DESC:FIELD OF INVENTION

The present invention relates to the synthesis of Carbon Nanotubes (CNTs) from industrial emission. More particularly, the invention relates to an apparatus and the method thereof synthesizing CNTs from industrially emitted gas (IEG) and also simultaneously reducing the carbon emissions and helping to reduce greenhouse effect using hybrid reactor.

BACKGROUND OF INVENTION

Carbon nanomaterial’s (CNMs) have been discovered in 1991, and since then, it may have many exceptional electrical, optical, magnetic and mechanical properties and attractive potential applications. These CNMs can be formed from a wide variety of different materials. Industrially emitted gas (IEG) can be considered as one of the most basic and inexpensive materials for the production of carbon nanomaterials.

Till date, a number of methods for the synthesis of CNMs have been reported, which can be grouped into three types: arc discharge (R.H. Baughman, 2002), laser ablation (C. Journet, 1997, Z. Shi, 2000) and catalytic chemical vapour deposition (CCVD) (M. Zhang, 2001, J. Kong, 1998, D.E. Resasco, 2002). Of these methods, the CCVD method has drawn more attention due to its potential for inexpensive and continuous production of CNMs in large amounts.

Carbon nanomaterial’s production increases with the addition of metal catalyst to the industrially emitted gas (IEG). Even CNMs synthesis takes place at respective temperatures, reaction time and complete decomposition of the catalytic precursor is expected which acts as a nucleation agent to enhance growth of the CNMs.

There are no complete studies about the synthesis of CNMs with industrially emitted gas (IEG) as a carbon source in the literature. The results obtained by the present invention demonstrate that industrially emitted gas (IEG) may be a good carbon source for the production of CNMs by the hybrid CCVD method, for which one of the reasons might be due to the mixture of the components such as CH4, CO and H2 in industrial emissions that are involved, in one way or another, in the formation process of CNMs.

SUMMARY OF INVENTION

This summary is provided to introduce concepts related to a production of carbon nanotubes in large scale continuously using industrial emission at industrial sites and the concepts are further described below in the detailed description. This summary is not intended to identify essential features of the claimed subject matter nor is it intended for use in determining or limiting the scope of the claimed subject matter.

The present invention discloses a process of synthesizing carbon nanotubes (CNTs) in large quantities with continuous process and high purity by hybrid reactor using industrially emitted gas (IEG) as a carbon source.

In one implementation, the present invention employs a novel hybrid CVD rector with the industrially emitted gas (IEG) as an input and produces CNTs at a very low cost and also simultaneously reducing the carbon emissions and helping to reduce green house effect.

In one implementation, an industrially emitted gas (IEG) conversion process in which the industrially emitted gas (IEG) introduced into a reactor, the reaction taking place at temperatures 700o C to allow the formation of CNTs inside the reactor is disclosed.

In one implementation, a reactor in which the reactor vessel is connected with a inlet jet for catalyst insertion, the reactor which will convert industrially emitted gas (IEG) to high density carbon and hydrogen at temperature 700oC is disclosed.

In one implementation, an apparatus for producing carbon nanotubes (CNT’s) using hybrid catalytic chemical vapour decomposition an industrially emitted gas (IEG) is disclosed. The apparatus comprises of one or more furnace which further comprises of one or more temperature controller; and one or more reactor for the production of said CNT’s. The reactor, at its one end, is configured to receive one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature, wherein said catalyst is present inside a precursor chamber located outside said furnace; and receive a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace. The temperature controller is configured to attain a particular temperature and thereby induces production of said CNT’s inside said reactor.

In one implementation, a method for producing carbon nanotubes (CNT’s) using a hybrid catalytic chemical vapour decomposition and an industrially emitted gas (IEG) in an apparatus is disclosed. The method comprises of:
· receiving one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature of first stage furnace, preferably, in a range of 300 °C to 400 °C, wherein said catalyst is metalocene and is present inside a precursor chamber located outside said furnace; and
· receiving a industrially emitted gas (IEG) by means of a one or more volatile separating chambers connected to a dryer, wherein said volatile separation chamber located outside said furnace; and
· receiving a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace and connected to a mist eliminator; and
· attaining a particular temperature in second stage furnace, preferably of 700 °C, using temperature controller, thereby inducing production of said CNT’s inside said reactor.

BRIEF DISCRIPTION OF THE ACCOMPANYING DRAWING

These and other features, aspects, and advantages of the present invention will become better understood, when the following detailed description is read with reference to the accompanying drawing in which like reference numerals represent like parts throughout the several drawings, wherein:

Figure 1 is a schematic representation of the complete process used in the present invention to produce carbon nanotubes in a continuous way from industrially emitted gas (IEG).

Figure 2 is a schematic representation of the volatile separating chamber, process used to separate volatiles continuously from the Industrially Emitted Gas (IEG).

Figure 3 is a schematic representation of the particle filter, process used to filter the particulate matter from the Industrially Emitted Gas (IEG).

Figure 4 is a schematic representation of the mist eliminator, process used to eliminate the moisture presence in the Industrially Emitted Gas (IEG).

Figure 5 is a schematic representation of the reactor with furnace, process used in detail of the feeding zone of the catalyst and Industrially Emitted Gas (IEG) and the position in which the synthesis of the CNT is made and shows the furnace in order to cover the reactor at appropriate temperatures.

Figure 6 is a schematic representation of the CNT collector with vacuum sucker, process used to collect the produce CNT from the reactor with the help of vacuum sucker.

Figure 7 is a schematic representation of the precursor chamber, process used to feed the catalyst into the reactor with help of dozing pump and jet sprayer.

Figure 8 is a method for producing carbon nanotubes (CNT’s) using hybrid catalytic chemical vapor decomposition and an industrially emitted gas (IEG) in an apparatus.

DETAILED DESCRIPTION OF THE PRESENT INVENTION

The present invention is directed to a process of continuous production of carbon nanotubes (CNTs).

While aspects of described a production of carbon nanotubes in large scale continuously using industrial emission at industrial sites may be implemented in any number of different environments, and/or configurations, the embodiments are described in the context of the following exemplary apparatus.

This apparatus for the CNT synthesis comprises:

Referring to figure 1 is a schematic representation for the production of CNTs; the industrially emitted gases (IEG) may enter a tar separating chambers 1, where the volatiles that may be present in the industrially emitted gas (IEG) may be separated from bottom of the Tar Separating Chambers. The residual gas includes some solid particles which are removed with the help of a filter 2.

The gas may further enter a mist eliminator 3, which traps the moisture present in the gas. The moisture free gas may then enters a reactor 8 in measured flows with a flow element 4.

The reactor 8 is a specially designed rector in which the CNTs are produced continuously. The CNTs are prepared in a vertical stainless steel tube reactor 8 within the furnace 11.

It may have two stage furnace systems. A catalyst metalocene may sent into the reactor 8, using in-situ method in the middle of the first stage furnace with the help of jet sprayer 12, of which the temperature is maintained between 300oC to 400oC. The precursor chamber 7 may produce the metalocene required with the help of metering/dosing pump 6 into the reactor 8. A particular flow of dried industrially emitted gas (IEG) is introduced in the reactor 8 with the help of a flow Element 4.

The second stage furnace is ramped at a particular heating rate to the preset reaction temperature and is held at a final temperature, between 700oC to 900oC, so that the formation of the CNT inside of reactor 8 is produced continuously.

At other end of the reactor 8 is connected to the blower/ vacuum pump 10, to suck the CNTs into the bag fiber filter 9 for the collection of the CNT.

Figure 1 also shows the concept of the present invention to demonstrative equipment. For the CNT production, a device of any type is used to admix the liquids, is fed with a mixture on an industrially emitted gas (IEG) and a catalyst in the suitable proportion to produce the formation of CNT.

The jet sprayer 12 may be within the heating zone of the first stage furnace is shown in the figure 5 that is controlled between 300oC to 400oC, to allow the passage of the liquid catalyst in vapour form, where the CNT will form.

The furnace 11 is heated continuously, and the positioning is made by means of clamps, in such a way that at the beginning of the process, the furnace 11 is heated till the CNTs synthesis temperature, for example, between 600oC and 1200oC, preferably to 700oC.

As in the first step, the reactor 8 may be fixed inside the furnace 11 and may be warmed up to reach the synthesis temperature, simultaneously the inert gas (that may include but not limited to helium, neon, argon, carbon dioxide, and the like) flow may be passed through the reactor 8 with the flow element 5 (being the most preferred, due to lowest cost) to create the inert atmosphere in the reactor 8. It may be understood that other suitable gasses may also be passed through the reactor 8 based on the applicability. After reaching the required temperature of the reactor 8 feed the industrially emitted gas (IEG) and catalyst reagents inside the reactor 8.

As there is no restriction in the diameter and length of the reactor 8, the flow may be adjusted preferably in base to the linear speed of the gas that will between 200 sccm to 1000 sccm, preferably 400 sccm. The reaction time may be chosen based on the length required by the CNTs. The growth speed is based on the synthesis condition of the synthesis and emissions and catalyst used, as well as on the proportion between these.

Simultaneously for the removal of the CNTs, CNTs formed in the internal surface of the reactor, it may be cleaned for every 30 min using inert gas under high pressure and sucks into the bag fiber filler chamber 9 for collecting CNTs using vacuum device 10. Without this being limitative, since we have all the time in which the CNT in the reactor 8 are in the synthesized position inside the furnace 11 to carry out the cleaning of the reactor 8. Once the reactor cleaning has concluded, the vacuum is deactivated. Meanwhile, the reactor 8 is in the synthesis position and once the time of CNT synthesis has been finalized, the industrially emitted gas (IEG) and catalyst feeding may be suspended preferably for 3 minutes.

The previously described method may include the following steps:

Feeding, a mixture of an industrially emitted gas (IEG) and catalyst, in the suitable proportion, into the reactor for the formation of the CNT. It may be understood that the catalyst and the IEG may be fed separately to the reactor.

Pre-heating system is controlled between 300oC to 400oC to pass the liquid towards the reactor 8 using jet spray 12.

The furnace 11 is positioning is made by means of clamps, the furnace 11 is has the synthesis temperature of the CNT, namely, between 600oC to 1200oC, preferably to 700oC.

The reactor 8 inside the furnace may be warmed up to reach the reaction temperature as mentioned above.

A flow of inert gas may be passed through the reactor 8 continuously from starting to end of the reaction.

The flow of industrially emitted gas (IEG) may be adjusted preferably on the basis of the linear speed of the gas that will be between 200 sccm to 1000 sccm, preferably 400 sccm.

Once the synthesis temperature is reached, the feeding of industrially emitted gas (IEG) and catalyst mixture may begin to allow the formation of the CNTs. The reaction time is chosen based on the length required for the carbon nanotubes.

Simultaneously, the CNTs formed in the internal surface of the reactor 8 are cleaned for every 30 min using inert gas under high pressure and also sucks into the bag fiber filler chamber 9 for collecting CNTs using vacuum device.

Once the reactor cleaning has concluded, the vacuum may be deactivated.

Once the time of CNT synthesis has been finalized, the industrially emitted gas (IEG) and catalyst feeding may be suspended preferably 3 minutes.

In one implementation, a method of producing carbon nanotubes using industrially emitted gas (IEG) having a production station may comprise of:
a) A tapping connection from the industrial emitting source from industry.
b) At least a pair of volatile separating chambers to separate tar from the industrially emitted gas (IEG), each chamber contains inlet for gas and water and outlet for tar and water, with a level gauge to show the water level.
c) At least one filter to remove the solid particles from the residual industrially emitted gas (IEG) coming out from the volatile separating chambers connected in line.
d) A mist eliminator chamber which traps the moisture present in the industrially emitted gas, having the inlet and outlet for gas.
e) A furnace is maintaining at a predetermined temperature to allow the synthesis of carbon nanotubes inside the reactor chamber, furnace designed in two part, part - 1 heater and part - 2 heater. Part -1 is maintained at predetermined temperature for converting catalyst from liquid phase to vapor phase and part -2 is for converting industrially emitted gas (EIG) to carbon nanotubes with support of vapor phase catalyst.
f) A bag fiber filter chamber to collect the carbon nanotubes in bag, which is connected to the outlet of reactor chamber.
g) A suction device connected to the extraction pipe, wherein the suction comprises for the collection of carbon nanotubes in bag fiber filter.
h) a control system is mounted on the front frame of the hybrid reactor.

In one implementation, the precursor chamber may be connected to the metering pump.

In one implementation, the metering pump flows with the predetermined flows of catalyst into the reactor from 0.1 to 10 ml/min.

In one implementation, the jet sprayer may be plugged at the inlet of the reactor chamber in the middle of the first state furnace, wherein it consists of inner and outer tube, whereas inner tube supply catalyst and outer tube supply gas into the reactor chamber for the production of carbon nanotubes within the predetermined temperature 300oC to 400oC.

In one implementation, the method and apparatus may produce a single walled carbon nanotubes using industrially emitted gas.

In one implementation, the method and apparatus may produce a multi walled carbon nanotubes using industrially emitted gas.

In one implementation, the catalyst Ferrocene was dissolved in solvent is predetermined 0.5, 1, 1.5 and 2 grms for the production of carbon nanotubes using industrially emitted gas (IEG).

In one implementation, the temperatures predetermined may be in the range of 700oC to 900oC for the production of carbon nanotubes using industrially emitted gas (IEG).

In one implementation, the carbon nanotubes may show homogeneity or heterogeneity in the sizes of the CNTs, with respect to the catalyst composition and temperature.

In one implementation, the catalyst particle size may be in the range of 10- 50nm.

In one implementation, the carbon nanotubes may be homogeneous and/or heterogeneous in size and size may vary in between 10 to 100 nm.

Referring now to figure 2 is a schematic representation of the volatile separating chamber 1, process used to separate volatiles continuously from the Industrially Emitted Gas (IEG). As shown in the figure 2, the separating chamber 1 may comprise of an industrial emission inlet 201, a sequence inlet line to particle eliminator 202, a level gauge of water 203, and a volatile drains outlet 204. In one implementation, water may be supplied to the IEG received in the chamber 1. A pump may be provided to feed water inside the chamber 1.

Referring now to figure 3 is a schematic representation of the particle filter 2, process used to filter the particulate matter from the Industrially Emitted Gas (IEG). As shown in figure 3 the filter 2 to separate particles in industrial emission receives the volatile free Industrially Emitted Gas (IEG) from the chamber 1. The filter may be provided with a differential pressure gauge 301 to adjust the pressure of the input from the chamber 1.

Referring now to figure 4 a schematic representation of the mist eliminator 3, process used to eliminate the moisture presence in the Industrially Emitted Gas (IEG) is shown. As shown in figure 4, the mist eliminator 3 receives a filtered IEG to a chamber to capture mist form the IEG. The eliminator 3 may include a level gauge 401, a water drain to remove the moisture 402, needle valve to outlet the moisture free gas to rotameter 403.

Referring now to figure 5 a schematic representation of the reactor with furnace, process used in detail of the feeding zone of the catalyst and Industrially Emitted Gas (IEG) and the position in which the synthesis of the CNT is made and shows the furnace in order to cover the reactor at appropriate temperatures. As shown in figure 5, the reaction chamber is shown. The chamber comprises of a furnace 11 enclosing a reactor 8 inside it. The furnace may include temperature controllers 13 connected to it which are configured to maintain temperature suitable for the reaction inside the reactor.

As shown in figure 5, the chamber comprises of an inlet of IEG which may be received from the rotameter and also include a jet sprayer 12 which is configured to provide an inlet to the catalyst from the same end. The other end of the reactor provides an outlet to the CNT’s formed inside the reactor and is connected to collection unit shown in figure 6.

Referring now to figure 6 a schematic representation of the CNT collector with vacuum sucker 10, process used to collect the produce CNT from the reactor 8 with the help of vacuum sucker 10 is shown. As shown in the figure 6, the collection unit comprises of bag filler 9, a collection chamber 601, a collecting outlet 602 and a Vacuum sucker 10 attached to it.

The uses and working of the collecting unit is explained above.

Referring now to figure 7 a schematic representation of the precursor chamber 7, process used to feed the catalyst into the reactor 8 with help of dozing pump 6 and jet sprayer is shown. As shown in the figure 7, the precursor tank 7 may include a precursor feeder 701, a ball valve 702, an air remover 703, a storage tank 704, a level gauge 705, a pulsation dampner 706 outlet connected to a dosing pump 6.

The task of precursor chamber / tank 7 is to store the catalyst which may be present along with a solvent inside the tank 704 and to provide the same to the reactor 8 during the initiation of the reaction.

Referring now to figure 8 a method for producing carbon nanotubes (CNT’s) using hybrid catalytic chemical vapor decomposition and industrially emitted gas (IEG) in an apparatus is shown.

In one implementation, a method for producing carbon nanotubes (CNT’s) using hybrid catalytic chemical vapour decomposition an industrially emitted gas (IEG) in an apparatus is disclosed. The method comprises of:
· receiving (802) one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature, preferably, in a range of 300 °C to 400 °C, wherein said catalyst is ferrocene and is present inside a precursor chamber located outside said furnace; and
· receiving (804) a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace and connected to a mist eliminator 3; and
· attaining (806) a particular temperature, preferably of 700 °C, using temperature controller, thereby inducing production of said CNT’s inside said reactor.

In one implementation, an apparatus for producing carbon nanotubes (CNT’s) using hybrid catalytic chemical vapour decomposition an industrially emitted gas (IEG) is disclosed. The apparatus comprises of one or more furnace which further comprises of one or more temperature controller; and one or more reactor for the production of said CNT’s. The reactor, at its one end, is configured to receive one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature, wherein said catalyst is present inside a precursor chamber located outside said furnace; and receive a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace. The temperature controller is configured to attain a particular temperature and thereby induces production of said CNT’s inside said reactor.

In one implementation, said rector is a vertical stainless steel tube reactor.

In one implementation, said catalyst is an organometallic compound and preferably ferrocene.

In one implementation, said catalyst is dissolved in a solvent.

In one implementation, said catalyst is in a particulate form with a particle size in a range of 5 - 50 nm.

In one implementation, said precursor chamber is configured to feed said catalyst into said reactor by a means of a metering pump.

In one implementation, said precursor chamber is configured to feed said catalyst into said reactor by means of an inlet means covered by said jet sprayer.

In one implementation, said jet sprayer is maintained at said controlled temperature, preferably, in a range of 300 °C to 400 °C.

In one implementation, dried industrially emitted gas (IEG) is a moisture free gas, which obtained from: said dryer coupled to one or more mist eliminator which is further coupled to one or more filter which is further coupled to one or more tar separating chamber, wherein: said tar separating chamber is configured to receive an industrially emitted gases (IEG) and separate volatiles present in said industrially emitted gas (IEG) from bottom of said tar separating chamber thereby forming residual gas; said filter is configured to remove solid particles, if any, from said residual gas; and said mist eliminator is configured to trap the moisture present in said residual gas, and thereby feed said residual gas to said dryer wherein said residual gas is dried to form said dried industrially emitted gas (IEG).

In one implementation, said particular temperature is in a range, of 600 °C to 1200 °C, and preferably of 700 °C.

In one implementation, said reactor, at other end, is connected to blower configured to suck said CNT’s into bag fiber filter for the collection of said CNT’s.

In one implementation, an inert gas is passed through said reactor, before inducing said production of CNT’s, to create an inert atmosphere in said reactor.

In one implementation, an inert gas is passed with a flow in a range, of 200 sccm to 1000 sccm, and preferably of 400 sccm.

In one implementation, the blower is configured to suck CNT’s using inert gas under high pressure.

In one implementation, said dried industrially emitted gas (IEG) from said dryer is feed to the reactor using rotameter.

In one implementation, CNT’s are of size between 10 to 100 nm.

In one implementation, an apparatus for producing carbon nanotubes (CNT’s) using a hybrid catalytic chemical vapor decomposition and industrially emitted gas (IEG), said apparatus comprising: a pair of volatile separating tanks, a particle filter, a moisture trapper, connected in line to a flow meter, and simultaneously connected to a reactor separately; a furnace enclosing the reactor is maintained at a suitable temperature to allow formation of CNTs inside the reactor; a vacuum system is connected end of the reactor to collect CNT’s in a bag fiber filter.

Although implementations for a production of carbon nanotubes in large scale continuously using industrial emission at industrial sites have been described in language specific to structural features and/or methods, it is to be understood that the appended claims are not necessarily limited to the specific features or methods described. Rather, the specific features and methods are disclosed as examples of implementations for a production of carbon nanotubes in large scale continuously using industrial emission at industrial sites.
,CLAIMS:1. An apparatus for producing carbon nanotubes (CNT’s) using a hybrid catalytic chemical vapor decomposition and an industrially emitted gas (IEG), said apparatus comprising:
one or more furnace comprising:
one or more temperature controller; and
one or more reactor for the production of said CNT’s, WHEREIN:
said reactor, at its one end, is configured to:
receive one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature, wherein said catalyst is present inside a precursor chamber located outside said furnace; and
receive a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace; and
said temperature controller is configured to attain a particular temperature and thereby induces production of said CNT’s inside said reactor.

2. The apparatus as claimed in claim 1, wherein said rector is a vertical stainless steel tube reactor.

3. The apparatus as claimed in any of the preceding claims wherein said catalyst is an organometallic compound and preferably metalocene.

4. The apparatus as claimed in any of the preceding claims wherein said catalyst is dissolved in a solvent.

5. The apparatus as claimed in any of the preceding claims wherein said catalyst is in a particulate form with a particle size in a range of 5- 50 nm.

6. The apparatus as claimed in any of the preceding claims wherein said precursor chamber is configured to feed said catalyst into said reactor by a means of a dozing pump.

7. The apparatus as claimed in any of the preceding claims wherein said precursor chamber is configured to feed said catalyst into said reactor by means of an inlet means covered by said jet sprayer.

8. The apparatus as claimed in any of the preceding claims wherein said jet sprayer is maintained at said controlled temperature, preferably, in a range of 300 °C to 400 °C.

9. The apparatus as claimed in any of the preceding claims wherein said dried industrially emitted gas (IEG) is a moisture free gas, which obtained from:
said dryer coupled to one or more mist eliminator which is further coupled to one or more filter which is further coupled to one or more tar separating chamber, wherein:
said tar separating chamber is configured to receive an industrially emitted gases (IEG) and separate volatiles present in said industrially emitted gas (IEG) from bottom of said tar separating chamber thereby forming residual gas;
said filter is configured to remove solid particles, if any, from said residual gas; and
said mist eliminator is configured to trap the moisture present in said residual gas, and thereby feed said residual gas to said dryer wherein said residual gas is dried to form said dried industrially emitted gas (IEG).

10. The apparatus as claimed in any of the preceding claims wherein said particular temperature is in a range, of 600 °C to 1200 °C, and preferably of 700 °C.

11. The apparatus as claimed in any of the preceding claims wherein said reactor, at other end, is connected to one or more blower configured to suck said CNT’s into one or more bag fiber filter for the collection of said CNT’s.

12. The apparatus as claimed in any of the preceding claims wherein an inert gas is passed through said reactor, before inducing said production of CNT’s, to create an inert atmosphere in said reactor.

13. The apparatus as claimed in any of the preceding claims wherein an inert gas is passed with a flow in a range, of 200 sccm to 1000 sccm, and preferably of 400 sccm.

14. The apparatus as claimed in any of the preceding claims wherein blower is configured to suck CNT’s using inert gas under high pressure.

15. The apparatus as claimed in any of the preceding claims wherein said dried industrially emitted gas (IEG) from said dryer is feed to said reactor using rotameter.

16. The apparatus as claimed in any of the preceding claims wherein CNT’s are of size between 10 to 100 nm.

17. The apparatus as claimed in any of the preceding claims comprises one or more separating chambers configured to provide an industrially emitted gas (IEG) to said dryer, wherein said separation chamber is located outside said furnace.

18. An apparatus for producing carbon nanotubes (CNT’s) using a hybrid catalytic chemical vapor decomposition and an industrially emitted gas (IEG), said apparatus comprising:
a pair of volatile separating tanks, a particle filter, a moisture trapper, connected in line to a flowmeter, and simultaneously connected to a reactor separately; a furnace enclosing the reactor is maintained at a suitable temperature to allow formation of CNTs inside the reactor;
a vacuum system is connected end of the reactor to collect CNT’s in a bag fiber filter.

19. A method for producing carbon nanotubes (CNT’s) using a hybrid catalytic chemical vapor decomposition and an industrially emitted gas (IEG) in an apparatus, said method comprising:
receiving one or more catalyst by a means of one or more jet sprayer maintained at a controlled temperature, preferably, in a range of 300 °C to 400 °C, wherein said catalyst is ferrocene and is present inside a precursor chamber located outside said furnace; and
receiving a dried industrially emitted gas (IEG) by a means of a flow element connected to one or more dryer, wherein said dryer is located outside said furnace and connected to a mist eliminator; and
attaining a particular temperature, preferably of 700°C, using temperature controller, thereby inducing production of said CNT’s inside said reactor.

20. The method as claimed in claim 15, wherein said dried industrially emitted gas (IEG) is a moisture free gas, which is obtained by:
receiving, by a tar separating chamber, an industrially emitted gases (IEG) and separating volatiles present in said industrially emitted gas (IEG) from bottom of said tar separating chamber thereby forming residual gas;
removing, by a filter, solid particles, if any, from said residual gas; and
trapping, using a mist eliminator, moisture present in said residual gas, and thereby feeding said residual gas to said dryer wherein said residual gas is dried to form said dried industrially emitted gas (IEG).

21. The method as claimed in any of the preceding claims comprises sucking, using one or more blower, said CNT’s produced inside said reactor into one or more bag fiber filter.

22. The method as claimed in any of the preceding claims comprises one or more separating chambers configured to provide an industrially emitted gas (IEG) to said dryer, wherein said separation chamber is located outside said furnace.