4773	55.681	55.6993	64.1688
(Poor quality)
TBIC	98.50%	--	--	--	---	--
(Good quality)
TAZ	97.71%	62.8727	65.0335	67.9919	68.0143	78.3564
Toluene	99.27%	198.0658	196.9931	197.7164	197.7814	227.8555
KOH (51.81%)	51.81%	1.4874	1.4089	1.4848	1.4853	1.7111
Washing Water	--	68.6203	67.2541	67.501	67.5232	77.7906
moles TBIC		0.562	0.559	0.561	0.562	0.647
moles TAZ		0.433	0.447	0.468	0.468	0.539
Moles Ratio		30.0%	25.0%	20.0%	20.0%	20.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		30.00%	25.00%	20.00%	20.00%	20.00%
TBIC compared
to TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for cooling		10	10	10	10	10
down until 50° C.,
min
Time for cooling		60	60	120	120	120
down at 10° C.,
min
Amicarbazone		88.1%	98.0%	99.7%	99.4%	98.1%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

		Reagents
Reactants	Purity (%)	B21	B22	B23	B24	B25
TBIC	81.20%	200.0000	64.1688	350.0000	300.0000	300.0000
(Poor quality)
TBIC	98.50%	--	--	--	---	--
(Good quality)
TAZ	97.71%	244.2196	78.3564	427.3842	366.3293	372.4959
Toluene	99.27%	710.1754	227.8555	1242.807	1065.2632	1065.2632
KOH (51.81%)	51.81%	5.3333	1.7111	9.332	7.9999	7.9999
Washing Water	--	242.4561	77.7906	424.2982	363.6842	363.6842
moles TBIC		2.017	0.647	3.529	3.025	3.025
moles TAZ		1.680	0.539	2.941	2.521	2.563
Moles Ratio		20.0%	20.0%	20.0%	20.0%	18.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		20.00%	20.00%	20.00%	20.00%	18.01%
TBIC compared
to TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for cooling		10	10	10	10	10
down until 50° C.,
min
Time for cooling		120	120	120	120	120
down at 10° C.,
min
Amicarbazone		97.3%	97.2%	97.4%	97.8%	98.2%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

		Reagents
Reactants	Purity (%)	B26	B27	B28	B29	B30
TBIC	81.20%	65.0000	62.1739	350.0000	350.0000	350.0000
(Poor quality)
TBIC	98.50%	--	--	--	---	--
(Good quality)
TAZ	97.71%	82.8223	82.8223	427.3842	420.332398	420.3324
Toluene	99.27%	230.8070	230.8070	1242.807	1242.807	1242.807
KOH (51.81%)	51.81%	1.7333	1.7333	9.332	9.4506	9.4506
Washing Water	--	78.7982	78.7982	424.2982	424.2982	424.2982
moles TBIC		0.655	0.627	3.529	3.529	3.529
moles TAZ		0.570	0.570	2.941	2.892	2.892
Moles Ratio		15.0%	10.0%	20.0%	22.0%	22.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		15.00%	10.00%	20.00%	22.01%	22.01%
TBIC compared
to TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for cooling		10	10	10	10	10
down until 50° C.,
min
Time for cooling		120	120	120	120	120
down at 10° C.,
min
Amicarbazone		88.5%	88.5%	98.7%	97.8%	97.7%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

		Reagents
Reactants	Purity (%)	B31	B32	B33	B34	B35
TBIC	81.20%	350.0000	350.0000	350.0000	116.6667	116.6667
(Poor quality)
TBIC	98.50%
(Good quality)
TAZ	97.71%	420.3324	420.3324	427.3842	142.4614	140.1108
Toluene	99.27%	1242.807	1242.807	1242.807	414.2690	414.2690
KOH (51.81%)	51.81%	9.4506	9.4506	9.4506	3.1502	3.1502
Washing Water	--	424.2982	424.2982	424,2982	141.4327	141.4327
moles TBIC		3.529	3.529	3.529	1.176	1.176
moles TAZ		2.892	2.892	2.941	0.980	0.964
Moles Ratio		22.0%	22.0%	20.0%	20.0%	22.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		22.01%	22.01%	20.00%	20.00%	22.01%
TBIC compared
to TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for cooling		10	10	10	10	10
down until 50° C.,
min
Time for cooling		120	120	120	120	120
down at 10° C.,
min
Amicarbazone		90.4%	90.7%	93.5%	91.6%	92.6%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

	Reactants
Reagents	Purity (%)	B37	B38	B39	B40
TBIC	81.20%	116.6667	115.7398	86.8049	86.8049
(Poor quality)
TBIC	98.50%
(Good quality)
TAZ	97.71%	135.6764	135.6764	104.2239	115.6264
Toluene	99.27%	414.2690	414.2690	310.7018	310.7018
KOH (51.81%)	51.81%	3.1502	3.1502	2.3626	2.3626
Washing Water	—	141.4327	141.4327	106.0746	106.0746
moles TBIC		1.176	1.167	0.875	0.875
moles TAZ		0.934	0.934	0.717	0.796
Moles Ratio		26.0%	25.0%	22.0%	10.0%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No
	distilled?
	Temperature	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30
	min
Molar excess of		26.00%	25.00%	22.04%	10.01%
TBIC compared
to TAZ
Time kept at		5	5	5	5
70° C., min
Time for cooling		10	10	10	10
down until
50° C., min
Time for cooling		120	120	120	120
down at 10° C.,
min
Amicarbazone		97.6%	90.8%	92.9%	89.6%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

		Reagents
Reactants	Purity (%)	B41	B42	B43	B44	B45
TBIC	81.20%	26.6154	212.9231	26.6154	26.6154	29.1667
(Poor quality)
TBIC	98.50%	--	--	--	--	--
(Good quality)
TAZ	97.71%	30.0000	240.0000	30.4699	29.3242	35.0277
Toluene	99.27%	95.2648	762.1183	95.2648	95.2648	103.5673
KOH (51.81%)	51.81%	0.7244	5.7953	0.7244	0.7244	0.7875
Washing Water	--	32.5237	260.1896	32.5237	32.5237	35.3582
moles TBIC		0.268	2.147	0.268	0.268	0.294
moles TAZ		0.206	1.651	0.210	0.202	0.241
Moles Ratio		30.00%	30.00%	28.00%	33.00%	22.01%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No	No
	distilled?
	Temperature	60	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30	30
	min
Molar excess of		30.00%	30.00%	28.00%	33.00%	22.01%
TBIC compared
to TAZ
Time kept at		5	5	5	5	5
70° C., min
Time for cooling		10	10	10	10	10
down until 50° C.,
min
Time for cooling		120	120	120	120	120
down at 10° C.,
min
Amicarbazone		98.2%	97.3%	93.5%	92.9%	89.3%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

	Reactants
Reagents	Purity (%)	B46	B47
TBIC	81.20%	29.1667	29.1667
(Poor quality)
TBIC	98.50%	—	—
(Good quality)
TAZ	97.71%	34.1898	32.8769
Toluene	99.27%	103.5673	103.5673
KOH (51.81%)	51.81%	0.7777	0.7777
Washing Water	—	35.3582	35.3582
moles TBIC		0.294	0.294
moles TAZ		0.235	0.226
Moles Ratio		25.00%	30.00%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No
	distilled?
	Temperature	60	60
	inside the flask,
	° C.
	Adding time,	30	30
	min
Molar excess of		25.00%	30.00%
TBIC compared
to TAZ
Time kept at		5	5
70° C., min
Time for cooling		10	10
down until
50° C., min
Time for cooling		120	120
down at 10° C.,
min
Amicarbazone		92.0%	96.1%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = More than 18%
Amicarbazone purity, % w/w = high purity

	Reactants
Reagents	Purity (%)	B49	B50	B51	B52
TBIC	81.20%	30.0000	30.0000	30.0000	30.0000
(Poor quality)
TBIC	98.50%	—	—	—	—
(Good quality)
TAZ	97.71%	40.7013	38.2273	41.8644	41.8644
Toluene	99.27%	106.5263	106.5263	106.5263	106.5263
KOH (51,81%)	51.81%	0.7716	0.7716	0.7716	0.7716
Washing Water	—	36.3684	36.3684	36.3684	36.3684
moles TBIC		0.302	0.302	0.302	0.302
moles TAZ		0.280	0.263	0.288	0.288
Moles Ratio		8.01%	15.00%	5.00%	5.00%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	Yes	Yes	Yes	Yes
	distilled?
	Temperature	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30
	min
Molar excess of		8.01%	15.00%	5.00%	5.00%
TBIC compared
to TAZ
Time kept at		5	5	5	5
70° C., min
Time for cooling		10	10	10	10
down until
50° C., min
Time for cooling		120	120	120	120
down at 10° C.,
min
Amicarbazone		95.5%	82.6%	82.6%	87.8%
purity, % w/w
Poor quality - TBIC = 81.20% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = Yes
Molar excess of TBIC compared to TAZ = less than 18%
Amicarbazone purity, % w/w = low purity

	Reactants
Reagents	Purity (%)	B54	B55	B57	B58
TBIC	81.20%	—	—	—	—
(Poor quality)
TBIC	98.50%	30.0000	30.0000	30.0000	30.0000
(Good quality)
TAZ	97.71%	42.2680	42.2680	42.2680	42.2680
Toluene	99.27%	106.5263	106.5263	106.5263	106.5263
KOH (51.81%)	51.81%	0.7716	0.7716	0.7716	0.7716
Washing Water	—	36.3684	36.3684	36.3684	36.3684
moles TBIC		0.302	0.302	0.302	0.302
moles TAZ		0.291	0.291	0.291	0.291
Moles Ratio		4.00%	4.00%	4.00%	4.00%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No	No
	distilled?
	Temperature	60	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30	30
	min
Molar excess of		4.00%	4.00%	4.00%	4.00%
TBIC compared
to TAZ
Time kept at		5	5	5	5
70° C., min
Time for cooling		10	10	10	10
down until
50° C., min
Time for cooling		120	120	120	120
down at 10° C.,
min
Amicarbazone		97.25%	94.56%	93.99%	97.10%
purity, % w/w
Good quality - TBIC = 98.50% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = less than 18%
Amicarbazone purity, % w/w = high purity (Since Good quality of TBIC is used)

	Reactants
Reagents	Purity (%)	B59	B60	B61
TBIC	81.20%	—	—	—
(Poor quality)
TBIC	98.50%	30.0000	30.0000	30.0000
(Good quality)
TAZ	97.71%	42.2680	42.6780	41.8662
Toluene	99.27%	106.5263	106.5263	106.5263
KOH (51.81%)	51.81%	0.7716	0.7716	0.7716
Washing Water	—	36.3684	36.3684	36.3684
moles TBIC		0.302	0.302	0.302
moles TAZ		0.291	0.294	0.288
Moles Ratio		4.00%	3.00%	5.00%
TBIZ/TAZ
TAZ	Azeotropic	Yes	Yes	Yes
	drying under
	vacuum?
TBIC adding	Was used TBIC	No	No	No
	distilled?
	Temperature	60	60	60
	inside the flask,
	° C.
	Adding time,	30	30	30
	min
Molar excess of		4.00%	3.00%	5.00%
TBIC compared
to TAZ
Time kept at		5	5	5
70° C., min
Time for cooling		10	10	10
down until
50° C., min
Time for cooling		120	120	120
down at 10° C.,
min
Amicarbazone		97.22%	98.27%	98.27%
purity, % w/w
Good quality - TBIC = 98.50% purity
Azeotropic drying of TAZ under vacuum = Yes
Was used TBIC distilled = No
Molar excess of TBIC compared to TAZ = less than 18%
Amicarbazone purity, % w/w = high purity (Since Good quality of TBIC is used)

Claims

1. A method for the preparation of Amicarbazone comprising reacting 4-Amino-2,4-dihydro-5-(1-methylethyl)-3H-1,2,4-triazol-3-one (TAZ) with tert-Butyl isocyanate (TBIC) having low purity to form Amicarbazone, wherein said low purity TBIC has a purity of less than or equal to 85%, andwherein 18% or more molar excess of TBIC with respect to TAZ is used.

2. The process according to claim 1, comprising: a) preparing a solution of TAZ, potassium hydroxide, and toluene;b) raising the temperature of the solution obtained in step (a) to the range of 50° C. to 70° C.;c) adding the low purity TBIC without distillation to the solution of step (b);d) heating the solution obtained in step c) at temperature in the range of 60° C. to 75° C.; ande) cooling the solution obtained in step (d) to form the Amicarbazone.

3. The process as claimed in claim 2, wherein the solution in step (e) is cooled to the temperature in the range of 40° C. to 50° C.

4. The process as claimed in claim 2, wherein the cooled solution of step e) is optionally seeded with Amicarbazone.

5. The process as claimed in claim 1, wherein the TBIC has a purity equal to or less than 80%.

6. The process as claimed in claim 1, wherein the molar excess of TBIC with respect to TAZ is in the range of 18% to 22%.

7. The process as claimed in claim 2, wherein the purity of Amicarbazone obtained in step (e) is more than 97%.