Pulp Thermal Hydrolysis Recirculation for Biogas Yield

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Solution Overview

Problem

Thermal hydrolysis processes for pulp treatment face challenges in minimizing investment costs, maximizing biogas production, stabilizing bacterial populations, and managing ammonia toxicity, particularly due to fluctuating loading conditions and equipment underutilization.

Innovation Solution

A method involving aerated or non-aerated hydrolysis of pulp, optional dilution, mesophilic or thermophilic digestion, dehydration, and recirculation of dehydrated pulp to maintain constant loading conditions, using thermal hydrolysis with controlled temperature and pressure, and pH management to optimize biogas production and equipment utilization.

Engineering Contradictions & Design Principles

VSEngineering Contradiction Analysis

1Productivity

If thermal hydrolysis is implemented to improve biogas production and digestion efficiency, then the investment costs are high, but the return on investment is long-term

Engineering Contradiction:
Improvebiogas productionVSAvoidinvestment cost
Core Design Contradiction:
ProductivityVSQuantity of substance

Solution Approach 1:

The patent implements dynamic control of the hydrolysis process by adjusting temperature, pressure, and residence time parameters based on real-time monitoring of biogas production and substrate characteristics. This allows optimization of the balance between investment costs and biogas production efficiency, enabling the system to adapt to varying operational conditions and maximize return on investment.

Inventive Principle:
Principle #15Dynamics

2Productivity

If feed concentration is increased to improve volumetric loading, then the rheological constraints are overcome, but ammonia toxicity increases

Engineering Contradiction:
Improvevolumetric loadingVSAvoidammonia toxicity
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent employs parameter changes by adjusting pH levels, temperature, and hydraulic retention time to control ammonia speciation and toxicity. By modifying these parameters, the system can maintain high volumetric loading while preventing ammonia from becoming toxic to methanogenic bacteria, thus resolving the contradiction between productivity and harmful factors.

Inventive Principle:
Principle #35Parameter changes

3Productivity

If pH is increased to improve biogas production, then the proportion of dissolved NH3 increases, but ammonia toxicity increases

Engineering Contradiction:
Improvebiogas productionVSAvoidammonia toxicity
Core Design Contradiction:
ProductivityVSObject-affected harmful factors

Solution Approach 1:

The patent implements feedback control mechanisms that continuously monitor pH, ammonia concentration, and biogas production rates. Based on this feedback, the system automatically adjusts operational parameters such as alkalinity addition, hydraulic retention time, and mixing intensity to maintain optimal pH levels that maximize biogas production while preventing ammonia toxicity buildup.

Inventive Principle:
Principle #23Feedback

4Adaptability or versatility

If loading variations are allowed to occur, then operational flexibility is improved, but bacterial population stability decreases

Engineering Contradiction:
Improveoperational flexibilityVSAvoidbacterial population stability
Core Design Contradiction:
Adaptability or versatilityVSStability of the object's composition

Solution Approach 1:

The patent applies beforehand cushioning by maintaining a buffer inventory of active bacterial populations and establishing reserve capacity in the digester system. This cushioning effect allows the system to absorb sudden loading variations without compromising bacterial population stability, thus enabling operational flexibility while protecting against shocks to the microbial consortium.

Inventive Principle:
Principle #11Beforehand cushioning (Prior cushioning)

Applied Scientific Principles

This section explains which scientific principles are used to turn an abstract innovation direction into a practical engineering solution.

Function Achieved in This Case

This approach minimizes investment costs, maximizes biogas production, stabilizes bacterial populations, and effectively manages ammonia toxicity by maintaining consistent loading and pH levels, ensuring efficient use of thermal hydrolysis and digestion equipment.

Implementation Method 1

thermal hydrolysis which combines the effects of heating at high temperature and generally of abrupt depressurization

Methodology Applied
Scientific EffectThermal hydrolysis: Hydrolysis

Implementation Method 2

heating at high temperature

Methodology Applied
Scientific EffectHeating: Heating

Implementation Method 3

The most common heating mode of these methods is steam injection, which is used to bring the sludge to the temperature required for the hydrolysis

Methodology Applied
Scientific EffectSteam injection: Phase Change

Implementation Method 4

thermal hydrolysis which combines the effects of heating at high temperature and generally of abrupt depressurization

Methodology Applied
Scientific EffectDepressurization: Depressurisation

Implementation Method 5

improve its capacity for digestion by anaerobic bacteria for the purpose of producing biogas

Methodology Applied
Scientific EffectAnaerobic digestion: Anaerobic Digestion

Implementation Method 6

a step of dehydration of the digested pulp resulting from the step iii)

Methodology Applied
Scientific EffectDehydration: Desiccation

Data Source

PatentUS10358368B2Optimisation of a pulp treatment method
Publication Date: 2019.07.23 SUEZ INTERNATIONAL
  • US10358368B2 patent drawing

AI summary

Disclosed is a method for treating pulp, particularly a method for treating sludge from wastewater treatment plants, for producing energy and/or organic materials that have undergone hygienization, including at least the following steps: a step of aerated or non-aerated thermal hydrolysis of the pulp, a digestion step, a dehydration step and a step of recirculating part of the dehydrated pulp into the step of thermal hydrolysis.