Tail-gas comprehensive utilization method in mercuric chloride catalyst

A mercuric chloride and tail gas technology, applied in chemical instruments and methods, separation methods, calcium/strontium/barium chloride and other directions, can solve the problems of hidden danger of secondary pollution, waste of exhaust heat, energy waste, etc., and achieve low production costs , energy saving, good effect of environmental protection

A mercuric chloride and tail gas technology, applied in chemical instruments and methods, separation methods, calcium/strontium/barium chloride and other directions, can solve the problems of hidden danger of secondary pollution, waste of exhaust heat, energy waste, etc., and achieve low production costs , energy saving, good effect of environmental protection

CN101455974AInactive Publication Date: 2009-06-17WANSHAN HONGJING MERCURY

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0013] The method for comprehensively utilizing the tail gas in the production of mercuric chloride catalyst comprises the following steps:

[0014] (1) Recovery of waste heat from tail gas: Based on the production of 2 tons of dry-based mercury chloride catalyst products, the flow rate of the tail gas at 105°C discharged from the dryer is 2900Nm 3 / h, through the pre-dryer connected in series behind the dryer, the heat conduction indirectly pre-dries the wet mercuric chloride catalyst; the temperature of the tail gas discharged from the pre-dryer is 44 ° C, and the pre-drying time is 17 hours; the chlorination after pre-drying The mercury catalyst is moved into the dryer and dried to the finished product;

[0015] (2) BaCl 2 -Ba(OH) 2 Solution countercurrent scrubbing: the tail gas from the pre-dryer is mixed with the tail gas from all processes in the production process of the mercury chloride catalyst, that is, the chemical activation process (only when the mercury chlori...

Embodiment 2

[0018] The method for comprehensively utilizing the tail gas in the production of mercuric chloride catalyst comprises the following steps:

[0019] (1) Recovery of waste heat from tail gas: Based on the production of 2 tons of dry-based mercuric chloride catalyst products, the flow rate of 100°C tail gas discharged from the dryer is 2900Nm 3 / h, through the air preheating heat exchanger connected in series behind it, the heat conduction countercurrent indirectly preheats the air at natural temperature, so as to realize the recovery and utilization of the waste heat of the exhaust gas, and the preheated air is sent into the electric hot stove and heated to After 130°C, it is used to dry mercury chloride catalyst products. The temperature of the tail gas discharged from the heat exchanger is 43°C.

[0020] (2) BaCl 2 -Ba(OH) 2 Solution countercurrent scrubbing: the tail gas from the pre-dryer is mixed with the tail gas from all processes in the production process of the merc...

Embodiment 3

[0023] The method for comprehensively utilizing the tail gas in the production of mercuric chloride catalyst comprises the following steps:

[0024] (1) Recovery of waste heat from tail gas: Based on the production of 2 tons of dry-based mercury chloride catalyst products, the flow rate of 103°C tail gas discharged from the dryer is 2900Nm 3 / h, through the air preheating heat exchanger connected in series behind it, the heat conduction countercurrent indirectly preheats the air at natural temperature, so as to realize the recovery and utilization of the waste heat of the exhaust gas, and the preheated air is sent into the electric hot stove and heated to After 130°C, it is used to dry mercury chloride catalyst products. The temperature of the tail gas discharged from the heat exchanger is 40°C.

[0025] (2) BaCl 2 -Ba(OH) 2 Solution countercurrent scrubbing: the tail gas from the pre-dryer is mixed with the tail gas from all processes in the production process of the mercu...

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Abstract

The invention discloses a comprehensive utilization method for tail gas in the production of a mercuric chloride catalyst. The method comprises the following steps: the temperature of tail gas coming from a dryer in the production of the mercuric chloride catalyst is between 90 and 105 DEG C; the discharge temperature of the tail gas of which the waste heat is recovered is controlled to be not higher than 45 DEG C through a heat exchange device serially connected with the back of the dryer; the tail gas of which the waste heat is recovered and the tail gas which comes from the other processes in the production of the mercuric chloride catalyst are mixed together, and enters from the lower part of a filler countercurrent gas-washing tower; mixture liquid of BaCl2 and Ba(OH)2 is continuously sprayed down from the top of the filler tower to perform countercurrent gas washing; liquid after washing flows into an anticorrosion circulation tank on the bottom of the tower; washing liquid is continuously circulated and sprayed under the action of a circulating anticorrosion pump; and the tail gas after washing is adsorbed to remove foam through dry activated carbon in an activated-carbon device for adsorbing and removing foam, so as to obtain the tail gas reaching discharge standard. The method can ensure that the tail gas after purification treatment reaches the discharge standard, and both solid waste and liquid waste generated can be directly used for producing the mercuric chloride catalyst, so as to save energy and reduce consumption.

Description

technical field [0001] The invention belongs to the technical field of chemical industry, and in particular relates to a method for comprehensively utilizing tail gas. Background technique [0002] Mercury chloride catalyst is a catalyst for the synthesis of vinyl chloride monomer (VCM) by the "calcium carbide-acetylene" method based on coal chemical industry, and is widely used in the polyvinyl chloride industry for acetylene process PVC. In the production process of mercuric chloride catalyst, the tail gas mainly contains 10-2000mg / Nm 3 Mercury chloride and 1-100mg / Nm 3 hydrochloric acid (HCl); when producing regenerated mercuric chloride catalyst, the tail gas also contains 1-50mg / Nm 3 Chlorine gas; tail gas temperature is 90-105°C. For these three harmful pollutants in the exhaust gas, environmental protection requires that they must be purified before they can be discharged. At present, there are mainly two traditional methods for treating tail gas: ① activated carb...

Claims

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Application Information

Patent Timeline
17 Jun 2009
Publication
CN101455974A
IPC
B01J27/138; B01J37/00; C01F11/24; B01D53/78; B01D53/68; B01D53/64; C07C17/02; C07C21/06
CPC
Y02P20/10; Y02P20/129; Y02P20/50
Inventors
张亚雄