Feedstock preparation
Rice straw (
Oryza sativa) was considered as the biomass feedstock for its pyrolysis in the present study. The locally available variety
i.e. Lalata, a semi-dwarf and medium duration rice crop, cultivated widely in Odisha was collected. The collected rice straw was initially washed with tap water for removing dust, soil or any other unwanted material stick to it during harvesting and transportation work. The straw was then naturally dried in the open air in order to reduce the moisture content to about 10%. The dried straw was finally shredded into small pieces and sieved in 3/8 mesh screen to make the size of the feedstock particle to about 10 mm. No pre-treatment was done with the straw.
Experimental set up
A domestic microwave oven (model LG, 28 L convection type), available commercially was modified to suit for the incorporation of thermocouple, condensing system, entry of nitrogen gas into the reactor by nitrogen cylinder and pyrolytic gas exit unit. The power supply to the microwave reactor varied from 300-1200 W according to the attainment of suitable temperature ranges for slow pyrolysis to occur with a view to the higher yield of biochar and microwave radiation frequency was of 2.45 GHz. Quartz reactor which is transparent to the microwave radiation was used inside the oven where feedstock was kept for its thermo-chemical conversion. The dimensions of the used quartz reactor were of 19 cm in height and 14 cm in diameter. The nitrogen gas with a purity of 99.9% was allowed to enter into the reactor for about 4-5 minutes before starting the experiment in order to create an inert atmosphere inside the reactor and to avoid the burning of the biomass feedstock when exposed to high temperature during pyrolysis process. A temperature controller with digital display unit was connected with the thermocouple in order to show and record the changes of temperatures occurring inside the reactor during experimentations. The condensing system was consisted of two-stage condensers, quenched with the supply of normal water of about 20-25°C for its circulation in converting the condensing vapour to bio-oil. The non-condensable vapour was collected in a tedlar bag to know its yield but not for analysis purpose. Similar was also in case of bio-oil. The power required for operating the microwave reactor was supplied from solar photovoltaic system. The schematic diagram of solar powered microwave assisted pyrolysis system for the present study is shown in Fig 2.
Biochar, as a microwave absorption enhancer, was mixed with the feedstock before placing in the reactor and its percentage was taken to be 5 % with respect to the weight of the input feedstock as per findings of previous researchers. For each batch of experiment, 450 g of shredded and sieved rice straw was kept in the quartz reactor. The reaction times during the pyrolysis process were varied from 15-20 minutes and power supply was at 700 W microwave power. The power supply was cut off to the reactor after attaining the above time duration. Self-cooling was allowed for the product remaining in the reactor after pyrolysis process was over. After about 3 hours, the cooled product
i.e. biochar was collected from the reactor, grinded into finer particles and stored in the air tight polythene bag for future use as a cementitious material. The percentage of biochar obtained after pyrolysis was about 30% of the input feedstock.
Preliminary studies undertaken
The quality and quantity of pyrolysis products depend significantly on the various operating parameters such as size of biomass feedstock, effects of nitrogen gas flow rate into microwave reactor, types and amount of microwave absorbers, input power, heating rate and residence time. The sizes of the feedstock and nitrogen gas flow rate were decided as per the previous studies of the researchers and were kept fixed for the present study. The size of rice straw at about 10 mm
(Ravikumar et al., 2017, Mutsengerere et al., 2019) and nitrogen gas flow rate at 50 ml/min
(Huang et al., 2013; Huang et al., 2015) were kept constant all through the experiments. Biochar (5% of the weight of the feedstock) was considered as an additive due to its low cost and easy availability among the users. Heating rate generally varies linearly with the level of input power. Hence the levels of input power to the microwave oven and the residence time for the pyrolysis process were considered to be the two important factors for the yield of the pyrolytic products during microwave pyrolysis. Preliminary studies were therefore carried out to decide the input power levels and reaction times for better yield of biochar before undertaking the final set of experiments for the study. In the present study, the five different microwave power levels (600 W, 700 W, 800 W, 900 W and 1000 W) and five different reaction times (5 min, 10 min, 15 min, 20 min and 25 min) were considered for their optimization with a view to obtain the higher yield of biochar. All the experiments were carried out in triplicate to ensure the good reproducibility of the experimental results. From the experimental investigations, the input power level and reaction time were respectively found to be 600 W and 15 minutes for higher yield of biochar i.e. about 28 per cent. The biochar obtained with 600 W input power level and 15 minutes’ reaction time was used for partial replacement of cement for further experimental investigations.
Composition analysis of cement and rice straw biochar using XRF analyser (IS: 12803: 1989)
XRF (X-ray fluorescence) analyser was used to study the composition of cement and biochar based cement. The facility of XRF analyser was availed in the Institute of Minerals and Materials Technology, (IMMT), Bhubaneswar, Odisha. XRF (X-ray fluorescence) is a non-destructive analytical technique used to determine the elemental composition of materials. XRF analyzer determines the chemistry of a sample by measuring the fluorescent (or secondary) X-ray emitted from a sample when it is excited by a primary X-ray source. Several techniques have been used for chemical analysis of cement, however, X-ray fluorescence (XRF) is the most popular technique used today. Because of its accuracy and simplicity of procedures, XRF is used by several researchers
(Elbagermia et al., 2014) and (
Bediako and Amankwah, 2015). In this method, about 10 g of each cement sample was mixed with boric acid in 10: 1 ratio and then the mixture was milled in a milling machine for two minutes with 800 rpm to produce a homogeneous mixture. The sample was placed in dice and pressed by a briquetting press machine for one minute and then transferred to the X-ray fluorescence analyzer for analysis, following IS 12803: 1989.
Concrete preparation
The reference concrete for the present investigation was prepared from cement, sand, coarse aggregates and water without any admixture. The aim of the study was to partially replace the cement with a supplementary cementing material i.e. biochar from rice straw. The proportion of the ingredients was estimated for preparing M 30 concrete with OPC 53 grade cement. This was considered as a reference material following IS 10262-2009. The cement: sand: aggregates ratios in the study were 1:1.4:2.2 and water cement ratio (W/C) = 0.4, following the IS code. To investigate the properties of the concrete that were used for casting the specimens, various laboratory tests were performed following the related IS codes. Literatures reveal that the performance of biochar based concrete is improved compared to the reference one with the same water cement ratio by replacing less than 10% of the biochar with the cement and beyond that, the quality of concrete is decreased due to dilution effect
i.e. production of less carbon silicate hydrate (C-S-H) gel, a hardening material in the concrete
(Akinyemi et al., 2020). Hence, in this study, the percentage of biochar, added with the cement was taken to be 5% with respect to the weight of the cement. The parameters studied were setting times and workability for fresh concrete and mechanical strengths (Compressive, split tensile and flexural strength) for the hardened concrete.
Performance assessment of concrete
(i) Setting time
Setting is defined as the onset of rigidity in fresh concrete. Setting precedes hardening. Initial setting time is the time elapsed between the moments that the water is added to the cement, to the time that the paste starts losing its plasticity. The final setting time is the time elapsed between the moment the water is added to the cement and the time when the paste has completely lost its plasticity and has attained sufficient firmness to resist certain definite pressure.
(ii) Workability
Workability refers to the property of fresh concrete and it indicates how easily the concrete can be handled and placed in the constructing structures with the ability for concrete to remain a stable, coherent, homogeneous mass during handling and vibration without the constituents segregating.
(iii) Strength
Compressive strength is the ability of material or structure to carry the loads under compression on its surface without any crack or deflection. A material under compression tends to reduce the size, while in tension, size elongates. The maximum compression that concrete bears without failure is noted. Split tensile strength is used in the design of structural light weight concrete members to evaluate the shear resistance provided by concrete. Flexural strength is one measure of the tensile strength of concrete. It is a measure of an unreinforced concrete beam to resist failure in bending.