CS2 reactor furnace

A carbon disulfide and reaction furnace technology, which is applied in the field of carbon disulfide production equipment, can solve problems such as insufficient preheating of raw materials, unreasonable heating methods, and corrosion of the inner furnace body, so as to save fuel, improve production efficiency and economic benefits, and improve thermal efficiency. Effect

Inactive Publication Date: 2003-09-10
SHANGHAI BAIJIN CHEM GROUP
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Problems solved by technology

[0010] The invention solves the problems of insufficient preheating of raw materials, serious corrosion of the inner furnace body, short service life, unreasonable heating method, unstable furnace temperature and serious waste of fuel in the above-mentioned carbon disulfide reaction device in the prior art, and designs a Carbon disulfide reaction device

Method used

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  • CS2 reactor furnace
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Embodiment 1

[0035] Embodiment 1 Get silicon bricks, the specification is 6 * 25 * 40 centimeters, build inner furnace body, sulfur gasification furnace, three furnace bodies of carbon material preheating furnace according to the above-mentioned method, diameter 0.8 meters, height 4 meters. The thickness of the thermal insulation outer wall is 0.5 meters, a two-ton gas-fired furnace, the diameter of the main fire channel is one meter, heating for 6-8 hours, when the temperature in the furnace reaches 700°C, take 840 kg of semi-coke and put it into the carbon material preheating furnace Preheat for about 2 hours, when the temperature of the carbon material reaches or approaches 700°C, take 3,000 kg of sulfur and add it to the sulfur gasifier in batches from the sulfur inlet, and at the same time take the preheated carbon material out of the carbon outlet and pass it through the inner Put the charcoal inlet on the upper part of the furnace body into the furnace to continue heating. At this ti...

Embodiment 2

[0036] Example 2 In the above reaction furnace, add 90.75Kg of coke powder, 3000Kg of sulfur in batches, react for 24 hours, and collect 3025Kg of carbon disulfide in total.

Embodiment 3

[0037] Example 3 The reaction furnace body is elliptical, with a major axis of 1 meter, a minor axis of 0.5 meters, and a height of 1.8 meters. The sulfur gasifier is a cylinder with a height of 1.8 meters and a radius of 0.5 meters. The above two furnace bodies are all made of high-alumina bricks. Built into shape. The carbon material preheating furnace is a circular cast iron furnace body with a radius of 0.6 meters and a height of 1.8 meters.

[0038] Embodiment 4 The body of the reaction furnace in the above example 3 is spherical. The diameter of the ball is 0.8 meters, and the bottom is a spherical shape fixed on the base of the furnace. There is a furnace cap on the upper part.

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Abstract

The CS2 reactor furnace includes inner furnace body of refractory material, outer furnace body of refractory material, and heating chamber between the inner surface body and the outer furnace body. In the peripheral of the inner surface body, there are sulfur gasifying furnace and carbon material preheating furnace, and the sulfur gasifying, furnace is connected via sulfur vapor duct to the bottom of the inner furnace body. The CS2 reactor furnace of the present invention has no sulfurizing and oxidizing corrosion of inner furnace body and thus long service life. The material preheating speeds the reaction and raise the product yield. Heating the coal-burning gas furnace via the main fire channel communicated with the furnace body can save fuel and stabilize furnace temperature.

Description

technical field [0001] The invention relates to a carbon disulfide production plant and the construction of the plant. Background technique [0002] In the prior art, there are mainly two kinds of reaction equipment for producing carbon disulfide by using solid carbon: ordinary reaction furnace and split type reaction furnace. The ordinary reaction furnace is also the traditional carbon disulfide reaction retort. It preheats the charcoal and puts it into the reaction furnace, then heats and liquefies the solid sulfur and passes it into the bottom of the reaction furnace, and continues to heat in the reaction furnace to the reaction temperature to promote sulfur and carbon. The reaction produces carbon disulfide, and charcoal or sulfur is added depending on the reaction during the reaction. Since the reaction to produce carbon disulfide must be carried out under airtight conditions, one is to maintain the furnace temperature; the other is to prevent gas leakage. And every t...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01B31/26
Inventor 孔庆然
Owner SHANGHAI BAIJIN CHEM GROUP
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