Method for deacidification in platinum hydrosynthesis process

A synthesis process and platinum water technology, applied in the field of acid removal, can solve the problems of large nitrogen consumption, low utilization rate of NaHCO, and existence of agglomerated particles, so as to save nitrogen cost, shorten nitrogen protection time, and improve utilization rate.

Inactive Publication Date: 2019-05-17
江苏晶华新材料科技有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] The prior art is to use solid NaHCO 3 At the same time, it is added to the synthesis system for acid removal, because NaHCO 3 It cannot be dissolved in the reaction system. Although there is a fast dispersion device, there will still be a large number of agglomerated particles in the reaction system, which cannot be fully utilized. Therefore, NaHCO 3 low utilization
And the reaction process needs to be carried out under the protection of nitrogen. If the temperature cannot be cooled quickly at the end of the reaction, the nitrogen protection needs to continue until natural cooling, which will consume a lot of nitrogen.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] This embodiment provides a method for removing acid in the existing platinum hydration synthesis process, comprising the following steps:

[0021] Step 1: Chloroplatinic acid hexahydrate, tetramethyldivinyldisiloxane and NaHCO 3 The powder is mixed in the reactor at a weight ratio of 1:50:6, wherein 1kg of chloroplatinic acid hexahydrate, 50kg of tetramethyldivinyldisiloxane, NaHCO 3 Powder 6kg.

[0022] Step 2: Infuse nitrogen gas for 10 minutes to remove air, then keep nitrogen gas continuously introduced while rapidly stirring the mixture and heating to 110°C, let the mixture react for 100 minutes;

[0023] Step 3: Stop heating after the reaction in the reactor is over, and continue to stir and disperse until the mixture is cooled. To make the mixture reach an acid-free state, add about 6kg of NaHCO 3 The powder needs to be stirred for about 60 minutes to cool the mixture. Since the reaction process needs to be carried out under the protection of nitrogen, if the t...

Embodiment 2

[0027] The present embodiment provides a method for removing acid in the platinum hydration synthesis process of the present invention, comprising the following steps:

[0028] Step 1: Mix chloroplatinic acid hexahydrate and tetramethyldivinyldisiloxane in a reaction kettle at a weight ratio of 1:50, wherein 1 kg of chloroplatinic acid hexahydrate, tetramethyldivinyldisiloxane Alkanes 50kg.

[0029] Step 2: Infuse nitrogen gas for 10 minutes to remove air, then keep nitrogen gas continuously introduced while rapidly stirring the mixture and heating to 110°C, let the mixture react for 100 minutes;

[0030] Step 3: Add NaHCO 3 Dissolve in deionized water to form NaHCO 3 aqueous solution for use;

[0031] Step 4: Stop heating after the reaction in the reactor finishes, NaHCO 3 Add the aqueous solution into the reaction kettle under rapid stirring, and continue to stir and disperse until the mixture is cooled. To make the mixture reach an acid-free state, only about 5kgNaHCO i...

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PUM

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Abstract

The invention provides a method for deacidification in the platinum hydrosynthesis process. The method comprises the following steps: firstly, chloroplatinic acid hexahydrate and divinyl tetramethyl disiloxane are mixed into a reaction kettle according to the weight ratio being 1:(20 to 100); then nitrogen is introduced to exhaust air, the nitrogen is kept to be continuously introduced, meanwhile,the mixed solution is quickly stirred and heated, and the mixed solution reacts for a period of time; then NaHCO3 is dissolved into deionized water to form a NaHCO3 aqueous solution for standby application; then heating is stopped after a reaction in the reaction kettle is completed, the NaHCO3 aqueous solution under the state of quick stirring is added into the reaction kettle, continuous stirring and dispersing are conducted for a period of time until the mixed solution is cooled; and then after dispersing and cooling are completed, the nitrogen is stopped to be introduced, the aqueous solution and a complex are naturally layered, and the upper-layer complex is taken out and then dehydrated so as to obtain acid-free and anhydrous platinum water. Compared with the prior art, according tothe method, the utilization rate of NaHCO3 can be increased, meanwhile, the nitrogen protection time in the reaction process can be shortened, and thus the nitrogen cost is saved.

Description

technical field [0001] The invention relates to a method for removing acid, in particular to a method for removing acid during platinum hydration synthesis. Background technique [0002] Platinum catalyst can be used as liquid addition silicone rubber, silicone gel, high temperature addition silicone rubber, silicone ink addition type rubber adhesive, and can also be used as a catalyst for the synthesis of polyether silicone oil, amino silicone oil, etc. The synthesis of platinum water is the pre-production process of platinum catalyst. During the preparation of platinum water, tetramethyldivinyldisiloxane and chloroplatinic acid hexahydrate undergo a complex reaction, and a large amount of H2 will be generated during the reaction process. + , usually using NaHCO 3 Neutralize and deacidify it. [0003] The prior art is to use solid NaHCO 3 At the same time, it is added to the synthesis system for acid removal, because NaHCO 3 It cannot be dissolved in the reaction system...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07F15/00B01J31/22
Inventor 光忠明
Owner 江苏晶华新材料科技有限公司
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