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Deslagging method for continuous production of methyl isocyanate

A technology of methyl isocyanate and polymethyl isocyanate, which is applied in the field of slag removal in the continuous production of methyl isocyanate, can solve the problems of high production cost, high labor intensity, environmental pollution, etc., and reduce equipment occupation and basic investment costs , reduce the labor intensity of employees, and improve the effect of solvent reuse rate

Active Publication Date: 2015-04-29
海利贵溪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

[0004] 1) The solid slag produced in the production process of methyl isocyanate must be manually opened to remove the slag, and the slag contains more than 20% of volatile components such as methyl carbamoyl chloride, methyl isocyanate and solvents, not only It is highly irritating and toxic. Workers must be fully equipped with anti-virus weapons to operate under high temperature and toxic and stimulating conditions. The labor intensity is high and there is a risk of poisoning;
[0005] 2) In order to reduce the harm to the human body, the production site generally uses water washing to decompose part of the methylcarbamoyl chloride and methyl isocyanate contained in the slag, which causes waste of water resources, burden of wastewater treatment, and hydrochloric acid generated by hydrolysis corrodes the equipment and a series of problems, and the slag still contains some volatile components such as methyl carbamoyl chloride, methyl isocyanate and solvents to cause environmental pollution;
[0006] 3) The solid residue containing volatile components such as methyl carbamoyl chloride, methyl isocyanate and solvent enters into incineration, resulting in increased production costs

Method used

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  • Deslagging method for continuous production of methyl isocyanate
  • Deslagging method for continuous production of methyl isocyanate
  • Deslagging method for continuous production of methyl isocyanate

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Composition of the liquid phase outlet material from the vapor-liquid separator: methylcarbamoyl chloride 165.71kg / hr, methyl isocyanate 15.12kg / hr, solvent chloroform 1539.48kg / hr, trimeric methyl isocyanate solid slag 2.90kg / hr. The liquid phase outlet material continuously enters the slag remover from the feed port 4 of the slag remover, and is continuously filtered under negative pressure. When the pressure of the filter cake is 0.09MPa, switch the incoming material to the standby slag remover, lower the stirring system 1 of the slag remover and start stirring, start the heating jacket 5, the stirring speed is 20rpm, and the superheated steam temperature is 150°C. Stir and heat to evaporate and remove volatile components such as methyl carbamoyl chloride, methyl isocyanate and solvent contained in the filter cake, and the steam is connected to the condenser through the steam outlet 2 to condense; after the filter cake is evaporated to dryness, stop the heating jacket...

Embodiment 2

[0028] Composition of the liquid phase outlet material from the vapor-liquid separator: methylcarbamoyl chloride 165.71kg / hr, methyl isocyanate 15.12kg / hr, solvent chloroform 1539.48kg / hr, trimeric methyl isocyanate solid slag 2.90kg / hr. The mixed material continuously enters the slag remover from the feed port 4, and is continuously filtered under negative pressure. When the pressure of the filter cake is 0.08MPa, switch the incoming material to the standby slag remover, lower the stirring system 1 of the slag remover and start stirring, start the heating jacket 5, the stirring speed is 15rpm, and the superheated steam temperature is 130°C. Stir and heat to evaporate and remove volatile components such as methyl carbamoyl chloride, methyl isocyanate and solvent contained in the filter cake, and the steam is connected to the condenser through the steam outlet 2 to condense; after the filter cake is evaporated to dryness, stop the heating jacket 5, Switch the stirring system 1 ...

Embodiment 3

[0030] Composition of the liquid phase outlet material from the vapor-liquid separator: methylcarbamoyl chloride 165.71kg / hr, methyl isocyanate 15.12kg / hr, solvent chloroform 1539.48kg / hr, trimeric methyl isocyanate solid slag 2.90kg / hr. The mixed material continuously enters the slag remover from the feed port, and is fed with nitrogen and filtered under pressure. When the pressure of the filter cake drops to 0.085MPa, switch the incoming material to the standby slag remover, lower the agitator that comes with the slag remover, start the stirring in the system 1, start the heating jacket 5, the stirring speed is 10rpm, and the superheated steam temperature is 140 ℃, stirring and heating to evaporate to remove volatile components such as methylcarbamoyl chloride, methyl isocyanate and solvent contained in the filter cake, and the steam is connected to the condenser through steam outlet 2 for condensation; after the filter cake is evaporated to dryness, stop the heating jacket ...

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Abstract

The invention discloses a deslagging method for continuous production of methyl isocyanate. The method comprises the following steps: installing a deslagging machine below an air and liquid separator; performing air and liquid separation on a methyl isocyanate solution obtained by reaction by using the air and liquid separator; condensing a gas phase component and then rectifying and purifying to obtain a methyl isocyanate product; putting a liquid phase component in the deslagging machine and automatically removing tripolymethyl isocyanate solid slags; and returning the rest unreacted methyl carbamyl chloride, a trichloromethane solvent and a small amount of the methyl isocyanate product to a liquid mixing tank from the outlet of the deslagging machine and further reacting. The method disclosed by the invention can be used for automatically removing solid slags generated in the continuous production of the methyl isocyanate, realizing integration of deslagging and dry-recycle by adopting the deslagging machine, completely preventing direct contact between toxic materials and a person, reducing the labor strength, reducing toxication accidents, effectively evaporating residual volatile components such as raw materials, products and solvents in the solid slags and increasing the total yield of the products and the recycle rate of the solvents.

Description

technical field [0001] The invention relates to a slag removal method for the continuous production of methyl isocyanate. Background technique [0002] Methyl isocyanate is an important pesticide intermediate, mainly used in the synthesis of carbamate pesticides, such as: carbofuran, methomyl, amethomyl, isoprocarb (Yechansan), secbucarb (Barba Sand), carbaryl, propoxur, Haoanwei, thiodicarb, carbosulfan, butylthiuron, etc. [0003] At present, most domestic production of methyl isocyanate uses phosgene and methylamine as raw materials to prepare methyl carbamoyl chloride (abbreviated as MCC), and then in the presence of an inert solvent such as chloroform, methyl carbamoyl chloride is decomposed and rectified to produce formazan base isocyanate (abbreviated as MIC). The existing production process of methyl isocyanate will produce polymer solid slag. Currently, a slag steaming kettle is generally used to remove the polymer solid slag generated in the production process, a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C265/04C07C263/10C07C263/20
Inventor 廖兰贵臧阳陵王晓光蒋卓良蒋彪庞怀林尹霖陈军
Owner 海利贵溪新材料科技有限公司
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