化工进展 ›› 2023, Vol. 42 ›› Issue (2): 985-999.DOI: 10.16085/j.issn.1000-6613.2022-0760
收稿日期:
2022-04-26
修回日期:
2022-06-21
出版日期:
2023-02-25
发布日期:
2023-03-13
通讯作者:
谭厚章
作者简介:
王毅斌(1990—),男,副研究员,研究方向为固废利用。E-mail:ybwang6639@mail.xjtu.edu.cn。
基金资助:
WANG Yibin(), FENG Jingwu, TAN Houzhang(), LI Liangyu
Received:
2022-04-26
Revised:
2022-06-21
Online:
2023-02-25
Published:
2023-03-13
Contact:
TAN Houzhang
摘要:
我国市政污泥产量即将突破9000万吨,无害化、减量化和资源化处置非常迫切。干污泥中磷元素含量占2%~6%,回收磷资源的潜力巨大,其可以减少有限磷矿的消耗,缓解全球磷危机。本文从污泥处置技术、脱水污泥中磷元素含量与形态、热化学(热解、焚烧、气化和水热炭化)处理中磷元素形态转变、污泥灰/炭中磷元素回收方法和含磷矿物的植物可吸收性五个方面对污泥中磷资源回收与利用展开论述,详细对比分析了温度、添加剂成分、掺混燃料种类等因素对热处理产物中磷元素形态的影响。最后,归纳分析了热处理产物中磷元素的回收工艺和不同因素的影响以及含磷矿物的植物可吸收性,以期为我国未来污泥资源化利用提供参考。
中图分类号:
王毅斌, 冯敬武, 谭厚章, 李良钰. 市政污泥热化学处置中磷元素形态转变与回收利用研究进展[J]. 化工进展, 2023, 42(2): 985-999.
WANG Yibin, FENG Jingwu, TAN Houzhang, LI Liangyu. Research progress on phosphorus speciation transformation and recovery during thermal chemical conversion of municipal sewage sludge[J]. Chemical Industry and Engineering Progress, 2023, 42(2): 985-999.
城市 | 日产量(含水率80%)/t·d-1 | 污泥处置技术路线 | 参考文献 |
---|---|---|---|
广州市 | 约3313.97 | 浓缩+深度机械脱水+热干化+建材利用 | [ |
北京市 | 6588~7684 | 中心城区以厌氧消化为主,周边城区以好氧发酵为主,多种工艺辅助。土地利用为主,建材利用为辅 | [ |
上海市 | 4200 | 以焚烧为主,土地利用为辅,卫生填埋应急 | [ |
武汉市 | 约1479.7 | 板框脱水+水泥/石灰炉窑混烧,建材利用为主,土地利用为辅,混合填埋保底 | [ |
重庆市 | 约3191.59 | 水泥炉窑协同处置,建材利用 | [ |
深圳市 | 5323 | 板框脱水+低温干化、外运处置 | [ |
昆明市 | 1059 | 土地利用和建材利用并行,填埋处置应急 | [ |
表1 我国不同城市污泥的处置技术路线
城市 | 日产量(含水率80%)/t·d-1 | 污泥处置技术路线 | 参考文献 |
---|---|---|---|
广州市 | 约3313.97 | 浓缩+深度机械脱水+热干化+建材利用 | [ |
北京市 | 6588~7684 | 中心城区以厌氧消化为主,周边城区以好氧发酵为主,多种工艺辅助。土地利用为主,建材利用为辅 | [ |
上海市 | 4200 | 以焚烧为主,土地利用为辅,卫生填埋应急 | [ |
武汉市 | 约1479.7 | 板框脱水+水泥/石灰炉窑混烧,建材利用为主,土地利用为辅,混合填埋保底 | [ |
重庆市 | 约3191.59 | 水泥炉窑协同处置,建材利用 | [ |
深圳市 | 5323 | 板框脱水+低温干化、外运处置 | [ |
昆明市 | 1059 | 土地利用和建材利用并行,填埋处置应急 | [ |
材料 | P2O5质量分数/% | 单质P(干基)质量分数/% | 备注 |
---|---|---|---|
污泥 | — | 2~6 | 浙江嘉兴污泥(5.8%)[ 上海竹园干污泥(2.14%)[ 0.2~5.5(德国)[ |
污泥灰 (焚烧) | 15.6~36[ (焚烧温度820~890℃) | 3.6~13.3 | 850℃<焚烧温度<950℃[ 4.8%/5.7%(英国)[ 3.6%~13.3%(德国焚烧灰中磷元素平均值9%)[ |
污泥炭 (热解) | — | 5~10.6 | 5.6%(西班牙)热解温度850℃[ 5.35%~7.08%热解温度300~500℃[ 9.99%~10.59%热解温度500℃/650℃/800℃[ |
污泥灰 (气化) | — | 5.1~14.9 | 气化温度850~950℃[ |
中国磷矿 | 33.8[ 我国磷矿中P2O5平均值为16.85[ | 7.4(平均值)[ | |
埃及磷矿 | 28.5[ | — | |
摩洛哥磷矿 | 34.0[ | — | |
多哥磷矿 | 35.5[ | — |
表2 不同热化学处理后污泥炭/灰与磷矿中磷元素水平的对比
材料 | P2O5质量分数/% | 单质P(干基)质量分数/% | 备注 |
---|---|---|---|
污泥 | — | 2~6 | 浙江嘉兴污泥(5.8%)[ 上海竹园干污泥(2.14%)[ 0.2~5.5(德国)[ |
污泥灰 (焚烧) | 15.6~36[ (焚烧温度820~890℃) | 3.6~13.3 | 850℃<焚烧温度<950℃[ 4.8%/5.7%(英国)[ 3.6%~13.3%(德国焚烧灰中磷元素平均值9%)[ |
污泥炭 (热解) | — | 5~10.6 | 5.6%(西班牙)热解温度850℃[ 5.35%~7.08%热解温度300~500℃[ 9.99%~10.59%热解温度500℃/650℃/800℃[ |
污泥灰 (气化) | — | 5.1~14.9 | 气化温度850~950℃[ |
中国磷矿 | 33.8[ 我国磷矿中P2O5平均值为16.85[ | 7.4(平均值)[ | |
埃及磷矿 | 28.5[ | — | |
摩洛哥磷矿 | 34.0[ | — | |
多哥磷矿 | 35.5[ | — |
磷酸盐 | 熔点/℃ | 参考文献 |
---|---|---|
CaNaPO4–Ca3(PO4)2(β) | 980 | [ |
Ca3(PO4)2–CaMg(SiO3)2 | 1300±5 | [ |
Ca3(PO4)2–Mg3(PO4)2 | 1120 | [ |
Ca3(PO4)2 | 1810 | [ |
K3PO4 | 1620 | [ |
Na3PO4 | 1583 | [ |
Mg3(PO4)2 | 1357 | [ |
MgNa4(PO4)2 | 1655 | [ |
AlPO4 | >1800 | [ |
FePO4 | 1208 | [ |
表3 不同磷酸盐的熔点
磷酸盐 | 熔点/℃ | 参考文献 |
---|---|---|
CaNaPO4–Ca3(PO4)2(β) | 980 | [ |
Ca3(PO4)2–CaMg(SiO3)2 | 1300±5 | [ |
Ca3(PO4)2–Mg3(PO4)2 | 1120 | [ |
Ca3(PO4)2 | 1810 | [ |
K3PO4 | 1620 | [ |
Na3PO4 | 1583 | [ |
Mg3(PO4)2 | 1357 | [ |
MgNa4(PO4)2 | 1655 | [ |
AlPO4 | >1800 | [ |
FePO4 | 1208 | [ |
污泥/污泥灰特性 | 工艺 | 磷元素回收效率 | 参考文献 |
---|---|---|---|
日本岐阜,四个污水处理厂采用生物除磷工艺污泥灰700吨/年 包含20%~35% P2O5 | 污泥灰回收磷元素,50~70℃ NaOH溶液浸取1.5h+ 20~50℃ Ca(OH)2沉淀9h,回收形式为羟基磷灰石 | 磷回收率30%~40% 磷肥包含25%~30%柠檬酸溶型P2O5,产量300吨/年 | [ |
瑞士苏黎世,污泥灰30000吨/年,灰中含有大于8%的P | 96%硫酸浸取,32%盐酸溶剂萃取,获得74%磷酸 | 磷回收率>95% | [ |
日本千叶市,污泥焚烧温度820~890℃,十种污泥灰中含有15.6%~36% P2O5 | 添入CaCO3调整污泥灰中CaO含量至45%,1250℃/1300℃焚烧10min,Ca5[(SiO4)(PO4)](PO4) | CaO强化处理污泥灰,提高产物中P2O5的柠檬酸可溶性,利于植物吸收 | [ |
褐色污泥灰,污泥中含有Al(PO3)3、AlPO4、SiP2O7和β-Ca3(PO4)2 | 污泥灰悬浮溶液中鼓入CO2的方式,进一步溶解灰中碱土金属磷酸盐,回收磷酸根的形式 | PO43-接近30mg·L-1 | [ |
西班牙,污泥530℃快速热解生物炭的燃烧灰(600℃/750℃/900℃)和气化灰(820℃) | 采用硫酸和乙二酸进行浸取,燃烧灰浸取所用酸浓度(0.06mol·L-1/0.16mol·L-1/0.53mol·L-1),气化灰浸取酸浓度为0.04mol·L-1 | 磷回收率>90% | [ |
表4 污泥/污泥灰中磷元素回收工艺
污泥/污泥灰特性 | 工艺 | 磷元素回收效率 | 参考文献 |
---|---|---|---|
日本岐阜,四个污水处理厂采用生物除磷工艺污泥灰700吨/年 包含20%~35% P2O5 | 污泥灰回收磷元素,50~70℃ NaOH溶液浸取1.5h+ 20~50℃ Ca(OH)2沉淀9h,回收形式为羟基磷灰石 | 磷回收率30%~40% 磷肥包含25%~30%柠檬酸溶型P2O5,产量300吨/年 | [ |
瑞士苏黎世,污泥灰30000吨/年,灰中含有大于8%的P | 96%硫酸浸取,32%盐酸溶剂萃取,获得74%磷酸 | 磷回收率>95% | [ |
日本千叶市,污泥焚烧温度820~890℃,十种污泥灰中含有15.6%~36% P2O5 | 添入CaCO3调整污泥灰中CaO含量至45%,1250℃/1300℃焚烧10min,Ca5[(SiO4)(PO4)](PO4) | CaO强化处理污泥灰,提高产物中P2O5的柠檬酸可溶性,利于植物吸收 | [ |
褐色污泥灰,污泥中含有Al(PO3)3、AlPO4、SiP2O7和β-Ca3(PO4)2 | 污泥灰悬浮溶液中鼓入CO2的方式,进一步溶解灰中碱土金属磷酸盐,回收磷酸根的形式 | PO43-接近30mg·L-1 | [ |
西班牙,污泥530℃快速热解生物炭的燃烧灰(600℃/750℃/900℃)和气化灰(820℃) | 采用硫酸和乙二酸进行浸取,燃烧灰浸取所用酸浓度(0.06mol·L-1/0.16mol·L-1/0.53mol·L-1),气化灰浸取酸浓度为0.04mol·L-1 | 磷回收率>90% | [ |
物质 | 化学式 | M①/P | 溶度积常数(25℃)lgKsp | 参考文献 |
---|---|---|---|---|
一水磷酸二氢钙 | Ca(H2PO4)2·H2O | 0.5 | -1.14 | [ |
磷酸二氢钙 | Ca(H2PO4)2 | 0.5 | -1.14 | [ |
二水磷酸氢钙 | CaHPO4·2H2O | 1.0 | -6.6 | [ |
磷酸氢钙 | CaHPO4 | 1.0 | -7.03~-6.7 | [ |
α-磷酸三钙 | α-Ca3(PO4)2 | 1.5 | -25.5 | [ |
β-磷酸三钙 | β-Ca3(PO4)2 | 1.5 | -28.9 | [ |
无定形磷酸三钙 | Ca3(PO4)2 | 1.5 | -25.5~-24.8 | [ |
磷酸四钙 | Ca4(PO4)2O | 2.0 | -38.0 | [ |
羟基磷灰石 | Ca5(PO4)3OH | 1.67 | -116.8 | [ |
氟磷灰石 | Ca5(PO4)3F | 1.67 | -60.51~-60 | [ |
氯磷灰石 | Ca5(PO4)3Cl | 1.67 | -53.08 | [ |
磷酸八钙 | Ca8H2(PO4)6·5H2O | 1.33 | -96.6/-46.97 | [ |
羟基磷灰石 | Ca10(PO4)6(OH)2 | 1.67 | -110.2 | [ |
氟磷灰石 | Ca10(PO4)6F2 | 1.67 | -55.9 | [ |
碳酸磷灰石 | Ca10(PO4)6(CO3)2 | 1.67 | -108.3 | [ |
磷镁石 | Mg3(PO4)2 | 1.5 | -27.7② | [ |
镁磷石 | MgHPO4·3H2O | 1.0 | -5.8② | [ |
鸟粪石 | MgNH4PO4·6H2O | 1.0 | -12.7② | [ |
含钾鸟粪石 | MgKPO4·6H2O | 2.0 | -22 | [ |
含钠鸟粪石 | MgNaPO4·6H2O | 2.0 | -11.6 | [ |
白磷钙石 | Ca9Mg(HPO4)(PO4)6 | 1.43 | -115.93~-109.48 | [ |
板磷铝矿 | AlPO4 | 1.0 | -20.0 | [ |
磷酸铝石 | AlPO4·2H2O | 1.0 | -30.5~-28.01 | [ |
磷酸铁 | FePO4 | 1.0 | -24.6~-22.0 | [ |
磷酸亚铁 | Fe3(PO4)2 | 1.5 | -29.88 | [ |
红磷铁矿 | FePO4·2H2O | 1.0 | -35.1~-33.6 | [ |
蓝铁矿 | Fe3(PO4)2·8H2O | 1.5 | -36.0 | [ |
表5 磷酸盐的溶度积常数
物质 | 化学式 | M①/P | 溶度积常数(25℃)lgKsp | 参考文献 |
---|---|---|---|---|
一水磷酸二氢钙 | Ca(H2PO4)2·H2O | 0.5 | -1.14 | [ |
磷酸二氢钙 | Ca(H2PO4)2 | 0.5 | -1.14 | [ |
二水磷酸氢钙 | CaHPO4·2H2O | 1.0 | -6.6 | [ |
磷酸氢钙 | CaHPO4 | 1.0 | -7.03~-6.7 | [ |
α-磷酸三钙 | α-Ca3(PO4)2 | 1.5 | -25.5 | [ |
β-磷酸三钙 | β-Ca3(PO4)2 | 1.5 | -28.9 | [ |
无定形磷酸三钙 | Ca3(PO4)2 | 1.5 | -25.5~-24.8 | [ |
磷酸四钙 | Ca4(PO4)2O | 2.0 | -38.0 | [ |
羟基磷灰石 | Ca5(PO4)3OH | 1.67 | -116.8 | [ |
氟磷灰石 | Ca5(PO4)3F | 1.67 | -60.51~-60 | [ |
氯磷灰石 | Ca5(PO4)3Cl | 1.67 | -53.08 | [ |
磷酸八钙 | Ca8H2(PO4)6·5H2O | 1.33 | -96.6/-46.97 | [ |
羟基磷灰石 | Ca10(PO4)6(OH)2 | 1.67 | -110.2 | [ |
氟磷灰石 | Ca10(PO4)6F2 | 1.67 | -55.9 | [ |
碳酸磷灰石 | Ca10(PO4)6(CO3)2 | 1.67 | -108.3 | [ |
磷镁石 | Mg3(PO4)2 | 1.5 | -27.7② | [ |
镁磷石 | MgHPO4·3H2O | 1.0 | -5.8② | [ |
鸟粪石 | MgNH4PO4·6H2O | 1.0 | -12.7② | [ |
含钾鸟粪石 | MgKPO4·6H2O | 2.0 | -22 | [ |
含钠鸟粪石 | MgNaPO4·6H2O | 2.0 | -11.6 | [ |
白磷钙石 | Ca9Mg(HPO4)(PO4)6 | 1.43 | -115.93~-109.48 | [ |
板磷铝矿 | AlPO4 | 1.0 | -20.0 | [ |
磷酸铝石 | AlPO4·2H2O | 1.0 | -30.5~-28.01 | [ |
磷酸铁 | FePO4 | 1.0 | -24.6~-22.0 | [ |
磷酸亚铁 | Fe3(PO4)2 | 1.5 | -29.88 | [ |
红磷铁矿 | FePO4·2H2O | 1.0 | -35.1~-33.6 | [ |
蓝铁矿 | Fe3(PO4)2·8H2O | 1.5 | -36.0 | [ |
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