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Method for preparing methyl hydride and hydrogen gas with mineralized garbage, leachate, kitchen garbage and sewage sludge

A technology for kitchen waste and mineralized waste, which is applied in the fields of biofuel, climate change adaptation, biological organic part treatment, etc. The effect of difficult ignition and simple operation

Inactive Publication Date: 2008-12-10
TONGJI UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese patent application "a method for the joint production of hydrogen from mineralized waste and swill waste and sludge" (application number: 200610027750.3) and "a method and device for hydrogen production by anaerobic fermentation of residual sludge in sewage plants" (application No.: 200310116142.6) discloses a method for anaerobic fermentation to produce hydrogen, but the concentration of hydrogen is usually at most 50-60%, which cannot be directly utilized
However, the hydrolysis phase in the traditional two-phase reactor is mainly to produce acid and remove CO 2 Almost no other gases are formed outside
However, in the current industrial practical application, the single-phase reactor has an absolute advantage, mainly because the traditional two-phase reactor is more expensive and difficult to operate and maintain than the single-phase reactor.

Method used

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  • Method for preparing methyl hydride and hydrogen gas with mineralized garbage, leachate, kitchen garbage and sewage sludge
  • Method for preparing methyl hydride and hydrogen gas with mineralized garbage, leachate, kitchen garbage and sewage sludge
  • Method for preparing methyl hydride and hydrogen gas with mineralized garbage, leachate, kitchen garbage and sewage sludge

Examples

Experimental program
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Embodiment 1

[0026] Please refer to the attached figure 1 . Pretreatment of food waste and sludge: first pick out chopsticks and hard bones in the food waste to avoid damage to the crusher, and then crush them to a particle size of 5-10mm; pass the sludge through a 1.25mm sieve; then measure their pH, water content and C / N, and then according to the water content measurement results, add corresponding quality tap water to adjust the water content to 90% by weight. Sludge, kitchen waste, leachate and mineralized waste by weight listed in Table 1 were taken (systems 1-3 in Table 1 are the experimental group, and system 4 is the control group). Then mix it evenly, put it in a 250ml serum bottle (the actual volume is 300ml), fill it with nitrogen for 1min to drive out the oxygen in the container, seal it quickly, and shake it at 20-55°C at a speed of 100-130 rpm Or start anaerobic digestion by stirring, and the reaction time lasts for 15 days. See Table 2 for the C / N and pH initial indicato...

Embodiment 2

[0032] The anaerobic fermentation tank implemented in this example is a two-phase integrated reactor (patent number: 200710047071.7). The front end of the reactor is a hydrolytic acidification phase, and as the reactor advances, it enters a methanogenic phase. The specific implementation steps are as follows:

[0033] The food waste was sorted to remove hard bones, chopsticks and other debris, and then crushed to a particle size of 5-10mm, and the pH, moisture content and C / N were measured. The results are shown in Table 3. Then, according to the moisture content measurement results, tap water of corresponding quality is added to adjust the moisture content of the sludge and kitchen waste to 90% by weight.

[0034] Mix the sludge, kitchen waste and leachate uniformly in a ratio of 60%: 10%: 30% by weight, and the amount of mineralized waste added is 5g / 100g combined matrix (sludge, kitchen waste and leachate wet weight) , The mixed matrix composed of mineralized waste and joi...

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Abstract

The invention relates to a method for producing methane and hydrogen by aged refuse, leachate, kitchen wastes and mud, comprising the following steps that: the kitchen wastes are crushed, the mud passes through a sieve with 1.25mm, the water contents of the mud and the kitchen wastes are adjusted to 90 weight percent; then the mud, the kitchen wastes and the leachate are taken according to the ratio of (10-90 percent) to (5-45 percent) to (5-45 percent), the aged refuse accounting for 5 percent of the total weight of the mud, the kitchen wastes and the leachate are added, and the C / N is between 7.0 and 7.5, the pH is between 5.8 and 6.2; the materials are pumped into an anaerobic fermentation tank, nitrogen passes through to expel oxygen in the tank, the reaction is carried out for 15 days at a temperature of between 20 and 55 DEG C, and gas mixture of CH4 and H2, with H2 concentration between 4 and 10 volume percent and CH4 concentration between 55 and 57 volume percent, is produced. The method has easy operation, low cost and precious economic and social benefits. The gas mixture produced by the method improves generating efficiency of the methane by 10 to 15 percent, and well solves the problem of difficult ignition in the process of methane power generation.

Description

technical field [0001] The invention relates to a method for producing methane and hydrogen from mineralized garbage, leachate, kitchen garbage and sludge. Specifically, it is a process in which the above-mentioned waste biomass is combined with anaerobic fermentation to simultaneously obtain methane and hydrogen. The invention belongs to the technical field of organic waste recycling. Background technique [0002] As primary energy sources, fossil fuels are becoming increasingly exhausted, and their extensive use has also caused serious environmental pollution problems. The primary energy sources represented by petroleum will eventually be replaced by other energy sources. The research and development of biomass energy technology has become one of the major hot topics in the world. However, due to the blind development of biomass fuel in recent years, there has been competition for land with grain, which may cause food famine and ecological damage. Countries such as the N...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C05F9/04C12P3/00C12P5/02
CPCY02A40/20Y02E50/10Y02E50/30Y02W30/40
Inventor 赵由才刘常青秦峰赵爱华牛冬杰柴晓利
Owner TONGJI UNIV