Coal treatment process and apparatus

Claim 2

In the proces of sequentially hydrogenating carbonaceous solid fuel reactant with in situ steam-derived hydrogen to produce hydrocarbons, recovering produced hydrocarbon and then oxidizing the fuel reactant residuum from the hydrogenation to produce heat energy, the improvement comprising mixing said fuel reactant in a molten inorganic salt to solution of the fuel reactant in said salt in advance of and for the hydrogenation reaction and maintaining the fuel reactant residuum from the hydrogenation so dissolved for the oxidation thereof.

Claim 3

Process according to claim 1 including effecting said hydrogenation and hydrocarbon recovery in a first reaction zone, and alternately heat energy producing oxidation in a second reaction zone and repetitively in said zones in said alternating relation, said molten inorganic salt being common to both of said zones, and adding fresh fuel reactant to said molten inorganic salt solution prior to hydrogenation of said reactant.

Claim 4

Process according to claim 1 in which said molten salt solution is freed of volatile hydrocarbons produced by hydrogenation by said recovery and introducing an oxidizing gas into said volatile hydrocarbon-free molten salt solution under fuel reactant oxidizing conditions to effect said oxidation, following said recovery of produced hydrocarbons.

Claim 5

Process according to claim 3 in which fuel oxidizing conditions include a reaction temperature between 400° and 1000° C and pressure between 1 and 25 atmospheres.

Claim 6

Process according to claim 4 in which hydrogenating conditions include a reaction temperature between 300° and 500° C and pressure between 1 and 10 atmospheres.

Claim 7

Process according to claim 3 in which said oxidizing gas comprises oxygen.

Claim 8

Process according to claim 6 in which said oxidizing gas is air.

Claim 9

Process according to claim 6 in which said oxidizing gas is free oxygen containing.

Claim 10

Process according to claim 3 including also effecting substantially complete combustion reaction of dissolved carbonaceous fuel in said molten salt.

Claim 11

Process according to claim 9 including also heat exchanging combustion gases from said combustion reaction with the oxidizing gas to be introduced into said molten salt solution.

Claim 12

Process according to claim 10 including also expanding said combustion gases through a turbine after said heat exchange and compressing said oxidizing gas with energy derived from said expansion.

Claim 13

Process according to claim 3 including also treating said molten salt to separate undissolved mineral by-products therefrom.

Claim 14

Process for the treatment of coal or like carbonaceous solid fuel reactant for the coproduction of hydrocarbons and heat energy, which includes introducing a single phase molten salt solution of said reactant into a first reaction zone, generating active hydrogen by steam dissociation within said zone, contacting said reactant with said active hydrogen within said first zone and under hydrogenating conditions sufficient to hydrogenate the relatively more reactive 50 to 85% by weight portion of said reactant, separating overhead a stream comprising produced hydrocarbons and recovering said hydrocarbons; passing the first reaction zone effluent comprising a molten salt solution of said reactant to a second reaction zone, introducing an oxidizing gas into the solution in said zone under combustion conditions sufficient to substantially completely oxidize said unreacted reactant with the release of the heat of combustion into said molten salt, passing combustion gases overhead from said second reaction zone, passing the molten salt second reaction zone effluent after transferring combustion heat therefrom back to the first reaction zone, adding fresh reactant to said effluent, and repeating the hydrogenation and combustion cycle.

Claim 15

Process for the treatment of coal or like carbonaceous solid fuel reactant for the coproduction of hydrocarbons and heat energy, which includes introducing a single phase molten salt solution of said reactant into a first reaction zone, generating active hydrogen by steam dissociation within said zone, contacting said reactant with said active hydrogen within said first zone and under hydrogenating conditions sufficient to hydrogenate the relatively more reactive 50 to 85% by weight portion of said reactant, separating overhead a stream comprising produced hydrocarbons and recovering said hydrocarbons; passing the first reaction zone effluent comprising a molten salt solution of said reactant to a second reaction zone, introducing an oxidizing gas into the solution in said zone under combustion conditions sufficient to substantially completely oxidize said unreacted reactant with the release of the heat of combustion into said molten salt, passing combustion gases overhead from said second reaction zone, passing the molten salt second reaction zone effluent after transferring combustion heat therefrom back to the first reaction zone, adding fresh reactant to said effluent, and repeating the hydrogenation and combustion cycle.

Claim 16

Process according to claim 13 including also removing a hydrocarbons stream from said molten salt in advance of each successive heat energy production step, and removing heat energy from said molten salt in advance of each successive hydrocarbon production step.

Claim 17

Process according to claim 14 including also cooling the removed hydrocarbons stream to condense vapors of normally liquid hydrocarbons therein.

Claim 18

Process according to claim 15 including expanding the removed hydrocarbons stream to effect cooling of hydrocarbons therein.

Claim 19

Process according to claim 16 including also compressing lower molecular weight hydrocarbons of said hydrocarbons stream with energy derived from the expansion of said stream.

Claim 20

Process according to claim 14 including also shift reacting the removed hydrocarbons stream, stripping said hydrocarbons stream of carbon oxides and hydrogen, and recovering hydrocarbons.

Claim 21

Process according to claim 18 including also depleting the removed hydrocarbons stream of fixed gas and compressing said hydrocarbon stream for recovery of hydrocarbons therein.

Claim 22

Process according to claim 19 in which the compression energy is derived from expansion of the removed hydrocarbons stream through an expansion turbine.

Claim 23

Process according to claim 14 including also heat exchanging said removed hydrocarbons stream with water, and adding the resultant steam to the steam to be introduced into the molten salt solution.

Claim 24

Process according to claim 21 including also shift reacting the removed hydrocarbons stream in advance of water heat exchange.

Claim 25

Process according to claim 14 including also depleting the molten salt of sulfur in advance of heat energy production.

Claim 26

Process for the treatment of coal or like carbonaceous solid fuel reactant for the coproduction of hydrocarbons and heat energy, which includes introducing a molten salt solution comprising 5 to 30% by weight of said reactant into a first reaction zone, contacting said reactant with dissociated steam derived active hydrogen within said zone for 0.2 to about 5 seconds and under hydrogenating conditions sufficient to hydrogenate the relatively more reactive 50 to 85% by weight portion of said reactant, including a salt temperature between 350° and 425° C and a pressure between 3 and 10 atmospheres, separating overhead a stream comprising produced hydrocarbons and treating said stream to recover said hydrocarbons; passing the first reaction zone effluent comprising a molten salt solution comprising 2 to 10% of the unreacted less volatile 15 to 50% by weight portion of said reactant to a second reaction zone, introducing an oxidizing gas into the solution in said zone under combustion conditions including a temperature between 600° and 900° C and a pressure between 3 and 10 atmospheres and sufficient to substantially completely oxidize said unreacted reactant with the release of the heat of combustion into said molten salt, passing combustion gases overhead from said second reaction zone, passing the combustion heated molten salt second reaction zone effluent back to the first reaction zone, adding fresh reactant thereto, and repeating the hydrogenation and combustion cycle.

Claim 27

Process for the treatment of coal or like carbonaceous solid fuel reactant for the coproduction of hydrocarbons and heat energy, which includes introducing a molten salt solution comprising 5 to 30% by weight of said reactant into a first reaction zone, contacting said reactant with dissociated steam derived active hydrogen within said zone for 0.2 to about 5 seconds and under hydrogenating conditions sufficient to hydrogenate the relatively more reactive 50 to 85% by weight portion of said reactant, including a salt temperature between 350° and 425° C and a pressure between 3 and 10 atmospheres, separating overhead a stream comprising produced hydrocarbons and treating said stream to recover said hydrocarbons; passing the first reaction zone effluent comprising a molten salt solution comprising 2 to 10% of the unreacted less volatile 15 to 50% by weight portion of said reactant to a second reaction zone, introducing an oxidizing gas into the solution in said zone under combustion conditions including a temperature between 600° and 900° C and a pressure between 3 and 10 atmospheres and sufficient to substantially completely oxidize said unreacted reactant with the release of the heat of combustion into said molten salt, passing combustion gases overhead from said second reaction zone, passing the combustion heated molten salt second reaction zone effluent back to the first reaction zone, adding fresh reactant thereto, and repeating the hydrogenation and combustion cycle.

Claim 28

Process according to claim 24 including also admixing pulverulent coal reactant and the reheated molten salt into solution in advance of said first reaction zone.

Claim 29

Process according to claim 24 wherein said active hydrogen is generated in situ in said first reaction zone from steam introduced into said zone.

Claim 30

Process according to claim 26 including also preheating steam to be introduced into said reaction zone with heat from said second reaction zone.

Claim 31

Process according to claim 27 including also passing steam concurrently through said molten salt solution in said first reaction zone.

Claim 32

Process according to claim 24 including also passing oxidizing gas countercurrently through the molten salt solution in said second reaction zone.

Claim 33

Process according to claim 24 including also transferring heat from said second reaction zone molten salt effluent to a different density, high specific heat, immiscible and inert liquid heat exchange medium.

Claim 34

Process according to claim 30 in which said liquid medium is metal.

Claim 35

Process according to claim 31 in which said metal is lead.

Claim 36

Process according to claim 31 including commingling said second reaction zone molten salt effluent and said metal in a first heat exchange zone.

Claim 37

Process according to claim 33 in which said second reaction zone molten salt effluent and said metal are passed countercurrently to each other.

Claim 38

Process according to claim 34 including also counterflowing said molten salt and said metal through respective recirculation loops, said loops intersecting at said salt-metal first heat exchange zone.

Claim 39

Process according to claim 30 including also transfering heat from said heat exchange medium liquid to steam.

Claim 40

Process according to claim 36 in which said liquid heat exchange medium is metal.

Claim 41

Process according to claim 37 in which said metal and said steam are passed countercurrently to each other.

Claim 42

Process according to claim 38 including also commingling said metal and said steam in a second heat exchange zone.

Claim 43

Process according to claim 39 including also using said second heat exchange zone heat to heat steam to be passed to said first reaction zone.

Claim 44

Process according to claim 37 including also passing steam from said heat exchange means to a power generation zone.