Device for on-line selective separation of organic acid from anaerobic digestion liquid

An anaerobic digestion and selective technology, which is applied in anaerobic digestion treatment, separation methods, and separation of dispersed particles, can solve the problems of difficult separation of mixed salt solutions, low product purity, and reactor failure, and achieve the reduction of chemicals Use, wide application scenarios, and avoid toxicity effects

Pending Publication Date: 2021-10-01
TONGJI UNIV
View PDF2 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the main problems faced by anaerobic digestion at present are: unstable methane production stage, low effective utilization rate and utilization value of methane, and inconvenient transportation and storage of methane; methanogenic archaea are extremely sensitive to changes in environmental conditions. It is very easy to cause the accumulation of organic acids, especially volatile fatty acids (Volatile Fatty Acids, VFAs), which will further inhibit the activity of methanogens. In severe cases, the reactor may fail or even need to be restarted
However, the microporous membrane separation method can only allow molecular organic acids to cross the membrane, and the pK of the above fatty acids a Both are around 4.8, the pK of lactic acid a Even as low as 3.8, so it is mostly used in batches by adding acid to the digestive juice to acidify it. Online use requires the digestive juice to maintain a very low pH (<5.5), and a too low pH will reduce microbial activity and lead to a decrease in production rate
[0006] The pH of the digestive juice that is conducive to microbial acid production is neutral or weakly acidic. Under this condition, the main form of the above-mentioned organic acids is the ionic state. Therefore, electrodialysis is an effective way to separate ionic organic acid salts, but the disadvantages are: are other inorganic ions (such as Cl - , CO 3 2- etc.) will cross the ion exchange membrane together, resulting in low product purity, and the further separation difficulty of the mixed salt solution is as follows: [Jones, R.J., Massanet-Nicolau, J., Guwy, A., Premier, G.C., Dinsdale, R.M.,Reilly,M.2015.Removal and recovery of inhibitory volatile fatty acids from mixed acid fermentations by conventional electrodialysis.Bioresource Technology,189,279-284]

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Device for on-line selective separation of organic acid from anaerobic digestion liquid

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0029] Further, the preparation method of the microporous membrane filled with the organic extractant is as follows: immerse the microporous membrane in the organic extractant, and treat it with ultrasonic (25kHz-30kHz, 240W) for 15min-30min so that the extractant can fully fill the micropores, take it out and absorb To remove residual organic solvents on the surface, wherein the extractants used to fill the microporous membrane include: conventional oxygen-containing extractants, such as esters and ethers; organic phosphorus extractants, such as trioctylphosphine oxide and tributyl phosphate; Aliphatic amine extractant, such as trioctylamine, dodecylamine.

[0030] In addition, the breathable microporous membrane has high permeability to highly volatile short-chain fatty acids, and the microporous membrane filled with extractant has a high permeability to C 4 The above fatty acids have higher selectivity and can be selected according to needs, such as choosing a gas-permeable...

Embodiment 1

[0039] In this embodiment, the volatile fatty acids are extracted from the simulated solution prepared in the laboratory, and a polytetrafluoroethylene gas-permeable membrane is selected for the microporous membrane for the volatile small molecular fatty acids; the simulated VFAs solution prepared in the laboratory is 2L in total, containing: acetic acid 1000mg / L, propionic acid 1000mg / L, butyric acid 1000mg / L, valeric acid 1000mg / L, and NaCl 3000mg / L. The pH was adjusted to 7.0 using 2M NaOH and 2M HCl. Since the simulated solution prepared does not contain suspended solids (Suspended Solid, SS), no microfilter is used, and it is directly circulated in the electrodialysis module of the experimental device through a magnetic pump. The electrodialysis module uses two sets of membrane stacks, such as figure 1 As shown, the circulation flow rate is set to 40L / h, the acid chamber 11 circulates with the same circulation flow rate, the NaOH in the microporous membrane contactor 12 ...

Embodiment 2

[0048] The experimental device of this embodiment is different from that of Reference Example 1. The difference is that the microporous membrane contactor is replaced by the microporous membrane contactor soaked and filled by the extractant trioctylamine, and the simulated solution is additionally added: caproic acid 1000mg / L, lactic acid 1000mg / L, other operating conditions are consistent with embodiment 1, the final recovery of each organic acid: acetic acid 39%, propionic acid 76%, butyric acid 85%, valeric acid 89%, hexanoic acid 91%, lactic acid 42% .

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

PropertyMeasurementUnit
pore sizeaaaaaaaaaa
areaaaaaaaaaaa
Login to view more

Abstract

The invention provides a device for on-line selective separation of organic acid from anaerobic digestion liquid. The device is connected with an anaerobic reactor filled with digestion liquid, and comprises a box body, a cathode and an anode arranged at two ends in the box body, and a plurality of groups of bipolar membranes and anion exchange membranes alternately stacked between the cathode and the anode, wherein the interior of the box body is divided into a plurality of compartments by the plurality of groups of bipolar membranes and anion exchange membranes, namely a cathode chamber, an anode chamber, a plurality of alkali chambers and a plurality of acid chambers, the alkali chambers and the acid chambers are arranged between the cathode chamber and the anode chamber at intervals, the alkali chambers and the anaerobic reactor are connected through pipelines to form a loop, a pipeline through which the digestive fluid in the anaerobic reactor enters the alkali chambers is provided with a micro-filter for performing micro-filtration on the digestive fluid, and a membrane contactor is embedded in each acid chamber. According to the invention, the energy consumption is greatly saved, and the stability and efficiency of anaerobic digestion are improved.

Description

technical field [0001] The invention belongs to the field of anaerobic digestion, in particular to a device for on-line selective separation of organic acids from anaerobic digestion liquid. Background technique [0002] After the implementation of garbage classification, a huge amount of biodegradable wet garbage (or called kitchen waste, perishable garbage) needs to be effectively treated and utilized as resources. The mainstream treatment method is to use anaerobic digestion technology to recover the energy in the form of methane while reducing the amount of biomass waste. However, the main problems faced by anaerobic digestion at present are: unstable methane production stage, low effective utilization rate and utilization value of methane, and inconvenient transportation and storage of methane; methanogenic archaea are extremely sensitive to changes in environmental conditions. It is very easy to cause the accumulation of organic acids, especially volatile fatty acids ...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Applications(China)
IPC IPC(8): C02F3/28C02F1/469C02F101/30
CPCC02F3/2866C02F1/4695C02F2101/30
Inventor 吕凡王志杰何品晶章骅彭伟邵立明
Owner TONGJI UNIV
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products