Subscriber access provided by Caltech Library
Combustion
Combustion Characteristics of Tight Sandstone Yu Zhou, Wei Chen, and Yafeng Lei Energy Fuels, Just Accepted Manuscript • DOI: 10.1021/acs.energyfuels.8b00417 • Publication Date (Web): 02 May 2018 Downloaded from http://pubs.acs.org on May 3, 2018
Just Accepted “Just Accepted” manuscripts have been peer-reviewed and accepted for publication. They are posted online prior to technical editing, formatting for publication and author proofing. The American Chemical Society provides “Just Accepted” as a service to the research community to expedite the dissemination of scientific material as soon as possible after acceptance. “Just Accepted” manuscripts appear in full in PDF format accompanied by an HTML abstract. “Just Accepted” manuscripts have been fully peer reviewed, but should not be considered the official version of record. They are citable by the Digital Object Identifier (DOI®). “Just Accepted” is an optional service offered to authors. Therefore, the “Just Accepted” Web site may not include all articles that will be published in the journal. After a manuscript is technically edited and formatted, it will be removed from the “Just Accepted” Web site and published as an ASAP article. Note that technical editing may introduce minor changes to the manuscript text and/or graphics which could affect content, and all legal disclaimers and ethical guidelines that apply to the journal pertain. ACS cannot be held responsible for errors or consequences arising from the use of information contained in these “Just Accepted” manuscripts.
is published by the American Chemical Society. 1155 Sixteenth Street N.W., Washington, DC 20036 Published by American Chemical Society. Copyright © American Chemical Society. However, no copyright claim is made to original U.S. Government works, or works produced by employees of any Commonwealth realm Crown government in the course of their duties.
Page 1 of 24 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Energy & Fuels
1
Combustion Characteristics of Tight Sandstone
2 3 4 5 6 7
Yu Zhou a, Wei Chen a,*, Yafeng, Lei b, a b
School of Energy, Soochow University, Suzhou, China General Electrical Company, Houston, TX 77041, USA
8 9 10
Corresponding Author: Wei Chen
11
School of Energy
12
Soochow University, Suzhou 215006, China
13
E-mail:
[email protected] 14 15
ACS Paragon Plus Environment
Energy & Fuels 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
16
Abstract
17
As a promising unconventional energy source, tight sandstone gas has attracted
18
increasing attention. Because of the extremely low porosity/permeability of tight
19
sandstone, large scale exploration and development are still challenging. Recently,
20
high-temperature combustion or pyrolysis is employed to increase sandstone porosity
21
/permeability. In this study, the sandstone samples obtained from Xinjiang province
22
China were heated for 30 minutes in air atmosphere at temperatures of 350 oC, 500 oC,
23
700 oC, 800 oC and 900 oC respectively. The combustion characteristics and property
24
changes of sandstone were investigated. In the beginning, thermal decomposition
25
process of sandstone and gas emission were tested using thermogravimetry combined
26
with fourier-transform infrared spectroscopy (TG-FTIR). Then, the mineral
27
composition and pore structure of different combusted sandstones were tested and
28
analyzed. Moreover, the effects of combustion temperature on particle size of
29
sandstone was also investigated. Finally, scanning electron microscopy (SEM)
30
technology was performed to study the surface appearance change of sandstone.
31
According to the experiment results, organic matters started releasing at 350-500 oC
32
and most of the minerals such as carbonate decomposed at 600-870 oC. During the
33
combustion process, carbon dioxide and water vapor were the main product gases.
34
With the increase of combustion temperature, the mean pore diameter increased from
35
8.0 nm to 22.6 nm while the particles size almost kept constant. In addition to the
36
increase of pore size, it can be found from SEM photos that the compact surface of
37
sandstone became smooth and some new pores and small cracks appeared on the
38
surface of sandstone after high-temperature combustion, especially at 900 oC. As a
39
result, high-temperature combustion is one of the feasible methods to improve the
40
porosity/permeability of sandstone.
ACS Paragon Plus Environment
Page 2 of 24
Page 3 of 24 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Energy & Fuels
41
Key Words: sandstone, combustion characteristics, mineral, organic matter, pore size
42
1. Introduction
43
With the development of natural gas extraction techniques, large scale extraction of
44
tight sandstone gas, shale gas , and coalbed methane has aroused increasing interest in
45
petroleum industry [1]. Countries such as China, Canada, and United States are
46
developing strong programs to study and explore large scale extraction of sandstone
47
gas. Permeability/porosity is the critical parameter in evaluating the capacity for
48
hydrocarbon flow transportation in the rocks [2, 3]. Tight gas sandstone reservoirs
49
are commonly characterized by low permeability (less than 0.1 mD), low porosity
50
(less than 10%), complicated pore structure and strong heterogeneities [1, 4]. Thus,
51
the extraction of large reserves of sandstone becomes challenging. Tight sandstone
52
has poor connectivity, which contains pores ranging from nano-scale to micro-scale
53
and the natural fractures were at millimeter scale [5, 6]. According to Liu et al., the
54
pore space of tight sandstone was mainly made up of intergranular pores, dissolved
55
pores and micro pores, and the micro pores in clay minerals dominated pore space and
56
permeability [6].
57
For most tight sandstones, main mineral compositions are quartz and feldspar, with a
58
small quantity of other minerals [7]. The high quartz content results in high
59
mechanical stability, but the variety of accessory minerals (feldspars, clays, iron
60
oxides and carbonate minerals) might lower its chemical and mechanical stability [8].
61
Due to the presence of various minerals, the pore connectivity became poor, which
62
resulted in the reduction of storage and gas transport capacity [9]. In order to increase
63
permeability of reservoirs, acids have already been used to react with minerals in
64
sandstones [10]. However, chemical acids have potential negative effects on the
65
ecology system. For example, the inject of the common mud acid (a combination of
ACS Paragon Plus Environment
Energy & Fuels 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
66
hydrofluoric acid and hydrochloric acid ( HF: HCl )) may not only cause the secondary
67
and tertiary precipitation damage, but also collapse the sandstone formation because of
68
unconsolidated formation caused by excessive corrosion of clay minerals [11].
69
Moreover, organic acids such as acetic and formic acids were also used to acidize
70
sandstone which could result in underwater contamination [12]
71
Recently, hydraulic fracturing and CO2 sequestration are regarded as the main
72
promising enhanced gas recovery techniques for tight gas reservoirs [13]. These
73
techniques have greatly increased gas production, but it can also threaten water
74
resource [14]. For example, hydraulic fracturing requires a large amount of water,
75
which is not applicable to some areas that lack water resources, especially in Xinjiang
76
province, China which is covered by large deserts. In addition, water-based fracturing
77
fluid increases water saturation and decrease gas permeability, then causes the
78
so-called permeability jail [15, 16]. Moreover, using CO2 for gas recovery needs to
79
consider the problems of pipe corrosion, pipe leaking and compressor investment [16].
80
Therefore, many researchers are searching for other exploitation technologies for gas
81
and oil extraction. For example, Wang et al. applied microwave heating to enhance
82
shale gas recovery [17]. Nicolini et al. applied nanofiltration to improve oil recovery
83
in sandstone reservoirs by changing the injection water salinity and ionic components
84
[18]. Recently, high-temperature combustion and pyrolysis have been used to enhance
85
shale rock permeability [19, 20]. With the increase of pore size and storage space of
86
sandstone, both porosity and permeability increased [21].
87
Many studies analyzed the mechanical properties of sandstone such as compressive
88
strength, elastic properties and mechanical wave in different normal conditions
89
[22-26]. Moreover, thermal conductivity of sandstone was also studied since it is
90
related to permeability and porosity [27, 28]. However, limited researches focus on
ACS Paragon Plus Environment
Page 4 of 24
Page 5 of 24 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Energy & Fuels
91
the high-temperature combustion characteristics of sandstone. Temperature could
92
affect the dissolution and precipitation processes of minerals through its impact on
93
mineral reaction rates and equilibrium constants of chemical reactions, etc [29]. For
94
sandstones, high temperature could cause thermal damage and change pore structure
95
[30-32]. Thus, it is necessary to investigate the geochemical prosperities and
96
combustion characteristics of sandstone at different combustion temperatures.
97
In this article, temperatures of 350 oC, 500 oC, 700 oC, 800 oC and 900 oC were applied
98
to sandstone samples combustion for 30 minutes, respectively. The effects of
99
combustion on the samples’ physical and geochemical properties such as pore size
100
and mineral compositions was investigated. Moreover, the combustion characteristics
101
and gas emission of sandstone samples were studied with TG-FTIR. The particle sizes
102
of sandstone samples under different combustion temperatures were also investigated.
103
2.
104
The sandstone samples were obtained from a drilling hole at Donggou basin, Xinjiang
105
province, China. It is located in northwest China and most of it is covered by deserts.
106
As mentioned before, it is not suitable to exploit oil and gas reservoirs using hydraulic
107
fracturing due to the lack of water resources. As a result, combustion and pyrolysis
108
technologies are being employed in tight sandstone gas recovery.
109
In the beginning of the experiments, a raw sandstone sample with gray color (Fig.1)
110
was crushed and screened to small particles (Fig. 2a) with size of 100-180 mesh
111
(0.088-0.150 mm). These raw small particles were heated at temperatures of 350 oC,
112
500 oC, 700 oC, 800 oC and 900 oC respectively, for 30 minutes in a tube furnace in air
113
environment. Afterwards, combusted and raw sandstone samples were collected for
114
XRD tests, liquid nitrogen absorption and desorption tests, and particle size
115
measurement.
Sample Preparation and Experiments
ACS Paragon Plus Environment
Energy & Fuels 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Page 6 of 24
116 117
Fig.1. Raw sandstone sample from Donggou basin
118
As shown in Fig. 2, the color of combusted sandstone samples gradually became puce
119
due to the decomposition of minerals and oxidization of organic matters with
120
increasing combustion temperature.
121
(a)
(b)
(d)
(e)
(c)
(f)
122 123
Fig. 2. The raw and combusted sandstone samples. (a) Raw, (b) 350 oC, (c) 500 oC, (d)
124
700 oC, (e) 800 oC, (f) 900 oC
125
2.1 Proximate Analysis
126
In the beginning of experiments, the raw sandstone samples were sent to a
127
commercial lab for proximate analysis. The proximate analysis provided the weight
128
percentages of moisture, ash, volatile matter (VM) and fixed carbon (FC) of sandstone
129
[33]. Table 1 gives proximate analysis of the sandstone samples on air dry basis.
130
Table 1. Proximate analysis of sandstone Air dry basis
Wt.%
ACS Paragon Plus Environment
Page 7 of 24 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
Energy & Fuels
Moisture Ash VM FC
0.85 98.21 0.71 0.23
131 132
2.2 TGA-FTIR Tests
133
In order to study the thermal decomposition process of sandstone samples, about 20
134
mg finely crushed raw samples were heated from ambient temperature to 900 oC with
135
a heating rate of 20 oC/min in a TG-FTIR instrument (STA6000-Frontier). As
136
temperature increased, mass loss and gas emission as a function of combustion
137
temperature were both recorded.
138
2.3 XRD Tests
139
Since minerals will decompose during combustion and it affects the pore connection
140
inside the sandstone samples, raw and combusted sandstone samples were used for
141
XRD tests to study the effects of combustion temperature on mineral decompositions
142
using an X-ray diffraction meter (D/MAX-2000PC). The scattering angle (2θ) was set
143
from 10° to 80° and scanning rate was set at 5°/min with a step size of 0.02°. The
144
relative content of raw sandstone samples was given in Table 2.
145
Table 2. The XRD analysis of mineral composition and relative content of sandstone
146
(Wt. %). Sample
Quartz Anorthose Orthoclase Calcite Illite Biotite
Donggou sandstone 5
3
12
70
9
1
147 148
2.4 Liquid Nitrogen Adsorption and Desorption Tests
149
Liquid nitrogen adsorption and desorption tests were performed to analyze the change
150
of pore microstructure such as pore volume and pore size after high-temperature
151
treating. Six groups of heated sandstone samples were measured using a Surface Area
ACS Paragon Plus Environment
Energy & Fuels 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60
152
and Pore Size Analyzer (TriStar II 3020).
153
2.5 Particle Size Measurement
154
In order to investigate the effect of combustion temperature on particle size change, the
155
six different types of sandstone samples (particle size 50-300 µm) were measured using
156
a laser scattering particle analyzer (Malvern Instruments MS3000). The measurements
157
were repeated for five times and average size distribution was obtained. Fig. 3 gives the
158
size distribution curves of raw sandstone particles. It was found that the peak volume
159
density (about 17 %) was at the size of 130 µm, which means the mean particle size of
160
this sandstone group is range of 125-135 µm.
161 162
Fig. 3. Size distribution of raw sandstone samples
163
3. Results and Discussions
164
3.1 Sandstone Sample Properties
165
It can be found from Table 1 that the total organic carbon (TOC) of the sandstone
166
samples including VM and FC is about 0.94 wt.%. TOC content of shale rock can be
167
divided into 5 types: poor (<0.5%), fair (0.5–1%), good (1–2%), very good (2–4%)
168
and excellent (>4%) [34]. Compared to shale, the TOC content of this sandstone is
169
fair (