CN101755034A - Integrated process and apparatus for producing coal-based jet fuel, diesel fuel, and distellate fuels - Google Patents
Integrated process and apparatus for producing coal-based jet fuel, diesel fuel, and distellate fuels Download PDFInfo
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- 239000000446 fuel Substances 0.000 title claims abstract description 69
- 238000000034 method Methods 0.000 title claims abstract description 69
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- 239000002283 diesel fuel Substances 0.000 title abstract description 11
- 239000000047 product Substances 0.000 claims description 64
- 238000005516 engineering process Methods 0.000 claims description 50
- 238000002156 mixing Methods 0.000 claims description 43
- 238000007670 refining Methods 0.000 claims description 43
- 239000001257 hydrogen Substances 0.000 claims description 21
- 229910052739 hydrogen Inorganic materials 0.000 claims description 21
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 19
- 239000006227 byproduct Substances 0.000 claims description 17
- 238000002309 gasification Methods 0.000 claims description 17
- 239000011280 coal tar Substances 0.000 claims description 15
- 238000003763 carbonization Methods 0.000 claims description 12
- 239000007788 liquid Substances 0.000 claims description 10
- 238000000638 solvent extraction Methods 0.000 claims description 10
- 238000005194 fractionation Methods 0.000 claims description 8
- 230000008676 import Effects 0.000 claims description 8
- 230000006872 improvement Effects 0.000 claims description 4
- 239000000284 extract Substances 0.000 claims description 3
- 239000003208 petroleum Substances 0.000 abstract description 4
- 239000003921 oil Substances 0.000 description 54
- 239000011269 tar Substances 0.000 description 11
- 238000004939 coking Methods 0.000 description 9
- 238000011160 research Methods 0.000 description 8
- 238000000926 separation method Methods 0.000 description 7
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- 238000004523 catalytic cracking Methods 0.000 description 4
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- 238000012857 repacking Methods 0.000 description 2
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- 239000004411 aluminium Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 229910021383 artificial graphite Inorganic materials 0.000 description 1
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- 238000004364 calculation method Methods 0.000 description 1
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Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G45/00—Refining of hydrocarbon oils using hydrogen or hydrogen-generating compounds
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
- C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
- C10B55/02—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/04—Liquid carbonaceous fuels essentially based on blends of hydrocarbons
- C10L1/08—Liquid carbonaceous fuels essentially based on blends of hydrocarbons for compression ignition
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Coal-based jet fuel, diesel fuel and/or distillate fuels are produced by selectively introducing a coal-based product directly into the petroleum refinery process flow to thereby create an integrated refinery process for producing the distillate fuels.
Description
The cross reference of related application
The U.S. Provisional Application series number 6O/907 that the name that the application of this world requires on April 20th, 2007 to submit to is called " INTEGRATED PROCESS AND APPARATUS FORPRODUCING COAL-BASED JET FUEL; DIESEL FUEL; ANDDISTILLATE FUELS (being used to produce coal-based jet fuel; diesel-fuel and the process integration and the equipment that distillate fuel) ", 882, the U.S. Patent Application Serial 12/068 that is called " INTEGRATEDPROCESS AND APPARATUS FOR PRODUCING COAL-BASEDJET FUEL; DIESEL FUEL; AND DISTILLATE FUELS (being used to produce coal-based jet fuel; diesel-fuel and the process integration and the equipment that distillate fuel) " with the name of submitting on February 13rd, 2008,937 rights and interests are incorporated herein its full content with for referencial use.
Technical field
Described invention relates to the field of mineral fuel.More specifically, the present invention relates to derive and be converted into the mineral fuel of the various fuel products that comprise jet fuel, diesel-fuel and other distillate fuel (distillate fuel) by coal.
Background technology
Along with the industrial requirement at the energy in the world wide continues to increase year by year, various countries continue to launch to make great efforts to seek and to research and develop new petroleum resources and substitute energy.In the U.S., quickening to make great efforts not rely on petroleum import more, and making the fuel cost stabilization and the final fuel cost that rises that reduces of rising to become.
According to estimates, the jet fuel of about 3,000,000 gallonages of the annual use of United States Air Force at present.In the future, their most of demands will stand strict standard, be included in the interior service temperature performance of scope of Fahrenheit 900 degree.These strict 105D military standard 105Ds that are used for jet fuel have reflected in the performance of aircraft and advanced gas turbine engine and the many progress aspect their thermostability.For many years, the energy research place that is positioned at the Pennsylvania State University in Pennsylvania Bai Ke campus is devoted to provide new and research that distillate fuel more efficiently aspect maintains the leading position.For example, for the fuel that is deriving from product of coal, be known as the example of the jet fuel of JP-900 especially, referring to the appendix 1 and autograph appendix 2 for " coal-based jet fuel chart (TheCoal-Based Jet Fuel Program) " of autograph for " JP-900 technical overview (JP-900 TechnologyOverview) " with the high-tech research in the field of the expectation ceiling temperature range capability of reflection fuel.
In response to the demand of growing import greater amount foreign country oil product, substitute energy and the research substitute to the petroleum-type product different, lower cost are being explored with commercial undertaking by many governments.Recently, according to newpapers and periodicals, about 800,000,000 dollars of every day flows to America's economy and buys oil product import product.
Summary of the invention
Those of skill in the art as energy exploration and production field are known, and coal has become the reliable and secure domestic energy for many years.In addition, coal is a kind of worldwide energy, and it is to obtain to guarantee supply the long run supply contract of configuration at present, be generally 20 years or more than.
In order to consider and estimate the value of coal-based jet fuel, at first need to define some terms that will use in this specification sheets more clearly to describe feasible alternative techniques and device structure.For this purpose, need the following term of definition:
(A) " coal derivatived fuel " is the product of coal of being produced by coal fully.Can obtain this product by so-called direct liquefaction coal.
(B) " coal derived fuel " be comprise significant part by the component of coal production and comprise in addition from other resource fuel of the component of oil for example.
Those of skill in the art as the fuel energy field are known, use has the existing refinery operations of relatively little transformation or repacking and the coal-based jet fuel that Infrastructure is made, (as hereinafter will further defining), because all refining technique steps are consistent with current refinery operations basically, be comparatively cheap basically therefore.
According on the one hand, disclosed at least one embodiment of the present invention under the transformation of minimum input type or situation about installing additional, is utilized existing refinery Infrastructure, produces distillating fuel of senior jet fuel and other economically.
According on the other hand, disclosed at least one embodiment of the present invention is carried out under the situation of minimum change at the refining technique to standard, utilizes existing refinery Infrastructure, produces senior jet fuel and other petroleum products economically.
According to another aspect, disclosed at least one embodiment of the present invention, under the situation of the oil refining process of standard and equipment being carried out minimum change or installing additional, utilize existing refinery operations and Infrastructure, produce jet fuel economically by product of coal.
From following description to novel process and equipment, especially when reading in conjunction with the following drawings, disclosed these and other significant improvement will become apparent in applicant's specification sheets.
Description of drawings
With reference to the accompanying drawings, these and other more detailed and concrete feature of the present invention is disclosed in the following description more completely, wherein:
Fig. 1 is the synoptic diagram of basic prior art oil refining flow process (layout).
Fig. 2 is the feel flow draw of block according to the available coal tar mixing process of the disclosed working of an invention scheme of applicant.
Fig. 3 is the feel flow draw of block according to the available co-carbonization technology of another embodiment of the disclosed invention of applicant.
Fig. 4 is the feel flow draw of block according to the available solvent extraction technology of another embodiment of the disclosed invention of applicant.
Fig. 5 is the feel flow draw of block according to the available gasification by product mixing process of another embodiment of the disclosed invention of applicant.
Fig. 6 is the synoptic diagram that illustrates according to the standard refinery Infrastructure through transforming of the craft embodiment combination of the another embodiment of the disclosed invention of applicant.
Fig. 7 is the feel flow draw of block with basic oil refining flow process of coal tar blending option.
Fig. 8 is the feel flow draw of block with basic oil refining flow process of co-carbonization option.
Fig. 9 is the feel flow draw of block with basic oil refining flow process of solvent extraction option.
Figure 10 is the feel flow draw of block with basic oil refining flow process of gasification additive term.
Embodiment
In the following description, for illustrative purposes, stated for example multiple details of schema and system architecture etc., thereby the further understanding to one or more embodiments of the present invention is provided.Yet, for those skilled in the art,, do not require that these details also will be conspicuous in order to realize the present invention.
As mentioned above, in order to obtain the economic advantages of utilizing factory of existing oil refinery Infrastructure, University of Pennsylvania Energy Research Institute (Penn State University EnergyInstitute) pays close attention to the research and development of coal-based jet fuel technology and equipment recently.The factory construction as the costliness of the brand-new factory of the desired process gas of DCL/Direct coal liquefaction factory (plant) or other fuel has been avoided in the utilization of this existing oil product Infrastructure.Explanation to the less transformation of the existing refinery Infrastructure of applicant's utilization or the production technique that is used for jet fuel and other fuel that installs additional directly causes estimating the significantly saving that each factory is about 2,000,000 dollars when the disclosure is implemented.
Fig. 1 is the synoptic diagram of basic prior art oil refining flow process.Operational path as described below can be incorporated in existing refinery operations and the Infrastructure with less relatively transformation or repacking.Produce JP 900 type jet fuels and other technology that distillates fuel and equipment according to being used to after applicant's the improvement, there are 4 kinds of different operational paths, wherein each operational path can make up with other operational path, thereby draws the multiple various feasible configurations that exceed following concrete described structure:
First technology: the coal tar mixing process, can understand this technology better with reference to figure 2.The coal tar mixing process is usually directed to the mixture that hydrogen treatment is mixed with the coal-tar products (for example, refining chemistry oil) that refines logistics (refinery stream) (for example, light cycle oil).Preferably, coal tar blending relates to coal derived liquid (refining chemistry oil (RCO)) that blending is obtained commercially and light cycle oil from catalytic cracking obtained.Light cycle oil (LCO) is the by product that the catalytic cracking in the oil refining is handled.
Second technology: co-carbonization technology, can understand this technology better with reference to figure 3.Co-carbonization technology relates to coal is added into mixing tank, and in this mixing tank, coal and petroleum products be mixing of clarified oil for example.Then, the mixture with coal and petroleum products is directed into delay coking device.Then, will be from the liquid fractionation and the hydrogen treatment of coker.Except that fuel product, this explained hereafter has as the potentiality of the senior carbon products that is used for aluminium melting anode (smelting anode) and is producing synthetic graphite and producing the coke of the potential application of gac.
The 3rd technology: solvent extraction technology, can understand this technology better with reference to figure 4.Solvent extraction technology relates under the temperature (200～400 ℃ are desirably about 350 ℃) that raises and uses light cycle oils to extract coal with one or more steps.The product of coal mixture of the extraction of gained is carried out hydrogen treatment and fractionation, producing the clean fuel liquid of expectation, and as described below, can in gasification by product mixing process, use the not coal of extraction.
The 4th technology: gasification by product mixing process, can understand this technology better with reference to figure 5.Gasification by product mixing process relates to the tar that by product produced of collection as gasification, and with this tar and for example light cycle oil blending of the petroleum refining logistics that is fit to.With the concoction hydrogen treatment of gained and fractionation to produce the clean fuel liquid of expectation.
With reference now to Fig. 1,, illustrates to be used to import the block diagram of product of coal in the oil refining Infrastructure after improvement with the available oil refining process Infrastructure with above-mentioned 4 kinds of production technique of generation JP-900 type jet fuel.
As it is apparent to refine oil the those of skill in the art in field, can only not make up general refinery structure in order to produce jet fuel.In above-mentioned PSU Energy Research Institute, study continuously, with further evaluation with improve various product and by product from combination oil and product of coal integrated refinery (combined oil and coal-product integratedrefinery).The coal-based jet fuel that studies show that in early days that carries out in PSU Energy Research Institute after basic early-stage Study can be realized necessary high-temperature stability, and does not reduce essential storage and low-temperature stability.Thereby obviously JP-900 jet fuel product will be provided for jet fuel with the two practical solution of the propelling energy that acts on the high-performance flight device with advanced ramjet design and big scatterer (significant heat sink).
With reference now to Fig. 2,, illustrates according to the above-mentioned available coal tar mixing process feel flow draw of block that is used for product of coal is imported first technology in applicant's technology of refining oil as shown in Figure 1.As shown in Figure 2, the coal tar blending relates to being called the oily coal derived liquid of refining chemistry and mixing from for example light cycle oil of catalytic cracking gained of will being obtained commercially.These two kinds of products are imported mixing tank 102 via intake pipeline 100 and 101 respectively.The output of mixing tank 102 is fed to hydrotreater 104, in hydrotreater 104, the output of mixing tank 102 is mixed with the hydrogen of being imported by input aperture 103.The output of hydrotreater 104 directly is fed to the separation column 105 with a plurality of delivery ports that comprise gasoline delivery port 106, jet fuel delivery port 107, diesel oil delivery port 108 and fuel oil delivery port 109.In order further to understand flow process by the various process-streams (process stream) of the oil refinery after improving, can be with reference to figure 1.
With reference now to Fig. 3,, illustrates according to the above-mentioned available co-carbonization process block of second technology schema that is used for second product of coal is imported applicant's technology of oil refinery as shown in Figure 1.Second technology in applicant's technology, promptly co-carbonization is based on coal is added into and makes for example clarified oil blended mixing tank 202 of coal and the oil that is easy to obtain.These two kinds of products are imported mixing tank 202 via input aperture 200 and 201 respectively.The output of mixing tank 202 is fed to delay coking device 203.The liquid of self-dalay coker 203 is fed to separation column 205 in the future, and this separation column 205 further is fed to hydrotreater 206 with process-stream.Hydrotreater 206 has the delivery port 207 that is used to import the input aperture 208 of hydrogen and is used for jet fuel.Except from the fuel product of separation column 205 and hydrotreater 206 outputs, are the senior carbon by products that can be used for for example producing aluminum anode from the coking by product of the output of delivery port 204.In order further to understand flow process by the various process-streams of oil refining after improving, can be with reference to figure 1.
With reference now to Fig. 4,, illustrates according to the available solvent extraction feel flow draw of block of the 3rd technology in the above-mentioned applicant's technology that is used for the 3rd alternative product of coal importing is refined oil as shown in Figure 1.In this technology, under the temperature (200～400 ℃ are desirably about 350 ℃) that raises, utilize light cycle oil to extract coal with one or more steps.This optimal process utilizes bituminous coal (bituminous coal) as feed coal (feed coal).Feed coal and light cycle oil are imported solvent extraction and tripping device 302 via input aperture 300 and 301 respectively.The main products of extraction process is the solid-state slurries of residue coal of extraction not in the light cycle oil.These slurries comprise the various chemical compounds that extract from the feed coal in solution.Slurries are carried out the solid/liquid separation process of pressure filtration etc.The liquid product output of tripping device 302 is fed to hydrotreater 304, in hydrotreater 304, the liquid product output is mixed with the hydrogen of importing by input aperture 303.The output of hydrotreater 304 directly is fed to the separation column 305 with a plurality of delivery ports that comprise gasoline delivery port 306, jet fuel delivery port 307, diesel oil delivery port 308 and fuel oil delivery port 309.Use 310 the raw material as gasification installation (feedstock) of product of coal that solid do not extract, described gasification installation is used to produce the needed a part of hydrogen of hydrogen treatment step, illustrates in greater detail below with reference to Fig. 5.In order further to understand flow process by the various process-streams of the oil refining after improving, can be with reference to figure 1.
With reference now to Fig. 5,, illustrates according to the available gasification by product of the 4th technology mixing process feel flow draw of block in the above-mentioned applicant's technology that is used for the 4th alternative product of coal importing is refined oil as shown in Figure 1.Some naphthalenes systems that the blending method of producing coal-based jet fuel requires to have discharged from coal or that formed by coal and indenes based compound source (source) are as raw material.Some Coal Gasification Technology is produced coal tar as by product.More significantly, this is known technology as so-called fixed bed (being also known as moving-bed) gasification, and wherein, strange (Lurgi) gasifier in Shandong is foremost and is commercial successful examples.In traditional gasification is used, tar is handled to obtain useful chemical products, tar is burnt as convenient fuel, perhaps tar is collected and disposed as rejected material.
In the disclosed gasification by product mixing process, the mix flow of coal and steam and oxygen is fed to coal gasifier 402 by input aperture 400 and 401 respectively here.Coal gasifier produces thick product gas 403, tar 405 and ash 404 output logistics.The tar that collection is produced by coal gasifier 402, and with this tar and suitable for example light cycle oil blending of refinery stream (stream).Tar and light cycle oil are directed into mixing tank 407 via input aperture 405 and 409 respectively.Tar and light cycle oil after the blending are fed to hydrotreater 412.To be fed to the gas sweetening and the conversion reactor 406 of the output logistics that produces carbon dioxide 408 and hydrogen 410 by the thick product gas that coal gasifier 402 produces.To be fed to hydrotreater 412 from the hydrogen of gas sweetening and conversion reactor 406 output logistics 410, in hydrotreater 412, it is used for tar and light cycle oil after hydrogen treatment is fed to hydrotreater 412 from input logistics 411 the blending.The output of hydrotreater 412 directly is fed to separation column or the distillation tower (distillation column) with a plurality of delivery ports that comprise gasoline delivery port 414, jet fuel delivery port 415, diesel oil delivery port 416 and fuel oil delivery port 417.The added benefit of this technology is to move gasifier self to produce hydrogen, and then, as described, this hydrogen can be used as the source of the hydrotreated hydrogen that is used for factory coal-tar middle oil blending downstream.
As refine oil the those of skill in the art in field and understand, in the integrated refinery Infrastructure of oil/product of coal, above-mentioned disclosed these four kinds auxiliary product of coal input units of this paper and technology structurally be independent of each other in the operation.
As described in Figure 6, on oil/product of coal integrated refinery Infrastructure, can be independently, simultaneously or this type of product of coal equipment and technology of parallel running or operation any amount.Thereby, can be with the refinery transformation of ad hoc structure, to comprise four kinds of whole product of coal input unit/technologies, perhaps can transform only to comprise one or both or three kinds in these input unit/technologies, in the time can specifying its specific product line, can when the particular coal product of handling as output, have great handiness thus.Can select this type of handiness of installing additional, to satisfy or to utilize or meet about being directed to the various cost factors or the space constraint of any particular refinery that one or more products of coal input things will transform.Thereby, for example, if the clarified oil supply that refinery can not obtain the co-carbonization device economically then can be transformed this refinery, to move or to concentrate on other product of coal input unit or technology.
Therefore, owing to there is the multiple feasible approach of making coal-based jet fuel, therefore aforesaid equipment and technology provide great diversity for fuel production industry.
As an example, as shown in Figure 6, the refinery that does not have delay coking device can only move mixing process.For the refinery that does not have catalytic cracking unit, can only move coking process.Also have the refinery of delay coking device for both having cat cracker, can move fully concurrently mixing process and coking process the two, by independently hydrogen treatment and fractionating step are carried (carry) product from each technology.Guarantee its special characteristics unless each technology has, otherwise the product of each parallel technology chain (processing train) is concocted in refinery as the scale of dividing other product.Alternatively,, can move blending and coking individually, make up the liquid product of each operation in these operations then for having the two refinery of cat cracker and delay coking device.Then, shown in further, the product that is made up is carried out hydrogen treatment and fractionation as a stream as Fig. 6.
As it is known to refine oil the those of skill in the art in field, shown in Fig. 1～6, in every respect in, refinery Infrastructure all will be under the stepless control that comprises the main control panel (not shown) that is obtained commercially numeral or analog calculation machine equipment.Refinery Infrastructure main control computer equipment (not shown in figure 1) is controlled by a series of selectable Software Production sequence of control in running, thereby suitably dispatch and be controlled at each functional element of system and the various refinement input things of the oil in the flow (flow level) and/or product of coal and liquid flow rate at the on period of integrated refinery Infrastructure, to produce the distillate product of expectation.
For the additional background of the technology controlling and process that specifically is applicable to refinery, the applicant asks interested personnel with reference to Royal Dutch Shell, The Petroleum Handbook.6
ThEdition, Elsevier Science Publishers, Amsterdam, 1983 (ISBN0-444042118-1), are incorporated herein by reference by especially the 331st～335 page.Usually about other useful handbook of technology controlling and process, the applicant advises the Handbook.7 with reference to Perry ' sChemical Engineers '
ThEdition.McGraw-Hill, NewYork (ISBN 0-07-049841-50), particularly the 8th chapter is incorporated herein by reference.
Fig. 7 is a feel flow draw of block of incorporating the standard oil refining flow process of coal tar mixing process option into.The coal tar mixing process is shown in Fig. 2 especially.
Fig. 8 is a feel flow draw of block of incorporating the standard oil refining flow process of co-carbonization process option into.Co-carbonization technology is shown in Fig. 3 especially.
Fig. 9 is a feel flow draw of block of incorporating the standard oil refining flow process of solvent extraction technology option into.This solvent extraction technology is shown in Fig. 4 especially.
Figure 10 is a feel flow draw of block of incorporating the standard oil refining flow process of gasification by product mixing process additive term into.Can understand this gasification by product mixing process better with reference to figure 5.
In the explanation of this paper, a plurality of details are provided, the example of composition and/or method for example is to provide the complete understanding to embodiment of the present invention.Yet, the those of skill in the art of association area will recognize, under can the one or more situation in lacking detail, perhaps under situation, implement embodiment of the present invention with other equipment, system, assembly, method, composition, material and/or parts etc.In other cases, at length do not specifically illustrate or illustrate known structure, material or operation, to avoid the making aspect of embodiment of the present invention not obvious.
Although understand the present invention very in detail with reference to particular of the present invention, can accomplished in various ways the present invention under the situation that does not deviate from the spirit or scope of the present invention.Therefore, following claims never should be defined in the description of the embodiment that this paper is comprised.
Claims (11)
1. in the oil refining flow process that comprises at least one fractionation plant and at least one hydrogen treating device, a kind of improvement that comprises some optional technologies, described optional technology is used for coal-based product is directly imported described oil refining flow process, creates thus to be used to produce coal-based jet fuel and other the associating oil refining process that distillates fuel.
2. associating oil refining process according to claim 1 is characterized in that, the described technology that is used to import described coal-based product comprises optional coal tar mixing process.
3. associating oil refining process according to claim 1 is characterized in that, the described technology that is used to import described coal-based product comprises optional co-carbonization technology.
4. an oil and coal-based product are united refining equipment, comprising:
At least one fractionation plant,
At least one hydrogen treating device, and
Be used for optionally coal-based product directly being directed into the equipment of the oil refining flow process that comprises described at least one fractionation plant and described at least one hydrogen treating device, make described oil and coal-based associating refining equipment can produce distillating fuel of coal-based jet fuel and other thus.
5. oil according to claim 4 and coal-based product associating refining equipment is characterized in that, the described equipment that is used for optionally described coal-based product being imported described oil refining flow process comprises coal tar blending equipment.
6. oil according to claim 4 and coal-based product associating refining equipment is characterized in that the described equipment that is used for optionally described coal-based product being imported described oil refining flow process comprises the co-carbonization introducing equipment.
7. oil according to claim 4 and coal-based product associating refining equipment is characterized in that the described equipment that is used for optionally described coal-based product being imported described oil refining flow process comprises solvent extraction equipment.
8. oil according to claim 4 and coal-based product associating refining equipment is characterized in that, the described equipment that is used for optionally described coal-based product being imported described oil refining flow process comprises gasification by product blending equipment.
9. oil according to claim 4 and coal-based product associating refining equipment, it is characterized in that described being used for comprises at least two equipment that are selected from the group that comprises coal tar blending equipment, co-carbonization equipment, solvent extraction equipment and gasification by product blending equipment with the equipment that described coal-based product imports described oil refining flow process.
10. oil according to claim 9 and coal-based product associating refining equipment is characterized in that, will directly be directed into described oil and coal-based product associating refining technique from the refined liquid that described coal-based product extracts.
11. oil according to claim 10 and coal-based product associating refining equipment, it is characterized in that, subsequently described refined liquid is directed into hydrogen treating device in turn, is directed into fractionation plant then, generate distillating fuel of jet fuel and other thus.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US90788207P | 2007-04-20 | 2007-04-20 | |
| US60/907,882 | 2007-04-20 | ||
| US12/068,937 US20080256852A1 (en) | 2007-04-20 | 2008-02-13 | Integrated process and apparatus for producing coal-based jet fuel, diesel fuel, and distillate fuels |
| US12/068,937 | 2008-02-13 | ||
| PCT/US2008/056575 WO2008130746A1 (en) | 2007-04-20 | 2008-03-12 | Integrated process and apparatus for producing coal-based jet fuel, diesel fuel, and distellate fuels |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN101755034A true CN101755034A (en) | 2010-06-23 |
Family
ID=39870794
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN200880012859A Pending CN101755034A (en) | 2007-04-20 | 2008-03-12 | Integrated process and apparatus for producing coal-based jet fuel, diesel fuel, and distellate fuels |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US20080256852A1 (en) |
| EP (1) | EP2137281A1 (en) |
| CN (1) | CN101755034A (en) |
| CA (1) | CA2684490A1 (en) |
| IN (1) | IN2009DN06587A (en) |
| WO (1) | WO2008130746A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114829548A (en) * | 2019-12-20 | 2022-07-29 | 耐思特公司 | Flexible integrated production facility system and method |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101724461B (en) * | 2009-12-07 | 2012-10-03 | 中国科学院山西煤炭化学研究所 | Method for processing coal tar of productive, lightweight and clean fuel oil though catalytic hydrogenation |
| US20150141723A1 (en) * | 2013-11-19 | 2015-05-21 | Uop Llc | Process for hydrotreating a coal tar stream |
| US20150136652A1 (en) * | 2013-11-19 | 2015-05-21 | Uop Llc | Process for hydrotreating a coal tar stream |
| RU2657733C1 (en) * | 2017-12-20 | 2018-06-15 | Федеральное государственное бюджетное учреждение науки Ордена Трудового Красного Знамени Институт нефтехимического синтеза им. А.В. Топчиева Российской академии наук (ИНХС РАН) | Method for producing high-density jet fuel for supersonic aviation |
| PL3810726T3 (en) * | 2018-08-31 | 2022-08-01 | Max Aicher Gmbh & Co. Kg | Method for producing a coking product |
| WO2020227613A1 (en) * | 2019-05-09 | 2020-11-12 | Arq Ip Limited | Processes for utilisation of purified coal to upgrade refinery process components in the manufacture of petroleum coke |
| JP2023541156A (en) * | 2020-09-11 | 2023-09-28 | エイアールキュー・アイピー・リミテッド | Method for producing incremental anisotropic coke |
| CN113372952B (en) * | 2021-06-07 | 2022-09-02 | 西北大学 | Method for producing aviation kerosene by utilizing coal tar rich cyclic hydrocarbon fraction |
Family Cites Families (92)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3533938A (en) * | 1967-09-06 | 1970-10-13 | Ashland Oil Inc | Jet fuel from blended conversion products |
| US3502564A (en) * | 1967-11-28 | 1970-03-24 | Shell Oil Co | Hydroprocessing of coal |
| US3617513A (en) * | 1969-01-03 | 1971-11-02 | Exxon Research Engineering Co | Coking of heavy feedstocks |
| US3642607A (en) * | 1970-08-12 | 1972-02-15 | Sun Oil Co | Coal dissolution process |
| US3687838A (en) * | 1970-09-14 | 1972-08-29 | Sun Oil Co | Coal dissolution process |
| US3930984A (en) * | 1970-10-01 | 1976-01-06 | Phillips Petroleum Company | Coal-anthracene oil slurry liquefied with carbon monoxide and barium-promoted catalysts |
| US3705092A (en) * | 1970-12-18 | 1972-12-05 | Universal Oil Prod Co | Solvent extraction of coal by a heavy oil |
| US3717570A (en) * | 1971-02-05 | 1973-02-20 | J Hochman | Simultaneous hydrofining of coker gas oil, vacuum gas oils and virgin kerosene |
| US3726784A (en) * | 1971-02-18 | 1973-04-10 | Exxon Research Engineering Co | Integrated coal liquefaction and hydrotreating process |
| US3726785A (en) * | 1971-03-03 | 1973-04-10 | Exxon Research Engineering Co | Coal liquefaction using high and low boiling solvents |
| US3796630A (en) * | 1971-10-04 | 1974-03-12 | Phillips Petroleum Co | Microbial production of dicarboxylic acids |
| BE792127A (en) * | 1971-12-06 | 1973-03-16 | Uss Eng & Consult | COAL CONVERSION PROCESS |
| US3920536A (en) * | 1972-05-08 | 1975-11-18 | Sun Research Development | Coal dissolving process |
| US3846275A (en) * | 1972-09-15 | 1974-11-05 | Universal Oil Prod Co | Coal liquefaction process |
| US3841991A (en) * | 1973-04-05 | 1974-10-15 | Exxon Research Engineering Co | Coal conversion process |
| GB1481799A (en) * | 1973-11-30 | 1977-08-03 | Coal Ind | Manufacture of coke |
| DE2457468A1 (en) * | 1973-12-07 | 1975-07-17 | Rio Tinto Rhodesia Ltd | PROCESS FOR THE PRODUCTION OF HYDROCARBON HEATING OIL FROM COAL |
| US3932266A (en) * | 1973-12-12 | 1976-01-13 | The Lummus Company | Synthetic crude from coal |
| GB1481800A (en) * | 1973-12-12 | 1977-08-03 | Coal Ind | Production of coke |
| US3960701A (en) * | 1974-06-03 | 1976-06-01 | Schroeder Wilburn C | Hydrogenation of coal to produce coke, pitch and electrode carbon |
| US3947346A (en) * | 1974-09-20 | 1976-03-30 | The Lummus Company | Coal liquefaction |
| JPS51122104A (en) * | 1975-04-16 | 1976-10-26 | Mitsui Cokes Kogyo Kk | Process for liquefying coals |
| US4056460A (en) * | 1975-12-01 | 1977-11-01 | Malek John M | Process for liquefying carbonaceous materials of high molecular weight and for separating liquefaction products |
| US4021329A (en) * | 1976-01-15 | 1977-05-03 | Suntech, Inc. | Process for dissolving sub-bituminous coal |
| US4097361A (en) * | 1976-08-24 | 1978-06-27 | Arthur G. Mckee & Company | Production of liquid and gaseous fuel products from coal or the like |
| GB1603619A (en) * | 1977-06-08 | 1981-11-25 | Mobil Oil Corp | Process for coal liquefaction |
| GB1597119A (en) * | 1977-06-08 | 1981-09-03 | Mobil Oil Corp | Two stage cool liquefaction scheme |
| GB1604230A (en) * | 1978-05-31 | 1981-12-02 | Mobil Oil Corp | Hydroprocessing coal liquids |
| US4133740A (en) * | 1977-10-21 | 1979-01-09 | Gulf Research & Development Company | Process for increasing the fuel yield of coal liquefaction products by extraction of asphaltenes, resins and aromatic compounds from said coal liquefaction products |
| US4158948A (en) * | 1978-08-16 | 1979-06-26 | Texaco Inc. | Conversion of solid fuels into fluid fuels |
| US4222846A (en) * | 1978-12-13 | 1980-09-16 | Gulf Oil Corporation | Coal liquefaction-gasification process including reforming of naphtha product |
| US4222845A (en) * | 1978-12-13 | 1980-09-16 | Gulf Oil Corporation | Integrated coal liquefaction-gasification-naphtha reforming process |
| US4266083A (en) * | 1979-06-08 | 1981-05-05 | The Rust Engineering Company | Biomass liquefaction process |
| US4303494A (en) * | 1979-08-06 | 1981-12-01 | Mobil Oil Corporation | Continuous reaction/separation method for nucleated growth reactions |
| US4452688A (en) * | 1979-09-04 | 1984-06-05 | Electric Power Research Institute | Integrated coal liquefication process |
| US4264430A (en) * | 1979-10-22 | 1981-04-28 | Chevron Research Company | Three-stage coal liquefaction process |
| US4331531A (en) * | 1979-10-22 | 1982-05-25 | Chevron Research Company | Three-stage coal liquefaction process |
| US4300996A (en) * | 1979-12-26 | 1981-11-17 | Chevron Research Company | Three-stage coal liquefaction process |
| US4292165A (en) * | 1980-02-07 | 1981-09-29 | Conoco, Inc. | Processing high sulfur coal |
| US4409092A (en) * | 1980-04-07 | 1983-10-11 | Ashland Oil, Inc. | Combination process for upgrading oil products of coal, shale oil and crude oil to produce jet fuels, diesel fuels and gasoline |
| US4332666A (en) * | 1980-05-06 | 1982-06-01 | Exxon Research & Engineering Co. | Coal liquefaction process wherein jet fuel, diesel fuel and/or ASTM No. 2 fuel oil is recovered |
| US4409089A (en) * | 1980-08-14 | 1983-10-11 | Mobil Oil Corporation | Coal liquefaction and resid processing with lignin |
| US4334976A (en) * | 1980-09-12 | 1982-06-15 | Mobil Oil Corporation | Upgrading of residual oil |
| US4379744A (en) * | 1980-10-06 | 1983-04-12 | Chevron Research Company | Coal liquefaction process |
| US4385980A (en) * | 1981-02-26 | 1983-05-31 | Conoco Inc. | Coal treating process |
| US4832831A (en) * | 1981-03-24 | 1989-05-23 | Carbon Fuels Corporation | Method of refining coal by hydrodisproportionation |
| US5240592A (en) * | 1981-03-24 | 1993-08-31 | Carbon Fuels Corporation | Method for refining coal utilizing short residence time hydrocracking with selective condensation to produce a slate of value-added co-products |
| US4475924A (en) * | 1981-03-24 | 1984-10-09 | Meyer Trust | Coal derived fuel composition and method of manufacture |
| US4394248A (en) * | 1981-09-18 | 1983-07-19 | Uop Inc. | Coal liquefaction process |
| US4428820A (en) * | 1981-12-14 | 1984-01-31 | Chevron Research Company | Coal liquefaction process with controlled recycle of ethyl acetate-insolubles |
| US4447312A (en) * | 1982-01-19 | 1984-05-08 | Mobil Oil Corporation | Process for improving the diesel fuel quality of coal derived liquids |
| AU552677B2 (en) * | 1982-02-22 | 1986-06-12 | New Energy Development Organisation | Process for liquifying brown coal |
| US4440622A (en) * | 1982-06-23 | 1984-04-03 | Mobil Oil Corporation | Integration of short-contact-time liquefaction and critical solvent deashing with gasification through methanol-to-gasoline |
| US4427532A (en) * | 1982-09-28 | 1984-01-24 | Mobil Oil Corporation | Coking of coal with petroleum residua |
| US4461694A (en) * | 1982-12-01 | 1984-07-24 | International Coal Refining Company | Coal liquefaction process with enhanced process solvent |
| US4476009A (en) * | 1983-03-24 | 1984-10-09 | Texaco Inc. | Process for improving the hydrogen donor properties of a coal liquefaction solvent |
| JPS61500319A (en) * | 1983-11-05 | 1986-02-27 | ゲ− エフ カ− ゲゼルシヤフト フユア コ−レフエルフリユ シグング ミツト ベシユレンクテル ハフツング | Coal liquefaction method |
| US4551224A (en) * | 1983-12-16 | 1985-11-05 | Texaco Inc. | Coal liquefaction process |
| US4514281A (en) * | 1984-03-21 | 1985-04-30 | International Coal Refining Company | Corrosion inhibition for distillation apparatus |
| DE3420197A1 (en) * | 1984-05-30 | 1985-12-12 | Ruhrkohle Ag, 4300 Essen | METHOD FOR PRODUCING A DIESEL FUEL FROM CARBON OIL |
| US4917791A (en) * | 1984-06-01 | 1990-04-17 | Kang Chia Chen Chu | Process and catalysts for hydroconversion of coal or petroleum asphaltene to distillate liquids |
| US4702748A (en) * | 1984-08-10 | 1987-10-27 | Northeastern University | Process for stabilization of coal liquid fractions |
| US4740294A (en) * | 1984-09-25 | 1988-04-26 | Kerr-Mcgee Corporation | Method for sequentially co-processing heavy hydrocarbon and carbonaceous materials |
| US4541916A (en) * | 1984-10-18 | 1985-09-17 | Gulf Research & Development Corporation | Coal liquefaction process using low grade crude oil |
| US4605486A (en) * | 1985-04-26 | 1986-08-12 | Exxon Research And Engineering Co. | Coal liquefaction process with increased naphtha yields |
| US4617106A (en) * | 1985-07-26 | 1986-10-14 | Air Products And Chemicals, Inc. | Catalysts for coal liquefaction processes |
| US4874506A (en) * | 1986-06-18 | 1989-10-17 | Hri, Inc. | Catalytic two-stage coal hydrogenation process using extinction recycle of heavy liquid fraction |
| US4971683A (en) * | 1987-06-08 | 1990-11-20 | Carbon Fuels Corporation | Method of refining coal by short residence time hydrodisproportionation to co-produce coal-based petroleum substitutes and methanol |
| US5021148A (en) * | 1988-11-29 | 1991-06-04 | Carbon Fuels Corporation | Method of refining coal by short residence time partial liquefaction to produce petroleum substitutes and chemical feedstocks |
| US5110452A (en) * | 1987-06-08 | 1992-05-05 | Carbon Fuels Corporation | Method of refining coal by catalyzed short residence time hydrodisproportionation to form a novel coal-derived fuel system |
| JP2617952B2 (en) * | 1987-10-27 | 1997-06-11 | 住友金属鉱山株式会社 | Catalyst for hydrotreating coal liquefaction solvent |
| US4828676A (en) * | 1987-12-07 | 1989-05-09 | Exxon Research And Engineering Company | Process for the production of ultra high octane gasoline, and other fuels from aromatic hydrocrackates |
| US5008005A (en) * | 1989-10-17 | 1991-04-16 | The United States Of America As Represented By The Department Of Energy | Integrated coke, asphalt and jet fuel production process and apparatus |
| US5151173A (en) * | 1989-12-21 | 1992-09-29 | Exxon Research And Engineering Company | Conversion of coal with promoted carbon monoxide pretreatment |
| US5110450A (en) * | 1989-12-21 | 1992-05-05 | Exxon Research And Engineering Company | Coal extract hydroconversion process comprising solvent enhanced carbon monoxide pretreatment |
| US5200063A (en) * | 1990-06-21 | 1993-04-06 | Exxon Research And Engineering Company | Coal hydroconversion process comprising solvent enhanced pretreatment with carbon monoxide |
| CA2022721C (en) * | 1990-08-03 | 1999-10-26 | Teresa Ignasiak | Process for converting heavy oil deposited on coal to distillable oil in a low severity process |
| US5145489A (en) * | 1990-11-28 | 1992-09-08 | Fuels Management Inc. | Method for coprocessing coal and oil |
| US5264188A (en) * | 1991-01-22 | 1993-11-23 | Phillips Petroleum Company | Multi-stage hydrotreating process and apparatus |
| US5176820A (en) * | 1991-01-22 | 1993-01-05 | Phillips Petroleum Company | Multi-stage hydrotreating process and apparatus |
| US5266189A (en) * | 1991-04-22 | 1993-11-30 | Amoco Corporation | Integrated low severity alcohol-base coal liquefaction process |
| US5256278A (en) * | 1992-02-27 | 1993-10-26 | Energy And Environmental Research Center Foundation (Eerc Foundation) | Direct coal liquefaction process |
| US5783065A (en) * | 1992-09-03 | 1998-07-21 | University Of Utah Research Foundation | Method for coal liquefaction |
| US5308477A (en) * | 1992-09-03 | 1994-05-03 | University Of Utah | Method for coal liquefaction |
| JPH0753965A (en) * | 1993-08-09 | 1995-02-28 | Nkk Corp | Liquefaction of coal |
| US5573556A (en) * | 1994-11-03 | 1996-11-12 | Exxon Research And Engineering Company | Conversion of solid carbonaceous material using polyoxoanions |
| US5817229A (en) * | 1995-11-06 | 1998-10-06 | Texaco Inc | Catalytic hydrocarbon upgrading process requiring no external hydrogen supply |
| US5676711A (en) * | 1996-02-21 | 1997-10-14 | Kuzara; Joseph K. | Oil conversion process |
| US5969013A (en) * | 1998-07-30 | 1999-10-19 | W.P. Hickman Systems Inc. | Coal tar compositions |
| US6964691B1 (en) * | 2000-12-29 | 2005-11-15 | Nalco Company | Method of preparing a synthetic fuel from coal |
| US6641624B1 (en) * | 2000-12-29 | 2003-11-04 | Ondeo Nalco Company | Method of preparing a synthetic fuel from coal |
| US7615142B2 (en) * | 2006-08-31 | 2009-11-10 | Headwaters Technology Innovation, Llc | Expanded bed reactor system and method for hydroprocessing wax produced by Fischer-Tropsch reaction and contaminated with solids |
-
2008
- 2008-02-13 US US12/068,937 patent/US20080256852A1/en not_active Abandoned
- 2008-03-12 WO PCT/US2008/056575 patent/WO2008130746A1/en active Application Filing
- 2008-03-12 CN CN200880012859A patent/CN101755034A/en active Pending
- 2008-03-12 CA CA002684490A patent/CA2684490A1/en not_active Abandoned
- 2008-03-12 EP EP08731939A patent/EP2137281A1/en not_active Withdrawn
-
2009
- 2009-10-15 IN IN6587DEN2009 patent/IN2009DN06587A/en unknown
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114829548A (en) * | 2019-12-20 | 2022-07-29 | 耐思特公司 | Flexible integrated production facility system and method |
Also Published As
| Publication number | Publication date |
|---|---|
| IN2009DN06587A (en) | 2015-07-24 |
| EP2137281A1 (en) | 2009-12-30 |
| CA2684490A1 (en) | 2008-10-30 |
| US20080256852A1 (en) | 2008-10-23 |
| WO2008130746A1 (en) | 2008-10-30 |
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