WO2023115862A1 - 一种耦合嵌入式热水解的污泥与餐厨协同消化工艺 - Google Patents

一种耦合嵌入式热水解的污泥与餐厨协同消化工艺 Download PDF

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WO2023115862A1
WO2023115862A1 PCT/CN2022/101091 CN2022101091W WO2023115862A1 WO 2023115862 A1 WO2023115862 A1 WO 2023115862A1 CN 2022101091 W CN2022101091 W CN 2022101091W WO 2023115862 A1 WO2023115862 A1 WO 2023115862A1
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sludge
treatment
thermal hydrolysis
kitchen
collaborative
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PCT/CN2022/101091
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French (fr)
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王佳伟
齐利格娃
李伟
任征然
文洋
孙冀垆
刘垚
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北京城市排水集团有限责任公司
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/30—Destroying solid waste or transforming solid waste into something useful or harmless involving mechanical treatment
    • B09B3/35—Shredding, crushing or cutting
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/60—Biochemical treatment, e.g. by using enzymes
    • B09B3/65—Anaerobic treatment
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/02—Biological treatment
    • C02F11/04—Anaerobic treatment; Production of methane by such processes
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/122—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering using filter presses
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/121—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering
    • C02F11/127—Treatment of sludge; Devices therefor by de-watering, drying or thickening by mechanical de-watering by centrifugation
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
    • C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
    • C02F11/147—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents using organic substances
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F11/00—Treatment of sludge; Devices therefor
    • C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00—Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/06—Natural gas; Synthetic natural gas obtained by processes not covered by C10G, C10K3/02 or C10K3/04
    • C10L3/08—Production of synthetic natural gas
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B2101/00—Type of solid waste
    • B09B2101/70—Kitchen refuse; Food waste
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • the invention belongs to the technical field of sludge treatment, and more specifically relates to a sludge and kitchen collaborative digestion process coupled with embedded thermal hydrolysis.
  • the "thermal hydrolysis + anaerobic fermentation" process line has made the sludge reduction rate reach 70%, the gas production rate in the anaerobic digestion process has increased significantly, and the quality of sludge as a resource utilization product has been greatly improved.
  • some sludges have low organic matter content.
  • the amount of biogas produced in the anaerobic digestion process still cannot sufficiently compensate the energy consumption of the sewage treatment plant, and the low carbon-nitrogen ratio in the sludge,
  • the pH and ammonia nitrogen concentration are high, which is prone to the risk of ammonia inhibition.
  • Food waste is characterized by high moisture (about 80% to 85%), high organic matter and high salt content, which is easy to rot and deteriorate, breeds germs, and also contains nitrogen, phosphorus, potassium, calcium and various trace elements.
  • One of the problems with the anaerobic digestion process of waste is that the hydrolysis rate is too fast and the pH value is low. It can be seen that sludge and kitchen have good complementarity in material properties.
  • thermal hydrolysis One of the main functions of thermal hydrolysis is to break the hydrolysis rate-limiting barrier of anaerobic digestion of sludge and significantly increase the biogas yield in the anaerobic digestion process.
  • thermal hydrolysis can increase the biogas yield by 100% ⁇ 200%; however, for solid organic matter with good anaerobic digestion performance such as primary sludge, kitchen waste, etc., the effect of thermal hydrolysis on the biogas yield is not obvious, and even due to the caramelization and aesthetics of the thermal hydrolysis process The occurrence of reactions such as Rad led to a decrease in biogas yield.
  • the purpose of the present invention is to address the defects of the prior art, and propose a process for synergistic digestion of sludge and kitchen coupled with embedded thermal hydrolysis.
  • the invention utilizes the good complementarity between sludge and kitchen in terms of material properties, optimizes the configuration of thermal hydrolysis in the advanced anaerobic digestion process system, and then alleviates the risk of sludge digestion ammonia inhibition; at the same time, it reduces the amount of refractory substances Generate, save investment in thermal hydrolysis; increase biogas yield, increase biogas production, realize energy self-sufficiency in sewage treatment plants based on the centralized treatment mode of regional organic solid waste, and ensure that organic nutrient soil meets relevant application standards.
  • the present invention provides a sludge and kitchen collaborative digestion process coupled with embedded thermal hydrolysis, the collaborative digestion process includes:
  • step S2 Mix the pulped kitchen waste in step S1 with the primary sludge after desanding and slag removal, and perform a first-level synergistic anaerobic digestion treatment to obtain a first-level synergistic anaerobic digestion product and first biogas;
  • step S9 Send the first filtrate obtained in step S3 and the second filtrate obtained in step S8 to the anammox unit for denitrification treatment, and return the anammox effluent to the water area of the sewage treatment plant for treatment;
  • the screening and pulping treatment includes: sequentially crushing and pulping the food waste from which plastics and/or metals have been removed.
  • the sand and slag obtained by performing sand and slag removal on the primary sludge are transported outside for disposal.
  • the water content of the mixed material of the pulped kitchen waste and the primary sludge after desanding and deslagging is in the range of 94% to 95%.
  • the operating temperature range of the oxygen digestion treatment is 37-55° C.
  • the hydraulic retention time range of the first-stage coordinated anaerobic digestion treatment is 15-20 days.
  • step S2 the pulped food waste is directly mixed with the primary sludge after desanding and slag removal without oil-water separation, and the mixed material is pumped into the first-stage synergistic anaerobic reactor for anaerobic Digestion yields first-order synergistic anaerobic digestion products and first biogas.
  • step S3 the first-stage synergistic anaerobic digestion product is mixed with the remaining activated sludge in the dewatering sludge storage tank, and polyacrylamide is added to the dewatering sludge storage tank, Obtaining a pre-dehydration mixture; pumping the pre-dehydration mixture into a centrifugal sludge dewatering machine for centrifugal dehydration treatment to obtain the dewatered cake and the first filtrate.
  • the moisture content of the dewatered cake is controlled at 75%-80%.
  • the polyacrylamide is used in an amount of 3 ⁇ ⁇ 5 ⁇ .
  • the reaction pressure of the thermal hydrolysis treatment ranges from 0.6 to 1.0 MPa
  • the reaction temperature ranges from 160° C. to 180° C.
  • the reaction duration ranges from 30 to 60 minutes.
  • the dehydrated cake enters the thermal hydrolysis buffer silo through the plunger pump, and then enters the system for performing the thermal hydrolysis treatment through the screw pump.
  • the thermally hydrolyzed sludge is subjected to sand removal treatment.
  • the operating temperature range of the secondary anaerobic digestion treatment is 37-55°C
  • the hydraulic retention time range of the secondary anaerobic digestion treatment is 12-20d.
  • the first biogas obtained in step S2 and the second biogas obtained in step S7 are sent to the biogas tank for storage and desulfurized by a desulfurization device; then the desulfurized biogas enters the cogeneration unit to produce 12.5 Saturated steam of ⁇ 15 bar is supplied to the system for the thermal hydrolysis treatment.
  • the electric energy produced is given priority to self-use, and the surplus electric energy is supplied externally.
  • step S8 the moisture content of the plate and frame mud cake is controlled below 60%.
  • the digested sludge enters the adjustment tank through a screw pump, and 4 ⁇ -6% of plate and frame chemicals are added for conditioning, and the conditioned sludge enters a plate and frame dehydrator for dehydration treatment.
  • first-level synergistic anaerobic digestion is performed on the easily degradable kitchen waste and primary sludge, making full use of the good complementarity between sludge and kitchen in terms of material properties, optimizing the organic matter ratio and pH, Adjust the carbon-nitrogen ratio of the digestion system to alleviate the risk of sludge digestion ammonia inhibition;
  • thermal hydrolysis is carried out after the first-stage synergistic anaerobic digestion product is mixed and dehydrated with excess sludge, which makes full use of the different effects of thermal hydrolysis on primary sludge and excess sludge, and reduces the amount of refractory substances Generate and optimize thermal hydrolysis configuration to save thermal hydrolysis investment;
  • the technology adopted in the present invention can increase the biogas yield and increase the biogas output, realize the energy self-sufficiency of the sewage treatment plant based on the centralized treatment mode of regional organic solid waste, and ensure that the organic nutrient soil meets the relevant application standards.
  • Fig. 1 shows a schematic flow chart of a sludge and kitchen collaborative digestion process coupled with embedded thermal hydrolysis provided by the present invention.
  • This embodiment provides a collaborative digestion process of sludge and kitchen coupled with embedded thermal hydrolysis, as shown in Figure 1, the collaborative digestion process includes:
  • S1 The food waste from which plastic and/or metal has been removed is sequentially crushed and pulped; the primary sludge is desanded and slag removed, and the sand slag is transported outside for disposal.
  • step S2 The pulped food waste in step S1 is directly mixed with the primary sludge after desanding and slag removal without oil-water separation.
  • the water content of the mixed material ranges from 94% to 95%, and the mixed material is pumped into a
  • the first-level synergistic anaerobic digester is used for anaerobic digestion to obtain the first-level synergistic anaerobic digestion product and the first biogas;
  • the operating temperature of the first-stage coordinated anaerobic digestion treatment is 40° C., and the hydraulic retention time of the first-order coordinated anaerobic digestion treatment is 15 days.
  • the moisture content of the dehydrated cake is controlled at 75% to 80%.
  • the polyacrylamide is used in an amount of 3 ⁇ ⁇ 5 ⁇ .
  • the reaction pressure of the thermal hydrolysis treatment is 0.6 MPa, the reaction temperature is 160° C., and the reaction duration is 30 minutes.
  • the operating temperature of the secondary anaerobic digestion treatment is 40° C., and the hydraulic retention time of the secondary anaerobic digestion treatment is 20 days.
  • the moisture content of the plate and frame mud cake is controlled below 60%.
  • step S9 send the first filtrate obtained in step S3 and the second filtrate obtained in step S8 to the anammox unit for denitrification treatment, and return the anammox effluent to the water area of the sewage treatment plant for treatment.
  • the first biogas obtained in step S2 and the second biogas obtained in step S7 are sent to the biogas tank for storage and desulfurization treatment through a desulfurization device; then the desulfurized biogas enters the cogeneration unit to produce 12.5bar saturated steam supply for all As for the thermal hydrolysis treatment system, in the present invention, the electric energy produced is given priority to self-use, and the surplus electric energy is supplied externally.

Abstract

本发明属于污泥处理技术领域，公开了一种耦合嵌入式热水解的污泥与餐厨协同消化工艺。该协同消化工艺包括：1)餐厨垃圾筛分制浆，初沉污泥除砂除渣；2)餐厨垃圾和初沉污泥混合进行一级协同厌氧消化；3)一级协同厌氧消化产物与剩余活性污泥混合后离心脱水；4)脱水泥饼热水解；5)热水解污泥除砂处理；6)稀释换热；7)二级厌氧消化；8)板框脱水；9)滤液厌氧氨氧化处理；10)泥饼养分复配生产有机营养土。本发明充分利用了污泥与餐厨在物料性质上的良好互补性，优化了热水解配置，减少难降解物质的生成，节省热水解投资；提高了沼气产率和沼气产量，基于区域有机固废的集中处理模式实现了污水处理厂的能源自给。

Description

一种耦合嵌入式热水解的污泥与餐厨协同消化工艺 技术领域
本发明属于污泥处理技术领域，更具体地，涉及一种耦合嵌入式热水解的污泥与餐厨协同消化工艺。
背景技术
“热水解+厌氧发酵”工艺线使得污泥减量化率达到70％，厌氧消化过程产气率大幅增加，并极大提高了污泥作为资源化利用产品的品质。但部分污泥有机质含量较低，经过热水解处理后，其厌氧消化过程产生的沼气量仍然不能对污水处理厂的能量消耗产生足够的抵偿，且污泥中较低的碳氮比，使得污泥在较高有机负荷下进行厌氧消化时，pH和氨氮浓度偏高，容易产生氨抑制的风险。
餐厨垃圾的特点是高水分(约80％～85％)、高有机质和高盐分含量，极易腐烂变质，滋生病菌，同时还含氮、磷、钾、钙及各种微量元素，餐厨垃圾厌氧消化过程的问题之一是水解速度太快导致pH值偏低。可见，污泥与餐厨在物料性质上具有良好的互补性。
热水解的主要作用之一是打破污泥厌氧消化的水解限速屏障，显著提高厌氧消化过程的沼气产率，对于剩余活性污泥，热水解使其沼气产率提高100％～200％；然而，对于本身厌氧消化性能良好的固体有机物如初沉污泥、餐厨垃圾等，热水解对沼气产率的提升作用并不明显，甚至会由于热水解过程的焦糖化和美拉德等反应的发生导致沼气产率下降。
综上，针对现有技术存在的技术问题：(1)现有的“热水解+厌氧消化”工艺产生的沼气量仍然不能对污水处理厂的能量消耗产生足够的抵偿；(2)现有的“热水解+厌氧消化”工艺，由于污泥碳氮比较低，较高有机负荷下进 行厌氧消化时，pH和氨氮浓度偏高，容易产生氨抑制的风险；(3)现有的“热水解+厌氧消化”工艺忽略了热水解对初沉污泥和剩余污泥作用效果的不同，增加了难降解物质的生成，浪费了热水解反应器容积进一步减少的潜力。亟待提出一种新的污泥消化方法，针对物料自身的厌氧消化性能优化热水解在高级厌氧消化工艺系统中的配置。
发明内容
本发明的目的是针对现有技术的缺陷，提出一种耦合嵌入式热水解的污泥与餐厨协同消化工艺。本发明利用了污泥与餐厨在物料性质上的良好互补性，优化了热水解在高级厌氧消化工艺系统中的配置，进而缓解了污泥消化氨抑制风险；同时减少难降解物质的生成，节省热水解投资；提高沼气产率、增加沼气产量，基于区域有机固废的集中处理模式实现污水处理厂的能源自给，并保证有机营养土满足相关施用标准。
为了实现上述目的，本发明提供了一种耦合嵌入式热水解的污泥与餐厨协同消化工艺，该协同消化工艺包括：
S1：将餐厨垃圾进行筛分制浆处理；将初沉污泥进行除砂除渣处理；
S2：将步骤S1的已制浆的餐厨垃圾和除砂除渣后的初沉污泥混合并进行一级协同厌氧消化处理，得到一级协同厌氧消化产物和第一沼气；
S3：将所述一级协同厌氧消化产物与来自污水处理厂水区的剩余活性污泥混合并进行离心脱水处理，得到脱水泥饼和第一滤液；
S4：将所述脱水泥饼进行热水解处理，得到热水解污泥；
S5：将所述热水解污泥进行除砂处理；
S6：将经除砂处理的热水解污泥进行稀释换热，至热水解污泥的含水率为88％～92％，温度为37℃～55℃；
S7：将经稀释换热的热水解污泥进行二级厌氧消化处理，得到消化污泥和第二沼气；
S8：将所述消化污泥进行板框脱水处理，得到板框泥饼和第二滤液；
S9：将步骤S3得到的第一滤液和步骤S8得到的第二滤液送入厌氧氨氧化单元进行脱氮处理，得到厌氧氨氧化出水回流至所述污水处理厂水区进行处理；
S10：将所述板框泥饼通过养分复配生产有机营养土。
根据本发明，优选地，在步骤S1中，所述筛分制浆处理包括：将去除塑料和/或金属的餐厨垃圾依次进行破碎和制浆处理。
在本发明中，将初沉污泥进行除砂除渣处理得到的砂渣外运处置。
根据本发明，优选地，在步骤S2中，已制浆的餐厨垃圾和除砂除渣后的初沉污泥的混合物料的含水率范围为94％～95％，所述一级协同厌氧消化处理的运行温度范围为37～55℃，所述一级协同厌氧消化处理的水力停留时间范围为15～20d。
在本发明中，在步骤S2中，将已制浆的餐厨垃圾无需油水分离，直接和除砂除渣后的初沉污泥混合，混合物料泵入一级协同厌氧反应器进行厌氧消化得到一级协同厌氧消化产物和第一沼气。
根据本发明，优选地，在步骤S3中，将所述一级协同厌氧消化产物与剩余活性污泥在脱水贮泥池中进行混合，并向所述脱水贮泥池中加入聚丙烯酰胺，得到预脱水混合物；将所述预脱水混合物泵入离心式污泥脱水机进行离心脱水处理，得到所述脱水泥饼和第一滤液。
根据本发明，优选地，所述脱水泥饼含水率控制在75％～80％。
根据本发明，优选地，以所述预脱水混合物的干固的总重量计，所述聚丙烯酰胺的用量为3‰～5‰。
根据本发明，优选地，在步骤S4中，所述热水解处理的反应压力范围为0.6～1.0MPa，反应温度范围为160℃～180℃，反应持续时间范围为30～60min。
在本发明中，将脱水泥饼通过柱塞泵进入热水解缓冲料仓，随后通过 螺杆泵进入进行所述热水解处理的系统。将所述热水解污泥进行除砂处理。
根据本发明，优选地，在步骤S7中，所述二级厌氧消化处理的运行温度范围为37～55℃，所述二级厌氧消化处理的水力停留时间范围为12～20d。
根据本发明，优选地，将步骤S2得到的第一沼气和步骤S7得到的第二沼气送入沼气柜进行储存并通过脱硫装置进行脱硫处理；然后将脱硫后的沼气进入热电联产单元生产12.5～15bar的饱和蒸汽供给进行所述热水解处理的系统，在本发明中，生产的电能优先自用，富余电能外供。
根据本发明，优选地，在步骤S8中，所述板框泥饼含水率控制在60％以下。
在本发明中，将所述消化污泥通过螺杆泵进入调节池，并投加4‰～6％的板框药剂进行调理，将调理好的污泥进入板框脱水机进行脱水处理。
在本发明中，将所述板框泥饼破碎后根据施用地的需求进行养分复配，按照本领域公知的相关规范进行施用。
本发明的技术方案的有益效果如下：
1.本发明中，将易降解的餐厨垃圾与初沉污泥先进行一级协同厌氧消化，充分利用污泥与餐厨在物料性质上的良好互补性，优化有机物配比及pH，调节消化体系碳氮比，缓解污泥消化氨抑制风险；
2.本发明中，一级协同厌氧消化产物与剩余污泥混合脱水后进行热水解，充分利用了热水解对初沉污泥和剩余污泥的作用效果不同，减少难降解物质的生成，并优化热水解配置，节省热水解投资；
3.本发明采用的工艺，可提高沼气产率、增加沼气产量，基于区域有机固废的集中处理模式实现污水处理厂的能源自给，并保证有机营养土满足相关施用标准。
本发明的其它特征和优点将在随后具体实施方式部分予以详细说明。
附图说明
通过结合附图对本发明示例性实施方式进行更详细的描述，本发明的上述以及其它目的、特征和优势将变得更加明显，其中，在本发明示例性实施方式中，相同的参考标号通常代表相同部件。
图1示出了本发明提供的一种耦合嵌入式热水解的污泥与餐厨协同消化工艺的流程示意图。
具体实施方式
下面将更详细地描述本发明的优选实施方式。虽然以下描述了本发明的优选实施方式，然而应该理解，可以以各种形式实现本发明而不应被这里阐述的实施方式所限制。相反，提供这些实施方式是为了使本发明更加透彻和完整，并且能够将本发明的范围完整地传达给本领域的技术人员。
实施例1
本实施例提供一种耦合嵌入式热水解的污泥与餐厨协同消化工艺，如图1所示，该协同消化工艺包括：
S1：将去除塑料和/或金属的餐厨垃圾依次进行破碎和制浆处理；将初沉污泥进行除砂除渣处理，砂渣外运处置。
S2：将步骤S1的已制浆的餐厨垃圾无需油水分离，直接和除砂除渣后的初沉污泥混合，混合物料的含水率范围为94％～95％，将混合物料泵入一级协同厌氧反应器进行厌氧消化得到一级协同厌氧消化产物和第一沼气；
所述一级协同厌氧消化处理的运行温度为40℃，所述一级协同厌氧消化处理的水力停留时间为15d。
S3：将所述一级协同厌氧消化产物与剩余活性污泥在脱水贮泥池中进行混合，并向所述脱水贮泥池中加入聚丙烯酰胺，得到预脱水混合物；将所述预脱水混合物泵入离心式污泥脱水机进行离心脱水处理，得到所述脱水泥饼和第一滤液；
所述脱水泥饼含水率控制在75％～80％。
以所述预脱水混合物的干固的总重量计，所述聚丙烯酰胺的用量为3‰～5‰。
S4：将脱水泥饼通过柱塞泵进入热水解缓冲料仓，随后通过螺杆泵进入进行所述热水解处理的系统进行热水解处理，得到热水解污泥；
所述热水解处理的反应压力为0.6MPa，反应温度为160℃，反应持续时间为30min。
S5：将所述热水解污泥进行除砂处理。
S6：将经除砂处理的热水解污泥进行稀释换热，至热水解污泥的含水率为88％～92％，温度为40℃。
S7：将经稀释换热的热水解污泥进行二级厌氧消化处理，得到消化污泥和第二沼气；
所述二级厌氧消化处理的运行温度为40℃，所述二级厌氧消化处理的水力停留时间为20d。
S8：将所述消化污泥通过螺杆泵进入调节池，并投加3.5％的C50板框药剂搅拌10min后加入4‰的C70板框药剂进行调理，将调理好的污泥进入板框脱水机进行脱水处理，得到板框泥饼和第二滤液；
所述板框泥饼含水率控制在60％以下。
S9：将步骤S3得到的第一滤液和步骤S8得到的第二滤液送入厌氧氨氧化单元进行脱氮处理，得到厌氧氨氧化出水回流至所述污水处理厂水区进行处理。
S10：将所述板框泥饼破碎后根据施用地的需求进行养分复配，按照本领域公知的相关规范进行施用。
将步骤S2得到的第一沼气和步骤S7得到的第二沼气送入沼气柜进行储存并通过脱硫装置进行脱硫处理；然后将脱硫后的沼气进入热电联产单元生产12.5bar的饱和蒸汽供给进行所述热水解处理的系统，在本发明中，生 产的电能优先自用，富余电能外供。
以上已经描述了本发明的各实施例，上述说明是示例性的，并非穷尽性的，并且也不限于所披露的各实施例。在不偏离所说明的各实施例的范围和精神的情况下，对于本技术领域的普通技术人员来说许多修改和变更都是显而易见的。

Claims (10)

  1. 一种耦合嵌入式热水解的污泥与餐厨协同消化工艺，其特征在于，该协同消化工艺包括：
    S1：将餐厨垃圾进行筛分制浆处理；将初沉污泥进行除砂除渣处理；
    S2：将步骤S1的已制浆的餐厨垃圾和除砂除渣后的初沉污泥混合并进行一级协同厌氧消化处理，得到一级协同厌氧消化产物和第一沼气；
    S3：将所述一级协同厌氧消化产物与来自污水处理厂水区的剩余活性污泥混合并进行离心脱水处理，得到脱水泥饼和第一滤液；
    S4：将所述脱水泥饼进行热水解处理，得到热水解污泥；
    S5：将所述热水解污泥进行除砂处理；
    S6：将经除砂处理的热水解污泥进行稀释换热，至热水解污泥的含水率为88％～92％，温度为37℃～55℃；
    S7：将经稀释换热的热水解污泥进行二级厌氧消化处理，得到消化污泥和第二沼气；
    S8：将所述消化污泥进行板框脱水处理，得到板框泥饼和第二滤液；
    S9：将步骤S3得到的第一滤液和步骤S8得到的第二滤液送入厌氧氨氧化单元进行脱氮处理，得到厌氧氨氧化出水回流至所述污水处理厂水区进行处理；
    S10：将所述板框泥饼通过养分复配生产有机营养土。
  2. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S1中，所述筛分制浆处理包括：将去除塑料和/或金属的餐厨垃圾依次进行破碎和制浆处理。
  3. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S2中，已制浆的餐厨垃圾和除砂除渣后的初沉污泥的混 合物料的含水率范围为94％～95％，所述一级协同厌氧消化处理的运行温度范围为37～55℃，所述一级协同厌氧消化处理的水力停留时间范围为15～20d。
  4. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S3中，将所述一级协同厌氧消化产物与剩余活性污泥在脱水贮泥池中进行混合，并向所述脱水贮泥池中加入聚丙烯酰胺，得到预脱水混合物；将所述预脱水混合物泵入离心式污泥脱水机进行离心脱水处理，得到所述脱水泥饼和第一滤液。
  5. 根据权利要求4所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，所述脱水泥饼含水率控制在75％～80％。
  6. 根据权利要求4所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，以所述预脱水混合物的干固的总重量计，所述聚丙烯酰胺的用量为3‰～5‰。
  7. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S4中，所述热水解处理的反应压力范围为0.6～1.0MPa，反应温度范围为160℃～180℃，反应持续时间范围为30～60min。
  8. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S7中，所述二级厌氧消化处理的运行温度范围为37～55℃，所述二级厌氧消化处理的水力停留时间范围为12～20d。
  9. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工 艺，其中，将步骤S2得到的第一沼气和步骤S7得到的第二沼气送入沼气柜进行储存并通过脱硫装置进行脱硫处理；然后将脱硫后的沼气进入热电联产单元生产12.5～15bar的饱和蒸汽供给进行所述热水解处理的系统。
  10. 根据权利要求1所述的耦合嵌入式热水解的污泥与餐厨协同消化工艺，其中，在步骤S8中，所述板框泥饼含水率控制在60％以下。
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Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103553289A (zh) * 2013-10-23 2014-02-05 同济大学 一种多级厌氧消化强化产气的方法
CN106676138A (zh) * 2017-01-19 2017-05-17 广西博世科环保科技股份有限公司 强化多原料两级全混厌氧消化产沼气的方法
US20180050941A1 (en) * 2016-08-22 2018-02-22 Anaergia Inc. Two stage anaerobic digestion with intermediate hydrolysis
CN109354185A (zh) * 2018-11-26 2019-02-19 同济大学 一种污泥热水解厌氧消化沼液的组合脱氮方法及装置
CN208995479U (zh) * 2018-10-05 2019-06-18 北京汇园生态科技有限公司 一种城市有机垃圾处理系统
CN110015828A (zh) * 2018-03-30 2019-07-16 长沙理工大学 活性污泥的两级厌氧消化处理方法及处理系统
CN209193764U (zh) * 2018-10-05 2019-08-02 北京汇园生态科技有限公司 一种有机垃圾处理系统
US20210323888A1 (en) * 2020-04-20 2021-10-21 Tongji University Method for sludge dewatering using kitchen waste to synergistically enhance anaerobic biological acidification and low-temperature thermal hydrolysis of excess sludge
CN114262137A (zh) * 2021-12-24 2022-04-01 北京城市排水集团有限责任公司 一种耦合嵌入式热水解的污泥与餐厨协同消化工艺

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5687929B2 (ja) * 2011-03-17 2015-03-25 三菱化工機株式会社 有機性廃棄物処理方法および有機性廃棄物処理装置
CN206069664U (zh) * 2016-08-30 2017-04-05 四川深蓝环保科技有限公司 餐厨垃圾及污泥二合一处理系统
CN106698879A (zh) * 2016-12-12 2017-05-24 广州恒德环保科技有限公司 一种餐厨垃圾处理方法
CN110116126B (zh) * 2019-05-22 2020-05-19 安徽省通源环境节能股份有限公司 一种餐厨垃圾、污泥协同处置方法

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103553289A (zh) * 2013-10-23 2014-02-05 同济大学 一种多级厌氧消化强化产气的方法
US20180050941A1 (en) * 2016-08-22 2018-02-22 Anaergia Inc. Two stage anaerobic digestion with intermediate hydrolysis
CN106676138A (zh) * 2017-01-19 2017-05-17 广西博世科环保科技股份有限公司 强化多原料两级全混厌氧消化产沼气的方法
CN110015828A (zh) * 2018-03-30 2019-07-16 长沙理工大学 活性污泥的两级厌氧消化处理方法及处理系统
CN208995479U (zh) * 2018-10-05 2019-06-18 北京汇园生态科技有限公司 一种城市有机垃圾处理系统
CN209193764U (zh) * 2018-10-05 2019-08-02 北京汇园生态科技有限公司 一种有机垃圾处理系统
CN109354185A (zh) * 2018-11-26 2019-02-19 同济大学 一种污泥热水解厌氧消化沼液的组合脱氮方法及装置
US20210323888A1 (en) * 2020-04-20 2021-10-21 Tongji University Method for sludge dewatering using kitchen waste to synergistically enhance anaerobic biological acidification and low-temperature thermal hydrolysis of excess sludge
CN114262137A (zh) * 2021-12-24 2022-04-01 北京城市排水集团有限责任公司 一种耦合嵌入式热水解的污泥与餐厨协同消化工艺

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