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 1563.    ---------------.  [INSTITUTE OF GAS TECHNOLOGY.]  Fischer-Tropsch Process, an Annotated Bibliography.  Rept. for Tech. Sec., Postwar Planning Cooperating Com., October 1945, p. 23.

      Compilation of every published type of 

       Fischer-Tropsch cobalt catalyst

  

  

Composition

  

Ratio of constituents, wt. basis

Reaction temp.,

°F.

Yield of primary product liquid, and solid hydrocarbons, gal./1,000 ft.3

  

  

Remarks

Co................................

100

410

0.33

  

Co-Al...........................

100:20

419

.07

  

Co-Cr..........................

100:20

419

.10

  

Co-Mg.........................

100:20

419

.34

  

Co-Mn.........................

100:20

419

.47

  

Co-ThO2......................

100:18

392

.10

  

Co-Zn..........................

100:20

419

.31

  

Co-Cu-ThO2................

100:33:15

482

.09

  

Co-Cu-ThO2................

100:12:2

387

16.20

  

Co2O3-MnO2-CuO......

100:75:50

523

.03

  

Co-Mn-kguhr...............

100:15:-

392

.90

  

Co-ThO2-kguhr............

100:18:100

374

.97

  

Co-ThO2-kguhr............

100:18:100

392

16.97

Middle pressure.

Co-ThO2-kguhr............

100:18:100

-----

17.56

  

Co-Cu-MgO-sugar-char

100:35:15:-

473

.33

See footnote 1.

Co-Cu-MgO-pumice....

100:35:15:-

473

.50

See footnote 2.

Co-Mn-Al-kguhr..........

100:15:5:-

419

.57

  

Co-Mn-Cu-kguhr.........

100:15:10:-

401

.81

  

Co-Cu-MnO2-ThO2-kguhr............................

100:5:12:4:125

365-410

1.11

  

Co-Cu-ThO2-Ce-kguhr

100:11:22:2.6:-

392

.25

Ignition of nitrates gave slightly higher yield.

Co-Cu-Th-starch-kguhr

100:12.5:3.76:150:125

410

.83

  

Co-Cu-Th-U-kguhr......

100:12.5:1.88:1.88:

125

410

.50

  

Co-Cu-Th-U-kguhr......

10:12.5:1.88:1.88:

125

410

1.00

  

Co-Cu-U-starch-kguhr.

100:12.5:3.76:150:150

414

.87

  

Co-Mg-Cu-Cr-(?)........

100:25:12.5:12.5:-

410

.39

CO:H2=1:1.

Co-Mg-Cu-Mo-(?)......

100:25:12.5:12.5:-

410

.35

CO:H2=1:1.

Co-Mg-Cu-Th-kguhr....

100:25:12.5:5:75

455

.42

  

Co-Mg-Cu-Th-(?)........

100:25:12.5:5:-

410

.54

CO:H2=1:1.

Co-Mg-Cu-U-(?).........

100:25:12.5:5:75

410

.56

CO:H2=1:1.

Co-Mg-Cu-W-(?)........

100:25:12.5:5:-

410

.44

CO:H2=2:3.

Co-Mn-Cu-Th-kaolin...

100:25:12.5:12.5:-

471

.46

  

Co-Cu-Th-U-starch-kguhr............................

100:12.5:1.88:1.88:

150:125

410

.97

  

Co-Mg-Cu-Th-Co-(?)..

100:30:10:5:0.77

455

.47

  

Co-Ni-Mn-U3O8-ThO2-kguhr............................

100:43:21:7:4:125

392

1.04

  

Co-Ni, Fe, CaO, S, Mn)-ThO2-kguhr..........

100(1.72):8

-----

.84

Naphthene production (?).

1 Lb. per 1,000 cu. ft.

2 Reference gives yield ten times larger.  A source of error has been    assumed.