Device and method for purifying methanol-to-olefin device washing water

A methanol-to-olefin and purification device technology, applied in the field of water treatment, can solve the problems of reducing the cleaning frequency of heat exchangers, air coolers and water-washing tower trays, blockage of equipment and pipelines, etc., and achieves long continuous operation period, easy regeneration, The effect of high separation efficiency

Active Publication Date: 2018-02-23
EAST CHINA UNIV OF SCI & TECH +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0005] In view of the above-mentioned problems existing in the prior art, the purpose of the present invention is to provide a purification device and purification method for the washing water of a methanol-to-olefins plant, which realizes the purification of spent catalyst fine powder and oil waxes in the water-washing water of a methanol-to-olefins plant. The removal of substances is simple and effective, and it solves the problem of clogging of equipment and pipes in the washing water circulation system caused by the high content of oil wax and catalyst in the washing water of the current MTO device, and reduces the cost of heat exchangers, air coolers and water washing tower trays. The frequency of cleaning effectively prolongs the continuous operation period of the system

Method used

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  • Device and method for purifying methanol-to-olefin device washing water

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Embodiment 1

[0038] In a 1.8 million tons / year methanol-to-olefins process, according to the method of the present invention, the washing water purification device of the present invention is used to purify the washing water containing solid catalyst and oil wax, so as to purify the washing water The purpose, its specific operation process and effects are described as follows:

[0039] 1. Material properties and related parameters

[0040] The methanol-to-olefin washing water is a multiphase mixture, and the water contains solid catalyst particles and insoluble oil droplets, wherein water is the continuous phase, and oil and solid catalyst are the dispersed phase medium. The washing water treatment capacity is 200t / h, and the density is 915.4 kg / m in the liquid phase operation state 3 , viscosity 0.255 cP, operating temperature 90°C, waste catalyst content 80 mg / L, average particle size 1.5 μm, oil content 85 mg / L;

[0041] 2. Washing water purification device

[0042] The device is mai...

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Abstract

The invention relates to the field of coal chemical wastewater treatment, in particular to a device and a method for purifying methanol-to-olefin device washing water. The method comprises the following steps: pumping out the washing water from the bottom of a washing tower, and sending to a granular-bed separator; enabling the washing water to run through the granular bed in a horizontal direction, intercepting particulate matters in water, and agglomerating microfine oil droplets in the water under the oil substance adsorbing and agglomerating actions of medium particles in the granular bed;performing settling separation on the agglomerated oil droplets under the action of gravity; after the granular bed adsorbs the particulate matters in the water till a saturated state, feeding wastewater from the bottom of the granular bed, mixing with gas, fluidizing the medium particles till a boiling state, releasing solid pollutants between bed layers, and sending the pollutants to a solid concentrating unit along with backwashing liquid. By the method, separation of catalyst particles and the oil substances from the washing water is achieved.

Description

technical field [0001] The invention belongs to the technical field of water treatment, and relates to a purification device and a purification method for washing water of a methanol-to-olefins device. Background technique [0002] Methanol to Olefins, referred to as MTO (Methanol to Olefins), refers to the process of preparing low-carbon olefins through catalytic reactions using methanol as a raw material. The reaction is generally realized by a fluidized bed reactor, and the currently used catalyst is SAPO-34 molecular sieve. Part of the catalyst particles will be entrained in the reaction product gas, and some unreacted methanol, aldehydes, ethers, alkanes, aromatics and other by-products will enter the water system together. After the product gas is cooled and washed by the quenching tower, most of the catalyst particles remain in the quenching water, while organic by-products and a small amount of fine catalyst powder enter the washing tower and remain in the washing w...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C02F1/28C02F1/00C02F1/40C02F103/36
CPCC02F1/001C02F1/28C02F1/40C02F2303/16C02F2103/36Y02P30/20Y02P30/40
Inventor 陈建琦钱柯伟吕文杰马世浩汪华林李军潘风光
Owner EAST CHINA UNIV OF SCI & TECH
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