Gasification system and process for high-efficiency recovery of heat energy via wet ash cooling method
A heat recovery and gasification system technology, applied in the gasification process, chemical industry, petroleum industry, etc., can solve the problems of low recovery and utilization efficiency of sensible heat, complex fly ash removal system, short service life, etc., to achieve Guaranteed long-term stable operation, reduced waste water discharge, and high heat recovery efficiency
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Embodiment 1
[0042] This embodiment provides a wet cold ash type high-efficiency heat energy recovery gasification system, which can be used to prepare downstream chemical products, such as figure 1 As shown, the gasification system includes: a gasification furnace 1 for preparing syngas and performing radiation heat exchange, and the gasification furnace 1 includes a gasification chamber 11 and a radiation heat exchange chamber 12, described in this embodiment The gasification furnace 1 adopts a structure in which the gasification chamber 11 and the radiation heat exchange chamber 12 are integrated, such as figure 2 shown.
[0043] The radiation heat exchange chamber 12 described in this embodiment is arranged below the gasification chamber 11, and a raw material inlet 111 is arranged on the top of the gasification chamber 11. The radiation heat exchange chamber 12 includes an internal Cylinder 126 and outer cylinder 124; the inner and outer wall surfaces of the inner cylinder 126 and t...
Embodiment 2
[0063] This embodiment provides a high-efficiency heat energy recovery gasification system, which can be used to prepare downstream fuel gas or IGCC products, such as Figure 5 As shown, the gasification system includes:
[0064] A gasifier 1 for preparing syngas and performing radiative heat exchange, the gasifier 1 described in this embodiment is the same as that in Embodiment 1.
[0065] Gas-solid separation and wet ash cooling device 2, the gas-solid separation and wet ash cooling device 2 includes wet ash cooling equipment in which a cyclone separator 21 communicates with the dry ash outlet of the cyclone separator. The wet cooling ash equipment is a wet cooling tank 22, and a spraying device is arranged in the wet cooling tank 22, which is used for spraying cooling liquid to cool down the high-temperature dry ash, and the sprayed cooling Black water is formed after the liquid is mixed with dry ash, and a black water discharge port is arranged on the wet cooling tank 22 ...
experiment example
[0076] The process system in this application can effectively recover the high-temperature heat energy in the synthesis gas. The output of (CO+H2) is 100,000Nm3 / h, the average reaction temperature of the gasification chamber 11 is 1400°C, and the annual operation time is 8000 hours. The output value in basic estimation embodiment 1 and embodiment 2, the result is as shown in the table below:
[0077]
[0078] Note: The price of 10MPag power steam is calculated at 120 yuan / ton, and the price of circulating cooling water is calculated at 0.1 yuan / ton.
[0079] It can be seen from the above table that the ratio of high-temperature sensible heat in the syngas converted to 10.0 MPag grade power steam can reach 50-70%. This process can produce 10.0MPag grade power steam 50-65 tons / h (the fuel gas or IGCC product product scheme is 70-80 tons / h), and the annual output value is 48-62.4 million yuan (the fuel gas or IGCC product product scheme is 48-62.4 million yuan) 67.20-76.8 mil...
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