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Frontiers of Environmental Science & Engineering

ISSN 2095-2201

ISSN 2095-221X(Online)

CN 10-1013/X

Postal Subscription Code 80-973

2018 Impact Factor: 3.883

Front. Environ. Sci. Eng.    2015, Vol. 9 Issue (2) : 181-189    https://doi.org/10.1007/s11783-014-0698-1
REVIEW ARTICLE
Advanced purification and comprehensive utilization of yellow phosphorous off gas
Ping NING(),Xiangyu WANG
Faculty of Environmental Science and Engineering, Kunming University of Science and Technology, Kunming 650500, China
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Abstract

Yellow phosphorous is an important raw material in the chemical industry. However, during the production of yellow phosphorous, high concentrations of carbon monoxide and other impurities are released. Without appropriate purification and removal, this off gas has potential to cause severe pollution problems once released. Purified yellow phosphorous off gas can be beneficially reused as a raw material in chemical production for synthesis of high value-added chemical reagents. In this paper, the significance of purification and reutilization of yellow phosphorous off gas are explored. The principles, processes, and main characteristics of the technologies for purification and reuse of yellow phosphorus off gas (including technical measurements of impurity reduction, relevant engineering cases, and public acceptance of the technologies) are summarized. In view of the existing problems and scientific development requirements, this paper proposes several recommendations for green production based on the concept of recycle economics. We conclude that advanced purification and comprehensive reutilization can be an effective solution for heavy pollution resulting from yellow phosphorous off gassing.

Keywords yellow phosphorous off gas      purification      comprehensive utilization     
Corresponding Author(s): Ping NING   
Online First Date: 30 April 2014    Issue Date: 13 February 2015
 Cite this article:   
Ping NING,Xiangyu WANG. Advanced purification and comprehensive utilization of yellow phosphorous off gas[J]. Front. Environ. Sci. Eng., 2015, 9(2): 181-189.
 URL:  
https://academic.hep.com.cn/fese/EN/10.1007/s11783-014-0698-1
https://academic.hep.com.cn/fese/EN/Y2015/V9/I2/181
chemical component proportion/(vol%)
CO 85–95
CO2 1–4
H2O ~ 5
H2 1–8
CH4 ~ 0.3
N2 2–5
O2 5000
H2S 800–3000
PH3 500–1300
SO2 ~100
COS ~500
CS2 ~200
Tab.1  Compositions of yellow phosphorous off gas [7]
temperature/°C phosphate content/(g?m-3)
20 0.170
25 0.287
30 0.472
35 0.572
40 0.775
44.1 1.084
Tab.2  Changes of phosphate content with different operation temperatures [10]
Fig.1  Chemicals synthesized by using purified yellow phosphorous off gas [1]
Fig.2  Schematic drawing of synthesis of formic acid by using yellow phosphorous off gas
items cost (10000 CNY)
1 engineering /including: 4977.0
(1) constructional engineering 783.0
(2) equipments 2894.5
(3) installation 1289.5
2 other expense 510.74
3 reserve fund 274.39
4 interest incurred during construction 95.80
5 current fund loan 473.57
total 6331.5
Tab.3  Total investment of the project of synthesizing 30kt methanol by using yellow phosphorous off gas [10]
items annual consumption unit price
1 yellow phosphorous off gas 9000 m3 0.10 CNY·m-3
2 sodium carbonate 45 m3 1500 CNY·t-1
3 ADA solution 150 m3 24000 CNY·t-1
4 dephosphorization catalyst 30 m3 6700 CNY·t-1
5 shifting catalyst 15 m3 11000 CNY·t-1
6 synthesis catalyst 18 m3 23000 CNY·t-1
7 electron 4800 k?W?h 0.35 CNY·(kW?h)-1
8 water 210000 m3 1.2 CNY·m-3
9 water vapor 180 kt 60 CNY·t-1
10 circulating water 6300000 m3 0.2 CNY·m-3
11 soft water 150000 m3 1 CNY·m-3
Tab.4  Total cost of materials, fuel, and energy of synthesizing 30 kiloton methanol by using yellow phosphorous off gas [10]
Fig.3  Schematic of the advanced purification of yellow phosphorous off gas. (1) Water seal; (2) vacuum pump; (3) caustic washing tower; (4) mist eliminator; (5) pump; (6) preheator; (7) reactor; (8) induced fan; (9) cooler; T - thermometer; P - pressure gauge; A - sampling; FD - feed gas; DW - drain water; ST - steam; WW - washing water; CW - cooling water; PG - product gas
Fig.4  Breakthrough curves of (a) PH3 and (b) H2S on AC modified with different impregnants
Fig.5  Purification of yellow phosphorous off gas by temperature swing adsorption and pressure swing adsorption
1 Wang X Q, Ning P, Chen W. Studies on purification of yellow phosphorus off-gas by combined washing, catalytic oxidation, and desulphurization at a pilot scale. Separation and Purification Technology, 2011, 80(3): 519–525
https://doi.org/10.1016/j.seppur.2011.06.006
2 Yang L P, Yi H H, Tang X L, Ning P, Yu Q F, Ye Z Q. Effect of rare earth addition on Cu-Fe/AC adsorbents for phosphine adsorption from yellow phosphorous tail gas. Journal of Rare Earths, 2010, 28: 322–325
https://doi.org/10.1016/S1002-0721(10)60321-3
3 Ning P, Yi H H, Yu Q F, Tang X L, Yang L P, Ye Z Q. Effect of zinc and cerium addition on property of copper-based adsorbents for phosphine adsorption. Journal of Rare Earths, 2010, 28(4): 581–586
https://doi.org/10.1016/S1002-0721(09)60158-7
4 Fan Y P, Hu S Y, Chen D J, Li Y R, Shen J Z. The evolution of phosphorus metabolism model in China. Journal of Cleaner Production, 2009, 17(9): 811–820
https://doi.org/10.1016/j.jclepro.2008.12.007
5 Xiong H, Yang X L, Li X G. Removal of sulfur and phosphorus from tail gas of in yellow phosphorus production by sodium hypochlorite oxidation process, Environmental Protection of Chemical. Industry., 2002, 22(3): 161–164
6 Ning P, Bart H J, Wang X Q, Ma L P, Chen L. Removal of P4, PH3 and H2S from yellow phosphoric tail gas by catalytic oxidation process. Engineering and Science, 2005, 7(6): 27–35
7 Ning P, Wang X Y, Bart H J, Tian S L, Zhang Y, Wang X Q. Removal of phosphorus and sulfur from yellow phosphorous off gas by metal-modified activated carbon. Journal of Cleaner Production, 2011, 19(13): 1547–1552
https://doi.org/10.1016/j.jclepro.2011.05.001
8 Quinn R, Dahl T A, Toseland B A. An evaluation of synthesis gas contaminants as methanol synthesis catalyst poisons. Applied Catalysis A, General, 2004, 272(1–2): 61–68
https://doi.org/10.1016/j.apcata.2004.05.015
9 Sun H, Hankins N P, Azzopardi B J, Hilal N, Almeida C A P. A pilot-plant study of the adsorptive micellar flocculation process: optimum design and operation. Separation and Purification Technology, 2008, 62(2): 273–280
https://doi.org/10.1016/j.seppur.2007.08.013
10 Chen S J. Comprehensive utilization of tail gas from phosphorus furnace. Phosphate and Compound Fertilizer, 2008, 23(1): 45–48 (in Chinese)
11 Ma L P, Ning P, Zhang Y Y, Wang X Q. Experimental and modeling of fixed-bed reactor for yellow phosphorous tail gas purification over impregnated activated carbon. Chemical Engineering Journal, 2008, 137(3): 471–479
https://doi.org/10.1016/j.cej.2007.04.032
12 Wang X Q, Ning P, Shi Y, Jiang M. Adsorption of low concentration phosphine in yellow phosphorus off-gas by impregnated activated carbon. Journal of Hazardous Materials, 2009, 171(1–3): 588–593
https://doi.org/10.1016/j.jhazmat.2009.06.046 pmid: 19656624
13 Danh N T, Teresa J B. Activated carbons with metal containing bentonite binders as adsorbents of hydrogen sulfide. Carbon, 2005, 43(2): 359–367
https://doi.org/10.1016/j.carbon.2004.09.023
14 Gonchamva L V, Clowes S K, Fogg R R, Ermakov A V, Hinch B J. Phosphine adsorption and the production of phosphide phases on Cu (001). Surface Science, 2002, 515(2–3): 553–566
https://doi.org/10.1016/S0039-6028(02)01978-7
15 Xiao Y H, Wang S D, Wu D Y, Yuan Q. Experimental and simulation study of hydrogen sulfide adsorption on impregnated activated carbon under anaerobic conditions. Journal of Hazardous Materials, 2008, 153(3): 1193–1200
https://doi.org/10.1016/j.jhazmat.2007.09.081 pmid: 17976901
16 Wang X Q, Ning P, Jiang M, Li Z Y, Yang Y H. Adsorption of low concentration H2S on impregnated activated carbon. Journal of Wuhan University of Technology, 2008, 30: 37–40
17 Ning P, Wang X Q, Wu M C, Chen L, Chen Y H, Pan K C, Wu Y. Purifying yellow phosphorous tail gas by caustic washing -catalytic oxidation. Chemical Engineering, 2004, 34(5): 61–65
18 Yi H H, Yu Q F, Tang X L, Ning P, Yang L P, Ye Z Q, Song J H. Phosphine adsorption removal from yellow phosphorus tail gas over CuO-ZnO-La2O3/activated carbon. Industrial & Engineering Chemistry Research, 2011, 50(7): 3960–3965
https://doi.org/10.1021/ie101622x
19 Andrey B, Teresa J B. H2S adsorption/oxidation on unmodified activated carbons: importance of prehumidification. Carbon, 2001, 39(15): 2303–2311
https://doi.org/10.1016/S0008-6223(01)00049-5
20 Bandosz T J. On the adsorption/oxidation of hydrogen sulfide on activated carbons at ambient temperatures. Journal of Colloid and Interface Science, 2002, 246(1): 1–20
https://doi.org/10.1006/jcis.2001.7952 pmid: 16290378
21 Li W C, Bai H, Hsu J N, Li S N, Chen C. Metal loaded zeolite adsorbents for phosphine removal. Industrial & Engineering Chemistry Research, 2008, 47(5): 1501–1505
https://doi.org/10.1021/ie071074n
22 Teresa J B. Effect of pore structure and surface chemistry of virgin activated carbons on removal of hydrogen sulfide. Carbon, 1999, 37(3): 483–491
https://doi.org/10.1016/S0008-6223(98)00217-6
23 Huang C C, Chen C H, Chu S M. Effect of moisture on H2S adsorption by copper impregnated activated carbon. Journal of Hazardous Materials, 2006, 136(3): 866–873
https://doi.org/10.1016/j.jhazmat.2006.01.025 pmid: 16497435
24 Itaya Y, Kawahara K, Lee C W, Kobayashi J, Kobayashi N, Hatano S, Mori S. Dry gas cleaning process by adsorption of H2S into activated cokes in gasification of carbon resources. Fuel, 2009, 88(9): 1665–1672
https://doi.org/10.1016/j.fuel.2009.04.005
25 Sakanishi K, Wu Z, Matsumura A, Saito I, Hanaoka T, Minowa T, Tada M, Iwasaki T. Simultaneous removal of H2S and COS using activated carbons and their supported catalysts. Catalysis Today, 2005, 104(1): 94–100
https://doi.org/10.1016/j.cattod.2005.03.060
26 Wang L, Cao B, Wang S D, Quan Y. H2S catalytic oxidation on impregnated activated carbon: Experiment and modeling. Chemical Engineering Journal, 2006, 118(3): 133–139
https://doi.org/10.1016/j.cej.2005.12.021
27 Quintanilla A, Casas J A, Rodriguez J J. Catalytic wet air oxidation of phenol with modified activated carbons and Fe/activated carbon catalysts. Applied Catalysis B: Environmental, 2007, 76(1–2): 135–145
https://doi.org/10.1016/j.apcatb.2007.05.019
28 Xiao Y H, Wang S D, Wu D Y, Yuan Q. Catalytic oxidation of hydrogen sulfide over unmodified and impregnated activated carbon. Separation and Purification Technology, 2008, 59(3): 326–332
https://doi.org/10.1016/j.seppur.2007.07.042
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