Method for co-production of carbon-based fertilizer by thermal cracking of straw
A technology of thermal cracking and carbon-based fertilizer, which is applied in the processing of tar, the manufacture of pyrolignoic acid, and the preparation/purification of carbon, etc., can solve the problem of high cost of producing carbon-based fertilizer, improve heat utilization efficiency, ensure carbonization quality, reduce effect of dust
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2018-09-14
- Estimated Expiration
- Not applicable · inactive patent
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Figure 1
Abstract
Description
technical field
[0001] The invention belongs to the technical field of biomass utilization, and specifically provides a production method of carbon-based fertilizer Background technique
[0002] Straw, use it as treasure, discard it as harm. Statistics show that my country's annual output of agricultural and forestry waste is about 1.4 billion tons, of which the straw of corn, rice, wheat and other staple crops is as high as 700 million tons, of which less than 1 / 3 has been returned to the field, and the utilization rate of straw fertilizer is insufficient 20%. In fact, straw carbonization-returning technology is an ideal straw utilization method. Straw carbonization refers to the pyrolysis of straw under oxygen-limited and certain temperature conditions to form a stable carbon-rich product, that is, biochar. Biochar has large porosity and specific surface area, strong adsorption capacity, anti-oxidation capacity and anti-biodegradation ability, so it can be widely used in ...
Examples
Embodiment 1
[0039] This embodiment provides a method for co-producing charcoal-based fertilizer by pyrolysis of straw, comprising:
[0040] The stalk particles are dried and preheated in an external heat mode, and then the dried and preheated stalks are thermally cracked under oxygen-limited conditions to obtain cracked products.
[0041] Gas-solid separation is performed on the obtained pyrolysis products to obtain pyrolysis gas and biomass charcoal. The obtained biochar is used to produce carbon-based fertilizer after crushing and cooling.
[0042] The obtained pyrolysis gas is subjected to purification treatment such as dust removal and washing in sequence, and then burned, and the flue gas generated by the combustion is transported to the drying and pyrolysis steps of straw particles, and used as a heat source.
[0043] At the same time, during drying, a part of the flue gas is in direct contact with the straw particles, replacing the air around the straw particles with flue gas, and...
Embodiment 2
[0045] This embodiment provides a method for co-producing charcoal-based fertilizer by pyrolysis of straw, comprising:
[0046]First, the straw goes through a crushing, granulating or briquetting treatment system to make straw granules.
[0047] Then, the straw particles are sent into the external heat rotary drying furnace through the feeding system. The drying furnace has an inner cylinder body, an outer cylinder body and a clamping cavity sandwiched between the two. The straw particles enter the inner cylinder body of the drying furnace. Preheat and dry at 150°C.
[0048] Next, the dried and preheated straw particles are transported into the external heating rotary pyrolysis furnace. Similarly, the furnace also has an inner cylinder, an outer cylinder and a cavity sandwiched between them, and the straw particles enter the inner cylinder. The cylinder is cracked at 530°C to generate pyrolysis gas and biochar.
[0049] The generated pyrolysis gas and biochar are separated b...
Embodiment 3
[0055] This embodiment provides a method for co-producing charcoal-based fertilizer by pyrolysis of straw, comprising:
[0056] First, the straw goes through a crushing, granulating or briquetting treatment system to make straw granules.
[0057] Then, the straw particles are sent into the external heat rotary drying furnace through the feeding system. The drying furnace has an inner cylinder body, an outer cylinder body and a clamping cavity sandwiched between the two. The straw particles enter the inner cylinder body of the drying furnace. Preheat and dry at 110°C.
[0058] Next, the dried and preheated straw particles are transported into the external heating rotary pyrolysis furnace. Similarly, the furnace also has an inner cylinder, an outer cylinder and a cavity sandwiched between them, and the straw particles enter the inner cylinder. The cylinder is cracked at 450°C to generate pyrolysis gas and biochar.
[0059] The generated pyrolysis gas and biochar are separated ...