U.S. patent application number 10/109418 was filed with the patent office on 2003-08-14 for process for producing a liquid fuel composition.
This patent application is currently assigned to ONSITE TECHNOLGY LLC. Invention is credited to Percell, James L..
Application Number | 20030153797 10/109418 |
Document ID | / |
Family ID | 28673624 |
Filed Date | 2003-08-14 |
United States Patent
Application |
20030153797 |
Kind Code |
A1 |
Percell, James L. |
August 14, 2003 |
Process for producing a liquid fuel composition
Abstract
A process to produce a flowable fuel or fuel supplement from
solid and/or liquid waste, such as municipal waste, industrial
wastes or mixtures thereof and the system to carry out the process
in which a feed of solid and liquid municipal waste, industrial
wastes or mixtures thereof to a treatment zone under conditions of
temperature to produce a solid char and vaporize liquids,
recombining the char and the liquids, recovered from the wastes
feed, to form a feed slurry containing solids, combining the feed
slurry with additional combustible waste liquids which are added at
a rate and amount to obtain a fuel slurry of specified properties,
particularly specified viscosity and BTU content, subjecting the
feed slurry and additional wastes to conditions of attrition in at
least one attrition zone to produce a product slurry containing
solids of fuel size, recovering the fuel slurry which be used as
fuel in partial oxidation processes. The liquid waste may be
collected as a product, particularly if they are high in organic
compounds.
Inventors: |
Percell, James L.; (Houston,
TX) |
Correspondence
Address: |
KENNETH H. JOHNSON
P.O. BOX 630708
HOUSTON
TX
77263
US
|
Assignee: |
ONSITE TECHNOLGY LLC
|
Family ID: |
28673624 |
Appl. No.: |
10/109418 |
Filed: |
March 28, 2002 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
|
|
60340786 |
Oct 30, 2001 |
|
|
|
Current U.S.
Class: |
585/240 ; 585/1;
585/241; 585/242 |
Current CPC
Class: |
C10G 1/02 20130101; C10L
1/322 20130101; C10L 5/48 20130101; Y02E 50/10 20130101; C10L 5/46
20130101; Y02E 50/30 20130101 |
Class at
Publication: |
585/240 ;
585/241; 585/242; 585/1 |
International
Class: |
C07C 001/00; C10G
001/00 |
Claims
The invention claimed is:
1. A process comprising providing a feed of solid and liquid waste
to a treatment zone under conditions of temperature to produce a
solid char and vaporize liquids, condensing and recovering said
vaporized liquids, combining said char and said recovered liquids
to form a feed slurry containing solids, combining said feed slurry
with additional wastes comprising combustible liquids and
recovering said fuel slurry as fuel product.
2. The process according to claim 1 wherein said feed slurry and
additional wastes are subjected to conditions of attrition in at
least one attrition zone to produce a product slurry containing
solids of fuel size.
3. The process according to claim 1 or 2 wherein said additional
wastes is added at a rate and amount to obtain a fuel slurry of
specified properties, particularly specified viscosity and BTU
content.
4. The process according to claim 3 wherein said conditions of
temperature are in the range of 150 to 1000.degree. F.
5. The process according to claim 1, 2 or 3 wherein said waste
comprises solid and liquid municipal waste.
6. The process according to claim 1, 2 or 3 wherein said waste
comprises agricultural waste.
7. The process according to claim 1, 2 or 3 wherein said waste
comprises refining waste.
8. The process according to claim 1, 2 or 3 wherein said waste
comprises non-infectious medical wastes.
8. The process according to claim 1, 2 or 3 wherein said waste
comprises petrochemical wastes.
9. A process comprising providing a feed of solid and liquid waste
to a treatment zone under conditions of temperature to produce a
solid char and vaporize liquids, condensing and recovering said
vaporized liquids, combining said char and said recovered liquids
to form a first slurry containing solids of a first size, combining
said first slurry with additional wastes comprising combustible
liquids, subjecting said first slurry and additional wastes to
conditions of attrition in a first attrition zone to produce a
second slurry containing solids of a second size, said second size
being smaller than said first size and recovering said second
slurry.
10. The process according to claim 9 comprising subjecting said
second slurry to attrition in a second attrition zone under
conditions of attrition to produce a third slurry containing solids
of a third size, said third size being smaller than said second
size and recovering said third slurry.
11. The process according to claim 10 comprising subjecting said
third slurry to attrition in a third attrition zone under attrition
conditions to produce a fuel slurry containing solids of fourth
size, said fourth size being smaller than said third size and
recovering said fuel slurry as fuel product.
12. The process according to claim 9 wherein said waste is
municipal waste, industrial waste or mixtures thereof.
13. The process according to claim 9 wherein said conditions of
temperature are in the range of 150 to 1000.degree. F.
14. The fuel product produced according to the process of claim 1,
2, 9 or 11.
15. A process comprising providing a feed of solid and liquid
municipal waste, industrial wastes or mixtures thereof to a
treatment zone under conditions of temperature to produce a solid
char and vaporize liquids, condensing and recovering said vaporized
liquids and recovering said liquids as product.
16. A process comprising providing a feed of solid and liquid
municipal waste, industrial wastes or mixtures thereof to a
treatment zone under conditions of temperature to produce a solid
char and vaporize liquids, condensing and recovering said vaporized
liquids, combining said char and a portion of said recovered
liquids to form a feed slurry containing solids, combining said
feed slurry with additional wastes comprising combustible liquids,
subjecting said feed slurry and additional wastes to conditions of
attrition in at least one attrition zone to produce a product
slurry containing solids of fuel size, recovering said fuel slurry
as fuel product.
17. The process according to claim 16 wherein a portion of said
recovered liquids are separated as product.
18. A process for the production of a fuel from a waste comprising:
(a) providing a feed of waste to a treatment zone under conditions
of temperature to produce a solid char and vaporize liquids; (b)
condensing and recovering said vaporized liquids; (c) removing a
portion of the recovered liquids as liquid fuel; (d) combining said
char and the remainder of the recovered liquids to form a feed
slurry containing solids; (e) combining said feed slurry with
additional wastes comprising combustible liquids; (f) subjecting
said feed slurry and additional wastes to conditions of attrition
in at least one attrition zone to produce a product slurry
containing solids of fuel size; and (g) recovering said fuel slurry
as fuel product.
19. The process according to claim 18 wherein said conditions of
temperature are in the range of 150 to 1000.degree. F.
20. The process according to claim 18 wherein said waste is
municipal solid waste, municipal liquid wastes, industrial solid
waste, industrial liquid wastes, sanitary sewage, tires, refining
waste, agricultural waste, animal waste, non-infectious medical
wastes, petrochemical wastes or mixtures thereof.
Description
BACKGROUND OF THE INVENTION
[0001] 1. Field of the Invention
[0002] This invention relates to the handling of waste materials
and more particularly in the converting of the waste material to a
usable fuel material.
[0003] In particular the invention relates to the preparation of a
definable liquid fuel.
[0004] 2. Related Information
[0005] The disposal of organic solid waste has become an
increasingly severe problem in view of the increasing population,
the concentration of populations in urban and suburban areas and
the increasing number of industries generating organic solid
wastes. Some national jurisdictions are about to enter a zero
landfill era, which necessitates the immediate solution to waste
and in particular solid waste disposal.
[0006] A large fraction of such organic waste is combustible and is
made up of such material as paper, textiles, leather, rubber, yard
wastes, wood, wood wastes and bark, garbage, plastics, paints,
industrial wastes and sludges and sanitary sewage treatment
products. The process of this invention is directed to the
conversion of the entire spectrum of wastes into products which can
be used as a fuel or fuel supplement.
[0007] Inasmuch as it is becoming increasingly difficult to dispose
of wastes, particularly solid waste by such previously used means
as dumping and filling, a critical need has arisen to find other
techniques for waste disposal, such techniques of necessity being
those which do not create pollution problems and of preference
those which do not require the expenditure of appreciable amounts
of energy. Moreover, if the end product or products of the disposal
process are themselves usable, the process is even more
desirable.
[0008] In general, the processes more recently proposed for solid
waste disposal may be classed as bulk reduction, conversion or
reclamation. Although some advances in bulk reduction
(densification) have been made, each of the techniques used
(baling, incineration, etc.) have inherent drawbacks including
disposal of the densified material, pollution control and the like.
Conversion is generally defined as the chemical or biochemical
transformation of the waste material into a useful product. The
techniques used include pyrolysis (destructive distillation or
decomposition at elevated temperatures, e.g.,
750.degree.-1600.degree. F., in the absence of air or other
reactive or oxidizing gases), composting (aerobic conversion of
cellulose waste into inert humus-like material by aerobic
bacteria), hydrogenation, wet oxidation, hydrolysis, anaerobic
digestion, biological fractionation and the like.
[0009] Recycling involves the separating out from the solid waste
of such materials as glass, plastics, metals, papers, textiles and
the like for reuse in one form or another. However, other than some
forms of papers, plastics and textiles, the combustible component
of organic solid wastes which has caloric value has not been
recovered. Only recently has any serious attempt been made to
convert the combustible materials to a form in which they could be
used as a fuel.
[0010] Older processes such as those in U.S. Pat. Nos. 3,961,961
and 4,008,053 used acid treatment to embrittle organic waste
material for grinding to produce solid fuels. More recently the
processes are used to produce liquid flowable fuels as in U.S. Pat.
Nos. 6,000,639 and 6,202,577.
[0011] It is a primary advantage of this invention that it is
possible to treat all waste including municipal and industrial
solid wastes and liquid wastes to form a consistent liquid flowable
fuel or fuel supplement using a relatively small amount of energy
and employing known system components. The resulting product
material is usable as a fuel or fuel supplement in existing
combustion equipment without requiring any substantial
modification. This product retains essentially all of the caloric
content of the original waste material from which it is formed. It
is another advantage that the process described can be carried out
with the expenditure of relatively little energy so that the net
result of the process is an energy gain in the form of caloric
fuel.
[0012] Still another advantage of this invention is that the
process does not involve substantial pyrolysis, decomposition or
chemical conversion and therefore does not generate pollution
control problems. It is a further advantage of this invention that
the process described can be carried out in available system
components and which can be readily adapted to conditions
prevailing within a given area to form a fuel product best suited
for the area in which it is produced or to be used. It is yet
another primary advantage of this invention that a unique fuel or
fuel supplement is produced. It is yet another advantage that such
a fuel or fuel supplement may be stored and handled without under
going decomposition.
[0013] Other advantages of the invention will be apparent
hereinafter.
SUMMARY OF THE INVENTION
[0014] Briefly the present invention is a process to produce
flowable fuel or fuel supplement from solid municipal waste,
industrial wastes or mixtures thereof and the system to carry out
the process. The resulting fuel products are characterized as a
combustible material with caloric value. They are further
characterized as being suitable for use as a fuel or in admixture
with other fuels in different forms for full and partial
oxidation.
[0015] The invention accordingly comprises the several steps and
system components and the relation of one or more of such steps or
system components with respect to each of the others and the fuel
slurry which possess the characteristics, properties and relation
of elements, all as exemplified in the detailed disclosure
hereinafter set forth.
[0016] The process comprises providing a feed of solid and liquid
municipal waste, industrial wastes or mixtures thereof to a
treatment zone under conditions of temperature to produce a solid
char and vaporize liquids, recovering the vaporized liquids as
product or combining said char and said recovered liquids to form a
feed slurry containing solids, combining said feed slurry with
additional wastes comprising combustible liquids, subjecting said
feed slurry and additional wastes to conditions of attrition in at
least one attrition zone to produce a product slurry containing
solids of fuel size, recovering said fuel slurry as fuel product.
Preferably the additional waste is added at a rate and amount to
obtain a fuel slurry of specified properties, particularly
specified viscosity and BTU content. The present process may also
be operated to recover a portion of the vaporized liquid as a
product and to recover a portion of the vaporized liquid and to
recombine it with the char.
[0017] In one embodiment the process comprises providing a feed of
solid and liquid municipal waste, industrial wastes or mixtures
thereof to a treatment zone under conditions of temperature to
produce a solid char and vaporize liquids, recovering and
condensing said vaporized liquids, combining said char and said
recovered liquids to form a first slurry containing solids of a
first size, combining said first slurry with additional wastes
comprising combustible liquids, subjecting said first slurry and
additional wastes to conditions of attrition in a first attrition
zone to produce a second slurry containing solids of a second size,
said second size being smaller than said first size, recovering
said second slurry and subjecting said second slurry to attrition
in a second attrition zone under conditions of attrition to produce
a third slurry containing solids of a third size, said third size
being smaller than said second size, recovering said third slurry
and subjecting said third slurry to attrition in a third attrition
zone under attrition conditions to produce a fuel slurry containing
solids of fourth size, said fourth size being smaller than said
third size and recovering said fuel slurry as fuel product.
[0018] For a fuller understanding of the nature and objects of the
invention, reference should be had to the following detailed
description taken in connection with the following drawing which is
a flow diagram of the process of this invention illustrating
various embodiments and modifications.
BRIEF DESCRIPTION OF THE DRAWINGS
[0019] FIG. 1 is a schematic representation of one embodiment of
the present invention.
[0020] FIG. 2 is a schematic representation of one embodiment of
the primary separator for the liquids and solids of the present
invention
DETAILED DESCRIPTION
[0021] A central element of the present system is a rotating drum
having an auger feed, an air tight seal, chain flails, and spiral
and lateral flights within the drum which is heated externally,
through which wastes are heated and processed to form the char and
to remove and recover the condensible materials which is described
in commonly owed U.S. Pat. No. 5,297,970, which is incorporated in
its entirety.
[0022] The material for treatment enters the unit through a hopper
and is then propelled by means of an auger into the heated,
rotating drum. Heat is applied to the outside of the rotating drum
by means of two gas burners mounted on the bottom of the trailer.
The flames, therefore, do not come in direct contact with the
treated material, with the heat being applied indirectly by
conduction through the drum wall.
[0023] The burners are mounted in separate fireboxes aligned in
tandem with the drum axis and are located far enough from the drum
so that the flame does not impinge upon the drum. The drum is
heated by radiation from the burner flames as well as from
convection of air heated by the burner flames. Rotation of the drum
prevents the burners from locally overheating the drum. In the
present process the temperature is maintained to create a char by
at least partially oxidizing the organic solids and embrittle the
solids. Temperatures in the range of 150 to 1000.degree. F. may be
used, depending, among other factors, on the nature of the starting
material and the type of apparatus which is to use the fuel.
[0024] A stationary shroud, or heat jacket, encompasses the
rotating drum and burners. Movement through the drum is regulated
by drum rotation and inclination and feed rate. The drum is tilted
slightly toward the exit end. The arrangements of internal flights
and chains in the drum are important factors in the efficient flow
of material through the drum.
[0025] The char, which may be characterized as a combustible
organic material, exits the lower end of the drum through a double
door arrangement which reduces the amount of dust exiting and
prevents air from entering the drum. A dust shroud encloses the
double door exit end of the drum.
[0026] The vapors inside the drum are drawn out by applying a
slight vacuum to the feed end of the drum. The withdrawn vapors are
then sent to a condensing unit and collected. An important feature
of the unit for this operation is an air tight seal between the
rotating drum and the stationary vent housing around the feed
auger. This seal must allow for some axial movement of the drum due
to expansion and contraction from heating as angular misalignment
and out-of-roundness.
[0027] On each end of the drum are steel "tires" which bear on
trunnion rollers mounted on the trailer and provide means for drum
rotation. Thrust rollers are incorporated into the trunnion
assembly on the feed end and bear on the edges of the tire to
prevent the drum from moving axially. Drum overall length changes
about 3.5 inches during the heat up and cool down cycles, resulting
in very large loads being applied to the thrust rollers. The steel
tires are mounted to the drum on thin spacer plates allowing air
circulation between the tires and drum. This is necessary to
prevent excessive head conduction to the trunnion rollers which
would greatly reduce the life of the roller bearings.
[0028] The feed to this element of the system is derived from any
wastes source such as municipal solid and/or liquid wastes (MSW),
industrial solid and/or liquid wastes, sanitary sewage, tires,
other industrial, refining, agricultural and animal waste,
non-infectious medical wastes and/or petrochemical wastes or
mixtures thereof. As of 1997 about 2.8 MM tons of industrial waste
was being combusted annually as shown in TABLE 1.
1TABLE 1 PRIME INDUSTRIAL SOURCE VOLUMES OF U.S. INDUSTRIAL
WASTES** Millions of Tons % of Total Waste Category Per Year Per
Year Industrial Organic Chemicals 1.600 56.2 Plastic
Materials/Synthetic Resins 0.496 17.4 Business Services 0.266 9.4
Pharmaceuticals 0.245 8.6 Petroleum Refining 0.114 4.0 Industrial
Inorganic Chemicals 0.095 3.3 Paints, Varnishes, Lacquers, Enamels
0.030 1.1 TOTALS 2.846 100 **Source: U.S. Environmental Protection
Agency from 1997 data published by the Gasification Technologies
Council.
[0029] MSW generally includes paper, textiles, leather, rubber,
yard wastes, wood, wood wastes and bark, garbage, plastics and
paints. It will be seen from TABLE 2 that such materials make up
the greater part of so-called solid municipal wastes.
2TABLE 2 Composition of a Typical Solid Municipal Waste % by
Weight, Dry Basis Combustible Organic Component Total Waste
Fraction Paper & Paperboard 40.0 52.9 Yard Wastes 12.0 15.5
Food Wastes 9.3 12.1 Wood 8.4 10.9 Textiles 2.5 3.2 Plastics 2.5
3.2 Rubber 1.1 1.4 Leather 0.6 0.9 Glass 10.3 Metal 7.1 Dirt
5.3
[0030] Thus substantially all of the organic material in solid
wastes, e.g., in solid municipal wastes, industrial waste and
agricultural waste can be subjected to the process of this
invention to form a fuel. Solid MSW wastes typically have a
moisture content of about 18%, almost all of which is associated
with the combustible organic fraction. The food wastes may contain
oleaginous materials in the form of meat fat, oils, etc. The
presence of such materials introduces no problems in the process of
this invention. Industrial wastes may include such items as
divergent as chlorinated hydrocarbons to solid resins. Although,
all of these materials may be fed to the rotating drum, normally
only solids are used and the liquids are added in the second step.
The rotating drum is of especial value in the initial particulation
of the solid materials and the removal of volatile materials from
the solids. The volatiles may be entrained, such as hydrocarbons
and water on dirt or may be constituent components such as the
break down of polymers under the temperature and handling
conditions in the rotary drum.
[0031] If the process begins with a mixed solid waste, e.g., a
solid municipal waste, it will generally be expedient to begin with
some form of primary size reduction such as shredding. The
preliminary step may conveniently be done in such equipment as
flail mills, hammer mills, shredders, shears, cage disintegrators,
chippers, cutters, disk mills, grinders, hoggers, rasp mills and
the like. Large metal items, such as washing machines and water
heaters may be removed prior to the initial sizing, since they are
not useful in the fuel product of the process. Similarly, metal
removal may be carried out along the process by magnets.
[0032] The physical separation of the organic combustible fraction
from the mixed waste may be accomplished by one or more of several
different known techniques including separation procedures based
upon differences in such physical characteristics as size, shape,
specific gravity, brittleness, elasticity, color reflectance,
magnetic susceptibility, electric conductivity, absorption of
electromagnetic radiation and radioactivity techniques and
apparatus for using these characteristics to sort out such
nonorganic materials as glass, metals, dirt, and the like are known
and described in the literature. (See for example "Solid Waste
Treatment Technology" by Alex Hershaft in Environmental Science
& Technology, Vol. 6 No. 5 pp 412-421 (1972).) It is, of
course, within the scope of this invention to begin with solid
organic waste material which requires no sorting or separating from
other waste materials. In such cases, it may be desirable or
necessary to perform a size reducing step using appropriate
equipment from the list given above.
[0033] Thus, for example, hammermills, shredders or grinders can be
employed to reduce such materials, as paper, wood, textiles or food
wastes to the desired degree of comminution.
[0034] In the operation of the rotary drum, there is most likely to
be a vaporous component removed, which is both aqueous and organic
compounds, e.g., hydrocarbons. Any system for condensing the
condensibles may be used, although that disclosed in commonly owned
U.S. Pat. No. 6,120,650, which is incorporated herein in its
entirety, is preferred, since it allows for separation of water and
organic compounds, if desired. Since the present process is
directed to the production of specific or consistent fuel product,
the greater control that can be exercised over the constitution of
the stream being processed, by being able to adjust the liquid
level and the BTU level, the better the process. In the present
process, it is contemplated in the preferred operation that all of
the recovered liquids from the rotating drum will be reunited with
the char from the drum, however, some feed compositions may
prohibit that, thus the ability to remove and hold some portion of
the liquid may make the feeds acceptable.
[0035] In the present process, the effluent from the rotating drum,
i.e., the char and a portion of the recovered condensibles are fed
to a first attrition unit, for sizing the solids and otherwise
dispersing and homogenizing the process liquor. A suitable
apparatus for this step is a hydropulper as used in paper
manufacturing. The solids in the process liquor are adjusted for
the apparatus in which they are used, e.g., generally from about 20
mm to less than about 0.2 mm for the reconstituted product,
comprising char and recovered vaporous liquids, to be useful as a
fuel. The hydropulper reduces the solid particles to no larger than
15 mm. Thus, one or more reductions in an attrition mill will be
necessary to reduce the particle size.
[0036] The reconstituted fuel product (char and aqueous liquids) of
this invention is particularly suited for use in the production of
synthesis gas (syngas). Suitable apparatus and processes or this
are those heretofore used for gasification of "black liquor" as
described in detail in U.S. Pat. Nos. 5,645,616 and 5,634,950 which
are incorporated herein in their entirety.
[0037] Referring now to FIG. 1 the water, hydrocarbons and solids
(char) are treated as shown. The recovered water conduit 6 and
organic liquids conduit 8 are recombined with the char (the solids
remaining after the heat treatment in the drum) conduit 16 and
waste water as required to maintain the fluidity of the combined
streams and fed via conduit 22 to hydropulper 20 where the size of
solid particles are reduced to less than 15 mm.
[0038] The char effluent 12 from the drum is subjected to metal
removal by hand or magnets and the metal remove via conduit 14.
[0039] The impeller 23, in addition to reducing the particle size
of the char, throws large objects not reduced by the initial feed
shredding to the trasher 28 for recycling. Impeller pump 26 passes
the slurry from the hydropulper to attrition mill 30, where the
solids are further reduced to less than 2 mm size. An recycle 36
returns a portion of the effluent from mill 30 to the hydropulper
to maintain the fluidity of the stream and passes the remainder to
a second attrition mill 40 via conduit 34 where the solids are
reduced to a particle size of less than 0.2 mm.
[0040] The particle size leaving each attrition unit is determined
by conventional screens used for such purposes in other
applications. The effluent from mill 40 goes to storage in a tank
50 via conduit 38.
[0041] In a preferred embodiment the fuel is fed via conduit 42 to
a partial oxidation unit 60, where it is partially oxidized to
H.sub.2 and CO. The flow for each component stream for this example
are shown in the TABLE 3.
3TABLE 3 CONDUIT NO. RATE 2 5 TONS/HR 4 200 LBS/HR 6 1 TONS/HR 8 2
TONS/HR 16 1.65 TONS/HR 14 700 LBS/HR 18 900 LBS/HR 22 5 TONS/HR 24
25 TONS/HR 32 600 GPM 34 100 GPM 36 500 GPM 38 100 GPM
[0042] Referring to the FIG. 2 the recovery of a volatile fraction
is shown in more detail. Rotating drum 210 receives feed which is
shredded, blended MSW or heterogeneous industrial waste via conduit
202, where it is heated to a temperatures up to 1000.degree. F. The
feed enters at the upper end and the traverses down its length
(about 75 feet) at a slight in conduit as the drum rotates. The
drum is heated by gas, e.g., natural gas via conduit 205. Line 210
carries drum vapors comprising hydrocarbons, water, and other
volatile constituents from drum 201. Line 212 carries cool oil
quench which is sprayed into transfer line 214 carrying the drum
vapors to cool the drum vapors and condense the major portion of
the hydrocarbons. The condensed vapors are collected in primary
separator 216 where the liquid hydrocarbon is separated via line
218A from water vapor and light hydrocarbons, such as methane and
non-condensibles such as CO and CO.sub.2 which exit the separator
via line 220A.
[0043] The hydrocarbon (oil phase) recovered via line 218A is sent
to filter 234 through pump 219 and line 218B. The filter may be,
for example, an oil cyclone where dirty oil blowdown is collected
via line 236 and recycled to the auger feed (not shown) to drum 201
or otherwise disposed of.
[0044] The clean oil recovered via line 238 is cooled by an air
cooled heat exchanger 240 exiting through line 242A. A portion may
be sent to storage or returned to the char, for example, in
hydropupler 20 of FIG. 1 via line 242B and a portion sent through
line 212 to quench the drum vapors in line 214.
[0045] Cool water is sprayed from line 222B into transfer line 220A
to condense out most of the water and some higher hydrocarbons,
which is collected by secondary separator 224 where the condensed
water and some hydrocarbons are recovered via line 226A. The
non-condensibles, depending on the composition and the relevant
environmental considerations, are recovered via line 228 and may be
used as auxiliary fuel for the drum burners 202.
[0046] The condensed material (mainly water) leaves secondary
separator 224 via line 226A and is pumped by pump 227 through line
226B to air cooled heat exchanger 232 hence into line 246A. A
portion of the material in line 246A is returned via line 244 to
transfer line 220A to aid in cooling the vaporous feed from the
primary separator 216. Also in this embodiment cooled material from
secondary separator 224 via line 222A, pump 223 and line 222B is
used to cool the incoming vapors in line 220A.
[0047] A portion of cooled condensed material from heat exchanger
232 is also sent to oil/water phase separator 248 via 246A where
water is recovered from the bottom of separator 248 via line 250
and may be recovered for disposal via line 254 or return to mix
with the char 252 in the hydropulper 20.
[0048] The hydrocarbon phase from separator 248 is recovered to
storage or hydropulper 20 via 256 and 242B. The operating
temperatures and pressures for the various streams from FIG. 2 are
shown in TABLE 4 below.
4TABLE 4 Stream No. 214 220A 218A 242A 242B 212 220B 222A 226A
Temp., 249 249 249 249 125 125 148 148 148 F. Press., 14 14 14 90
75 75 13 13 13 PSIA Stream No. 226B 246A 222B 244 246B 256 254 242
250 Temp., 148 115 203 115 115 115 115 123 115 .degree. F. Press,
90 75 17 75 75 75 75 75 75 PSIA
* * * * *