A process and device for purifying h2s in industrial tail gas
A chemical tail gas and process technology, applied in chemical instruments and methods, hydrogen sulfide, inorganic chemistry, etc., can solve the problems of hydrogen sulfide gas loss, low hydrogen sulfide concentration, large loss, etc., to achieve improved utilization, environmental friendliness, and safety sex high effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0027] like figure 1 As shown, the feed gas is the hydrogen sulfide tail gas of natural gas NHD desulfurization process, containing 20% hydrogen sulfide, 56% carbon dioxide, 9.5% hydrocarbons, water and other trace components of the feed gas:
[0028] A method for purifying H in industrial tail gas 2 The process of S, comprising the following steps:
[0029] S1, after filtering the feed gas, combine with the H from the top of the deheavy hydrocarbon tower 10 2 The mixed gas of S and propane exchanges heat in the raw material heat exchanger 1, pressurizes it to 1.5-5.0 MPa with the raw material compressor 2, and sends it to the raw material gas drying system 3 for drying and dehydration;
[0030] S2, pressurized and dried feed gas in step S1 and CO-enriched gas from the top of decarbonization tower 5 2 After exchanging heat in the gas-to-gas heat exchanger 4, the gas is sent to the decarbonization tower 5 for rectification, and the CO-enriched gas is separated. 2 Componen...
Embodiment 2
[0043] The raw material gas is the hydrogen sulfide tail gas of the low-temperature methanol washing process of natural gas, containing 13% hydrogen sulfide, 63% carbon dioxide, 9.7% hydrocarbons, and other trace components of the raw gas:
[0044] A method for purifying H in industrial tail gas 2 The process of S, comprising the following steps:
[0045] S1, after filtering the feed gas, combine with the H from the top of the deheavy hydrocarbon tower 10 2 The mixed gas of S and propane is heat-exchanged in the raw material heat exchanger 1, and pressurized to 1.5-5.0 MPa by the raw material compressor 2;
[0046] S2. Combining the raw material gas pressurized in step S1 with the CO-enriched gas from the top of the decarbonization tower 5 2 After exchanging heat in the gas-to-gas heat exchanger 4, the gas is sent to the decarbonization tower 5 for rectification, and the CO-enriched gas is separated. 2 Components with lower boiling points such as gas and nitrogen are separa...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

